[Title 40 CFR ]
[Code of Federal Regulations (annual edition) - July 1, 2003 Edition]
[From the U.S. Government Printing Office]
[[Page i]]
40
Part 63 (Secs. 63.1440--End)
Revised as of July 1, 2003
Protection of Environment
Containing a codification of documents of general
applicability and future effect
As of July 1, 2003
With Ancillaries
Published by
Office of the Federal Register
National Archives and Records
Administration
A Special Edition of the Federal Register
[[Page ii]]
----------------------------------------------------------
As of July 1, 2003
Title 40, Part 63 (Secs. 63.1200--End)
Revised as of July 1, 2002
Is Replaced by Two Volumes
Title 40, Part 63 (Secs. 63.1200--63.1439)
and
Title 40, Part 63 (Secs. 63.1440--End)
----------------------------------------------------------
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[[Page iii]]
Table of Contents
Page
Explanation................................................. v
Title 40:
Chapter I--Environmental Protection Agency
(Continued) 3
Finding Aids:
Material Approved for Incorporation by Reference........ 1187
Table of CFR Titles and Chapters........................ 1189
Alphabetical List of Agencies Appearing in the CFR...... 1207
List of CFR Sections Affected........................... 1217
[[Page iv]]
----------------------------
Cite this Code: CFR
To cite the regulations in
this volume use title,
part and section number.
Thus, 40 CFR 63.1440
refers to title 40, part
63, section 1440.
----------------------------
[[Page v]]
EXPLANATION
The Code of Federal Regulations is a codification of the general and
permanent rules published in the Federal Register by the Executive
departments and agencies of the Federal Government. The Code is divided
into 50 titles which represent broad areas subject to Federal
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parts covering specific regulatory areas.
Each volume of the Code is revised at least once each calendar year
and issued on a quarterly basis approximately as follows:
Title 1 through Title 16.................................as of January 1
Title 17 through Title 27..................................as of April 1
Title 28 through Title 41...................................as of July 1
Title 42 through Title 50................................as of October 1
The appropriate revision date is printed on the cover of each
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LEGAL STATUS
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HOW TO USE THE CODE OF FEDERAL REGULATIONS
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[[Page vi]]
Many agencies have begun publishing numerous OMB control numbers as
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OBSOLETE PROVISIONS
Provisions that become obsolete before the revision date stated on
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INCORPORATION BY REFERENCE
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This material, like any other properly issued regulation, has the force
of law.
What is a proper incorporation by reference? The Director of the
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the requirements of 1 CFR part 51 are met. Some of the elements on which
approval is based are:
(a) The incorporation will substantially reduce the volume of
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(b) The matter incorporated is in fact available to the extent
necessary to afford fairness and uniformity in the administrative
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(c) The incorporating document is drafted and submitted for
publication in accordance with 1 CFR part 51.
Properly approved incorporations by reference in this volume are
listed in the Finding Aids at the end of this volume.
What if the material incorporated by reference cannot be found? If
you have any problem locating or obtaining a copy of material listed in
the Finding Aids of this volume as an approved incorporation by
reference, please contact the agency that issued the regulation
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The Federal Register Index is issued monthly in cumulative form.
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the revision dates of the 50 CFR titles.
[[Page vii]]
REPUBLICATION OF MATERIAL
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Raymond A. Mosley,
Director,
Office of the Federal Register.
July 1, 2003.
[[Page ix]]
THIS TITLE
Title 40--Protection of Environment is composed of twenty-nine
volumes. The parts in these volumes are arranged in the following order:
parts 1-49, parts 50-51, part 52 (52.01-52.1018), part 52 (52.1019-End),
parts 53-59, part 60 (60.1-End), part 60 (Appendices), parts 61-62, part
63 (63.1-63.599), part 63 (63.600-1-63.1199), part 63 (63.1200-63.1439),
part 63 (63.1440-End) parts 64-71, parts 72-80, parts 81-85, part 86
(86.1-86.599-99) part 86 (86.600-1-End), parts 87-99, parts 100-135,
parts 136-149, parts 150-189, parts 190-259, parts 260-265, parts 266-
299, parts 300-399, parts 400-424, parts 425-699, parts 700-789, and
part 790 to End. The contents of these volumes represent all current
regulations codified under this title of the CFR as of July 1, 2003.
Chapter I--Environmental Protection Agency appears in all twenty-
nine volumes. An alphabetical Listing of Pesticide Chemicals Index
appears in parts 150-189. Regulations issued by the Council on
Environmental Quality appear in the volume containing part 790 to End.
The OMB control numbers for title 40 appear in Sec. 9.1 of this chapter.
[[Page x]]
[[Page 1]]
TITLE 40--PROTECTION OF ENVIRONMENT
(This book contains part 63)
--------------------------------------------------------------------
Part
chapter i--Environmental Protection Agency (Continued)...... 63
[[Page 3]]
CHAPTER I--ENVIRONMENTAL PROTECTION AGENCY (CONTINUED)
--------------------------------------------------------------------
Editorial Note: 1. Subchapter C--Air programs is contained in volumes
40 CFR parts 50-51, part 52.01-52.1018, part 52.1019-end, parts 53-59,
part 60, parts 61-62, part 63 (63.1-63.599), part 63 (63.600-63.1199),
part 63 (63.1200-63.1439), part 63 (63.1440-end) parts 64-71, parts 72-
80, parts 81-85, part 86 (86.1-86.599-99), part 86 (86.600-1 to end) and
parts 87-99.
2. Nomenclature changes to chapter I appear at 65 FR 47324, 47325,
Aug. 2, 2000.
SUBCHAPTER C--AIR PROGRAMS (CONTINUED)
Part Page
63 National emission standards for hazardous
air pollutants for source categories.... 5
[[Page 5]]
SUBCHAPTER C--AIR PROGRAMS (CONTINUED)
PART 63--NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES--Table of Contents
Subpart QQQ--National Emission Standards for Hazardous Air Pollutants
for Primary Copper Smelting
What This Subpart Covers
63.1440 What is the purpose of this subpart?
63.1441 Am I subject to this subpart?
63.1442 What parts of my plant does this subpart cover?
63.1443 When do I have to comply with this subpart?
Emission Limitations and Work Practice Standards
63.1444 What emissions limitations and work practice standards must I
meet for my copper concentrate dryers, smelting furnaces, slag
cleaning vessels, and copper converter departments?
63.1445 What work practice standards must I meet for my fugitive dust
sources?
63.1446 What alternative emission limitation may I meet for my combined
gas streams?
Operation and Maintenance Requirements
63.1447 What are my operation and maintenance requirements?
General Compliance Requirements
63.1448 What are my general requirements for complying with this
subpart?
Initial Compliance Requirements
63.1449 By what date must I conduct performance tests or other initial
compliance demonstrations?
63.1450 What test methods and other procedures must I use to demonstrate
initial compliance with the emission limitations?
63.1451 How do I demonstrate initial compliance with the emission
limitations, work practice standards, and operation and
maintenance requirements that apply to me?
Continuous Compliance Requirements
63.1452 What are my monitoring requirements?
63.1453 How do I demonstrate continuous compliance with the emission
limitations, work practice standards, and operations and
maintenance requirements that apply to me?
Notifications, Reports and Records
63.1454 What notifications must I submit and when?
63.1455 What reports must I submit and when?
63.1456 What records must I keep and how long must I keep my records?
Other Requirements and Information
63.1457 What part of the General Provisions apply to me?
63.1458 Who implements and enforces this subpart?
63.1459 What definitions apply to this subpart?
Table 1 to Subpart QQQ of Part 63--Applicability of General Provisions
to Subpart QQQ.
Figure 1 to Subpart QQQ of Part 63--Data Summary Sheet for Determination
of Average Opacity.
Subpart RRR--National Emission Standards for Hazardous Air Pollutants
for Secondary Aluminum Production
General
63.1500 Applicability.
63.1501 Dates.
63.1502 Incorporation by reference.
63.1503 Definitions.
63.1504 [Reserved]
Emission Standards and Operating Requirements
63.1505 Emission standards for affected sources and emission nits.
63.1506 Operating requirements.
63.1507-63.1509 [Reserved]
Monitoring and Compliance Provisions
63.1510 Monitoring requirements.
63.1511 Performance test/compliance demonstration general requirements.
63.1512 Performance test/compliance demonstration requirements and
procedures.
63.1513 Equations for determining compliance.
63.1514 [Reserved]
Notifications, Reports, And Records
63.1515 Notifications.
63.1516 Reports.
63.1517 Records.
Other
63.1518 Applicability of general provisions.
63.1519 Delegation of authority.
63.1520 [Reserved]
[[Page 6]]
Table 1 to Subpart RRR--Emission Standards for New and Existing Affected
Sources
Table 2 to Subpart RRR--Summary of Operating Requirements for New and
Existing Affected Sources and Emission Units
Table 3 to Subpart RRR--Summary of Monitoring Requirements for New and
Existing Affected Sources and Emission Units
Appendix A to Subpart RRR--General Provisions Applicability to Subpart
RRR
Subpart SSS [Reserved]
Subpart TTT--National Emission Standards for Hazardous Air Pollutants
for Primary Lead Smelting
63.1541 Applicability.
63.1542 Definitions.
63.1543 Standards for process and process fugitive sources.
63.1544 Standards for fugitive dust sources.
63.1545 Compliance dates.
63.1546 Test methods.
63.1547 Monitoring requirements.
63.1548 Notification requirements.
63.1549 Recordkeeping and reporting requirements.
63.1550 Delegation of authority.
Subpart UUU--National Emission Standards for Hazardous Air Pollutants
for Petroleum Refineries: Catalytic Cracking Units, Catalytic Reforming
Units, and Sulfur Recovery Units
What This Subpart Covers
63.1560 What is the purpose of this subpart?
63.1561 Am I subject to this subpart?
63.1562 What parts of my plant are covered by this subpart?
63.1563 When do I have to comply with this subpart?
Catalytic Cracking Units, Catalytic Reforming Units, Sulfur Recovery
Units, and Bypass Lines
63.1564 What are my requirements for metal HAP emissions from catalytic
cracking units?
63.1565 What are my requirements for organic HAP emissions from
catalytic cracking units?
63.1566 What are my requirements for organic HAP emissions from
catalytic reforming units?
63.1567 What are my requirements for inorganic HAP emissions from
catalytic reforming units?
63.1568 What are my requirements for HAP emissions from sulfur recovery
units?
63.1569 What are my requirements for HAP emissions from bypass lines?
General Compliance Requirements
63.1570 What are my general requirements for complying with this
subpart?
63.1571 How and when must I conduct a performance test or other initial
compliance demonstration?
63.1572 What are my monitoring installation, operation, and maintenance
requirements?
63.1573 What are my monitoring alternatives?
Notifications, Reports, and Records
63.1574 What notifications must I submit and when?
63.1575 What reports must I submit and when?
63.1576 What records must I keep, in what form, and for how long?
Other Requirements and Information
63.1577 What parts of the General Provisions apply to me?
63.1578 Who implements and enforces this subpart?
63.1579 What definitions apply to this subpart?
Tables
Table 1 to Subpart UUU of Part 63--Metal HAP Emission Limits for
Catalytic Cracking Units
Table 2 to Subpart UUU of Part 63--Operating Limits for Metal HAP
Emissions from Catalytic Cracking Units
Table 3 to Subpart UUU of Part 63--Continuous Monitoring Systems for
Metal HAP Emissions from Catalytic Cracking Units
Table 4 to Subpart UUU of Part 63--Requirements for Performance Tests
for Metal HAP Emissions from Catalytic Cracking Units Not
Subject to the New Source Performance Standard (NSPS) for
Particulate Matter (PM)
Table 5 to Subpart UUU of Part 63--Initial Compliance with Metal HAP
Emission Limits for Catalytic Cracking Units
Table 6 to Subpart UUU of Part 63--Continuous Compliance with Metal HAP
Emission Limits for Catalytic Cracking Units
Table 7 to Subpart UUU of Part 63--Continuous Compliance with Operating
Limits for Metal HAP Emissions from Catalytic Cracking Units
Table 8 to Subpart UUU of Part 63--Organic HAP Emission Limits for
Catalytic Cracking Units
Table 9 to Subpart UUU of Part 63--Operating Limits for Organic HAP
Emissions from Catalytic Cracking Units
[[Page 7]]
Table 10 to Subpart UUU of Part 63--Continuous Monitoring Systems for
Organic HAP Emissions from Catalytic Cracking Units
Table 11 to Subpart UUU of Part 63--Requirements for Performance Tests
for Organic HAP Emissions from Catalytic Cracking Units Not
Subject to the New Source Performance Standard (NSPS) for
Carbon Monoxide (CO)
Table 12 to Subpart UUU of Part 63--Initial Compliance with Organic HAP
Emission Limits for Catalytic Cracking Units
Table 13 to Subpart UUU of Part 63--Continuous Compliance with Organic
HAP Emission Limits for Catalytic Cracking Units
Table 14 to Subpart UUU of Part 63--Continuous Compliance with Operating
Limits for Organic HAP Emissions from Catalytic Cracking Units
Table 15 to Subpart UUU of Part 63--Organic HAP Emission Limits for
Catalytic Reforming Units
Table 16 to Subpart UUU of Part 63--Operating Limits for Organic HAP
Emissions from Catalytic Reforming Units
Table 17 to Subpart UUU of Part 63--Continuous Monitoring Systems for
Organic HAP Emissions from Catalytic Reforming Units
Table 18 to Subpart UUU of Part 63--Requirements for Performance Tests
for Organic HAP Emissions from Catalytic Reforming Units
Table 19 to Subpart UUU of Part 63--Initial Compliance with Organic HAP
Emission Limits for Catalytic Reforming Units
Table 20 to Subpart UUU of Part 63--Continuous Compliance with Organic
HAP Emission Limits for Catalytic Reforming Units
Table 21 to Subpart UUU of Part 63--Continuous Compliance with Operating
Limits for Organic HAP Emissions from Catalytic Reforming
Units
Table 22 to Subpart UUU of Part 63--Inorganic HAP Emission Limits for
Catalytic Reforming Units
Table 23 to Subpart UUU of Part 63--Operating Limits for Inorganic HAP
Emission Limitations for Catalytic Reforming Units
Table 24 to Subpart UUU of Part 63--Continuous Monitoring Systems for
Inorganic HAP Emissions from Catalytic Reforming Units
Table 25 to Subpart UUU of Part 63--Requirements for Performance Tests
for Inorganic HAP Emissions from Catalytic Reforming Units
Table 26 to Subpart UUU of Part 63--Initial Compliance with Inorganic
HAP Emission Limits for Catalytic Reforming Units
Table 27 to Subpart UUU of Part 63--Continuous Compliance with Inorganic
HAP Emission Limits for Catalytic Reforming Units
Table 28 to Subpart UUU of Part 63--Continuous Compliance with Operating
Limits for Inorganic HAP Emissions from Catalytic Reforming
Units
Table 29 to Subpart UUU of Part 63--HAP Emission Limits for Sulfur
Recovery Units
Table 30 to Subpart UUU of Part 63--Operating Limits for HAP Emissions
from Sulfur Recovery Units
Table 31 to Subpart UUU of Part 63--Continuous Monitoring Systems for
HAP Emissions from Sulfur Recovery Units
Table 32 to Subpart UUU of Part 63--Requirements for Performance Tests
for HAP Emissions from Sulfur Recovery Units Not Subject to
the New Source Performance Standards (NSPS) for Sulfur Oxides
Table 33 to Subpart UUU of Part 63--Initial Compliance with HAP Emission
Limits for Sulfur Recovery Units
Table 34 to Subpart UUU of Part 63--Continuous Compliance with HAP
Emission Limits for Sulfur Recovery Units
Table 35 to Subpart UUU of Part 63--Continuous Compliance with Operating
Limits for HAP Emissions from Sulfur Recovery Units
Table 36 to Subpart UUU of Part 63--Work Practice Standards for HAP
Emissions from Bypass Lines
Table 37 to Subpart UUU of Part 63--Requirements for Performance Tests
for Bypass Lines
Table 38 to Subpart UUU of Part 63--Initial Compliance with Work
Practice Standards for HAP Emissions from Bypass Lines
Table 39 to Subpart UUU of Part 63--Continuous Compliance with Work
Practice Standards for HAP Emissions from Bypass Lines
Table 40 to Subpart UUU of Part 63--Requirements for Installation,
Operation, and Maintenance of Continuous Opacity Monitoring
Systems and Continuous Emission Monitoring Systems
Table 41 to Subpart UUU of Part 63--Requirements for Installation,
Operation, and Maintenance of Continuous Parameter Monitoring
Systems
Table 42 to Subpart UUU of Part 63--Additional Information for Initial
Notification of Compliance Status
Table 43 to Subpart UUU of Part 63--Requirements for Reports
[[Page 8]]
Table 44 to Subpart UUU of Part 63--Applicability of NESHAP General
Provisions to Subpart UUU
Subpart VVV--National Emission Standards for Hazardous Air Pollutants:
Publicly Owned Treatment Works
Applicability
63.1580 Am I subject to this subpart?
63.1581 Does the subpart distinguish between different types of POTW
treatment plants?
Industrial POTW Treatment Plant Description and Requirements
63.1582 What are the characteristics of an industrial POTW treatment
plant?
63.1583 What are the emission points and control requirements for an
industrial POTW treatment plant?
63.1584 When do I have to comply?
63.1585 How does an industrial POTW treatment plant demonstrate
compliance?
Non-industrial POTW Treatment Plant Requirements
63.1586 What are the emission points and control requirements for a non-
industrial POTW treatment plant?
63.1587 When do I have to comply?
63.1588 What inspections must I conduct?
63.1589 What records must I keep?
63.1590 What reports must I submit?
General Requirements
63.1591 What are my notification requirements?
63.1592 Which General Provisions apply to my POTW treatment plant?
63.1593 How will the EPA determine if I am in compliance with this
subpart?
63.1594 Who enforces this subpart?
63.1595 List of definitions.
Table 1 to Subpart VVV--Applicability of 40 CFR Part 63 General
Provisions to Subpart VVV
Subpart WWW [Reserved]
Subpart XXX--National Emission Standards for Hazardous Air Pollutants
for Ferroalloys Production: Ferromanganese and Silicomanganese
63.1620-63.1649 [Reserved]
63.1650 Applicability and compliance dates.
63.1651 Definitions.
63.1652 Emission standards.
63.1653 Opacity standards.
63.1654 Operational and work practice standards.
63.1655 Maintenance requirements.
63.1656 Performance testing, test methods, and compliance
demonstrations.
63.1657 Monitoring requirements.
63.1658 Notification requirements.
63.1659 Reporting requirements.
63.1660 Recordkeeping requirements.
63.1661 Delegation of authorities.
63.1662-63.1679 [Reserved]
Subpart AAAA--National Emission Standards for Hazardous Air Pollutants:
Municipal Solid Waste Landfills
What This Subpart Covers
63.1930 What is the purpose of this subpart?
63.1935 Am I subject to this subpart?
63.1940 What is the affected source of this subpart?
63.1945 When do I have to comply with this subpart?
63.1947 When do I have to comply with this subpart if I own or operate a
bioreactor?
63.1950 When am I no longer required to comply with this subpart?
63.1952 When am I no longer required to comply with the requirements of
this subpart if I own or operate a bioreactor?
Standards
63.1955 What requirements must I meet?
General and Continuing Compliance Requirements
63.1960 How is compliance determined?
63.1965 What is a deviation?
63.1975 How do I calculate the 3-hour block average used to demonstrate
compliance?
Notifications, Reports and Records
63.1980 What records and reports must I keep and submit?
Other Requirements and Information
63.1985 Who enforces this subpart?
63.1990 What definitions apply to this subpart?
Tables to Subpart AAAA of Part 63
Table 1 of Subpart AAAA of Part 63--Applicability of NESHAP General
Provisions to Subpart AAAA
Subpart CCCC--National Emission Standards for Hazardous Air Pollutants:
Manufacturing of Nutritional Yeast
What This Subpart Covers
63.2130 What is the purpose of this subpart?
63.2131 Am I subject to this subpart?
63.2132 What parts of my plant does this subpart cover?
63.2133 When do I have to comply with this subpart?
[[Page 9]]
Emission Limitations
63.2140 What emission limitations must I meet?
General Compliance Requirements
63.2150 What are my general requirements for complying with this
subpart?
Testing and Initial Compliance Requirements
63.2160 By what date must I conduct an initial compliance demonstration?
63.2161 What performance tests and other procedures must I use if I
monitor brew ethanol?
63.2162 When must I conduct subsequent performance tests?
63.2163 If I monitor fermenter exhaust, what are my monitoring
installation, operation, and maintenance requirements?
63.2164 If I monitor brew ethanol, what are my monitoring installation,
operation, and maintenance requirements?
63.2165 How do I demonstrate initial compliance with the emission
limitations if I monitor fermenter exhaust?
63.2166 How do I demonstrate initial compliance with the emission
limitations if I monitor brew ethanol?
Continuous Compliance Requirements
63.2170 How do I monitor and collect data to demonstrate continuous
compliance?
63.2171 How do I demonstrate continuous compliance with the emission
limitations?
Notifications, Reports, And Records
63.2180 What notifications must I submit and when?
63.2181 What reports must I submit and when?
63.2182 What records must I keep?
63.2183 In what form and how long must I keep my records?
Other Requirements And Information
63.2190 What parts of the General Provisions apply to me?
63.2191 Who implements and enforces this subpart?
63.2192 What definitions apply to this subpart?
Table 1 to Subpart CCCC--Emission Limitations
Table 2 to Subpart CCCC--Requirements for Performance Tests (Brew
Ethanol Monitoring Only)
Table 3 to Subpart CCCC--Initial Compliance With Emission Limitations
Table 4 to Subpart CCCC--Continuous Compliance with Emission Limitations
Table 5 to Subpart CCCC--Requirements for Reports
Table 6 to Subpart CCCC--Applicability of General Provisions to Subpart
CCCC
Subpart GGGG--National Emission Standards for Hazardous Air Pollutants:
Solvent Extraction for Vegetable Oil Production
What This Subpart Covers
63.2830 What is the purpose of this subpart?
63.2831 Where can I find definitions of key words used in this subpart?
63.2832 Am I subject to this subpart?
63.2833 Is my source categorized as existing or new?
63.2834 When do I have to comply with the standards in this subpart?
Standards
63.2840 What emission requirements must I meet?
Compliance Requirements
63.2850 How do I comply with the hazardous air pollutant emission
standards?
63.2851 What is a plan for demonstrating compliance?
63.2852 What is a startup, shutdown, and malfunction plan?
63.2853 How do I determine the actual solvent loss?
63.2854 How do I determine the weighted average volume fraction of HAP
in the actual solvent loss?
63.2855 How do I determine the quantity of oilseed processed?
Notifications, Reports, and Records
63.2860 What notifications must I submit and when?
63.2861 What reports must I submit and when?
63.2862 What records must I keep?
63.2863 In what form and how long must I keep my records?
Other Requirements and Information
63.2870 What parts of the General Provisions apply to me?
63.2871 Who implements and enforces this subpart?
63.2872 What definitions apply to this subpart?
Subpart HHHH--National Emission Standards for Hazardous Air Pollutants
for Wet-Formed Fiberglass Mat Production
What This Subpart Covers
63.2980 What is the purpose of this subpart?
63.2981 Does this subpart apply to me?
63.2982 What parts of my plant does this subpart cover?
[[Page 10]]
Emission Limitations
63.2983 What emission limits must I meet?
63.2984 What operating limits must I meet?
63.2985 When do I have to comply with these standards?
63.2986 How do I comply with the standards?
Operation, Maintenance, and Monitoring Plan
63.2987 What must my operation, maintenance, and monitoring (OMM) plan
include?
63.2988 [Reserved]
63.2989 How do I change my (OMM) plan?
63.2990 Can I conduct short-term experimental production runs that cause
parameters to deviate from operating limits?
Testing and Initial Compliance Requirements
63.2991 When must I conduct performance tests?
63.2992 How do I conduct a performance test?
63.2993 What test methods must I use in conducting performance tests?
63.2994 How do I verify the performance of monitoring equipment?
63.2995 What equations must I use to determine compliance?
Monitoring Requirements
63.2996 What must I monitor?
63.2997 What are the requirements for monitoring devices?
Notifications, Reports, and Records
63.2998 What records must I maintain?
63.2999 In what form and for how long must I maintain records?
63.3000 What notifications and reports must I submit?
Other Requirements and Information
63.3001 What sections of the general provisions apply to me?
63.3002 Who implements and enforces this subpart?
63.3003 Incorporation by reference.
63.3004 What definitions apply to this subpart?
63.3005--63.3079 [Reserved]
Table 1 to Subpart HHHH--Minimum Requirements for Monitoring and
Recordkeeping
Table 2 to Subpart HHHH--Applicability of General Provisions (40 CFR
Part 63, Subpart A) to Subpart HHHH
Appendix A to Subpart HHHH--Method for Determining Free-Formaldehyde in
Urea-Formaldehyde Resins by Sodium Sulfite (Iced & Cooled)
Appendix B to Subpart HHHH--Method for the Determination of Loss-on-
Ignition
Subpart JJJJ--National Emission Standards for Hazardous Air Pollutants:
Paper and Other Web Coating
What This Subpart Covers
63.3280 What is in this subpart?
63.3290 Does this subpart apply to me?
63.3300 Which of my emission sources are affected by this subpart?
63.3310 What definitions are used in this subpart?
Emission Standards and Compliance Dates
63.3320 What emission standards must I meet?
63.3321 What operating limits must I meet?
63.3330 When must I comply?
General Requirements for Compliance With the Emission Standards and for
Monitoring and Performance Tests
63.3340 What general requirements must I meet to comply with the
standards?
63.3350 If I use a control device to comply with the emission standards
what monitoring must I do?
63.3360 What performance tests must I conduct?
Requirements for Showing Compliance
63.3370 How do I demonstrate compliance with the emission standards?
Notifications, Reports, and Records
63.3400 What notifications and reports must I submit?
63.3410 What records must I keep?
Delegation of Authority
63.3420 What authorities may be delegated to the States?
Tables to Subpart JJJJ of Part 63
Subpart NNNN--National Emission Standards for Hazardous Air Pollutants:
Surface Coating of Large Appliances
What This Subpart Covers
63.4080 What is the purpose of this subpart?
63.4081 Am I subject to this subpart?
63.4082 What parts of my plant does this subpart cover?
63.4083 When do I have to comply with this subpart?
Emission Limitations
63.4090 What emission limits must I meet?
63.4091 What are my options for meeting the emission limits?
63.4092 What operating limits must I meet?
[[Page 11]]
63.4093 What work practice standards must I meet?
General Compliance Requirements
63.4100 What are my general requirements for complying with this
subpart?
63.4101 What parts of the General Provisions apply to me?
Notifications, Reports, and Records
63.4110 What notifications must I submit?
63.4120 What reports must I submit?
63.4130 What records must I keep?
63.4131 In what form and for how long must I keep my records?
Compliance Requirements for the Compliant Material Option
63.4140 By what date must I conduct the initial compliance
demonstration?
63.4141 How do I demonstrate initial compliance with the emission
limitations?
63.4142 How do I demonstrate continuous compliance with the emission
limitations?
Compliance Requirements for the Emission Rate Without Add-On Controls
Option
63.4150 By what date must I conduct the initial compliance
demonstration?
63.4151 How do I demonstrate initial compliance with the emission
limitations?
63.4152 How do I demonstrate continuous compliance with the emission
limitations?
Compliance Requirements for the Emission Rate With Add-On Controls
Option
63.4160 By what date must I conduct performance tests and other initial
compliance demonstrations?
63.4161 How do I demonstrate initial compliance?
63.4162 [Reserved]
63.4163 How do I demonstrate continuous compliance with the emission
limitations?
63.4164 What are the general requirements for performance tests?
63.4165 How do I determine the emission capture system efficiency?
63.4166 How do I determine the add-on control device emission
destruction or removal efficiency?
63.4167 How do I establish the emission capture system and add-on
control device operating limits during the performance test?
63.4168 What are the requirements for continuous parameter monitoring
system installation, operation, and maintenance?
Other Requirements and Information
63.4180 Who implements and enforces this subpart?
63.4181 What definitions apply to this subpart?
Tables to Subpart NNNN of Part 63
Table 1 to Subpart NNNN of Part 63--Operating Limits if Using the
Emission Rate with Add-on Controls Option
Table 2 to Subpart NNNN of Part 63--Applicability of General Provisions
to Subpart NNNN
Table 3 to Subpart NNNN of Part 63--Default Organic HAP Mass Fraction
for Solvents and Solvent Blends
Table 4 to Subpart NNNN of Part 63--Default Organic Mass Fraction for
Petroleum Solvent Groups
Subpart OOOO--National Emission Standards for Hazardous Air Pollutants:
Printing, Coating, and Dyeing of Fabrics and Other Textiles
What This Subpart Covers
Sec.
63.4280 What is the purpose of this subpart?
63.4281 Am I subject to this subpart?
63.4282 What parts of my plant does this subpart cover?
63.4283 When do I have to comply with this subpart?
Emission Limitations
63.4290 What emission limits must I meet?
63.4291 What are my options for meeting the emission limits?
63.4292 What operating limits must I meet?
63.4293 What work practice standards must I meet?
General Compliance Requirements
63.4300 What are my general requirements for complying with this
subpart?
63.4301 What parts of the General Provisions apply to me?
Notifications, Reports, and Records
63.4310 What notifications must I submit?
63.4311 What reports must I submit?
63.4312 What records must I keep?
63.4313 In what form and for how long must I keep my records?
Compliance Requirements for the Compliant Material Option
63.4320 By what date must I conduct the initial compliance
demonstration?
63.4321 How do I demonstrate initial compliance with the emission
limitations?
63.4322 How do I demonstrate continuous compliance with the emission
limitations?
Compliance Requirements for the Emission Rate Without Add-On Controls
Option
63.4330 By what date must I conduct the initial compliance
demonstration?
[[Page 12]]
63.4331 How do I demonstrate initial compliance with the emission
limitations?
63.4332 How do I demonstrate continuous compliance with the emission
limitations?
Compliance Requirements for the Emission Rate With Add-On Controls
Option
63.4340 By what date must I conduct performance tests and other initial
compliance demonstrations?
63.4341 How do I demonstrate initial compliance?
63.4342 How do I demonstrate continuous compliance with the emission
limitations?
Compliance Requirements for the Organic HAP Overall Control Efficiency
and Oxidizer Outlet Organic HAP Concentration Options
63.4350 By what date must I conduct performance tests and other initial
compliance demonstrations?
63.4351 How do I demonstrate initial compliance?
63.4352 How do I demonstrate continuous compliance with the emission
limitations?
Performance Testing and Monitoring Requirements
63.4360 What are the general requirements for performance tests?
63.4361 How do I determine the emission capture system efficiency?
63.4362 How do I determine the add-on control device emission
destruction or removal efficiency?
63.4363 How do I establish the add-on control device operating limits
during the performance test?
63.4364 What are the requirements for CPMS installation, operation, and
maintenance?
Other Requirements and Information
63.4370 Who implements and enforces this subpart?
63.4371 What definitions apply to this subpart?
Tables to Subpart OOOO of Part 63
Table 1 to Subpart OOOO of Part 63. Emission Limits for New or
Reconstructed and Existing Affected Sources in the Printing,
Coating, and Dyeing of Fabrics and Other Textiles Source
Category
Table 2 to Subpart OOOO of Part 63. Operating Limits if Using Add-On
Control Devices and Capture System
Table 3 to Subpart OOOO of Part 63. Applicability of General Provisions
to Subpart OOOO
Table 4 to Subpart OOOO of Part 63. Default Organic HAP Mass Fraction
for Solvents and Solvent Blends
Table 5 to Subpart OOOO of Part 63. Default Organic HAP Mass Fraction
for Petroleum Solvent Groups
Subpart QQQQ--National Emission Standards for Hazardous Air Pollutants:
Surface Coating of Wood Building Products
What This Subpart Covers
63.4680 What is the purpose of this subpart?
63.4681 Am I subject to this subpart?
63.4682 What parts of my plant does this subpart cover?
63.4683 When do I have to comply with this subpart?
Emission Limitations
63.4690 What emission limits must I meet?
63.4691 What are my options for meeting the emission limits?
63.4692 What operating limits must I meet?
63.4693 What work practice standards must I meet?
General Compliance Requirements
63.4700 What are my general requirements for complying with this
subpart?
63.4701 What parts of the General Provisions apply to me?
Notifications, Reports, and Records
63.4710 What notifications must I submit?
63.4720 What reports must I submit?
63.4730 What records must I keep?
63.4731 In what form and for how long must I keep my records?
Compliance Requirements for the Compliant Material Option
63.4740 By what date must I conduct the initial compliance
demonstration?
63.4741 How do I demonstrate initial compliance with the emission
limitations?
63.4742 How do I demonstrate continuous compliance with the emission
limitations?
Compliance Requirements for the Emission Rate Without Add-On Controls
Option
63.4750 By what date must I conduct the initial compliance
demonstration?
63.4751 How do I demonstrate initial compliance with the emission
limitations?
63.4752 How do I demonstrate continuous compliance with the emission
limitations?
Compliance Requirements for the Emission Rate With Add-On Controls
Option
63.4760 By what date must I conduct performance tests and other initial
compliance demonstrations?
[[Page 13]]
63.4761 How do I demonstrate initial compliance?
63.4762 [Reserved]
63.4763 How do I demonstrate continuous compliance with the emission
limitations?
63.4764 What are the general requirements for performance tests?
63.4765 How do I determine the emission capture system efficiency?
63.4766 How do I determine the add-on control device emission
destruction or removal efficiency?
63.4767 How do I establish the emission capture system and add-on
control device operating limits during the performance test?
63.4768 What are the requirements for continuous parameter monitoring
system installation, operation, and maintenance?
Other Requirements and Information
63.4780 Who implements and enforces this subpart?
63.4781 What definitions apply to this subpart?
Tables to Subpart QQQQ of Part 63
Table 1 to Subpart QQQQ of Part 63--Emission Limits for New or
Reconstructed Affected Sources
Table 2 to Subpart QQQQ of Part 63--Emission Limits for Existing
Affected Sources
Table 3 to Subpart QQQQ of Part 63--Operating Limits if Using the
Emission Rate with Add-on Controls Option
Table 4 to Subpart QQQQ of Part 63--Applicability of General Provisions
to Subpart QQQQ of Part 63
Table 5 to Subpart QQQQ of Part 63--Default Organic HAP Mass Fraction
for Solvents and Solvent Blends
Table 6 to Subpart QQQQ of Part 63--Default Organic HAP Mass Fraction
for Petroleum Solvent Groups
Subpart RRRR--National Emission Standards for Hazardous Air Pollutants:
Surface Coating of Metal Furniture
What This Subpart Covers
63.4880 What is the purpose of this subpart?
63.4881 Am I subject to this subpart?
63.4882 What parts of my plant does this subpart cover?
63.4883 When do I have to comply with this subpart?
Emission Limitations
63.4890 What Emission Limits Must I Meet?
63.4891 What are my options for demonstrating compliance with the
emission limits?
63.4892 What operating limits must I meet?
63.4893 What work practice standards must I meet?
General Compliance Requirements
63.4900 What are my general requirements for complying with this
subpart?
63.4901 What parts of the General Provisions apply to me?
Notifications, Reports, and Records
63.4910 What notifications must I submit?
63.4920 What reports must I submit?
63.4930 What records must I keep?
63.4931 In what form and for how long must I keep my records?
Compliance Requirements for the Compliant Material Option
63.4940 By what date must I conduct the initial compliance
demonstration?
63.4941 How do I demonstrate initial compliance with the emission
limitations?
63.4942 How do I demonstrate continuous compliance with the emission
limitations?
Compliance Requirements for the Emission Rate Without Add-On Controls
Option
63.4950 By what date must I conduct the initial compliance
demonstration?
63.4951 How do I demonstrate initial compliance with the emission
limitations?
63.4952 How do I demonstrate continuous compliance with the emission
limitations?
Compliance Requirements for the Emission Rate With Add-On Controls
Option
63.4960 By what date must I conduct performance tests and other initial
compliance demonstrations?
63.4961 How do I demonstrate initial compliance?
63.4962 How do I demonstrate continuous compliance with the emission
limitations?
63.4963 What are the general requirements for performance tests?
63.4964 How do I determine the emission capture system efficiency?
63.4965 How do I determine the add-on control device emission
destruction or removal efficiency?
63.4966 How do I establish the emission capture system and add-on
control device operating limits during the performance test?
63.4967 What are the requirements for continuous parameter monitoring
system installation, operation, and maintenance?
Other Requirements and Information
63.4980 Who implements and enforces this subpart?
[[Page 14]]
63.4981 What definitions apply to this subpart?
Table 1 to Subpart RRRR of Part 63. Operating Limits if Using the
Emission Rate with Add-on Controls Option
Table 2 to Subpart RRRR of Part 63. Applicability of General Provisions
to Subpart RRRR
Table 3 to Subpart RRRR of Part 63. Default Organic HAP Mass Fraction
for Solvents and Solvent Blends
Table 4 to Subpart RRRR of Part 63. Default Organic HAP Mass Fraction
for Petroleum Solvent Groups
Subpart SSSS--National Emission Standards for Hazardous Air Pollutants:
Surface Coating of Metal Coil
What This Subpart Covers
63.5080 What is in this subpart?
63.5090 Does this subpart apply to me?
63.5100 Which of my emissions sources are affected by this subpart?
63.5110 What special definitions are used in this subpart?
Emission Standards and Compliance Dates
63.5120 What emission standards must I meet?
63.5121 What operating limits must I meet?
63.5130 When must I comply?
General Requirements for Compliance with the Emission Standards and for
Monitoring and Performance Tests
63.5140 What general requirements must I meet to comply with the
standards?
63.5150 If I use a control device to comply with the emission standards,
what monitoring must I do?
63.5160 What performance tests must I complete?
Requirements for Showing Compliance
63.5170 How do I demonstrate compliance with the standards?
Reporting and Recordkeeping
63.5180 What reports must I submit?
63.5190 What records must I maintain?
Delegation of Authority
63.5200 What authorities may be delegated to the States?
63.5201-63.5209 [Reserved]
Tables to Subpart SSSS of Part 63
Table 1 to Subpart SSSS of Part 63--Operating Limits if Using Add-on
Control Devices and Capture System
Table 2 to Subpart SSSS of Part 63--Applicability of General Provisions
to Subpart SSSS
Subpart TTTT--National Emission Standards for Hazardous Air Pollutants
for Leather Finishing Operations
What This Subpart Covers
63.5280 What is the purpose of this subpart?
63.5285 Am I subject to this subpart?
63.5290 What parts of my facility does this subpart cover?
63.5295 When do I have to comply with this subpart?
Standards
63.5305 What emission standards must I meet?
Compliance Requirements
63.5320 How does my affected major source comply with the HAP emission
standards?
63.5325 What is a plan for demonstrating compliance and when must I have
one in place?
63.5330 How do I determine the compliance ratio?
63.5335 How do I determine the actual HAP loss?
63.5340 How do I determine the allowable HAP loss?
63.5345 How do I distinguish between the two upholstery product process
operations?
63.5350 How do I distinguish between the water-resistant/specialty and
nonwater-resistant leather product process operations?
63.5355 How do I monitor and collect data to demonstrate continuous
compliance?
63.5360 How do I demonstrate continuous compliance with the emission
standards?
Testing and Initial Compliance Requirements
63.5375 When must I conduct a performance test or initial compliance
demonstration?
63.5380 How do I conduct performance tests?
63.5385 How do I measure the quantity of finish applied to the leather?
63.5390 How do I measure the HAP content of a finish?
63.5395 How do I measure the density of a finish?
63.5400 How do I measure the quantity of leather processed?
Notifications, Reports, and Records
63.5415 What notifications must I submit and when?
63.5420 What reports must I submit and when?
[[Page 15]]
63.5425 When must I start recordkeeping to determine my compliance
ratio?
63.5430 What records must I keep?
63.5435 In what form and how long must I keep my records?
Other Requirements and Information
63.5450 What parts of the General Provisions apply to me?
63.5455 Who administers this subpart?
63.5460 What definitions apply to this subpart?
Figure 1 to Subpart TTTT of Part 63--Example Logs for Recording Leather
Finish Use and HAP Content
Tables to Subpart TTTT of Part 63
Table 1 to Subpart TTTT of Part 63--Leather Finishing HAP Emission
Limits for Determining the Allowable HAP Loss
Table 2 to Subpart TTTT of Part 63--Applicability of General Provisions
to Subpart TTTT
Subpart UUUU--National Emission Standards for Hazardous Air Pollutants
for Cellulose Products Manufacturing
What This Subpart Covers
63.5480 What is the purpose of this subpart?
63.5485 Am I subject to this subpart?
63.5490 What parts of my plant does this subpart cover?
63.5495 When do I have to comply with this subpart?
Emission Limits, Operating Limits, and Work Practice Standards
63.5505 What emission limits, operating limits, and work practice
standards must I meet?
General Compliance Requirements
63.5515 What are my general requirements for complying with this
subpart?
Testing and Initial Compliance Requirements
63.5530 How do I demonstrate initial compliance with the emission limits
and work practice standards?
63.5535 What performance tests and other procedures must I use?
63.5540 By what date must I conduct a performance test or other initial
compliance demonstration?
63.5545 What are my monitoring installation, operation, and maintenance
requirements?
Continuous Compliance Requirements
63.5555 How do I demonstrate continuous compliance with the emission
limits, operating limits, and work practice standards?
63.5560 How do I monitor and collect data to demonstrate continuous
compliance?
Notifications, Reports, and Records
63.5575 What notifications must I submit and when?
63.5580 What reports must I submit and when?
63.5585 What records must I keep?
63.5590 In what form and how long must I keep my records?
Other Requirements and Information
63.5595 What compliance options do I have if part of my affected source
is subject to both this subpart and another subpart?
63.5600 What other requirements apply to me?
63.5605 Who implements and enforces this subpart?
63.5610 What definitions apply to this subpart?
Tables to Subpart UUUU OF Part 63
Table 1 to Subpart UUUU of Part 63--Emission Limits and Work Practice
Standards
Table 2 to Subpart UUUU of Part 63--Operating Limits
Table 3 to Subpart UUUU of Part 63--Initial Compliance With Emission
Limits and Work Practice Standards
Table 4 to Subpart UUUU of Part 63--Requirements for Performance Tests
Table 5 to Subpart UUUU of Part 63--Continuous Compliance with Emission
Limits and Work Practice Standards
Table 6 to Subpart UUUU of Part 63--Continuous Compliance with Operating
Limits
Table 7 to Subpart UUUU of Part 63--Requirements for Notifications
Table 8 to Subpart UUUU of Part 63--Requirements for Reports
Table 9 to Subpart UUUU of Part 63--Requirements for Recordkeeping
Table 10 to Subpart UUUU of Part 63--Applicability of General Provisions
to Subpart UUUU
Subpart VVVV--National Emission Standards for Hazardous Air Pollutants
for Boat Manufacturing
What the Subpart Covers
63.5680 What is the purpose of this subpart?
63.5683 Does this subpart apply to me?
63.5686 How do I demonstrate that my facility is not a major source?
63.5689 What parts of my facility are covered by this subpart?
[[Page 16]]
63.5692 How do I know if my boat manufacturing facility is a new source
or an existing source?
63.5695 When must I comply with this subpart?
Standards for Open Molding Resin and Gel Coat Operations
63.5698 What emission limit must I meet for open molding resin and gel
coat operations?
63.5701 What are my options for complying with the open molding emission
limit?
63.5704 What are the general requirements for complying with the open
molding emission limit?
63.5707 What is an implementation plan for open molding operations and
when do I need to prepare one?
63.5710 How do I demonstrate compliance using emissions averaging?
63.5713 How do I demonstrate compliance using compliant materials?
63.5714 How do I demonstrate compliance if I use filled resins?
Demonstrating Compliance for Open Molding Operations Controlled by Add-
on Control Devices
63.5715 What operating limits must I meet?
63.5716 When must I conduct a performance test?
63.5719 How do I conduct a performance test?
63.5722 How do I use the performance test data to demonstrate initial
compliance?
63.5725 What are the requirements for monitoring and demonstrating
continuous compliance?
Standards for Closed Molding Resin Operations
63.5728 What standards must I meet for closed molding resin operations?
Standards for Resin and Gel Coat Mixing Operations
63.5731 What standards must I meet for resin and gel coat mixing
operations?
Standards for Resin and Gel Coat Application Equipment Cleaning
Operations
63.5734 What standards must I meet for resin and gel coat application
equipment cleaning operations?
63.5737 How do I demonstrate compliance with the resin and gel coat
application equipment cleaning standards?
Standards for Carpet and Fabric Adhesive Operations
63.5740 What emission limit must I meet for carpet and fabric adhesive
operations?
Standards for Aluminum Recreational Boat Surface Coating Operations
63.5743 What standards must I meet for aluminum recreational boat
surface coating operations?
63.5746 How do I demonstrate compliance with the emission limits for
aluminum wipedown solvents and aluminum coatings?
63.5749 How do I calculate the organic HAP content of aluminum wipedown
solvents?
63.5752 How do I calculate the organic HAP content of aluminum
recreational boat surface coatings?
63.5753 How do I calculate the combined organic HAP content of aluminum
wipedown solvents and aluminum recreational boat surface
coatings?
63.5755 How do I demonstrate compliance with the aluminum recreational
boat surface coating spray gun cleaning work practice
standards?
Methods for Determining Hazardous Air Pollutant Content
63.5758 How do I determine the organic HAP content of materials?
Notifications, Reports, and Records
63.5761 What notifications must I submit and when?
63.5764 What reports must I submit and when?
63.5767 What records must I keep?
63.5770 In what form and for how long must I keep my records?
Other Information You Need To Know
63.5773 What parts of the General Provisions apply to me?
63.5776 Who implements and enforces this subpart?
Definitions
63.5779 What definitions apply to this subpart?
Table 1 to Subpart VVVV--Compliance Dates for New and Existing Boat
Manufacturing Facilities
Table 2 to Subpart VVVV--Alternative HAP Content Requirements for Open
Molding Resin and Gel Coat Operations
Table 3 to Subpart VVVV--MACT Model Point Value Formulas for Open
Molding Operations
Table 4 to Subpart VVVV--Operating Limits If Using an Add-on Control
Device for Open Molding Operations
Table 5 to Subpart VVVV--Default Organic HAP Contents of Solvents and
Solvent Blends
Table 6 to Subpart VVVV--Default Organic HAP Contents of Petroleum
Solvent Groups
[[Page 17]]
Table 7 to Subpart VVVV--Applicability and Timing of Notifications
Table 8 to Subpart VVVV--Applicability of General Provisions (40 CFR
Part 63, Subpart A) to Subpart VVVV
Subpart WWWW--National Emissions Standards for Hazardous Air Pollutants:
Reinforced Plastic Composites Production
What This Subpart Covers
63.5780 What is the purpose of this subpart?
63.5785 Am I subject to this subpart?
63.5787 What if I also manufacture fiberglass boats or boat parts?
63.5790 What parts of my plant does this subpart cover?
63.5795 How do I know if my reinforced plastic composites production
facility is a new affected source or an existing affected
source?
Calculating Organic HAP Emissions Factors for Open Molding and
Centrifugal Casting
63.5796 What are the organic HAP emissions factor equations in Table 1
to this subpart and how are they used in this subpart?
63.5797 How do I determine the organic HAP content of my resins and gel
coats?
63.5798 What if I want to use, or I manufacture, an application
technology (new or existing) whose organic HAP emissions
characteristics are not represented by the equations in Table
1 to this subpart?
63.5799 How do I calculate my facility's organic HAP emissions on a tpy
basis for purposes of determining which paragraphs of
Sec. 63.5805 apply?
Compliance Dates and Standards
63.5800 When do I have to comply with this subpart?
63.5805 What standards must I meet to comply with this subpart?
Options for Meeting Standards
63.5810 What are my options for meeting the standards for open molding
and centrifugal casting operations at new and existing
sources?
63.5820 What are my options for meeting the standards for continuous
lamination/casting operations?
63.5830 What are my options for meeting the standards for pultrusion
operations subject to the 60 weight percent organic HAP
emissions reductions requirement?
General Compliance Requirements
63.5835 What are my general requirements for complying with this
subpart?
Testing and Initial Compliance Requirements
63.5840 By what date must I conduct a performance test or other initial
compliance demonstration?
63.5845 When must I conduct subsequent performance tests?
63.5850 How do I conduct performance tests, performance evaluations, and
design evaluations?
63.5855 What are my monitor installation and operation requirements?
63.5860 How do I demonstrate initial compliance with the standards?
Emissions Factor, Percent Reduction, and Capture Efficiency Calculation
Procedures for Continuous Lamination/Casting Operations
63.5865 What data must I generate to demonstrate compliance with the
standards for continuous lamination/casting operations?
63.5870 How do I calculate annual uncontrolled and controlled organic
HAP emissions from my wet-out area(s) and from my oven(s) for
continuous lamination/casting operations?
63.5875 How do I determine the capture efficiency of the enclosure on my
wet-out area and the capture efficiency of my oven(s) for
continuous lamination/casting operations?
63.5880 How do I determine how much neat resin plus is applied to the
line and how much neat gel coat plus is applied to the line
for continuous lamination/casting operations?
63.5885 How do I calculate percent reduction to demonstrate compliance
for continuous lamination/casting operations?
63.5890 How do I calculate an organic HAP emissions factor to
demonstrate compliance for continuous lamination/casting
operations?
Continuous Compliance Requirements
63.5895 How do I monitor and collect data to demonstrate continuous
compliance?
63.5900 How do I demonstrate continuous compliance with the standards?
Notifications, Reports, and Records
63.5905 What notifications must I submit and when?
63.5910 What reports must I submit and when?
63.5915 What records must I keep?
63.5920 In what form and how long must I keep my records?
Other Requirements and Information
63.5925 What parts of the General Provisions apply to me?
[[Page 18]]
63.5930 Who implements and enforces this subpart?
63.5935 What definitions apply to this subpart?
Tables to Subpart WWWW of Part 63
Table 1 to Subpart WWWW of Part 63--Equations to Calculate Organic HAP
Emissions Factors for Specific Open Molding and Centrifugal
Casting Process Streams
Table 2 to Subpart WWWW of Part 63--Compliance Dates for New and
Existing Reinforced Plastic Composites Facilities
Table 3 to Subpart WWWW of Part 63--Organic HAP Emissions Limits for
Existing Open Molding Sources, New Open Molding Sources
Emitting Less Than 100 TPY of HAP, and New and Existing
Centrifugal Casting and Continuous Lamination/Casting Sources
That Emit Less Than 100 TPY of HAP
Table 4 to Subpart WWWW of Part 63--Work Practice Standards
Table 5 to Subpart WWWW of Part 63--Alternative Organic HAPEmissions
Limits for Open Molding, Centrifugal Casting, and SMC
Manufacturing Operations Where the Standard is Based on a 95
Percent Reduction Requirement
Table 6 to Subpart WWWW of Part 63--Basic Requirements for Performance
Tests, Performance Evaluations, and Design Evaluations for New
and Existing Sources Using Add-On Control Devices
Table 7 to Subpart WWWW of Part 63--Options Allowing Use of the Same
Resin Across Different Operations That Use the Same Resin Type
Table 8 to Subpart WWWW of Part 63--Initial Compliance With Organic HAP
Emissions Limits
Table 9 to Subpart WWWW of Part 63--Initial Compliance With Work
Practice Standards.
Table 10 to Subpart WWWW of Part 63--Data Requirements for New and
Existing Continuous Lamination Lines and Continuous Casting
Lines Complying with a Percent Reduction Limit on a Per Line
Basis
Table 11 to Subpart WWWW of Part 63--Data Requirements for New and
Existing Continuous Lamination and Continuous Casting Lines
Complying with a Percent Reduction Limit or a Lbs/Ton Limit on
an Averaging Basis
Table 12 to Subpart WWWW of Part 63--Data Requirements for New and
Existing Continuous Lamination Lines and Continuous Casting
Lines Complying with a Lbs/Ton Organic HAP Emissions Limit on
a Per Line Basis
Table 13 to Subpart WWWW of Part 63--Applicability and Timing of
Notifications
Table 14 to Subpart WWWW of Part 63--Requirements for Reports
Table 15 to Subpart WWWW of Part 63--Applicability of General Provisions
(Subpart A) to Subpart WWWW of Part 63
Appendix A to Subpart WWWW of Part 63--Test Method for Determining Vapor
Suppressant Effectiveness
Subpart XXXX--National Emission Standards for Hazardous Air Pollutants:
Rubber Tire Manufacturing
What This Subpart Covers
63.5980 What is the purpose of this subpart?
63.5981 Am I subject to this subpart?
63.5982 What parts of my facility does this subpart cover?
63.5983 When do I have to comply with this subpart?
Emission Limits for Tire Production Affected Sources
63.5984 What emission limits must I meet for tire production affected
sources?
63.5985 What are my alternatives for meeting the emission limits for
tire production affected sources?
Emission Limits for Tire Cord Production Affected Sources
63.5986 What emission limits must I meet for tire cord production
affected sources?
63.5987 What are my alternatives for meeting the emission limits for
tire cord production affected sources?
Emission Limitations for Puncture Sealant Application Affected Sources
63.5988 What emission limitations must I meet for puncture sealant
application affected sources?
63.5989 What are my alternatives for meeting the emission limitations
for puncture sealant application affected sources?
General Compliance Requirements
63.5990 What are my general requirements for complying with this
subpart?
General Testing and Initial Compliance Requirements
63.5991 By what date must I conduct an initial compliance demonstration
or performance test?
63.5992 When must I conduct subsequent performance tests?
63.5993 What performance tests and other procedures must I use?
[[Page 19]]
Testing and Initial Compliance Requirements for Tire Production Affected
Sources
63.5994 How do I conduct tests and procedures for tire production
affected sources?
63.5995 What are my monitoring installation, operation, and maintenance
requirements?
63.5996 How do I demonstrate initial compliance with the emission limits
for tire production affected sources?
Testing and Initial Compliance Requirements for Tire Cord Production
Affected Sources
63.5997 How do I conduct tests and procedures for tire cord production
affected sources?
63.5998 What are my monitoring installation, operation, and maintenance
requirements?
63.5999 How do I demonstrate initial compliance with the emission limits
for tire cord production affected sources?
Testing and Initial Compliance Requirements for Puncture Sealant
Application Affected Sources
63.6000 How do I conduct tests and procedures for puncture sealant
application affected sources?
63.6001 What are my monitoring installation, operation, and maintenance
requirements?
63.6002 How do I demonstrate initial compliance with the emission limits
for puncture sealant application affected sources?
Continuous Compliance Requirements for Tire Production Affected Sources
63.6003 How do I monitor and collect data to demonstrate continuous
compliance with the emission limits for tire production
affected sources?
63.6004 How do I demonstrate continuous compliance with the emission
limits for tire production affected sources?
Continuous Compliance Requirements for Tire Cord Production Affected
Sources
63.6005 How do I monitor and collect data to demonstrate continuous
compliance with the emission limits for tire cord production
affected sources?
63.6006 How do I demonstrate continuous compliance with the emission
limits for tire cord production affected sources?
Continuous Compliance Requirements for Puncture Sealant Application
Affected Sources
63.6007 How do I monitor and collect data to demonstrate continuous
compliance with the emission limitations for puncture sealant
application affected sources?
63.6008 How do I demonstrate continuous compliance with the emission
limitations for puncture sealant application affected sources?
Notifications, Reports, and Records
63.6009 What notifications must I submit and when?
63.6010 What reports must I submit and when?
63.6011 What records must I keep?
63.6012 In what form and how long must I keep my records?
Other Requirements and Information
63.6013 What parts of the General Provisions apply to me?
63.6014 Who implements and enforces this subpart?
63.6015 What definitions apply to this subpart?
Tables to Subpart XXXX of Part 63
Table 1 to Subpart XXXX of Part 63--Emission Limits for Tire Production
Affected Sources
Table 2 to Subpart XXXX of Part 63--Emission Limits for Tire Cord
Production Affected Sources
Table 3 to Subpart XXXX of Part 63--Emission Limits for Puncture Sealant
Application Affected Sources
Table 4 to Subpart XXXX of Part 63--Operating Limits for Puncture
Sealant Application Control Devices
Table 5 to Subpart XXXX of Part 63--Requirements for Performance Tests
Table 6 to Subpart XXXX of Part 63--Initial Compliance with the Emission
Limits for Tire Production Affected Sources
Table 7 to Subpart XXXX of Part 63--Initial Compliance with the Emission
Limits for Tire Cord Production Affected Sources
Table 8 to Subpart XXXX of Part 63--Initial Compliance with the Emission
Limits for Puncture Sealant Application Affected Sources
Table 9 to Subpart XXXX of Part 63--Minimum Data for Continuous
Compliance with the Emission Limits for Tire Production
Affected Sources
Table 10 to Subpart XXXX of Part 63--Continuous Compliance with the
Emission Limits for Tire Production Affected Sources
Table 11 to Subpart XXXX of Part 63--Minimum Data for Continuous
Compliance with the Emission Limits for Tire Cord Production
Affected Sources
Table 12 to Subpart XXXX of Part 63--Continuous Compliance with the
Emission Limits for Tire Cord Production Affected Sources
[[Page 20]]
Table 13 to Subpart XXXX of Part 63--Minimum Data for Continuous
Compliance with the Emission Limitations for Puncture Sealant
Application Affected Sources
Table 14 to Subpart XXXX of Part 63--Continuous Compliance with the
Emission Limitations for Puncture Sealant Application Affected
Sources
Table 15 to Subpart XXXX of Part 63--Requirements for Reports
Table 16 to Subpart XXXX of Part 63--Selected Hazardous Air Pollutants
Table 17 to Subpart XXXX of Part 63--Applicability of General Provisions
to This Subpart XXXX
Subparts YYYY--AAAAA [Reserved]
Subpart BBBBB--National Emission Standards for Hazardous Air Pollutants
for Semiconductor Manufacturing
What This Subpart Covers
63.7180 What is the purpose of this subpart?
63.7181 Am I subject to this subpart?
63.7182 What parts of my facility does this subpart cover?
63.7183 When do I have to comply with this subpart?
Emission Standards
63.7184 What emission limitations, operating limits, and work practice
standards must I meet?
Compliance Requirements
63.7185 What are my general requirements for complying with this
subpart?
63.7186 By what date must I conduct performance tests or other initial
compliance demonstrations?
63.7187 What performance tests and other compliance procedures must I
use?
63.7188 What are my monitoring installation, operation, and maintenance
requirements?
Applications, Notifications, Reports, and Records
63.7189 What applications and notifications must I submit and when?
63.7190 What reports must I submit and when?
63.7191 What records must I keep?
63.7192 In what form and how long must I keep my records?
Other Requirements and Information
63.7193 What parts of the General Provisions apply to me?
63.7194 Who implements and enforces this subpart?
63.7195 What definitions apply to this subpart?
Tables to Subpart BBBBB of Part 63
Table 1 to Subpart BBBBB of Part 63--Requirements for Performance Tests
Table 2 to Subpart BBBBB of Part 63--Applicability of General Provisions
to Subpart BBBBB
Subpart CCCCC--National Emission Standards for Hazardous Air Pollutants
for Coke Ovens: Pushing, Quenching, and Battery Stacks
What This Subpart Covers
63.7280 What is the purpose of this subpart?
63.7281 Am I subject to this subpart?
63.7282 What parts of my plant does this subpart cover?
63.7283 When do I have to comply with this subpart?
Emission Limitations and Work Practice Standards
63.7290 What emission limitations must I meet for capture systems and
control devices applied to pushing emissions?
63.7291 What work practice standards must I meet for fugitive pushing
emissions if I have a by-product coke oven battery with
vertical flues?
63.7292 What work practice standards must I meet for fugitive pushing
emissions if I have a by-product coke oven battery with
horizontal flues?
63.7293 What work practice standards must I meet for fugitive pushing
emissions if I have a non-recovery coke oven battery?
63.7294 What work practice standard must I meet for soaking?
63.7295 What requirements must I meet for quenching?
63.7296 What emission limitations must I meet for battery stacks?
Operation and Maintenance Requirements
63.7300 What are my operation and maintenance requirements?
General Compliance Requirements
63.7310 What are my general requirements for complying with this
subpart?
Initial Compliance Requirements
63.7320 By what date must I conduct performance tests or other initial
compliance demonstrations?
63.7321 When must I conduct subsequent performance tests?
63.7322 What test methods and other procedures must I use to demonstrate
initial compliance with the emission limits for particulate
matter?
63.7323 What procedures must I use to establish operating limits?
[[Page 21]]
63.7324 What procedures must I use to demonstrate initial compliance
with the opacity limits?
63.7325 What test methods and other procedures must I use to demonstrate
initial compliance with the TDS or constituent limits for
quench water?
63.7326 How do I demonstrate initial compliance with the emission
limitations that apply to me?
63.7327 How do I demonstrate initial compliance with the work practice
standards that apply to me?
63.7328 How do I demonstrate initial compliance with the operation and
maintenance requirements that apply to me?
Continuous Compliance Requirements
63.7330 What are my monitoring requirements?
63.7331 What are the installation, operation, and maintenance
requirements for my monitors?
63.7332 How do I monitor and collect data to demonstrate continuous
compliance?
63.7333 How do I demonstrate continuous compliance with the emission
limitations that apply to me?
63.7334 How do I demonstrate continuous compliance with the work
practice standards that apply to me?
63.7335 How do I demonstrate continuous compliance with the operation
and maintenance requirements that apply to me?
63.7336 What other requirements must I meet to demonstrate continuous
compliance?
Notifications, Reports, and Records
63.7340 What notifications must I submit and when?
63.7341 What reports must I submit and when?
63.7342 What records must I keep?
63.7343 In what form and how long must I keep my records?
Other Requirements and Information
63.7350 What parts of the General Provisions apply to me?
63.7351 Who implements and enforces this subpart?
63.7352 What definitions apply to this subpart?
Tables to Subpart CCCCC of Part 63
Table 1 to Subpart CCCCC of Part 63--Applicability of General Provisions
to Subpart CCCCC
Subparts DDDDD--EEEEE [Reserved]
Subpart FFFFF--National Emission Standards for Hazardous Air Pollutants
for Integrated Iron and Steel Manufacturing Facilities
What This Subpart Covers
63.7780 What is the purpose of this subpart?
63.7781 Am I subject to this subpart?
63.7782 What parts of my plant does this subpart cover?
63.7783 When do I have to comply with this subpart?
Emission Limitations
63.7790 What emission limitations must I meet?
Operation and Maintenance Requirements
63.7800 What are my operation and maintenance requirements?
General Compliance Requirements
63.7810 What are my general requirements for complying with this
subpart?
Initial Compliance Requirements
63.7820 By what date must I conduct performance tests or other initial
compliance demonstrations?
63.7821 When must I conduct subsequent performance tests?
63.7822 What test methods and other procedures must I use to demonstrate
initial compliance with the emission limits for particulate
matter?
63.7823 What test methods and other procedures must I use to demonstrate
initial compliance with the opacity limits?
63.7824 What test methods and other procedures must I use to establish
and demonstrate initial compliance with the operating limits?
63.7825 How do I demonstrate initial compliance with the emission
limitations that apply to me?
63.7826 How do I demonstrate initial compliance with the operation and
maintenance requirements that apply to me?
Continuous Compliance Requirements
63.7830 What are my monitoring requirements?
63.7831 What are the installation, operation, and maintenance
requirements for my monitors?
63.7832 How do I monitor and collect data to demonstrate continuous
compliance?
63.7833 How do I demonstrate continuous compliance with the emission
limitations that apply to me?
[[Page 22]]
63.7834 How do I demonstrate continuous compliance with the operation
and maintenance requirements that apply to me?
63.7835 What other requirements must I meet to demonstrate continuous
compliance?
Notifications, Reports, and Records
63.7840 What notifications must I submit and when?
63.7841 What reports must I submit and when?
63.7842 What records must I keep?
63.7843 In what form and how long must I keep my records?
Other Requirements and Information
63.7850 What parts of the General Provisions apply to me?
63.7851 Who implements and enforces this subpart?
63.7852 What definitions apply to this subpart?
Tables to Subpart FFFFF of Part 63
Table 1 to Subpart FFFFF of Part 63--Emission and Opacity Limits
Table 2 to Subpart FFFFF of Part 63--Initial Compliance with Emission
and Opacity Limits
Table 3 to Subpart FFFFF of Part 63--Continuous Compliance with Emission
and Opacity Limits
Table 4 to Subpart FFFFF of Part 63--Applicability of General Provisions
to Subpart FFFFF
Subparts GGGGG--IIIII [Reserved]
Subpart JJJJJ--National Emission Standards for Hazardous Air Pollutants
for Brick and Structural Clay Products Manufacturing
What This Subpart Covers
63.8380 What is the purpose of this subpart?
63.8385 Am I subject to this subpart?
63.8390 What parts of my plant does this subpart cover?
63.8395 When do I have to comply with this subpart?
Emission Limitations
63.8405 What emission limitations must I meet?
63.8410 What are my options for meeting the emission limitations?
General Compliance Requirements
63.8420 What are my general requirements for complying with this
subpart?
63.8425 What do I need to know about operation, maintenance, and
monitoring plans?
Testing and Initial Compliance Requirements
63.8435 By what date must I conduct performance tests?
63.8440 When must I conduct subsequent performance tests?
63.8445 How do I conduct performance tests and establish operating
limits?
63.8450 What are my monitoring installation, operation, and maintenance
requirements?
63.8455 How do I demonstrate initial compliance with the emission
limitations?
Continuous Compliance Requirements
63.8465 How do I monitor and collect data to demonstrate continuous
compliance?
63.8470 How do I demonstrate continuous compliance with the emission
limitations?
Notifications, Reports, and Records
63.8480 What notifications must I submit and when?
63.8485 What reports must I submit and when?
63.8490 What records must I keep?
63.8495 In what form and for how long must I keep my records?
Other Requirements and Information
63.8505 What parts of the General Provisions apply to me?
63.8510 Who implements and enforces this subpart?
63.8515 What definitions apply to this subpart?
Tables to Subpart JJJJJ of Part 63
Table 1 to Subpart JJJJJ of Part 63--Emission Limits
Table 2 to Subpart JJJJJ of Part 63--Operating Limits
Table 3 to Subpart JJJJJ of Part 63--Requirements for Performance Tests
Table 4 to Subpart JJJJJ of Part 63--Initial Compliance with Emission
Limitations
Table 5 to Subpart JJJJJ of Part 63--Continuous Compliance with Emission
Limits and Operating Limits
Table 6 to Subpart JJJJJ of Part 63--Requirements for Reports
Table 7 to Subpart JJJJJ of Part 63--Applicability of General Provisions
to Subpart JJJJJ
Subpart KKKKK--National Emission Standards for Hazardous Air Pollutants
for Clay Ceramics Manufacturing
What This Subpart Covers
63.8530 What is the purpose of this subpart?
63.8535 Am I subject to this subpart?
63.8540 What parts of my plant does this subpart cover?
[[Page 23]]
63.8545 When do I have to comply with this subpart?
Emission Limitations and Work Practice Standards
63.8555 What emission limitations and work practice standards must I
meet?
63.8560 What are my options for meeting the emission limitations and
work practice standards?
General Compliance Requirements
63.8570 What are my general requirements for complying with this
subpart?
63.8575 What do I need to know about operation, maintenance, and
monitoring plans?
Testing and Initial Compliance Requirements
63.8585 By what date must I conduct performance tests?
63.8590 When must I conduct subsequent performance tests?
63.8595 How do I conduct performance tests and establish operating
limits?
63.8600 What are my monitoring installation, operation, and maintenance
requirements?
63.8605 How do I demonstrate initial compliance with the emission
limitations and work practice standards?
Continuous Compliance Requirements
63.8615 How do I monitor and collect data to demonstrate continuous
compliance?
63.8620 How do I demonstrate continuous compliance with the emission
limitations and work practice standards?
Notifications, Reports, and Records
63.8630 What notifications must I submit and when?
63.8635 What reports must I submit and when?
63.8640 What records must I keep?
63.8645 In what form and for how long must I keep my records?
Other Requirements and Information
63.8655 What parts of the General Provisions apply to me?
63.8660 Who implements and enforces this subpart?
63.8665 What definitions apply to this subpart?
Tables to Subpart KKKKK of Part 63
Table 1 to Subpart KKKKK of Part 63--Emission Limits
Table 2 to Subpart KKKKK of Part 63--Operating Limits
Table 3 to Subpart KKKKK of Part 63--Work Practice Standards
Table 4 to Subpart KKKKK of Part 63--Requirements for Performance Tests
Table 5 to Subpart KKKKK of Part 63--Initial Compliance with Emission
Limitations and Work Practice Standards
Table 6 to Subpart KKKKK of Part 63--Continuous Compliance with Emission
Limitations and Work Practice Standards
Table 7 to Subpart KKKKK of Part 63--Requirements for Reports
Table 8 to Subpart KKKKK of Part 63--Applicability of General Provisions
to Subpart KKKKK
Subpart LLLLL--National Emission Standards for Hazardous Air Pollutants:
Asphalt Processing and Asphalt Roofing Manufacturing
What This Subpart Covers
63.8680 What is the purpose of this subpart?
63.8681 Am I subject to this subpart?
63.8682 What parts of my plant does this subpart cover?
63.8683 When must I comply with this subpart?
Emission Limitations
63.8684 What emission limitations must I meet?
General Compliance Requirements
63.8685 What are my general requirements for complying with this
subpart?
Testing and Initial Compliance Requirements
63.8686 By what date must I conduct performance tests or other initial
compliance demonstrations?
63.8687 What performance tests, design evaluations, and other procedures
must I use?
63.8688 What are my monitoring installation, operation, and maintenance
requirements?
63.8689 How do I demonstrate initial compliance with the emission
limitations?
Continuous Compliance Requirements
63.8690 How do I monitor and collect data to demonstrate continuous
compliance?
63.8691 How do I demonstrate continuous compliance with the operating
limits?
Notifications, Reports, and Records
63.8692 What notifications must I submit and when?
63.8693 What reports must I submit and when?
63.8694 What records must I keep?
63.8695 In what form and how long must I keep my records?
[[Page 24]]
Other Requirements and Information
63.8696 What parts of the General Provisions apply to me?
63.8697 Who implements and enforces this subpart?
63.8698 What definitions apply to this subpart?
Tables to Subpart LLLLL of Part 63
Table 1 to Subpart LLLLL of Part 63--Emission Limitations
Table 2 to Subpart LLLLL of Part 63--Operating Limits
Table 3 to Subpart LLLLL of Part 63--Requirements for Performance Tests
Table 4 to Subpart LLLLL of Part 63--Initial Compliance With Emission
Limitations
Table 5 to Subpart LLLLL of Part 63--Continuous Compliance with
Operating Limits
Table 6 to Subpart LLLLL of Part 63--Requirements for Reports
Table 7 to Subpart LLLLL of Part 63--Applicability of General Provisions
to Subpart LLLLL
Subpart MMMMM--National Emission Standards for Hazardous Air Pollutants:
Flexible Polyurethane Foam Fabrication Operations
What This Subpart Covers
63.8780 What is the purpose of this subpart?
63.8782 Am I subject to this subpart?
63.8784 What parts of my plant does this subpart cover?
63.8786 When do I have to comply with this subpart?
Emission Limitations
63.8790 What emission limitations must I meet?
General Compliance Requirements
63.8794 What are my general requirements for complying with this
subpart?
Testing and Initial Compliance Requirements
63.8798 By what date must I conduct performance tests or other initial
compliance demonstrations?
63.8800 What performance tests and other procedures must I use to
demonstrate compliance with the emission limit for flame
lamination?
63.8802 What methods must I use to demonstrate compliance with the
emission limitation for loop slitter adhesive use?
63.8806 How do I demonstrate initial compliance with the emission
limitations?
Continuous Compliance Requirements
63.8810 How do I monitor and collect data to demonstrate continuous
compliance?
63.8812 How do I demonstrate continuous compliance with the emission
limitations?
Notifications, Reports, and Records
63.8816 What notifications must I submit and when?
63.8818 What reports must I submit and when?
63.8820 What records must I keep?
63.8822 In what form and how long must I keep my records?
Other Requirements and Information
63.8826 What parts of the General Provisions apply to me?
63.8828 Who implements and enforces this subpart?
63.8830 What definitions apply to this subpart?
Tables to Subpart MMMMM of Part 63
Table 1 to Subpart MMMMM of Part 63--Emission Limits
Table 2 to Subpart MMMMM of Part 63--Operating Limits for New or
Reconstructed Flame Lamination Affected Sources
Table 3 to Subpart MMMMM of Part 63--Performance Test Requirements for
New or Reconstructed Flame Lamination Affected Sources
Table 4 to Subpart MMMMM of Part 63--Initial Compliance With Emission
Limits
Table 5 to Subpart MMMMM of Part 63--Continuous Compliance with Emission
Limits and Operating Limits
Table 6 to Subpart MMMMM of Part 63--Requirements for Reports
Table 7 to Subpart MMMMM of Part 63--Applicability of General Provisions
to Subpart MMMMM
Subpart NNNNN--National Emission Standards for Hazardous Air Pollutants:
Hydrochloric Acid Production
What This Subpart Covers
Sec.
63.8980 What is the purpose of this subpart?
63.8985 Am I subject to this subpart?
63.8990 What parts of my plant does this subpart cover?
63.8995 When do I have to comply with this subpart?
Emission Limitations and Work Practice Standards
63.9000 What emission limitations and work practice standards must I
meet?
[[Page 25]]
General Compliance Requirements
63.9005 What are my general requirements for complying with this
subpart?
Testing and Initial Compliance Requirements
63.9010 By what date must I conduct performance tests?
63.9015 When must I conduct subsequent performance tests?
63.9020 What performance tests and other procedures must I use?
63.9025 What are my monitoring installation, operation, and maintenance
requirements?
63.9030 How do I demonstrate initial compliance with the emission
limitations and work practice standards?
Continuous Compliance Requirements
63.9035 How do I monitor and collect data to demonstrate continuous
compliance?
63.9040 How do I demonstrate continuous compliance with the emission
limitations and work practice standards?
Notifications, Reports, and Records
63.9045 What notifications must I submit and when?
63.9050 What reports must I submit and when?
63.9055 What records must I keep?
63.9060 In what form and how long must I keep my records?
Other Requirements and Information
63.9065 What parts of the General Provisions apply to me?
63.9070 Who implements and enforces this subpart?
63.9075 What definitions apply to this subpart?
Tables to Subpart NNNNN of Part 63
Table 1 to Subpart NNNNN of Part 63--Emission Limits and Work Practice
Standards
Table 2 to Subpart NNNNN of Part 63--Operating Limits
Table 3 to Subpart NNNNN of Part 63--Performance Test Requirements for
HCl Production Affected Sources
Table 4 to Subpart NNNNN of Part 63--Initial Compliance with Emission
Limitations and Work Practice Standards
Table 5 to Subpart NNNNN of Part 63--Continuous Compliance with Emission
Limitations and Work Practice Standards
Table 6 to Subpart NNNNN of Part 63--Requirements for Reports
Table 7 to Subpart NNNNN of Part 63--Applicability of General Provisions
to Subpart NNNNN
Subpart OOOOO [Reserved]
Subpart PPPPP--National Emission Standards for Hazardous Air Pollutants
for Engine Test Cells/Stands
What This Subpart Covers
63.9280 What is the purpose of subpart PPPPP?
63.9285 Am I subject to this subpart?
63.9290 What parts of my plant does this subpart cover?
63.9295 When do I have to comply with this subpart?
Emission Limitations
63.9300 What emission limitation must I meet?
63.9301 What are my options for meeting the emission limits?
63.9302 What operating limits must I meet?
General Compliance Requirements
63.9305 What are my general requirements for complying with this
subpart?
63.9306 What are my continuous parameter monitoring system (CPMS)
installation, operation, and maintenance requirements?
63.9307 What are my continuous emissions monitoring system installation,
operation, and maintenance requirements?
Testing and Initial Compliance Requirements
63.9310 By what date must I conduct the initial compliance
demonstrations?
63.9320 What procedures must I use?
63.9321 What are the general requirements for performance tests?
63.9322 How do I determine the emission capture system efficiency?
63.9323 How do I determine the add-on control device emission
destruction or removal efficiency?
63.9324 How do I establish the emission capture system and add-on
control device operating limits during the performance test?
63.9330 How do I demonstrate initial compliance with the emission
limitation?
Continuous Compliance Requirements
63.9335 How do I monitor and collect data to demonstrate continuous
compliance?
63.9340 How do I demonstrate continuous compliance with the emission
limitation?
Notifications, Reports, and Records
63.9345 What notifications must I submit and when?
[[Page 26]]
63.9350 What reports must I submit and when?
63.9355 What records must I keep?
63.9360 In what form and how long must I keep my records?
Other Requirements and Information
63.9365 What parts of the General Provisions apply to me?
63.9370 Who implements and enforces this subpart?
63.9375 What definitions apply to this subpart?
Tables to Subpart PPPPP of Part 63
Table 1 to Subpart PPPPP of Part 63. Emission Limitations
Table 2 to Subpart PPPPP of Part 63. Operating Limits
Table 3 to Subpart PPPPP of Part 63. Requirements for Initial Compliance
Demonstrations
Table 4 to Subpart PPPPP of Part 63. Initial Compliance with Emission
Limitations
Table 5 to Subpart PPPPP of Part 63. Continuous Compliance with Emission
Limitations
Table 6 to Subpart PPPPP of Part 63. Requirements for Reports
Table 7 to Subpart PPPPP of Part 63. Applicability of General Provisions
to Subpart PPPPP
Subpart QQQQQ--National Emission Standards for Hazardous Air Pollutants
for Friction Materials Manufacturing Facilities
What This Subpart Covers
63.9480 What is the purpose of this subpart?
63.9485 Am I subject to this subpart?
63.9490 What parts of my plant does this subpart cover?
63.9495 When do I have to comply with this subpart?
Emission Limitations
63.9500 What emission limitations must I meet?
General Compliance Requirements
63.9505 What are my general requirements for complying with this
subpart?
Initial Compliance Demonstration Requirements
63.9510 By what date must I conduct my initial compliance demonstration?
63.9515 How do I demonstrate initial compliance with the emission
limitation that applies to me?
63.9520 What procedures must I use to demonstrate initial compliance?
63.9525 What are the installation, operation, and maintenance
requirements for my weight measurement device?
Continuous Compliance Requirements
63.9530 How do I demonstrate continuous compliance with the emission
limitation that applies to me?
Notifications, Reports, and Records
63.9535 What notifications must I submit and when?
63.9540 What reports must I submit and when?
63.9545 What records must I keep?
63.9550 In what form and how long must I keep my records?
Other Requirements and Information
63.9555 What parts of the General Provisions apply to me?
63.9560 Who implements and enforces this subpart?
63.9565 What definitions apply to this subpart?
63.9570 How do I apply for alternative compliance requirements?
63.9571-63.9579 [Reserved]
Table 1 to Subpart QQQQQ--Applicability of General Provisions to Subpart
QQQQQ
Subpart SSSSS--National Emission Standards for Hazardous Air Pollutants
for Refractory Products Manufacturing
What This Subpart Covers
63.9780 What is the purpose of this subpart?
63.9782 Am I subject to this subpart?
63.9784 What parts of my plant does this subpart cover?
63.9786 When do I have to comply with this subpart?
Emission Limitations and Work Practice Standards
63.9788 What emission limits, operating limits, and work practice
standards must I meet?
63.9790 What are my options for meeting the emission limits?
General Compliance Requirements
63.9792 What are my general requirements for complying with this
subpart?
63.9794 What do I need to know about operation, maintenance, and
monitoring plans?
Testing and Initial Compliance Requirements
63.9796 By what date must I conduct performance tests?
63.9798 When must I conduct subsequent performance tests?
[[Page 27]]
63.9800 How do I conduct performance tests and establish operating
limits?
63.9802 How do I develop an emissions profile?
63.9804 What are my monitoring system installation, operation, and
maintenance requirements?
63.9806 How do I demonstrate initial compliance with the emission
limits, operating limits, and work practice standards?
Continuous Compliance Requirements
63.9808 How do I monitor and collect data to demonstrate continuous
compliance?
63.9810 How do I demonstrate continuous compliance with the emission
limits, operating limits, and work practice standards?
Notifications, Reports, and Records
63.9812 What notifications must I submit and when?
63.9814 What reports must I submit and when?
63.9816 What records must I keep?
63.9818 In what form and how long must I keep my records?
Other Requirements and Information
63.9820 What parts of the General Provisions apply to me?
63.9822 Who implements and enforces this subpart?
63.9824 What definitions apply to this subpart?
Tables to Subpart SSSSS of Part 63
Table 1 to Subpart SSSSS of Part 63.--Emission Limits
Table 2 to Subpart SSSSS of Part 63.--Operating Limits
Table 3 to Subpart SSSSS of Part 63.--Work Practice Standards
Table 4 to Subpart SSSSS to Part 63.--Requirements for Performance Tests
Table 5 to Subpart SSSSS of Part 63.--Initial Compliance with Emission
Limits
Table 6 to Subpart SSSSS of Part 63.--Initial Compliance with Work
Practice Standards
Table 7 to Subpart SSSSS to Part 63.--Continuous Compliance with
Emission Limits
Table 8 to Subpart SSSSS of Part 63.--Continuous Compliance with
Operating Limits
Table 9 to Subpart SSSSS of Part 63.--Continuous Compliance with Work
Practice Standards
Table 10 to Subpart SSSSS of Part 63.--Requirements for Reports
Table 11 to Subpart SSSSS of Part 63.--Applicability of General
Provisions to Subpart SSSSS
Appendix A to Part 63--Test Methods
Appendix B to Part 63--Sources Defined for Early Reduction Provisions
Appendix C to Part 63--Determination of the Fraction Biodegraded
(Fbio) in a Biological Treatment Unit
Appendix D to Part 63--Alternative Validation Procedure for EPA Waste
and Wastewater Methods
Appendix E to Part 63--Monitoring Procedure for Nonthoroughly Mixed Open
Biological Treatment Systems at Kraft Pulp Mills Under Unsafe
Sampling Conditions
Authority: 42 U.S.C. 7401 et seq.
Source: 57 FR 61992, Dec. 29, 1992, unless otherwise noted.
Subpart QQQ--National Emission Standards for Hazardous Air Pollutants
for Primary Copper Smelting
Source: 67 FR 40491, June 12, 2002
What This Subpart Covers
Sec. 63.1440 What is the purpose of this subpart?
This subpart establishes national emission standards for hazardous
air pollutants (NESHAP) for primary copper smelters. This subpart also
establishes requirements to demonstrate initial and continuous
compliance with all applicable emission limitations, work practice
standards, and operation and maintenance requirements in this subpart.
Sec. 63.1441 Am I subject to this subpart?
You are subject to this subpart if you own or operate a primary
copper smelter that is (or is part of) a major source of hazardous air
pollutant (HAP) emissions on the first compliance date that applies to
you, and your primary copper smelter uses batch copper converters as
defined in Sec. 63.1459. Your primary copper smelter is a major source
of HAP if it emits or has the potential to emit any single HAP at the
rate of 10 tons or more per year or any combination of HAP at a rate of
25 tons or more per year.
Sec. 63.1442 What parts of my plant does this subpart cover?
(a) This subpart applies to each new and existing affected source at
your primary copper smelter. The affected sources are each copper
concentrate
[[Page 28]]
dryer, each smelting furnace, each slag cleaning vessel, each copper
converter department, and the entire group of fugitive emission sources,
as defined in Sec. 63.1459.
(b) An affected source at your primary copper smelter is existing if
you commenced construction or reconstruction of the affected source
before April 20, 1998.
(c) An affected source at your primary copper smelter is new if you
commenced construction or reconstruction of the affected source on or
after April 20, 1998. An affected source is reconstructed if it meets
the definition of ``reconstruction'' in Sec. 63.2.
Sec. 63.1443 When do I have to comply with this subpart?
(a) If you have an existing affected source, you must comply with
each emission limitation, work practice standard, and operation and
maintenance requirement in this subpart that applies to you no later
than June 13, 2005.
(b) If you have a new affected source and its initial startup date
is on or before June 12, 2002, you must comply with each emission
limitation, work practice standard, and operation and maintenance
requirement in this subpart that applies to you by June 12, 2002.
(c) If you have a new affected source and its initial startup date
is after June 12, 2002, you must comply with each emission limitation,
work practice standard, and operation and maintenance requirement in
this subpart that applies to you upon initial startup.
(d) If your primary copper smelter is an area source that becomes a
major source of HAP, the compliance dates listed in paragraphs (d)(1)
and (2) of this section apply to you.
(1) Any portion of the existing primary copper smelter that is a new
affected source or a new reconstructed source must be in compliance with
this subpart upon startup.
(2) All other parts of the primary copper smelter must be in
compliance with this subpart no later than 3 years after it becomes a
major source.
(e) You must meet the notification and schedule requirements in
Sec. 63.1454. Several of these notifications must be submitted before
the compliance date for your affected source.
Emission Limitations and Work Practice Standards
Sec. 63.1444 What emissions limitations and work practice standards must I meet for my copper concentrate dryers, smelting furnaces, slag cleaning vessels, and
copper converter departments?
(a) Copper concentrate dryers. For each copper concentrate dryer,
you must comply with the emission limitation in paragraph (a)(1) or (2)
of this section that applies to you.
(1) For each existing copper concentrate dryer, you must not cause
to be discharged to the atmosphere from the dryer vent any gases that
contain total particulate matter in excess of 50 milligrams per dry
standard cubic meter (mg/dscm) as measured using the test methods
specified in Sec. 63.1450(a).
(2) For each new copper concentrate dryer, you must not cause to be
discharged to the atmosphere from the dryer vent any gases that contain
total particulate matter in excess of 23 mg/dscm as measured using the
test methods specified in Sec. 63.1450(a).
(b) Smelting furnaces. For each smelting furnace, you must comply
with the emission limitations and work practice standards in paragraphs
(b)(1) and (2) of this section.
(1) For each smelting furnace, you must not cause to be discharged
to the atmosphere any process off-gas that contains nonsulfuric acid
particulate matter in excess of 6.2 mg/dscm as measured using the test
methods specified in Sec. 63.1450(b). Process off-gas from a smelting
furnace is generated when copper ore concentrates and fluxes are being
smelted to form molten copper matte and slag layers.
(2) For each smelting furnace, you must control the process fugitive
emissions released when tapping copper matte or slag from the smelting
furnace according to paragraphs (b)(2)(i) and (ii) of this section.
(i) At all times when copper matte or slag is tapped from the
smelting furnace, you must operate a capture system that collects the
gases and fumes released from the tapping port in use.
[[Page 29]]
The design and placement of this capture system must be such that the
tapping port opening, launder, and receiving vessel (e.g., ladle, slag
pot) are positioned within the confines or influence of the capture
system's ventilation draft during those times when the copper matte or
slag is flowing from the tapping port opening.
(ii) You must not cause to be discharged to the atmosphere from the
capture system used to comply with paragraph (b)(2)(i) of this section
any gases that contain total particulate matter in excess of 23 mg/dscm
as measured using the test methods specified in Sec. 63.1450(a).
(c) Slag cleaning vessels. For each slag cleaning vessel, you must
comply with the emission limitations and work practice standards in
paragraphs (c)(1) through (3) of this section that apply to you.
(1) For each slag cleaning vessel, except as provided for in
paragraph (c)(2) of this section, you must not cause to be discharged to
the atmosphere any process off-gas that contains nonsulfuric acid
particulate matter in excess of 6.2 mg/dscm as measured using the test
methods specified in Sec. 63.1450(b).
(2) As an alternative to complying with the emission limit for
nonsulfuric acid particulate matter in paragraph (c)(1) of this section,
for each existing slag cleaning vessel you may choose to comply with the
emission limit for total particulate matter specified in this paragraph
(c)(2). You must not cause to be discharged to the atmosphere any
process off-gas that contains total particulate matter in excess of 46
mg/dscm as measured using the test methods specified in Sec. 63.1450(a).
(3) For each slag cleaning vessel, you must control process fugitive
emissions released when tapping copper matte or slag from the slag
cleaning vessel according to paragraphs (c)(3)(i) and (ii) of this
section.
(i) At all times when copper matte or slag is tapped from the slag
cleaning vessel, you must operate a capture system that collects the
gases and fumes released from the tapping port in use. The design and
placement of this capture system must be such that the tapping port
opening, launder, and receiving vessel (e.g., ladle, slag pot) are
positioned within the confines or influence of the capture system's
ventilation draft during those times when the copper matte or slag is
flowing from the tapping port opening.
(ii) You must not cause to be discharged to the atmosphere from the
capture system used to comply with paragraph (c)(3)(i) of this section
any gases that contain total particulate matter in excess of 23 mg/dscm
as measured using the test methods specified in Sec. 63.1450(a).
(d) Existing copper converter departments. For each existing copper
converter department, you must comply with the emission limitations and
work practice standards in paragraphs (d)(1) through (6) of this section
that apply to you.
(1) You must operate a capture system that collects the process off
gas vented from each batch copper converter. At all times when one or
more batch copper converters are blowing, you must operate the capture
system according to the written operation and maintenance plan that has
been prepared according to the requirements in Sec. 63.1447(b).
(2) If your copper converter department uses Pierce-Smith
converters, the capture system design must include use of a primary hood
that covers the entire mouth of the converter vessel when the copper
converter is positioned for blowing. Additional hoods (e.g., secondary
hoods) or other capture devices must be included in the capture system
design as needed to achieve the opacity limit in paragraph (d)(4) of
this section. The capture system design may use multiple intake and duct
segments through which the ventilation rates are controlled
independently of each other, and individual duct segments may be
connected to separate control devices.
(3) If your copper converter department uses Hoboken converters, the
capture system must collect all process off-gas vented during blowing
through the side-flue intake on each converter vessel.
(4) You must operate the capture system such that any visible
emissions exiting the roof monitors or roof exhaust fans on the building
housing the copper converter department meet the
[[Page 30]]
opacity limit as specified in paragraphs (d)(4)(i) and (ii) of this
section.
(i) The opacity of any visible emissions exiting the roof monitors
or roof exhaust fans on the building housing the copper converter
department must not exceed 4 percent as determined by a performance test
conducted according to Sec. 63.1450(c).
(ii) The opacity limit in paragraph (d)(4)(i) of this section
applies only at those times when a performance test is conducted
according to Sec. 63.1450(c). The requirements for compliance with
opacity and visible emission standards specified in Sec. 63.6(h) do not
apply to this opacity limit.
(5) You must not cause to be discharged to the atmosphere from any
Pierce-Smith converter primary hood capture system or Hoboken converter
side-flue intake capture system any process off-gas that contains
nonsulfuric acid particulate matter in excess of 6.2 mg/dscm as measured
using the test methods specified in Sec. 63.1450(b).
(6) You must not cause to be discharged to the atmosphere from any
secondary capture system any gases that contain total particulate matter
in excess of 23 mg/dscm as measured using the test methods specified in
Sec. 63.1450(a).
(e) New copper converter departments. For each new copper converter
department for which construction commenced on or after April 20, 1998,
the use of batch copper converters is prohibited.
(f) Baghouses. For each baghouse applied to meet any total
particulate matter emission limit in paragraphs (a) through (d) of this
section, you must operate the baghouse such that the bag leak detection
system does not alarm for more than 5 percent of the total operating
time in any semiannual reporting period.
(g) Venturi wet scrubbers. For each venturi wet scrubber applied to
meet any total particulate matter emission limit in paragraphs (a)
through (d) of this section, you must maintain the hourly average
pressure drop and scrubber water flow rate at or above the minimum
levels established during the initial or subsequent performance test.
(h) Other control devices. For each control device other than a
baghouse or venturi wet scrubber applied to meet any total particulate
matter emission limit in paragraphs (a) through (d) of this section, you
must operate the control device as specified in paragraphs (h)(1) and
(2) of this section.
(1) You must select one or more operating parameters, as appropriate
for the control device design, that can be used as representative and
reliable indicators of the control device operation.
(2) You must maintain the hourly average value for each of the
selected parameters at or above the minimum level or at or below the
maximum level, as appropriate for the selected parameter, established
during the initial or subsequent performance test.
Sec. 63.1445 What work practice standards must I meet for my fugitive dust sources?
(a) You must control particulate matter emissions from fugitive dust
sources at your primary copper smelter by operating according to a
written fugitive dust control plan that has been approved by the
designated authority. For the purpose of complying with this paragraph
(a) you may use an existing fugitive dust control plan provided that the
plan complies with the requirements of this section. A fugitive dust
control plan is considered to be approved if the plan has been
incorporated in your applicable State implementation plan, and the
document addresses the fugitive dust sources specified in paragraph (b)
of this section and includes the information specified in paragraph (c)
of this section.
(b) Your fugitive dust control plan must address each of the
fugitive dust emission sources listed in paragraphs (b)(1) through (6)
of this section that are located at your primary copper smelter.
(1) On-site roadways used by trucks or other motor vehicles (e.g.,
front-end loaders) when transporting bulk quantities of fugitive dust
materials. Paved roads and parking areas that are not used by these
vehicles do not need to be included in the plan (e.g., employee and
visitor parking lots).
[[Page 31]]
(2) Unloading of fugitive dust materials from trucks or railcars.
(3) Outdoor piles used for storage of fugitive dust materials.
(4) Bedding areas used for blending copper concentrate and other
feed constituents.
(5) Each transfer point in conveying systems used to transport
fugitive dust materials. These points include, but are not limited to,
transfer of material from one conveyor belt to another and transfer of
material to a hopper or bin.
(6) Other site-specific sources of fugitive dust emissions that the
Administrator or delegated permitting authority designate to be included
in your fugitive dust control plan.
(c) Your fugitive dust control plan must describe the control
measures you use to control fugitive dust emissions from each source
addressed in the plan, as applicable and appropriate for your site
conditions. Examples of control measures include, but are not limited
to, locating the source inside a building or other enclosure, installing
and operating a local hood capture system over the source and venting
the captured gas stream to a control device, placing material stockpiles
below grade, installing wind screens or wind fences around the source,
spraying water on the source as weather conditions require, applying
appropriate dust suppression agents on the source, or combinations of
these control measures.
(d) The requirement for you to operate according to a written
fugitive dust control plan must be incorporated in your operating permit
that is issued by the designated permitting authority under part 70 of
this chapter. A copy of your fugitive dust control plan must be sent to
the designated permitting authority on or before the compliance date for
your primary copper smelter, as specified in Sec. 63.1443.
Sec. 63.1446 What alternative emission limitation may I meet for my combined gas streams?
(a) For situations where you combine gas streams from two or more
affected sources for discharge to the atmosphere through a single vent,
you may choose to meet the requirements in paragraph (b) of this section
as an alternative to complying with the individual total particulate
matter emission limits specified in Sec. 63.1444 that apply to you. This
alternative emission limit for a combined gas stream may be used for any
combination of the affected source gas steams specified in paragraphs
(a)(1) through (5) of this section.
(1) Gas stream discharged from a copper concentrate dryer vent that
would otherwise be subject to Sec. 63.1444(a)(1) or (2);
(2) Gas stream discharged from a smelting furnace capture system
that would otherwise be subject to Sec. 63.1444(b)(2)(ii);
(3) Process off-gas stream discharged from a slag cleaning vessel
that would otherwise be subject to Sec. 63.1444(c)(2);
(4) Gas stream discharged from a slag cleaning vessel capture system
that would otherwise be subject to Sec. 63.1444(c)(3)(ii); and
(5) Gas stream discharged from a batch copper converter secondary
capture system that would otherwise be subject to Sec. 63.1444(d)(5).
(b) You must meet the requirements specified in paragraphs (b)(1)
and (2) of this section for the combined gas stream discharged through a
single vent.
(1) For each combined gas stream discharged through a single vent,
you must not cause to be discharged to the atmosphere any gases that
contain total particulate matter in excess of the emission limit
calculated using the procedure in paragraph (b)(2) of this section and
measured using the test methods specified in Sec. 63.1450(a).
(2) You must calculate the alternative total particulate matter
emission limit for your combined gas stream using Equation 1 of this
section. The volumetric flow rate value for each of the individual
affected source gas streams that you use for Equation 1 (i.e., the flow
rate of the gas stream discharged from the affected source but before
this gas stream is combined with the other gas streams) is to be the
average of the volumetric flow rates measured using the test method
specified in Sec. 63.1450(a)(1)(ii):
[[Page 32]]
[GRAPHIC] [TIFF OMITTED] TR12JN02.025
Where
EAlt = Alternative total particulate matter emission limit
for the combined gas stream discharged to atmosphere through a single
vent (mg/dscm);
Ed = Total particulate matter emission limit applicable to
copper concentrate dryer as specified in Sec. 63.1444(a)(1) or (2) (mg/
dscm);
Qd = Copper concentrate dryer exhaust gas stream volumetric
flow rate before being combined with other gas streams (dscm);
Esv = Total particulate matter emission limit for smelting
furnace capture system as specified in Sec. 63.1444(b)(2)(ii) (mg/dscm);
Qsv = Smelting furnace capture system exhaust gas stream
volumetric flow rate before being combined with other gas streams
(dscm);
Escvp = Total particulate matter emission limit for slag
cleaning vessel process off-gas as specified in Sec. 63.1444(c)(2) (mg/
dscm);
Qscvp = Slag cleaning vessel process off-gas volumetric flow
rate before being combined with other gas streams (dscm);
Escvf = Total particulate matter emission limit for slag
cleaning vessel capture system as specified in Sec. 63.1444(c)(3)(ii)
(mg/dscm);
Qscvf = Slag cleaning vessel capture system exhaust gas
stream volumetric flow rate before being combined with other gas streams
(dscm);
Ecc = Total particulate emission limit for the batch copper
converter secondary capture system as specified in Sec. 63.1544(d)(5)
(mg/dscm); and
Qcc = Batch copper converter capture system exhaust gas
stream volumetric flow rate before being combined with other gas streams
(dscm).
(c) For each baghouse applied to meet any total particulate matter
emission limit in paragraph (b) of this section, you must operate the
baghouse such that the bag leak detection system does not alarm for more
than 5 percent of the total operating time in any semiannual reporting
period.
(d) For each venturi wet scrubber applied to meet any total
particulate matter emission limit in paragraph (b) of this section, you
must maintain the hourly average pressure drop and scrubber water flow
rate at or above the minimum levels established during the initial or
subsequent performance test.
(e) For each control device other than a baghouse or venturi wet
scrubber applied to meet any total particulate matter emission limit in
paragraph (b) of this section, you must operate the control device as
specified in paragraphs (e)(1) and (2) of this section.
(1) You must select one or more operating parameters, as appropriate
for the control device design, that can be used as representative and
reliable indicators of the control device operation.
(2) You must maintain the hourly average value for each of the
selected parameters at or above the minimum level or at or below the
maximum level, as appropriate for the selected parameter, established
during the initial or subsequent performance test.
Operation and Maintenance Requirements
Sec. 63.1447 What are my operation and maintenance requirements?
(a) As required by Sec. 63.6(e)(1)(i), you must always operate and
maintain your affected source, including air pollution control and
monitoring equipment, in a manner consistent with good air pollution
control practices for minimizing emissions at least to the levels
required by this subpart.
(b) You must prepare and operate at all times according to a written
operation and maintenance plan for each capture system and control
device subject to standards in Sec. 63.1444 or Sec. 63.1446. The plan
must address the requirements in paragraphs (b)(1) through (3)
[[Page 33]]
of this section as applicable to the capture system or control device.
(1) Preventative maintenance. You must perform preventative
maintenance for each capture system and control device according to
written procedures specified in your operation and maintenance plan. The
procedures must include a preventative maintenance schedule that is
consistent with the manufacturer's instructions for routine and long-
term maintenance.
(2) Capture system inspections. You must conduct monthly inspections
of the equipment components of the capture system that can affect the
performance of the system to collect the gases and fumes emitted from
the affected source (e.g., hoods, exposed ductwork, dampers, fans)
according to written procedures specified in your operation and
maintenance plan. The inspection procedure must include the requirements
in paragraphs (b)(2)(i) through (iii) of this section as applicable to
the capture system or control device.
(i) Observations of the physical appearance of the equipment to
confirm the physical integrity of the equipment (e.g., verify by visual
inspection no holes in ductwork or hoods, no flow constrictions caused
by dents, or accumulated dust in ductwork).
(ii) Inspection, and if necessary testing, of equipment components
to confirm that the component is operating as intended (e.g., verify by
appropriate measures that flow or pressure sensors, damper plates,
automated damper switches and motors are operating according to
manufacture or engineering design specifications).
(iii) In the event that a defective or damaged component is detected
during an inspection, you must initiate corrective action according to
written procedures specified in your operation and maintenance plan to
correct the defect or deficiency as soon as practicable.
(3) Copper converter department capture system operating limits. You
must establish, according to the requirements in paragraph (b)(3)(i)
through (iii) of this section, operating limits for the capture system
that are representative and reliable indicators of the performance of
capture system when it is used to collect the process off-gas vented
from batch copper converters during blowing.
(i) Select operating limit parameters appropriate for the capture
system design that are representative and reliable indicators of the
performance of the capture system when it is used to collect the process
off-gas vented from batch copper converters during blowing. At a
minimum, you must use appropriate operating limit parameters that
indicate the level of the ventilation draft and the damper position
settings for the capture system when operating to collect the process
off-gas from the batch copper converters during blowing. Appropriate
operating limit parameters for ventilation draft include, but are not
limited to, volumetric flow rate through each separately ducted hood,
total volumetric flow rate at the inlet to control device to which the
capture system is vented, fan motor amperage, or static pressure. Any
parameter for damper position setting may be used that indicates the
duct damper position relative to the fully open setting.
(ii) For each operating limit parameter selected in paragraph
(b)(3)(i) of this section, designate the value or setting for the
parameter at which the capture system operates during batch copper
converter blowing. If your blister copper production operations allow
for more than one batch copper converter to be operating simultaneously
in the blowing mode, designate the value or setting for the parameter at
which the capture system operates during each possible batch copper
converter blowing configuration that you may operate at your smelter
(i.e., the operating limits with one converter blowing, with two
converters blowing, with three converters blowing, as applicable to your
smelter).
(iii) Include documentation in the plan to support your selection of
the operating limits established for the capture system. This
documentation must include a description of the capture system design, a
description of the capture system operation during blister copper
production, a description of each selected operating limit parameter, a
rationale for why you chose the parameter, a description of the method
[[Page 34]]
used to monitor the parameter according to the requirements in
Sec. 63.1452(a), and the data used to set the value or setting for the
parameter for each of your batch copper converter configurations.
(4) Baghouse leak detection corrective actions. In the event a bag
leak detection system alarm is triggered, you must initiate corrective
action according to written procedures specified in your operation and
maintenance plan to determine the cause of the alarm within 1 hour of
the alarm, initiate corrective action to correct the cause of the
problem within 24 hours of the alarm, and complete the corrective action
as soon as practicable. Corrective actions may include, but are not
limited to, the activities listed in paragraphs (b)(3)(i) through (vi)
of this section.
(i) Inspecting the baghouse for air leaks, torn or broken bags or
filter media, or any other condition that may cause an increase in
emissions.
(ii) Sealing off defective bags or filter media.
(iii) Replacing defective bags or filter media or otherwise
repairing the control device.
(iv) Sealing off a defective baghouse compartment.
(v) Cleaning the bag leak detection system probe, or otherwise
repair the bag leak detection system.
(vi) Shutting down the process producing the particulate emissions.
General Compliance Requirements
63.1448 What are my general requirements for complying with this subpart?
(a) You must be in compliance with the emission limitations, work
practice standards, and operation and maintenance requirements in this
subpart at all times, except during periods of startup, shutdown, and
malfunction as defined in Sec. 63.2.
(b) During the period between the compliance date specified for your
affected source in Sec. 63.1443, and the date upon which continuous
monitoring systems have been installed and certified and any applicable
operating limits have been set, you must maintain a log detailing the
operation and maintenance of the process and emissions control
equipment.
(c) You must develop and implement a written startup, shutdown, and
malfunction plan according to the provisions in Sec. 63.6(e)(3).
Initial Compliance Requirements
Sec. 63.1449 By what dates must I conduct performance tests or other initial compliance demonstrations?
(a) As required in Sec. 63.7(a)(2), you must conduct a performance
test within 180 calendar days of the compliance date that is specified
in Sec. 63.1443 for your affected source to demonstrate initial
compliance with each emission and opacity limit in Sec. 63.1443 and
Sec. 63.1446 that applies to you.
(b) For each work practice standard and operation and maintenance
requirement that applies to you where initial compliance is not
demonstrated using a performance test or opacity observation, you must
demonstrate initial compliance within 30 calendar days after the
compliance date that is specified for your affected source in
Sec. 63.1443.
Sec. 63.1450 What test methods and other procedures must I use to demonstrate initial compliance with the emission limitations?
(a) Total particulate matter emission limits. You must conduct each
performance test to determine compliance with the total particulate
matter emission limits in Sec. 63.1444 or Sec. 63.1446 that apply to you
according to the requirements for representative test conditions
specified in Sec. 63.7(e)(1) and using the test methods and procedures
in paragraphs (a)(1) through (5) of this section.
(1) Determine the concentration of total particulate matter
according to the test methods in appendix A to part 60 of this chapter
as specified in paragraphs (a)(1)(i) through (iii) of this section.
(i) Method 1 to select sampling port locations and the number of
traverse points. Sampling ports must be located at the outlet of the
control device and prior to any releases to the atmosphere.
(ii) Method 2, 2F, or 2G to determine the volumetric flow rate of
the stack gas.
[[Page 35]]
(iii) Method 3, 3A, or 3B to determine the dry molecular weight of
the stack gas.
(iv) Method 4 to determine the moisture content of the stack gas.
(v) Method 5, 5D, or 17, as applicable, to determine the
concentration of total particulate matter. You can also use ASTM D4536-
96 incorporated by reference in Sec. 63.14 as an alternative to the
sampling equipment and operating procedures in Method 5 or 17 when
testing a positive pressure baghouse, but you must use the sample
traverse location and number of sampling points described in Method 5D.
(2) As an alternative to using the applicable method specified in
paragraph (a)(1)(v) of this section, you may determine total particulate
matter emissions from the control device using Method 29 in appendix A
of part 60 of this chapter provided that you follow the procedures and
precautions prescribed in Method 29. If the control device is a positive
pressure baghouse, you must also follow the measurement procedure
specified in sections 4.1 through 4.3 of Method 5D.
(3) You must conduct three separate test runs for each performance
test. Each test run must have a minimum sampling time of 60 minutes and
a minimum sampling volume of 0.85 dscm. For the purpose of determining
compliance with the applicable total particulate matter emission limit,
the arithmetic mean of the results for the three separate test runs is
used.
(4) For a venturi wet scrubber applied to emissions from an affected
source and subject to operating limits in Sec. 63.1444(g) or
Sec. 63.1446(d) for pressure drop and scrubber water flow rate, you must
establish site-specific operating limits according to the procedures in
paragraph (a)(4)(i) and (ii) of this section.
(i) Using the continuous parameter monitoring system (CPMS) required
in Sec. 63.1452, measure and record the pressure drop and scrubber water
flow rate during each run of the particulate matter performance test.
(ii) Compute and record the hourly average pressure drop and
scrubber water flow rate for each individual test run. Your operating
limits are the lowest average pressure drop and scrubber water flow rate
value in any of the three runs that meet the applicable emission limit.
(5) For a control device other than a baghouse or venturi wet
scrubber applied to emissions from an affected source and subject to
site-specific operating limit(s) in Sec. 63.1444(h) or Sec. 63.1446(e)
for appropriate, site-specific operating parameters that are
representative and reliable indicators of the control device
performance, you must establish a site-specific operating limit(s)
according to the procedures in paragraph (a)(5)(i) through (iv) of this
section.
(i) Select one or more operating parameters, as appropriate for the
control device design, that can be used as representative and reliable
indicators of the control device operation.
(ii) Using the CPMS required in Sec. 63.1452, measure and record the
selected operating parameters for the control device during each run of
the total particulate matter performance test.
(iii) Compute and record the hourly average value for each of the
selected operating parameters for each individual test run. Your
operating limits are the lowest value or the highest value, as
appropriate for the selected operating parameter, measured in any of the
three runs that meet the applicable emission limit.
(iv) You must prepare written documentation to support your
selection of the operating parameters used for the control device. This
documentation must include a description of each selected parameter, a
rationale for why you chose the parameter, a description of the method
used to monitor the parameter, and the data recorded during the
performance test and used to set the operating limit(s).
(b) Nonsulfuric acid particulate matter emission limits. You must
conduct each performance test to determine compliance with the
nonsulfuric acid particulate matter emission limits in Sec. 63.1444 that
apply to you according to the requirements for representative test
conditions specified in Sec. 63.7(e)(1) and using the test methods and
procedures in paragraphs (b)(1) and (2) of this section.
[[Page 36]]
(1) Determine the concentration of nonsulfuric acid particulate
matter according to the test methods in appendix A to part 60 of this
chapter as specified in paragraphs (b)(1)(i) through (v) of this
section.
(i) Method 1 to select sampling port locations and the number of
traverse points. Sampling ports must be located at the outlet of the
control device and prior to any releases to the atmosphere.
(ii) Method 2, 2F, or 2G to determine the volumetric flow rate of
the stack gas.
(iii) Method 3, 3A, or 3B to determine the dry molecular weight of
the stack gas.
(iv) Method 4 to determine the moisture content of the stack gas.
(v) Method 5B to determine the nonsulfuric acid particulate matter
emissions.
(2) You must conduct three separate test runs for each performance
test. Each test run must have a minimum sampling time of 240 minutes and
a minimum sampling volume of 3.4 dscm. For the purpose of determining
compliance with the nonsulfuric acid particulate matter emission limit,
the arithmetic mean of the results for the three separate test runs is
used.
(c) Copper converter department capture system opacity limit. You
must conduct each performance test to determine compliance with the
opacity limit in Sec. 63.1444 using the test methods and procedures in
paragraphs (c)(1) through (9) of this section.
(1) You must conduct the performance test during the period when the
primary copper smelter is operating under conditions representative of
the smelter's normal blister copper production rate. You may not conduct
a performance test during periods of startup, shutdown, or malfunction.
Before conducting the performance test, you must prepare a written test
plan specifying the copper production conditions to be maintained
throughout the opacity observation period and including a copy of the
written documentation you have prepared according to paragraph (a)(3) of
this section to support the established operating limits for the copper
converter department capture system. You must submit a copy of the test
plan for review and approval by the Administrator or delegated
authority. During the observation period, you must collect appropriate
process information and copper converter department capture system
operating information to prepare documentation sufficient to verify that
all opacity observations were made during the copper production and
capture system operating conditions specified in the approved test plan.
(2) You must notify the Administrator or delegated authority before
conducting the opacity observations to allow the Administrator or
delegated authority the opportunity to have authorized representatives
attend the test. Written notification of the location and scheduled date
for conducting the opacity observations must be received by the
Administrator on or before 30 calendar days before this scheduled date.
(3) You must gather the data needed for determining compliance with
the opacity limit using qualified visible emission observers and process
monitors as described in paragraphs (c)(3)(i) and (ii) of this section.
(i) Opacity observations must be performed by a sufficient number of
qualified visible emission observers to obtain two complete concurrent
sets of opacity readings for the required observation period. Each
visible emission observer must be certified as a qualified observer by
the procedure specified in section 3 of Method 9 in appendix A of part
60 of this chapter. The entire set of readings during the required
observation period does not need to be made by the same two observers.
More than two observers may be used to allow for substitutions and
provide for observer rest breaks. The owner or operator must obtain
proof of current visible emission reading certification for each
observer.
(ii) A person (or persons) familiar with the copper production
operations conducted at the smelter must serve as the indoor process
monitor. The indoor process monitor is stationed at a location inside
the building housing the batch copper converters such that he or she can
visually observe and record operations that occur in the batch copper
converter aisle during the times
[[Page 37]]
that the visible emission observers are making opacity readings. More
than one indoor process monitor may be used to allow for substitutions
and provide for rest breaks.
(4) You must make all opacity observations using Method 9 in
appendix A to part 60 of this chapter and following the procedures
described in paragraphs (c)(4)(i) and (ii) of this section.
(i) Each visible emission observer must make his or her readings at
a position from the outside of the building that houses the copper
converter department such that the observer's line-of-sight is
approximately perpendicular to the longer axis of the converter
building, and the observer has an unobstructed view of the building roof
monitor sections or roof exhaust fan outlets that are positioned over
each of the batch copper converters inside the building. Opacity
readings can only be made during those times when the observer's
position meets the sun orientation and other conditions specified in
section 2.1 of Method 9.
(ii) At 15-second intervals, each visible emission observer views
the building roof monitor sections or roof exhaust fan outlets that are
positioned over each of the batch copper converters inside the building
and reads the opacity of the visible plumes. If no plume is visible, the
observer records zero as the opacity value for the 15-second interval.
In situations when it is possible for an observer to distinguish two or
more visible emission plumes from the building roof monitor sections or
roof exhaust fan outlets, the observer must identify, to the extent
feasible, the plume having the highest opacity and record his or her
opacity reading for that plume as the opacity value for the 15-second
interval.
(5) You must make opacity observations for a period of sufficient
duration to obtain a minimum of 120 1-minute intervals during which at
least one copper converter is blowing and no interferences have occurred
from other copper production events, as specified in paragraph (c)(7) of
this section, which generate visible emissions inside the building that
potentially can interfere with the visible emissions from the converter
capture systems as seen by the outside observers. To obtain the required
number of 1-minute intervals, the observation period may be divided into
two or more segments performed on the same day or on different days if
conditions prevent the required number of opacity readings from being
obtained during one continuous time period. Examples of these conditions
include, but are not limited to, changes in the sun's orientation
relative to visible emission observers' positions such that the Method 9
conditions are no longer met or an unexpected thunder storm. If the
total observation period is divided into two or more segments, all
opacity observations must be made during the same set of copper
production conditions described in your approved test plan as required
by paragraph (c)(1) of this section.
(6) You must gather indoor process information during all times that
the visible emission observers are making opacity readings outside the
building housing the copper converter department. The indoor process
monitor must continually observe the operations occurring in the copper
converter department and prepare a written record of his or her
observations using the procedure specified in paragraphs (c)(6)(i)
through (iv) of this section.
(i) At the beginning of each observation period or segment, the
clock time setting on the watch or clock to be used by the indoor
process monitor must be synchronized with the clock time settings for
the timepieces to be used by the outdoor opacity observers.
(ii) During each period or segment when opacity readings are being
made by the visible emission observers, the indoor process monitor must
continuously observe the operations occurring in the copper converter
department and record his or her observations in a log book, on data
sheets, or other type of permanent written format.
(iii) When a batch copper converter is blowing, a record must be
prepared for the converter that includes, but is not limited to, the
clock times for when blowing begins and when blowing ends and the
converter blowing rate. This information may be recorded by the indoor
process monitor or by a separate, automated computer data system.
[[Page 38]]
(iv) The process monitor must record each event other than converter
blowing that occurs in or nearby the converter aisle that he or she
observes to generate visible emissions inside the building. The recorded
entry for each event must include, but is not limited to, a description
of the event and the clock times when the event begins and when the
event ends.
(7) You must prepare a summary of the data for the entire
observation period using the information recorded during the observation
period by the outdoor visible emission observers and the indoor process
monitor and the procedure specified in paragraphs (c)(7)(i) through (iv)
of this section.
(i) Using the field data sheets, identify the 1-minute clock times
for which a total of eight opacity readings were made and recorded by
both observers at 15-second intervals according to the test procedures
(i.e., a total of four opacity values have been recorded for the 1-
minute interval by each of the two observers). Calculate the average of
the eight 15-second interval readings recorded on the field data sheets
by the two observers during the clock time minute interval (add the four
consecutive 15-second interval opacity readings made by Observer A
during the specified clock time minute, plus the four consecutive 15-
second interval opacity readings made by Observer B during the same
clock time minute, and divide the resulting total by eight). Record the
clock time and the opacity average for the 1-minute interval on a data
summary sheet. Figure 1 of this subpart shows an example of the format
for the data summary sheet you may use, but are not required to use.
(ii) Using the data summary sheets prepared according to paragraph
(c)(7)(i) of this section and the process information recorded according
to paragraph (c)(6)(iii) of this section, identify those 1-minute
intervals for which at least one of the batch copper converters was
blowing.
(iii) Using the data summary sheets prepared according to paragraph
(c)(7)(ii) of this section and the process information recorded
according to paragraph (c)(6)(iv) of this section, identify the 1-minute
intervals during which at least one copper converter was blowing but
none of the interference events listed in paragraphs (c)(7)(iii)(A)
through (F) of this section occurred. Other ancillary activities not
listed but conducted in or adjacent to the converter aisle during the
opacity observations are not considered to be interference events (e.g.,
converter aisle cleaning, placement of smoking ladles or skulls on the
converter aisle floor).
(A) Charging of copper matte, reverts, or other materials to a batch
copper converter;
(B) Skimming slag or other molten materials from a batch copper
converter;
(C) Pouring of blister copper or other molten materials from a batch
copper converter;
(D) Return of slag or other molten materials to the flash smelting
furnace or slag cleaning vessel;
(E) Roll-out or roll-in of the batch copper converter; or
(F) Smoke and fumes generated inside the converter building by
operation of the smelting furnace, the slag cleaning vessel (if used),
anode refining and casting processes that drift into the copper
converter department.
(iv) Using the data summary sheets prepared according to paragraph
(c)(7)(iii) of this section, up to five 1-minute intervals following an
interference event may be eliminated from data used for the compliance
determination calculation specified in paragraph (c)(8) of this section
by applying a time delay factor. The time delay factor must be a
constant number of minutes not to exceed 5 minutes that is added to the
clock time recorded when cessation of the interference event occurs. The
same time delay factor must be used for all interference events (i.e., a
constant time delay factor for the smelter of 1 minute, 2 minutes, 3
minutes, 4 minutes, or 5 minutes). The number of minutes to be used for
the time delay factor is determined based on the site-specific equipment
and converter building configuration. An explanation of the rationale
for selecting the value used for the time delay factor must be prepared
and included in the test report.
[[Page 39]]
(8) You must use the data summary prepared in paragraph (c)(7) of
this section to calculate the average opacity value for a minimum of 120
1-minute intervals during which at least one copper converter was
blowing with no interference events as determined according to
paragraphs (c)(7)(iii) and (iv) of this section. Average opacity is
calculated using Equation 1 of this section:
[GRAPHIC] [TIFF OMITTED] TR12JN02.026
Where
VEave = Average opacity to be used for compliance
determination (percent);
n = Total number of 1-minute intervals during which at least one
copper converter was blowing with no interference events as determined
according to paragraphs (c)(7)(iii) and (iv) of this section (at least
120 1-minute intervals);
i = 1-minute interval ``i'' during which at least one copper
converter was blowing with no interference events as determined
according to paragraphs (c)(7)(iii) and (iv) of this section; and
VEi = Average opacity value calculated for the eight
opacity readings recorded during 1-minute interval ``i'' (percent).
(9) You must certify that the copper converter department capture
system operated during the performance test at the operating limits
established in your capture system operation and maintenance plan using
the procedure specified in paragraphs (c)(9)(i) through (iv) of this
section.
(i) Concurrent with all opacity observations, measure and record
values for each of the operating limit parameters in your capture system
operation and maintenance plan according to the monitoring requirements
specified in Sec. 63.1452(a).
(ii) For any dampers that are manually set and remain in the same
position at all times the capture system is operating, the damper
position must be visually checked and recorded at the beginning and end
of each opacity observation period segment.
(iii) Review the recorded monitoring data. Identify and explain any
times during batch copper converter blowing when the capture system
operated outside the applicable operating limits.
(iv) Certify in your performance test report that during all
observation period segments, the copper converter department capture
system was operating at the values or settings established in your
capture system operation and maintenance plan.
Sec. 63.1451 How do I demonstrate initial compliance with the emission limitations, work practice standards, and operation and maintenance requirements that
apply to me?
(a) Total particulate matter emission limits. For each copper
concentrate dryer, smelting furnace, slag cleaning vessel, and copper
converter department subject to a total particulate matter emission
limits in Sec. 63.1444 or Sec. 63.1446 that applies to you, you have
demonstrated initial compliance if you meet both of the conditions in
paragraphs (a)(1) and (2) of this section.
(1) The average concentration of total particulate matter from a
control device applied to emissions from the affected source, measured
according to the performance test procedures in Sec. 63.1450(a), did not
exceed the applicable emission limit.
(2) You have submitted a notification of compliance status according
to the requirements in Sec. 63.1454(e).
(b) Nonsulfuric acid particulate matter emissions limits. For each
smelting furnace, slag cleaning vessel, and copper converter departments
subject to the nonsulfuric acid particulate matter emissions limit in
Sec. 63.1444 as applies to you, you have demonstrated initial compliance
if you meet both of the conditions in paragraphs (b)(1) and (2) of this
section.
(1) The average concentration of nonsulfuric acid particulate matter
in the process off-gas discharged from the affected source, measured
according to the performance test procedures in Sec. 63.1450(b), did not
exceed 6.2 mg/dscm.
(2) You have submitted a notification of compliance status according
to the requirements in Sec. 63.1454(e).
[[Page 40]]
(c) For each existing copper converter department subject to the
opacity limit in Sec. 63.1444, you have demonstrated initial compliance
if you meet both of the conditions in paragraphs (c)(1) and (2) of this
section.
(1) The opacity of visible emissions exiting the roof monitors or
roof exhaust fans on the building housing the copper converter
department measured according to the performance test procedures in
Sec. 63.1450(c), did not exceed 4 percent opacity.
(2) You have submitted a notification of compliance status according
to the requirements in Sec. 63.1454(e).
(d) Copper converter department capture systems. You have
demonstrated initial compliance of the copper converter department
capture system if you meet all of the conditions in paragraphs (d)(1)
through (4) of this section.
(1) Prepared the capture system operation and maintenance plan
according to the requirements of paragraph (a) of this section;
(2) Conducted an initial performance test according to the
procedures of Sec. 63.1450(c) demonstrating the opacity of any visible
emissions exiting the roof monitors or roof exhaust fans on the building
housing the copper converter department does not exceed 4 percent
opacity;
(3) Included in your notification of compliance status a copy of
your written capture system operation and maintenance plan and have
certified in your notification of compliance status that you will
operate the copper converter department capture system at all times
during blowing at the values or settings established for the operating
limits in that plan; and
(4) Submitted a notification of compliance status according to the
requirements in Sec. 63.1454(e).
(e) Baghouses. For each baghouse subject to operating limits in
Sec. 63.1444(f) or Sec. 63.1446(c), you have demonstrated initial
compliance if you meet all of the conditions in paragraphs (e)(1)
through (3) of this section.
(1) You have included in your written operation and maintenance plan
required under Sec. 63.1447(b) detailed descriptions of the procedures
you use for inspection, maintenance, bag leak detection, and corrective
action for the baghouse.
(2) You have certified in your notification of compliance status
that you will operate the baghouse according to your written operation
and maintenance plan.
(3) You have submitted the notification of compliance status
according to the requirements in Sec. 63.1454(e).
(f) Venturi wet scrubbers. For each venturi wet scrubber subject to
operating limits in Sec. 63.1444(g) or Sec. 63.1446(d), you have
demonstrated initial compliance if you meet all of the conditions in
paragraphs (f)(1) through (3) of this section.
(1) Established site-specific operating limits for pressure drop and
scrubber water flow rate and have a record of the pressure drop and
scrubber water flow rate measured during the performance test you
conduct to demonstrate initial compliance with paragraph (a) of this
section.
(2) Certified in your notification of compliance status that you
will operate the venturi wet scrubber within the established operating
limits for pressure drop and scrubber water flow rate.
(3) Submitted a notification of compliance status according to the
requirements in Sec. 63.1454(e).
(g) Other control devices. For each control device other than a
baghouse or venturi wet scrubber subject to operating limits in
Sec. 63.1444(h) or Sec. 63.1446(e), you have demonstrated initial
compliance if you meet all of the conditions in paragraphs (g)(1)
through (4) of this section.
(1) Selected one or more operating parameters, as appropriate for
the control device design, that can be used as representative and
reliable indicators of the control device operation.
(2) Established site-specific operating limits for each of the
selected operating parameters based on values measured during the
performance test you conduct to demonstrate initial compliance with
paragraph (a) of this section and have prepared written documentation
according to the requirements in Sec. 63.1450(a)(5)(iv).
(3) Included in your notification of compliance status a copy of the
written documentation you have prepared
[[Page 41]]
to demonstrate compliance with paragraph (g)(2) of this section and have
certified in your notification of compliance status that you will
operate the control device within the established operating limits.
(4) Submitted a notification of compliance status according to the
requirements in Sec. 63.1454(e).
(h) Fugitive dust sources. For all fugitive dust sources subject to
work practice standards in Sec. 63.1445, you have demonstrated initial
compliance if you meet all of the conditions in paragraphs (i)(1)
through (3) of this section.
(1) Prepared a written fugitive dust control plan according to the
requirements in Sec. 63.1454 and it has been approved by the designated
authority.
(2) Certified in your notification of compliance status that you
will control emissions from the fugitive dust sources according to the
procedures in the approved plan.
(3) Submitted the notification of compliance status according to the
requirements in Sec. 63.1454(e).
(i) Operation and maintenance requirements. You have demonstrated
initial compliance with the operation and maintenance requirements that
apply to you if you meet all of the conditions in paragraphs (i)(1)
through (3) of this section.
(1) Prepared an operation and maintenance plan according to the
requirements in Sec. 63.1454(b).
(2) Certified in your notification of compliance status that you
will operate each capture system and control device according to the
procedures in the plan.
(3) Submitted the notification of compliance status according to the
requirements in Sec. 63.1454(e).
Continuous Compliance Requirements
Sec. 63.1452 What are my monitoring requirements?
(a) Copper converter department capture systems. For each operating
limit established under your capture system operation and maintenance
plan, you must install, operate, and maintain an appropriate monitoring
device according the requirements in paragraphs (a)(1) though (6) of
this section to measure and record the operating limit value or setting
at all times the copper converter department capture system is operating
during batch copper converter blowing. Dampers that are manually set and
remain in the same position at all times the capture system is operating
are exempted from the requirements of this paragraph (a).
(1) Install the monitoring device, associated sensor(s), and
recording equipment according to the manufacturers' specifications.
Locate the sensor(s) used for monitoring in or as close to a position
that provides a representative measurement of the parameter being
monitored.
(2) If a flow measurement device is used to monitor the operating
limit parameter, you must meet the requirements in paragraph (a)(2)(i)
through (iv) of this section.
(i) Locate the flow sensor and other necessary equipment such as
straightening vanes in a position that provides a representative flow.
(ii) Use a flow sensor with a minimum tolerance of 2 percent of the
flow rate.
(iii) Reduce swirling flow or abnormal velocity distributions due to
upstream and downstream disturbances.
(iv) Conduct a flow sensor calibration check at least semiannually.
(3) If a pressure measurement device is used to monitor the
operating limit parameter, you must meet the requirements in paragraph
(a)(3)(i) through (v) of this section.
(i) Locate the pressure sensor(s) in or as close to a position that
provides a representative measurement of the pressure.
(ii) Minimize or eliminate pulsating pressure, vibration, and
internal and external corrosion.
(iii) Use a gauge with a minimum tolerance of 0.5 inch of water or a
transducer with a minimum tolerance of 1 percent of the pressure range.
(iv) Check pressure tap pluggage daily.
(v) Using a manometer, check gauge calibration quarterly and
transducer calibration monthly.
(4) Conduct calibration and validation checks any time the sensor
exceeds the manufacturer's specifications or you install a new sensor.
[[Page 42]]
(5) At least monthly, inspect all components for integrity, all
electrical connections for continuity, and all mechanical connections
for leakage.
(6) Record the results of each inspection, calibration, and
validation check.
(b) Baghouses. For each baghouse subject to the operating limit in
Sec. 63.1444(f) or Sec. 63.1446(c) for the bag leak detection system
alarm, you must at all times monitor the relative change in particulate
matter loadings using a bag leak detection system according to the
requirements in paragraph (b)(1) of this section and conduct regular
inspections according to the requirements in paragraph (b)(2) of this
section.
(1) You must install, operate, and maintain each bag leak detection
system according to the requirements in paragraphs (b)(1)(i) through
(vii) of this section.
(i) The system must be certified by the manufacturer to be capable
of detecting emissions of particulate matter at concentrations of 10
milligrams per actual cubic meter (0.0044 grains per actual cubic foot)
or less.
(ii) The system must provide output of relative changes in
particulate matter loadings.
(iii) The system must be equipped with an alarm that will sound when
an increase in relative particulate loadings is detected over a preset
level. The alarm must be located such that it can be heard by the
appropriate plant personnel.
(iv) Each system that works based on the triboelectric effect must
be installed, operated, and maintained in a manner consistent with the
guidance document, ``Fabric Filter Bag Leak Detection Guidance,'' EPA-
454/R-98-015, September 1997. You may obtain a copy of this guidance
document by contacting the National Technical Information Service (NTIS)
at 800-553-6847. You may install, operate, and maintain other types of
bag leak detection systems in a manner consistent with the
manufacturer's written specifications and recommendations.
(v) To make the initial adjustment of the system, establish the
baseline output by adjusting the sensitivity (range) and the averaging
period of the device. Then, establish the alarm set points and the alarm
delay time.
(vi) Following the initial adjustment, do not adjust the sensitivity
or range, averaging period, alarm set points, or alarm delay time,
except as detailed in your operation and maintenance plan. Do not
increase the sensitivity by more than 100 percent or decrease the
sensitivity by more than 50 percent over a 365-day period unless a
responsible official certifies, in writing, that the baghouse has been
inspected and found to be in good operating condition.
(vii) Where multiple detectors are required, the system's
instrumentation and alarm may be shared among detectors.
(2) You must conduct baghouse inspections at their specified
frequencies according to the requirements in paragraphs (b)(2)(i)
through (viii) of this section.
(i) Monitor the pressure drop across each baghouse cell each day to
ensure pressure drop is within the normal operating range identified in
the manual.
(ii) Confirm that dust is being removed from hoppers through weekly
visual inspections or other means of ensuring the proper functioning of
removal mechanisms.
(iii) Check the compressed air supply for pulse-jet baghouses each
day.
(iv) Monitor cleaning cycles to ensure proper operation using an
appropriate methodology.
(v) Check bag cleaning mechanisms for proper functioning through
monthly visual inspection or equivalent means.
(vi) Make monthly visual checks of bag tension on reverse air and
shaker-type baghouses to ensure that bags are not kinked (kneed or bent)
or laying on their sides. You do not have to make this check for shaker-
type baghouses using self-tensioning (spring-loaded) devices.
(vii) Confirm the physical integrity of the baghouse through
quarterly visual inspections of the baghouse interior for air leaks.
(viii) Inspect fans for wear, material buildup, and corrosion
through quarterly visual inspections, vibration detectors, or equivalent
means.
(c) Venturi wet scrubbers. For each venturi wet scrubber subject to
the operating limits for pressure drop and scrubber water flow rate in
Sec. 63.1444(g)
[[Page 43]]
or Sec. 63.1446(d), you must at all times monitor the hourly average
pressure drop and water flow rate using a CPMS. You must install,
operate, and maintain each CPMS according to the requirements in
paragraphs (c)(1) and (2) of this section.
(1) For the pressure drop CPMS, you must meet the requirements in
paragraphs (c)(1)(i) through (vi) of this section.
(i) Locate the pressure sensor(s) in or as close to a position that
provides a representative measurement of the pressure and that minimizes
or eliminates pulsating pressure, vibration, and internal and external
corrosion.
(ii) Use a gauge with a minimum measurement sensitivity of 0.5 inch
of water or a transducer with a minimum measurement sensitivity of 1
percent of the pressure range.
(iii) Check the pressure tap for pluggage daily.
(iv) Using a manometer, check gauge calibration quarterly and
transducer calibration monthly.
(v) Conduct calibration checks any time the sensor exceeds the
manufacturer's specified maximum operating pressure range, or install a
new pressure sensor.
(vi) At least monthly, inspect all components for integrity, all
electrical connections for continuity, and all mechanical connections
for leakage.
(2) For the scrubber water flow rate CPMS, you must meet the
requirements in paragraphs (c)(2)(i) through (iv) of this section.
(i) Locate the flow sensor and other necessary equipment in a
position that provides a representative flow and that reduces swirling
flow or abnormal velocity distributions due to upstream and downstream
disturbances.
(ii) Use a flow sensor with a minimum measurement sensitivity of 2
percent of the flow rate.
(iii) Conduct a flow sensor calibration check at least semiannually
according to the manufacturer's instructions.
(iv) At least monthly, inspect all components for integrity, all
electrical connections for continuity, and all mechanical connections
for leakage.
(d) Other control devices. For each control device other than a
baghouse or venturi wet scrubber subject to the operating limits for
appropriate parameters in Sec. 63.1444(h) or Sec. 63.1446(e), you must
at all times monitor the hourly average pressure drop and water flow
rate using a CPMS. You must install, operate, and maintain each CPMS
according to the equipment manufacturer's specifications and the
requirements in paragraphs (d)(1) though (5) of this section.
(1) Locate the sensor(s) used for monitoring in or as close to a
position that provides a representative measurement of the parameter
being monitored.
(2) Determine the hourly average of all recorded readings.
(3) Conduct calibration and validation checks any time the sensor
exceeds the manufacturer's specifications or you install a new sensor.
(4) At least monthly, inspect all components for integrity, all
electrical connections for continuity, and all mechanical connections
for leakage.
(5) Record the results of each inspection, calibration, and
validation check.
(e) Except for monitoring malfunctions, associated repairs, and
required quality assurance or control activities (including as
applicable, calibration checks and required zero and span adjustments),
you must monitor continuously (or collect data at all required
intervals) at all times an affected source is operating.
(f) You may not use data recorded during monitoring malfunctions,
associated repairs, and required quality assurance or control activities
in data averages and calculations used to report emission or operating
levels or to fulfill a minimum data availability requirement, if
applicable. You must use all the data collected during all other periods
in assessing compliance.
(g) A monitoring malfunction is any sudden, infrequent, not
reasonably preventable failure of the monitor to provide valid data.
Monitoring failures that are caused in part by poor maintenance or
careless operation are not malfunctions.
[[Page 44]]
Sec. 63.1453 How do I demonstrate continuous compliance with the emission limitations, work practice standards, and operation and maintenance requirements that
apply to me?
(a) Particulate matter emission limits. For each affected source
subject to a particulate matter emission limit Sec. 63.1444 or
Sec. 63.1446 as applies to you, you must demonstrate continuous
compliance according to the requirements in paragraphs (a)(1) and (2) of
this section.
(1) For each copper concentrate dryer, smelting furnace, slag
cleaning vessel, and copper converter department subject to a total
particulate matter emission limit in Sec. 63.1444 or Sec. 63.1446 as
applies to you, you must demonstrate continuous compliance by meeting
the conditions in paragraphs (a)(1)(i) and (ii) of this section.
(i) Maintain the average concentration of total particulate matter
in the gases discharged from the affected source at or below the
applicable emission limit.
(ii) Conduct subsequent performance tests following your initial
performance test no less frequently than once per year according to the
performance test procedures in Sec. 63.1450(a).
(2) For each smelting furnace, slag cleaning vessel, and copper
converter department subject to the nonsulfuric acid particulate matter
emission limit in Sec. 63.1444 as applies to you, you must demonstrate
continuous compliance by meeting the conditions in paragraphs (a)(2)(i)
and (ii) of this section.
(i) Maintain the average concentration of nonsulfuric acid
particulate matter in the process off-gas discharged from the affected
source at or below 6.2 mg/dscm.
(ii) Conduct subsequent performance tests following your initial
performance test no less frequently than once per year according to the
performance test procedures in Sec. 63.1450(b).
(b) Copper converter department capture systems. You must
demonstrate continuous compliance of the copper converter department
capture system by meeting the requirements in paragraphs (b)(1) through
(4) of this section.
(1) Operate the copper converter department capture system at all
times during blowing at or above the lowest values or settings
established for the operating limits and demonstrated to achieve the
opacity limit according to the applicable requirements of this subpart;
(2) Inspect and maintain the copper converter department capture
system according to the applicable requirements in Sec. 63.1447 and
recording all information needed to document conformance with these
requirements;
(3) Monitor the copper converter department capture system according
to the requirements in Sec. 63.1452(a) and collecting, reducing, and
recording the monitoring data for each of the operating limit parameters
according to the applicable requirements of this subpart; and
(4) Conduct subsequent performance tests according to the
requirements of Sec. 63.1450(c) following your initial performance test
no less frequently than once per year to demonstrate that the opacity of
any visible emissions exiting the roof monitors or roof exhaust fans on
the building housing the copper converter department does not exceed 4
percent opacity.
(c) Baghouses. For each baghouse subject to the operating limit for
the bag leak detection system alarm in Sec. 63.1444(f) or
Sec. 63.1446(c), you must demonstrate continuous compliance by meeting
the requirements in paragraphs (c)(1) through (3) of this section.
(1) Maintain the baghouse such that the bag leak detection system
alarm does not sound for more than 5 percent of the operating time
during any semiannual reporting period. To determine the percent of time
the alarm sounded use the procedures in paragraphs (c)(1)(i) through (v)
of this section.
(i) Alarms that occur due solely to a malfunction of the bag leak
detection system are not included in the calculation.
(ii) Alarms that occur during startup, shutdown, or malfunction are
not included in the calculation if the condition is described in the
startup, shutdown, and malfunction plan, and all the actions you took
during the startup, shutdown, or malfunction were consistent with the
procedures in the startup, shutdown, and malfunction plan.
[[Page 45]]
(iii) Count 1 hour of alarm time for each alarm when you initiated
procedures to determine the cause of the alarm within 1 hour.
(iv) Count the actual amount of time you took to initiate procedures
to determine the cause of the alarm if you did not initiate procedures
to determine the cause of the alarm within 1 hour of the alarm.
(v) Calculate the percentage of time the alarm on the bag leak
detection system sounds as the ratio of the sum of alarm times to the
total operating time multiplied by 100.
(2) Maintain records of the times the bag leak detection system
alarm sounded, and for each valid alarm, the time you initiated
corrective action, the corrective action(s) taken, and the date on which
corrective action was completed.
(3) Inspect and maintain each baghouse according to the requirements
in Sec. 63.1451(b)(2) and recording all information needed to document
conformance with these requirements. If you increase or decrease the
sensitivity of the bag leak detection system beyond the limits specified
in Sec. 63.1451(b)(1)(vi), you must include a copy of the required
written certification by a responsible official in the next semiannual
compliance report.
(d) Venturi wet scrubbers. For each venturi wet scrubber subject to
the operating limits for pressure drop and scrubber water flow rate in
Sec. 63.1444(g) or Sec. 63.1446(d), you must demonstrate continuous
compliance by meeting the requirements of paragraphs (d)(1) through (3)
of this section.
(1) Maintain the hourly average pressure drop and scrubber water
flow rate at levels no lower than those established during the initial
or subsequent performance test;
(2) Inspect and maintain each venturi wet scrubber CPMS according to
Sec. 63.1452(c) and recording all information needed to document
conformance with these requirements; and
(3) Collect and reduce monitoring data for pressure drop and
scrubber water flow rate according to Sec. 63.1452(e) and recording all
information needed to document conformance with these requirements.
(e) Other control devices. For each control device other than a
baghouse or venturi wet scrubber subject to the operating limits for
site-specific operating parameters in Sec. 63.1444(h) or
Sec. 63.1446(e), you must demonstrate continuous compliance by meeting
the requirements of paragraphs (e)(1) through (3) of this section:
(1) Maintain the hourly average rate at levels no lower than those
established during the initial or subsequent performance test;
(2) Inspect and maintain each venturi wet scrubber CPMS according to
Sec. 63.1452(d) and recording all information needed to document
conformance with these requirements; and
(3) Collect and reduce monitoring data for selected parameters
according to Sec. 63.1452(e) and recording all information needed to
document conformance with these requirements.
(f) Fugitive dust sources. For each fugitive dust source subject to
work practice standards in Sec. 63.1445, you must demonstrate continuous
compliance by implementing all of fugitive control measures specified
for the source in your written fugitive dust control plan.
Notifications, Reports and Records
Sec. 63.1454 What notifications must I submit and when?
(a) You must submit all of the notifications in Secs. 63.6(h)(4) and
(h)(5), 63.7(b) and (c), 63.8(f)(4), and 63.9(b) through (h) that apply
to you by the specified dates.
(b) As specified in Sec. 63.9(b)(2), if you start your affected
source before June 12, 2002, you must submit your initial notification
not later than October 10, 2002.
(c) As specified in Sec. 63.9(b)(3), if you start your new affected
source on or after June 12, 2002, you must submit your initial
notification not later than 120 calendar days after you become subject
to this subpart.
(d) If you are required to conduct a performance test, you must
submit a notification of intent to conduct a performance test at least
60 calendar days before the performance test is scheduled to begin as
required in Sec. 63.7(b)(1).
[[Page 46]]
(e) If you are required to conduct a performance test, opacity
observation, or other initial compliance demonstration, you must submit
a notification of compliance status according to Sec. 63.9(h)(2)(ii) by
the date specified in paragraph (e)(1) or (2) of this section as applies
to you.
(1) For each initial compliance demonstration that does not include
a performance test, you must submit the notification of compliance
status before the close of business on the 30th calendar day following
the completion of the initial compliance demonstration.
(2) For each initial compliance demonstration that includes a
performance test, you must submit the notification of compliance status,
including the performance test results, before the close of business on
the 60th calendar day following the completion of the performance test
according to Sec. 63.10(d)(2).
Sec. 63.1455 What reports must I submit and when?
(a) You must submit each report in paragraphs (a)(1) and (2) of this
section that applies to you.
(1) You must submit a compliance report semiannually according to
the requirements in paragraph (b) of this section and containing the
information in paragraph (c) of this section.
(2) You must submit an immediate startup, shutdown, and malfunction
report if you had a startup, shutdown, or malfunction during the
reporting period that is not consistent with your startup, shutdown, and
malfunction plan. You must report the actions taken for the event by fax
or telephone within 2 working days after starting actions inconsistent
with the plan. You must submit the information in Sec. 63.10(d)(5)(ii)
of this part by letter within 7 working days after the end of the event
unless you have made alternative arrangements with the permitting
authority.
(b) Unless the Administrator has approved a different schedule under
Sec. 63.10(a), you must submit each compliance report required in
paragraph (a) of this section according to the applicable requirements
in paragraphs (b)(1) through (5) of this section.
(1) The first compliance report must cover the period beginning on
the compliance date that is specified for your affected source in
Sec. 63.1443 and ending on June 30 or December 31, whichever date comes
first after the compliance date that is specified for your source in
Sec. 63.1443.
(2) The first compliance report must be postmarked or delivered no
later than July 31 or January 31, whichever date comes first after your
first compliance report is due.
(3) Each subsequent compliance report must cover the semiannual
reporting period from January 1 through June 30 or the semiannual
reporting period from July 1 through December 31.
(4) Each subsequent compliance report must be postmarked or
delivered no later than July 31 or January 31, whichever date comes
first after the end of the semiannual reporting period.
(5) For each affected source that is subject to permitting
regulations pursuant to 40 CFR part 70 or 40 CFR part 71, and if the
permitting authority has established dates for submitting semiannual
reports pursuant to 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR
71.6(a)(3)(iii)(A) of this chapter, you may submit the first and
subsequent compliance reports according to the dates the permitting
authority has established instead of according to the dates in
paragraphs (b)(1) through (4) of this section.
(c) Each compliance report must contain the information in
paragraphs (c)(1) through (3) of this section and, as applicable,
paragraphs (c)(4) through (8) of this section.
(1) Company name and address.
(2) Statement by a responsible official, as defined in 40 CFR 63.2,
with that official's name, title, and signature, certifying the accuracy
and completeness of the content of the report.
(3) Date of report and beginning and ending dates of the reporting
period.
(4) If you had a startup, shutdown or malfunction during the
reporting period and you took actions consistent with your startup,
shutdown, and malfunction plan, the compliance report must include the
information in Sec. 63.10(d)(5)(i).
[[Page 47]]
(5) If there are no deviations from any emission limitations
(emission limit, operating limit, opacity limit) that applies to you and
there are no deviations from the requirements for work practice
standards in this subpart, a statement that there were no deviations
from the emission limitations, work practice standards, or operation and
maintenance requirements during the reporting period.
(6) If there were no periods during which an operating parameter
monitoring system was out-of-control as specified in Sec. 63.8(c)(7), a
statement that there were no periods during which the monitoring system
was out-of-control during the reporting period.
(7) For each deviation from an emission limitation (emission limit,
operating limit, opacity limit) and for each deviation from the
requirements for work practice standards that occurs at an affected
source where you are not using a continuous monitoring system to comply
with the emission limitations or work practice standards in this
subpart, the compliance report must contain the information in
paragraphs (b)(1) through (4) of this section and the information in
paragraphs (b)(7)(i) and (ii) of this section. This includes periods of
startup, shutdown, and malfunction.
(i) The total operating time of each affected source during the
reporting period.
(ii) Information on the number, duration, and cause of deviations
(including unknown cause, if applicable), as applicable, and the
corrective action taken.
(8) For each deviation from an emission limitation (emission limit,
operating limit, opacity limit, and visible emission limit) occurring at
an affected source where you are using a operating parameter monitoring
system to comply with the emission limitation in this subpart, you must
include the information in paragraphs (b)(1) through (4) of this section
and the information in paragraphs (c)(8)(i) through (xi) of this
section. This includes periods of startup, shutdown, and malfunction.
(i) The date and time that each malfunction started and stopped.
(ii) The date and time that each monitoring system was inoperative,
except for zero (low-level) and high-level checks.
(iii) The date, time and duration that each monitoring system was
out-of-control, including the information in Sec. 63.8(c)(8).
(iv) The date and time that each deviation started and stopped, and
whether each deviation occurred during a period of startup, shutdown, or
malfunction or during another period.
(v) A summary of the total duration of the deviation during the
reporting period and the total duration as a percent of the total source
operating time during that reporting period.
(vi) A breakdown of the total duration of the deviations during the
reporting period into those that are due to startup, shutdown, control
equipment problems, process problems, other known causes, and other
unknown causes.
(vii) A summary of the total duration of monitoring system downtime
during the reporting period and the total duration of monitoring system
downtime as a percent of the total source operating time during that
reporting period.
(viii) A brief description of the process units.
(ix) A brief description of the monitoring system.
(x) The date of the latest monitoring system certification or audit.
(xi) A description of any changes in continuous monitoring systems,
processes, or controls since the last reporting period.
(d) If you have obtained a Title V operating permit pursuant to 40
CFR part 70 or 40 CFR part 71 must report all deviations as defined in
this subpart in the semiannual monitoring report required by 40 CFR
70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A). If you submit a
compliance report pursuant to paragraph (a) of this section along with,
or as part of, the semiannual monitoring report required by 40 CFR
70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A), and the compliance
report includes all required information concerning deviations from any
emission limitation(including any operating limit), or work practice
requirement in this subpart, submission of the compliance report is
deemed to satisfy
[[Page 48]]
any obligation to report the same deviations in the semiannual
monitoring report. However, submission of a compliance report does not
otherwise affect any obligation you may have to report deviations from
permit requirements to the permit authority.
Sec. 63.1456 What records must I keep and how long must I keep my records?
(a) You must keep the records listed in paragraphs (a)(1) through
(7) of this section.
(1) A copy of each notification and report that you submitted to
comply with this subpart, including all documentation supporting any
initial notification or notification of compliance status that you
submitted, according to the requirements in Sec. 63.10(b)(2)(xiv).
(2) The records in Sec. 63.6(e)(3)(iii) through (v) related to
startup, shutdown, and malfunction.
(3) Records of performance tests and performance evaluations as
required in Sec. 63.10(b)(2)(viii).
(4) For each monitoring system, you must keep the records specified
in paragraphs (a)(4)(i) through (iv) of this section.
(i) Records described in Sec. 63.10(b)(2)(vi) through (xi).
(ii) Monitoring data recorded by the monitoring system during a
performance evaluation as required in Sec. 63.6(h)(7)(i) and (ii).
(iii) Previous (i.e., superseded) versions of the performance
evaluation plan as required in Sec. 63.8(d)(3).
(iv) Records of the date and time that each deviation started and
stopped, and whether the deviation occurred during a period of startup,
shutdown, or malfunction or during another period.
(5) For each performance test you conduct to demonstrate compliance
with a opacity limit according to Sec. 63.1450(c), you must keep the
records specified in paragraphs (a)(5)(i) through (ix) of this section.
(i) Dates and time intervals of all opacity observation period
segments;
(ii) Description of overall smelter operating conditions during each
observation period. Identify, if any, the smelter copper production
process equipment that was out-of-service during the performance test
and explain why this equipment was not in operation;
(iii) Name, affiliation, and copy of current visible emission
reading certification for each visible emission observer participating
in the performance test;
(iv) Name, title, and affiliation for each indoor process monitor
participating in the performance test;
(v) Copies of all visible emission observer opacity field data
sheets;
(vi) Copies of all indoor process monitor operating log sheets;
(vii) Copies of all data summary sheets used for data reduction;
(viii) Copy of calculation sheets of the average opacity value used
to demonstrate compliance with the opacity limit; and
(ix) Documentation according to the requirements in
Sec. 63.1450(c)(9)(iv) to support your selection of the site-specific
capture system operating limits used for each batch copper converter
capture system when blowing.
(6) For each baghouse subject to the operating limit in
Sec. 63.1444(f) or Sec. 63.1446(c), you must keep the records specified
in paragraphs (a)(6)(i) and (ii) of this section.
(i) Records of alarms for each bag leak detection system.
(ii) Description of the corrective actions taken following each bag
leak detection alarm.
(7) For each control device other than a baghouse or venturi wet
scrubber subject to site-specific operating limits in Sec. 63.1444(g) or
Sec. 63.1446(f), you must keep documentation according to the
requirements in Sec. 63.1450(a)(5)(iv) to support your selection of the
site-specific operating limits for the control device.
(b) Your records must be in a form suitable and readily available
for expeditious review, according to Sec. 63.10(b)(1).
(c) As specified in Sec. 63.10(b)(1), you must keep each record for
5 years following the date of each occurrence, measurement, maintenance,
corrective action, report, or record.
(d) You must keep each record on site for at least 2 years after the
date of each occurrence, measurement, maintenance, corrective action,
report, or record, according to Sec. 63.10(b)(1). You
[[Page 49]]
can keep the records off site for the remaining 3 years.
Other Requirements and Information
Sec. 63.1457 What part of the general provisions apply to me?
Table 2 to this subpart shows which parts of the general provisions
in Secs. 63.1 through 63.15 apply to you.
Sec. 63.1458 Who implements and enforces this subpart?
(a) This subpart can be implemented and enforced by us, the United
States Environmental Protection Agency (U.S. EPA), or a delegated
authority such as your State, local, or tribal agency. If the U.S. EPA
Administrator has delegated authority to your State, local, or tribal
agency, then that agency has the authority to implement and enforce this
subpart. You should contact your U.S. EPA Regional Office to find out if
this subpart is delegated to your State, local, or tribal agency.
(b) In delegating implementation and enforcement authority of this
subpart to a State, local, or tribal agency under 40 CFR part 63,
subpart E, the authorities listed in paragraph (c) of this section are
retained by the U.S. EPA Administrator and are not transferred to the
State, local, or tribal agency.
(c) The authorities that will not be delegated to State, local, or
tribal agencies are as listed in paragraphs (c)(1) through (4) of this
section.
(1) Approval of alternatives to the emission limitations and work
practice standards in Secs. 63.1444 through 63.1446 under Sec. 63.6(g).
(2) Approval of major alternatives to test methods under
Sec. 63.7(f) and as defined in Sec. 63.90.
(3) Approval of major alternatives to monitoring under Sec. 63.8(f)
and as defined in Sec. 63.90.
(4) Approval of major alternatives to recordkeeping and reporting
under Sec. 63.10(f) and as defined in Sec. 63.90.
Sec. 63.1459 What definitions apply to this subpart?
Terms used in this subpart are defined in the Clean Air Act, in
Sec. 63.2, and in this section as follows:
Bag leak detection system means a system that is capable of
continuously monitoring relative particulate matter (dust) loadings in
the exhaust of a baghouse in order to detect bag leaks and other upset
conditions. A bag leak detection system includes, but is not limited to,
an instrument that operates on triboelectric, light scattering,
transmittance or other effect to continuously monitor relative
particulate matter loadings.
Baghouse means a control device that collects particulate matter by
filtering the gas stream through bags. A baghouse is also referred to as
a ``fabric filter.''
Batch copper converter means a Pierce-Smith converter or Hoboken
converter in which copper matte is oxidized to form blister copper by a
process that is performed in discrete batches using a sequence of
charging, blowing, skimming, and pouring.
Blowing means the operating mode for a batch copper converter during
which air or oxygen-enriched air is injected into the molten converter
bath.
Capture system means the collection of components used to capture
gases and fumes released from one or more emission points, and to convey
the captured gases and fumes to a control device. A capture system may
include, but is not limited to, the following components as applicable
to a given capture system design: duct intake devices, hoods,
enclosures, ductwork, dampers, manifolds, plenums, and fans.
Charging means the operating mode for a batch copper converter
during which molten or solid material is added into the vessel.
Control device means the air pollution control equipment used to
collect particulate matter emissions. Examples of such equipment
include, but are not limited to, a baghouse, an electrostatic
precipitator, and a wet scrubber.
Copper concentrate dryer means a vessel in which copper concentrates
are heated in the presence of air to reduce the moisture content of the
material. Supplemental copper-bearing feed materials and fluxes may be
added or mixed with the copper concentrates fed to a copper concentrate
dryer.
Copper converter department means the area at a primary copper
smelter in
[[Page 50]]
which the copper converters are located.
Copper matte means a material predominately composed of copper and
iron sulfides produced by smelting copper ore concentrates.
Deviation means any instance in which an affected source subject to
this subpart or an owner or operator of such a source fails to meet any
of the following:
(1) Any requirement or obligation established by this subpart
including, but not limited to, any emission limitation (including any
operating limit) or work practice standard;
(2) Any term or condition that is adopted to implement an applicable
requirement in this subpart and that is included in the operating permit
for any affected source required to obtain such a permit; or
(3) Any emission limitation (including any operating limit) or work
practice standard in this subpart during startup, shutdown, or
malfunction, regardless whether or not such failure is permitted by this
subpart.
Emission limitation means any emission limit, opacity limit,
operating limit, or visible emission limit.
Fugitive dust material means copper concentrate, dross, reverts,
slag, speiss, or other solid copper-bearing materials.
Fugitive dust source means a stationary source of particulate matter
emissions resulting from the handling, storage, transfer, or other
management of fugitive dust materials where the source is not associated
with a specific process, process vent, or stack. Examples of a fugitive
dust source include, but are not limited to, on-site roadways used by
trucks transporting copper concentrate, unloading of materials from
trucks or railcars, outdoor material storage piles, and transfer of
material to hoppers and bins.
Holding means the operating mode for a batch copper converter during
which the molten bath is maintained in the vessel but no blowing is
performed nor is material added into or removed from the vessel.
Opacity means the degree to which emissions reduce the transmission
of light.
Particulate matter means any finely divided solid or liquid
material, other than uncombined water, as measured by the specific
reference method.
Pouring means the operating mode for a batch copper converter during
which molten copper is removed from the vessel.
Primary copper smelter means any installation or any intermediate
process engaged in the production of copper from copper sulfide ore
concentrates through the use of pyrometallurgical techniques.
Responsible official means responsible official as defined in 40 CFR
70.2.
Skimming means the batch copper converter operating mode during
which molten slag is removed from the vessel.
Slag cleaning vessel means a vessel that receives molten copper-
bearing material and the predominant use of the vessel is to separate
this material into molten copper matte and slag layers.
Smelting furnace means a furnace, reactor, or other type of vessel
in which copper ore concentrate and fluxes are melted to form a molten
mass of material containing copper matte and slag. Other copper-bearing
materials may also be charged to the smelting furnace.
Work practice standard means any design, equipment, work practice,
or operational standard, or combination thereof, that is promulgated
pursuant to section 112(h) of the Clean Air Act.
As required in Sec. 63.1457, you must comply with the requirements
of the NESHAP General Provisions (40 CFR part 63, subpart A) shown in
the following table:
Table 1 to Subpart QQQ of Part 63--Applicability of General Provisions
to Subpart QQQ
----------------------------------------------------------------------------------------------------------------
Citation Subject Applies to subpart QQQ Explanation
----------------------------------------------------------------------------------------------------------------
Sec. 63.1........................... Applicability.......... Yes....................
Sec. 63.2........................... Definitions............ Yes....................
[[Page 51]]
Sec. 63.3........................... Units and Abbreviations Yes....................
Sec. 63.4........................... Prohibited Activities.. Yes....................
Sec. 63.5........................... Construction and Yes....................
Reconstruction.
Sec. 63.6(a)-(g).................... Compliance with Yes....................
Standards and
Maintenance
requirements.
Sec. 63.6(h)........................ Determining compliance No..................... Subpart QQQ specifies
with Opacity and VE the requirements and
standards. test protocol used to
determine compliance
with the opacity
limits.
Sec. 63.6(i)-(j).................... Extension of Compliance Yes....................
and Presidential
Compliance Exemption.
Sec. 63.7(a)(1)-(2)................. Applicability and No..................... Subpart QQQ specifies
Performance Test Dates. performance test
applicability and
dates.
Sec. 63.7(a)(3), (b)-(h)............ Performance Testing Yes....................
Requirements.
Sec. 63.8 except for (a)(4),(c)(4), Monitoring Requirements Yes....................
and (f)(6).
Sec. 63.8(a)(4)..................... Additional Monitoring No..................... Subpart QQ does not
Requirements for require flares.
Control devices in
Sec. 63.11.
Sec. 63.8(c)(4)..................... Continuous Monitoring No..................... Subpart QQQ specifies
System Requirements. requirements for
operation of CMS.
Sec. 63.8(f)(6)..................... RATA Alternative....... No..................... Subpart QQQ does not
require continuous
emission monitoring
systems.
Sec. 63.9........................... Notification Yes....................
Requirements.
Sec. 63.9(g)(5)..................... DATA reduction......... No..................... Subpart QQQ specifies
data reduction
requirements
Sec. 63.10 except for (b)(2)(xiii) Recordkeeping and Yes....................
and (c)(7)-(8). reporting Requirements.
Sec. 63.10(b)(2)(xiii).............. CMS Records for RATA No..................... Subpart QQQ does not
Alternative. require continuous
emission monitoring
systems.
Sec. 63.10(c)(7)-(8)................ Records of Excess No..................... Subpart QQQ specifies
Emissions and record keeping
Parameter Monitoring requirements
Accedences for CMS.
Sec. 63.11.......................... Control Device No..................... Subpart QQQ does not
Requirements. require flares
Sec. 63.12.......................... State Authority and Yes....................
Delegations.
Secs. 63.13-63.15................... Addresses, Yes....................
Incorporation by
Reference,
Availability of
Information.
----------------------------------------------------------------------------------------------------------------
Figure 1 to Subpart QQQ of Part 63--Data Summary Sheet for Determination
of Average Opacity
----------------------------------------------------------------------------------------------------------------
Average
Visible opacity for 1-
emissions minute
Average interference interval
Number of Converter aisle opacity for 1- observed blowing
Clock time converters activity minute during 1- without
blowing interval minute visible
(percent) interval? emission
(yes or no) interferences
(percent)
----------------------------------------------------------------------------------------------------------------
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[[Page 52]]
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Subpart RRR--National Emission Standards for Hazardous Air Pollutants
for Secondary Aluminum Production
Source: 65 FR 15710, Mar. 23, 2000, unless otherwise noted.
General
Sec. 63.1500 Applicability.
(a) The requirements of this subpart apply to the owner or operator
of each secondary aluminum production facility as defined in
Sec. 63.1503.
(b) The requirements of this subpart apply to the following affected
sources, located at a secondary aluminum production facility that is a
major source of hazardous air pollutants (HAPs) as defined in Sec. 63.2:
(1) Each new and existing aluminum scrap shredder;
(2) Each new and existing thermal chip dryer;
(3) Each new and existing scrap dryer/delacquering kiln/decoating
kiln;
(4) Each new and existing group 2 furnace;
(5) Each new and existing sweat furnace;
(6) Each new and existing dross-only furnace;
(7) Each new and existing rotary dross cooler; and
(8) Each new and existing secondary aluminum processing unit.
(c) The requirements of this subpart pertaining to dioxin and furan
(D/F) emissions and associated operating, monitoring, reporting and
recordkeeping requirements apply to the following affected sources,
located at a secondary aluminum production facility that is an area
source of HAPs as defined in Sec. 63.2:
(1) Each new and existing thermal chip dryer;
(2) Each new and existing scrap dryer/delacquering kiln/decoating
kiln;
(3) Each new and existing sweat furnace;
(4) Each new and existing secondary aluminum processing unit,
containing one or more group 1 furnace emission units processing other
than clean charge.
(d) The requirements of this subpart do not apply to facilities and
equipment used for research and development that are not used to produce
a saleable product.
(e) The owner or operator of a secondary aluminum production
facility subject to the provisions of this subpart, is subject to the
title V permitting requirements under 40 CFR parts 70 and 71, as
applicable. The permitting authority may defer the affected facility
from the title V permitting requirements until December 9, 2004, if the
secondary aluminum production facility is not a major source and is not
located at a major source as defined under 40 CFR 63.2, 70.2, or 71.2,
and is not otherwise required to obtain a title V permit. If an affected
facility receives a deferral from title V permitting requirements under
this section, the source must submit a title V permit application by
December 9, 2005. The affected facility must continue to comply with the
provisions of this subpart applicable to area sources, even if a
deferral from title V permitting requirements has been granted to the
facility by the permitting authority.
[[Page 53]]
(f) An aluminum die casting facility, aluminum foundry, or aluminum
extrusion facility shall be considered to be an area source if it does
not emit, or have the potential to emit considering controls, 10 tons
per year or more of any single listed HAP or 25 tons per year of any
combination of listed HAP from all emission sources which are located in
a contiguous area and under common control, without regard to whether or
not such sources are regulated under this subpart or any other subpart.
In the case of an aluminum die casting facility, aluminum foundry, or
aluminum extrusion facility which is an area source and is subject to
regulation under this subpart only because it operates a thermal chip
dryer, no furnace operated by such a facility shall be deemed to be
subject to the requirements of this subpart if it melts only clean
charge, internal scrap, or customer returns.
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 79814, Dec. 30, 2002]
Sec. 63.1501 Dates.
(a) The owner or operator of an existing affected source must comply
with the requirements of this subpart by March 24, 2003.
(b) Except as provided in paragraph (c) of this section, the owner
or operator of a new affected source that commences construction or
reconstruction after February 11, 1999 must comply with the requirements
of this subpart by March 24, 2000 or upon startup, whichever is later.
(c) The owner or operator of any affected source which is
constructed or reconstructed at any existing aluminum die casting
facility, aluminum foundry, or aluminum extrusion facility which
otherwise meets the applicability criteria set forth in Sec. 63.1500
must comply with the requirements of this subpart by March 24, 2003 or
upon startup, whichever is later.
[67 FR 59791, Sept. 24, 2002]
Sec. 63.1502 Incorporation by reference.
(a) The following material is incorporated by reference in the
corresponding sections noted. The incorporation by reference (IBR) of
certain publications listed in the rule will be approved by the Director
of the Office of the Federal Register as of the date of publication of
the final rule in accordance with 5 U.S.C. 552(a) and 1 CFR part 51.
This material is incorporated as it exists on the date of approval:
(1) Chapters 3 and 5 of ``Industrial Ventilation: A Manual of
Recommended Practice,'' American Conference of Governmental Industrial
Hygienists, (23rd edition, 1998), IBR approved for Sec. 63.1506(c), and
(2) ``Interim Procedures for Estimating Risks Associated with
Exposures to Mixtures of Chlorinated Dibenzo-p-Dioxins and -
Dibenzofurans (CDDs and CDFs) and 1989 Update'' (EPA/625/3-89/016).
(b) The material incorporated by reference is available for
inspection at the Office of the Federal Register, 800 North Capitol
Street NW, Suite 700, Washington, DC; and at the Air and Radiation
Docket and Information Center, U.S. EPA, 1200 Pennsylvania Ave., NW.,
Washington, DC. The material is also available for purchase from the
following addresses:
(1) Customer Service Department, American Conference of Governmental
Industrial Hygienists (ACGIH), 1330 Kemper Meadow Drive, Cincinnati, OH
45240-1634, telephone number (513) 742-2020; and
(2) The National Technical Information Service (NTIS), 5285 Port
Royal Road, Springfield, VA, NTIS no. PB 90-145756.
Sec. 63.1503 Definitions.
Terms used in this subpart are defined in the Clean Air Act as
amended (CAA), in Sec. 63.2, or in this section as follows:
Add-on air pollution control device means equipment installed on a
process vent that reduces the quantity of a pollutant that is emitted to
the air.
Afterburner means an air pollution control device that uses
controlled flame combustion to convert combustible materials to
noncombustible gases; also known as an incinerator or a thermal
oxidizer.
Aluminum scrap means fragments of aluminum stock removed during
manufacturing (i.e., machining), manufactured aluminum articles or parts
rejected or discarded and useful only as
[[Page 54]]
material for reprocessing, and waste and discarded material made of
aluminum.
Aluminum scrap shredder means a unit that crushes, grinds, or breaks
aluminum scrap into a more uniform size prior to processing or charging
to a scrap dryer/delacquering kiln/decoating kiln, or furnace. A bale
breaker is not an aluminum scrap shredder.
Bag leak detection system means an instrument that is capable of
monitoring particulate matter loadings in the exhaust of a fabric filter
(i.e., baghouse) in order to detect bag failures. A bag leak detection
system includes, but is not limited to, an instrument that operates on
triboelectric, light scattering, light transmittance, or other effect to
monitor relative particulate matter loadings.
Chips means small, uniformly-sized, unpainted pieces of aluminum
scrap, typically below 1\1/4\ inches in any dimension, primarily
generated by turning, milling, boring, and machining of aluminum parts.
Clean charge means furnace charge materials including molten
aluminum, T-bar, sow, ingot, billet, pig, alloying elements, aluminum
scrap known by the owner or operator to be entirely free of paints,
coatings, and lubricants; uncoated/unpainted aluminum chips that have
been thermally dried or treated by a centrifugal cleaner; aluminum scrap
dried at 343 [deg]C (650 [deg]F) or higher; aluminum scrap delacquered/
decoated at 482 [deg]C (900 [deg]F) or higher, and runaround scrap.
Cover flux means salt added to the surface of molten aluminum in a
group 1 or group 2 furnace, without agitation of the molten aluminum,
for the purpose of preventing oxidation.
Customer returns means any aluminum product which is returned by a
customer to the aluminum company that originally manufactured the
product prior to resale of the product or further distribution in
commerce, and which contains no paint or other solid coatings (i.e.,
lacquers).
D/F means dioxins and furans.
Dioxins and furans means tetra-, penta-, hexa-, and octachlorinated
dibenzo dioxins and furans.
Dross means the slags and skimmings from aluminum melting and
refining operations consisting of fluxing agent(s), impurities, and/or
oxidized and non-oxidized aluminum, from scrap aluminum charged into the
furnace.
Dross-only furnace means a furnace, typically of rotary barrel
design, dedicated to the reclamation of aluminum from dross formed
during melting, holding, fluxing, or alloying operations carried out in
other process units. Dross and salt flux are the sole feedstocks to this
type of furnace.
Emission unit means a group 1 furnace or in-line fluxer at a
secondary aluminum production facility.
Fabric filter means an add-on air pollution control device used to
capture particulate matter by filtering gas streams through filter
media; also known as a baghouse.
Feed/charge means, for a furnace or other process unit that operates
in batch mode, the total weight of material (including molten aluminum,
T-bar, sow, ingot, etc.) and alloying agents that enter the furnace
during an operating cycle. For a furnace or other process unit that
operates continuously, feed/charge means the weight of material
(including molten aluminum, T-bar, sow, ingot, etc.) and alloying agents
that enter the process unit within a specified time period (e.g., a time
period equal to the performance test period). The feed/charge for a
dross only furnace includes the total weight of dross and solid flux.
Fluxing means refining of molten aluminum to improve product
quality, achieve product specifications, or reduce material loss,
including the addition of solvents to remove impurities (solvent flux);
and the injection of gases such as chlorine, or chlorine mixtures, to
remove magnesium (demagging) or hydrogen bubbles (degassing). Fluxing
may be performed in the furnace or outside the furnace by an in-line
fluxer.
Furnace hearth means the combustion zone of a furnace in which the
molten metal is contained.
Group 1 furnace means a furnace of any design that melts, holds, or
processes aluminum that contains paint, lubricants, coatings, or other
foreign materials with or without reactive fluxing, or processes clean
charge with reactive fluxing.
[[Page 55]]
Group 2 furnace means a furnace of any design that melts, holds, or
processes only clean charge and that performs no fluxing or performs
fluxing using only nonreactive, non-HAP-containing/non-HAP-generating
gases or agents.
HCl means, for the purposes of this subpart, emissions of hydrogen
chloride that serve as a surrogate measure of the total emissions of the
HAPs hydrogen chloride, hydrogen fluoride and chlorine.
In-line fluxer means a device exterior to a furnace, located in a
transfer line from a furnace, used to refine (flux) molten aluminum;
also known as a flux box, degassing box, or demagging box.
Internal scrap means all aluminum scrap regardless of the level of
contamination which originates from castings or extrusions produced by
an aluminum die casting facility, aluminum foundry, or aluminum
extrusion facility, and which remains at all times within the control of
the company that produced the castings or extrusions.
Internal runaround means scrap material generated on-site by
aluminum extruding, rolling, scalping, forging, forming/stamping,
cutting, and trimming operations that do not contain paint or solid
coatings. Aluminum chips generated by turning, boring, milling, and
similar machining operations that have not been dried at 343 [deg]C (650
[deg]F) or higher, or by an equivalent non-thermal drying process, are
not considered internal runaround.
Lime means calcium oxide or other alkaline reagent.
Lime-injection means the continuous addition of lime upstream of a
fabric filter.
Melting/holding furnace means a group 1 furnace that processes only
clean charge, performs melting, holding, and fluxing functions, and does
not transfer molten aluminum to or from another furnace except for
purposes of alloy changes, off-specification product drains, or
maintenance activities.
Operating cycle means for a batch process, the period beginning when
the feed material is first charged to the operation and ending when all
feed material charged to the operation has been processed. For a batch
melting or holding furnace process, operating cycle means the period
including the charging and melting of scrap aluminum and the fluxing,
refining, alloying, and tapping of molten aluminum (the period from tap-
to-tap).
PM means, for the purposes of this subpart, emissions of particulate
matter that serve as a measure of total particulate emissions and as a
surrogate for metal HAPs contained in the particulates, including but
not limited to, antimony, arsenic, beryllium, cadmium, chromium, cobalt,
lead, manganese, mercury, nickel, and selenium.
Pollution prevention means source reduction as defined under the
Pollution Prevention Act of 1990 (e.g., equipment or technology
modifications, process or procedure modifications, reformulation or
redesign of products, substitution of raw materials, and improvements in
housekeeping, maintenance, training, or inventory control), and other
practices that reduce or eliminate the creation of pollutants through
increased efficiency in the use of raw materials, energy, water, or
other resources, or protection of natural resources by conservation.
Reactive fluxing means the use of any gas, liquid, or solid flux
(other than cover flux) that results in a HAP emission. Argon and
nitrogen are not reactive and do not produce HAP.
Reconstruction means the replacement of components of an affected
source or emission unit such that the fixed capital cost of the new
components exceeds 50 percent of the fixed capital cost that would be
required to construct a comparable new affected source, and it is
technologically and economically feasible for the reconstructed source
to meet relevant standard(s) established in this subpart. Replacement of
the refractory in a furnace is routine maintenance and is not a
reconstruction. The repair and replacement of in-line fluxer components
(e.g., rotors/shafts, burner tubes, refractory, warped steel) is
considered to be routine maintenance and is not considered a
reconstruction. In-line fluxers are typically removed to a maintenance/
repair area and are replaced with repaired units. The replacement of an
existing in-line fluxer with a repaired unit is not considered a
reconstruction.
[[Page 56]]
Residence time means, for an afterburner, the duration of time
required for gases to pass through the afterburner combustion zone.
Residence time is calculated by dividing the afterburner combustion zone
volume in cubic feet by the volumetric flow rate of the gas stream in
actual cubic feet per second.
Rotary dross cooler means a water-cooled rotary barrel device that
accelerates cooling of dross.
Runaround scrap means scrap materials generated on-site by aluminum
casting, extruding, rolling, scalping, forging, forming/stamping,
cutting, and trimming operations and that do not contain paint or solid
coatings. Uncoated/unpainted aluminum chips generated by turning,
boring, milling, and similar machining operations may be clean charge if
they have been thermally dried or treated by a centrifugal cleaner, but
are not considered to be runaround scrap.
Scrap dryer/delacquering kiln/decoating kiln means a unit used
primarily to remove various organic contaminants such as oil, paint,
lacquer, ink, plastic, and/or rubber from aluminum scrap (including used
beverage containers) prior to melting.
Secondary aluminum processing unit (SAPU). An existing SAPU means
all existing group 1 furnaces and all existing in-line fluxers within a
secondary aluminum production facility. Each existing group 1 furnace or
existing in-line fluxer is considered an emission unit within a
secondary aluminum processing unit. A new SAPU means any combination of
individual group 1 furnaces and in-line fluxers within a secondary
aluminum processing facility which either were constructed or
reconstructed after February 11, 1999, or have been permanently
redesignated as new emission units pursuant to Sec. 63.1505(k)(6). Each
of the group 1 furnaces or in-line fluxers within a new SAPU is
considered an emission unit within that secondary aluminum processing
unit.
Secondary aluminum production facility means any establishment using
clean charge, aluminum scrap, or dross from aluminum production, as the
raw material and performing one or more of the following processes:
scrap shredding, scrap drying/delacquering/decoating, thermal chip
drying, furnace operations (i.e., melting, holding, sweating, refining,
fluxing, or alloying), recovery of aluminum from dross, in-line fluxing,
or dross cooling. A secondary aluminum production facility may be
independent or part of a primary aluminum production facility. For
purposes of this subpart, aluminum die casting facilities, aluminum
foundries, and aluminum extrusion facilities are not considered to be
secondary aluminum production facilities if the only materials they melt
are clean charge, customer returns, or internal scrap, and if they do
not operate sweat furnaces, thermal chip dryers, or scrap dryers/
delacquering kilns/decoating kilns. The determination of whether a
facility is a secondary aluminum production facility is only for
purposes of this subpart and any regulatory requirements which are
derived from the applicability of this subpart, and is separate from any
determination which may be made under other environmental laws and
regulations, including whether the same facility is a ``secondary metal
production facility'' as that term is used in 42 U.S.C. Sec. 7479(1) and
40 CFR 52.21(b)(1)(i)(A) (``prevention of significant deterioration of
air quality'').
Sidewell means an open well adjacent to the hearth of a furnace with
connecting arches between the hearth and the open well through which
molten aluminum is circulated between the hearth, where heat is applied
by burners, and the open well, which is used for charging scrap and
solid flux or salt to the furnace, injecting fluxing agents, and
skimming dross.
Sweat furnace means a furnace used exclusively to reclaim aluminum
from scrap that contains substantial quantities of iron by using heat to
separate the low-melting point aluminum from the scrap while the higher
melting-point iron remains in solid form.
TEQ means the international method of expressing toxicity
equivalents for dioxins and furans as defined in ``Interim Procedures
for Estimating Risks Associated with Exposures to Mixtures of
Chlorinated Dibenzo-p-Dioxins and -Dibenzofurans (CDDs and CDFs) and
[[Page 57]]
1989 Update'' (EPA-625/3-89-016), available from the National Technical
Information Service (NTIS), 5285 Port Royal Road, Springfield, Virginia
22161, NTIS no. PB 90-145756.
THC means, for the purposes of this subpart, total hydrocarbon
emissions that also serve as a surrogate for the emissions of organic
HAP compounds.
Thermal chip dryer means a device that uses heat to evaporate oil or
oil/water mixtures from unpainted/uncoated aluminum chips. Pre-heating
boxes or other dryers which are used solely to remove water from
aluminum scrap are not considered to be thermal chip dryers for purposes
of this subpart.
Three-day, 24-hour rolling average means daily calculations of the
average 24-hour emission rate (lbs/ton of feed/charge), over the 3 most
recent consecutive 24-hour periods, for a secondary aluminum processing
unit.
Total reactive chlorine flux injection rate means the sum of the
total weight of chlorine in the gaseous or liquid reactive flux and the
total weight of chlorine in the solid reactive chloride flux, divided by
the total weight of feed/charge, as determined by the procedure in
Sec. 63.1512(o).
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 79814, Dec. 30, 2002]
Sec. 63.1504 [Reserved]
Emission Standards and Operating Requirements
Sec. 63.1505 Emission standards for affected sources and emission units.
(a) Summary. The owner or operator of a new or existing affected
source must comply with each applicable limit in this section. Table 1
to this subpart summarizes the emission standards for each type of
source.
(b) Aluminum scrap shredder. On and after the compliance date
established by Sec. 63.1501, the owner or operator of an aluminum scrap
shredder at a secondary aluminum production facility that is a major
source must not discharge or cause to be discharged to the atmosphere:
(1) Emissions in excess of 0.023 grams (g) of PM per dry standard
cubic meter (dscm) (0.010 grain (gr) of PM per dry standard cubic foot
(dscf)); and
(2) Visible emissions (VE) in excess of 10 percent opacity from any
PM add-on air pollution control device if a continuous opacity monitor
(COM) or visible emissions monitoring is chosen as the monitoring
option.
(c) Thermal chip dryer. On and after the compliance date established
by Sec. 63.1501, the owner or operator of a thermal chip dryer must not
discharge or cause to be discharged to the atmosphere emissions in
excess of:
(1) 0.40 kilogram (kg) of THC, as propane, per megagram (Mg) (0.80
lb of THC, as propane, per ton) of feed/charge from a thermal chip dryer
at a secondary aluminum production facility that is a major source; and
(2) 2.50 micrograms ([mu]g) of D/F TEQ per Mg (3.5 x 10-5
gr per ton) of feed/charge from a thermal chip dryer at a secondary
aluminum production facility that is a major or area source.
(d) Scrap dryer/delacquering kiln/decoating kiln. On and after the
compliance date established by Sec. 63.1501:
(1) The owner or operator of a scrap dryer/delacquering kiln/
decoating kiln must not discharge or cause to be discharged to the
atmosphere emissions in excess of:
(i) 0.03 kg of THC, as propane, per Mg (0.06 lb of THC, as propane,
per ton) of feed/charge from a scrap dryer/delacquering kiln/decoating
kiln at a secondary aluminum production facility that is a major source;
(ii) 0.04 kg of PM per Mg (0.08 lb per ton) of feed/charge from a
scrap dryer/delacquering kiln/decoating kiln at a secondary aluminum
production facility that is a major source;
(iii) 0.25 [mu]g of D/F TEQ per Mg (3.5 x 10-6 gr of D/F
TEQ per ton) of feed/charge from a scrap dryer/delacquering kiln/
decoating kiln at a secondary aluminum production facility that is a
major or area source; and
(iv) 0.40 kg of HCl per Mg (0.80 lb per ton) of feed/charge from a
scrap dryer/delacquering kiln/decoating kiln at a secondary aluminum
production facility that is a major source.
(2) The owner or operator of a scrap dryer/delacquering kiln/
decoating kiln at a secondary aluminum production facility that is a
major source must
[[Page 58]]
not discharge or cause to be discharged to the atmosphere visible
emissions in excess of 10 percent opacity from any PM add-on air
pollution control device if a COM is chosen as the monitoring option.
(e) Scrap dryer/delacquering kiln/decoating kiln: alternative
limits. The owner or operator of a scrap dryer/ delacquering kiln/
decoating kiln may choose to comply with the emission limits in this
paragraph (e) as an alternative to the limits in paragraph (d) of this
section if the scrap dryer/delacquering kiln/decoating kiln is equipped
with an afterburner having a design residence time of at least 1 second
and the afterburner is operated at a temperature of at least 750 [deg]C
(1400 [deg]F) at all times. On and after the compliance date established
by Sec. 63.1501:
(1) The owner or operator of a scrap dryer/delacquering kiln/
decoating kiln must not discharge or cause to be discharged to the
atmosphere emissions in excess of:
(i) 0.10 kg of THC, as propane, per Mg (0.20 lb of THC, as propane,
per ton) of feed/charge from a scrap dryer/delacquering kiln/decoating
kiln at a secondary aluminum production facility that is a major source;
(ii) 0.15 kg of PM per Mg (0.30 lb per ton) of feed/charge from a
scrap dryer/delacquering kiln/decoating kiln at a secondary aluminum
production facility that is a major source;
(iii) 5.0 [mu]g of D/F TEQ per Mg (7.0 x 10-5 gr of D/F
TEQ per ton) of feed/charge from a scrap dryer/delacquering kiln/
decoating kiln at a secondary aluminum production facility that is a
major or area source; and
(iv) 0.75 kg of HCl per Mg (1.50 lb per ton) of feed/charge from a
scrap dryer/delacquering kiln/decoating kiln at a secondary aluminum
production facility that is a major source.
(2) The owner or operator of a scrap dryer/ delacquering kiln/
decoating kiln at a secondary aluminum production facility that is a
major source must not discharge or cause to be discharged to the
atmosphere visible emissions in excess of 10 percent opacity from any PM
add-on air pollution control device if a COM is chosen as the monitoring
option.
(f) Sweat furnace. The owner or operator of a sweat furnace shall
comply with the emission standard of paragraph (f)(2) of this section.
(1) The owner or operator is not required to conduct a performance
test to demonstrate compliance with the emission standard of paragraph
(f)(2) of this section, provided that, on and after the compliance date
of this rule, the owner or operator operates and maintains an
afterburner with a design residence time of 0.8 seconds or greater and
an operating temperature of 1600 [deg]F or greater.
(2) On and after the compliance date established by Sec. 63.1501,
the owner or operator of a sweat furnace at a secondary aluminum
production facility that is a major or area source must not discharge or
cause to be discharged to the atmosphere emissions in excess of 0.80
nanogram (ng) of D/F TEQ per dscm (3.5 x 10-\10\ gr per dscf)
at 11 percent oxygen (O2).
(g) Dross-only furnace. On and after the compliance date established
by Sec. 63.1501, the owner or operator of a dross-only furnace at a
secondary aluminum production facility that is a major source must not
discharge or cause to be discharged to the atmosphere:
(1) Emissions in excess of 0.15 kg of PM per Mg (0.30 lb of PM per
ton) of feed/charge.
(2) Visible emissions in excess of 10 percent opacity from any PM
add-on air pollution control device if a COM is chosen as the monitoring
option.
(h) Rotary dross cooler. On and after the compliance date
established by Sec. 63.1501, the owner or operator of a rotary dross
cooler at a secondary aluminum production facility that is a major
source must not discharge or cause to be discharged to the atmosphere:
(1) Emissions in excess of 0.09 g of PM per dscm (0.04 gr per dscf).
(2) Visible emissions in excess of 10 percent opacity from any PM
add-on air pollution control device if a COM is chosen as the monitoring
option.
(i) Group 1 furnace. The owner or operator of a group 1 furnace must
use the limits in this paragraph to determine the emission standards for
a SAPU.
[[Page 59]]
(1) 0.20 kg of PM per Mg (0.40 lb of PM per ton) of feed/charge from
a group 1 furnace, that is not a melting/holding furnace processing only
clean charge, at a secondary aluminum production facility that is a
major source;
(2) 0.40 kg of PM per Mg (0.80 lb of PM per ton) of feed/charge from
a group 1 melting/holding furnace processing only clean charge at a
secondary aluminum production facility that is a major source;
(3) 15 [mu]g of D/F TEQ per Mg (2.1 x 10-4 gr of D/F TEQ
per ton) of feed/charge from a group 1 furnace at a secondary aluminum
production facility that is a major or area source. This limit does not
apply if the furnace processes only clean charge; and
(4) 0.20 kg of HCl per Mg (0.40 lb of HCl per ton) of feed/charge
or, if the furnace is equipped with an add-on air pollution control
device, 10 percent of the uncontrolled HCl emissions, by weight, for a
group 1 furnace at a secondary aluminum production facility that is a
major source.
(5) The owner or operator of a group 1 furnace at a secondary
aluminum production facility that is a major source must not discharge
or cause to be discharged to the atmosphere visible emissions in excess
of 10 percent opacity from any PM add-on air pollution control device if
a COM is chosen as the monitoring option.
(6) The owner or operator may determine the emission standards for a
SAPU by applying the group 1 furnace limits on the basis of the aluminum
production weight in each group 1 furnace, rather than on the basis of
feed/charge.
(7) The owner or operator of a sidewell group 1 furnace that
conducts reactive fluxing (except for cover flux) in the hearth, or that
conducts reactive fluxing in the sidewell at times when the level of
molten metal falls below the top of the passage between the sidewell and
the hearth, must comply with the emission limits of paragraphs (i)(1)
through (4) of this section on the basis of the combined emissions from
the sidewell and the hearth.
(j) In-line fluxer. Except as provided in paragraph (j)(3) of this
section for an in-line fluxer using no reactive flux material, the owner
or operator of an in-line fluxer must use the limits in this paragraph
to determine the emission standards for a SAPU.
(1) 0.02 kg of HCl per Mg (0.04 lb of HCl per ton) of feed/charge;
(2) 0.005 kg of PM per Mg (0.01 lb of PM per ton) of feed/charge.
(3) The emission limits in paragraphs (j)(1) and (j)(2) of this
section do not apply to an in-line fluxer that uses no reactive flux
materials.
(4) The owner or operator of an in-line fluxer at a secondary
aluminum production facility that is a major source must not discharge
or cause to be discharged to the atmosphere visible emissions in excess
of 10 percent opacity from any PM add-on air pollution control device
used to control emissions from the in-line fluxer, if a COM is chosen as
the monitoring option.
(5) The owner or operator may determine the emission standards for a
SAPU by applying the in-line fluxer limits on the basis of the aluminum
production weight in each in-line fluxer, rather than on the basis of
feed/charge.
(k) Secondary aluminum processing unit. On and after the compliance
date established by Sec. 63.1501, the owner or operator must comply with
the emission limits calculated using the equations for PM and HCl in
paragraphs (k)(1) and (2) of this section for each secondary aluminum
processing unit at a secondary aluminum production facility that is a
major source. The owner or operator must comply with the emission limit
calculated using the equation for D/F in paragraph (k)(3) of this
section for each secondary aluminum processing unit at a secondary
aluminum production facility that is a major or area source.
(1) The owner or operator must not discharge or allow to be
discharged to the atmosphere any 3-day, 24-hour rolling average
emissions of PM in excess of:
[GRAPHIC] [TIFF OMITTED] TR23MR00.000
Where,
[[Page 60]]
LtiPM = The PM emission limit for individual emission unit i
in paragraph (i)(1) and (2) of this section for a group 1 furnace or in
paragraph (j)(2) of this section for an in-line fluxer;
Tti = The feed/charge rate for individual emission unit I;
and
LcPM = The PM emission limit for the secondary aluminum
processing unit.
Note: In-line fluxers using no reactive flux materials cannot be
included in this calculation since they are not subject to the PM limit.
(2) The owner or operator must not discharge or allow to be
discharged to the atmosphere any 3-day, 24-hour rolling average
emissions of HCl in excess of:
[GRAPHIC] [TIFF OMITTED] TR30DE02.001
Where,
LtiHCl = The HCl emission limit for individual emission unit
i in paragraph (i)(4) of this section for a group 1 furnace or in
paragraph (j)(1) of this section for an in-line fluxer; and
LcHCl = The HCl emission limit for the secondary aluminum
processing unit.
Note: In-line fluxers using no reactive flux materials cannot be
included in this calculation since they are not subject to the HCl
limit.
(3) The owner or operator must not discharge or allow to be
discharged to the atmosphere any 3-day, 24-hour rolling average
emissions of D/F in excess of:
[GRAPHIC] [TIFF OMITTED] TR23MR00.002
Where,
LtiD/F = The D/F emission limit for individual emission unit
i in paragraph (i)(3) of this section for a group 1 furnace; and
LcD/F = The D/F emission limit for the secondary aluminum
processing unit.
Note: Clean charge furnaces cannot be included in this calculation
since they are not subject to the D/F limit.
(4) The owner or operator of a SAPU at a secondary aluminum
production facility that is a major source may demonstrate compliance
with the emission limits of paragraphs (k)(1) through (3) of this
section by demonstrating that each emission unit within the SAPU is in
compliance with the applicable emission limits of paragraphs (i) and (j)
of this section.
(5) The owner or operator of a SAPU at a secondary aluminum
production facility that is an area source may demonstrate compliance
with the emission limits of paragraph (k)(3) of this section by
demonstrating that each emission unit within the SAPU is in compliance
with the emission limit of paragraph (i)(3) of this section.
(6) With the prior approval of the responsible permitting authority,
an owner or operator may redesignate any existing group 1 furnace or in-
line fluxer at a secondary aluminum production facility as a new
emission unit. Any emission unit so redesignated may thereafter be
included in a new SAPU at that facility. Any such redesignation will be
solely for the purpose of this MACT standard and will be irreversible.
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 59792, Sept. 24, 2002;
67 FR 79816, Dec. 30, 2002]
Sec. 63.1506 Operating requirements.
(a) Summary. (1) On and after the compliance date established by
Sec. 63.1501, the owner or operator must operate all new and existing
affected sources and control equipment according to the requirements in
this section.
(2) The owner or operator of an existing sweat furnace that meets
the specifications of Sec. 63.1505(f)(1) must operate the sweat furnace
and control equipment according to the requirements of this section on
and after the compliance date of this standard.
(3) The owner or operator of a new sweat furnace that meets the
specifications of Sec. 63.1505(f)(1) must operate the sweat furnace and
control equipment according to the requirements of this section by March
23, 2000 or upon startup, whichever is later.
(4) Operating requirements are summarized in Table 2 to this
subpart.
[[Page 61]]
(b) Labeling. The owner or operator must provide and maintain easily
visible labels posted at each group 1 furnace, group 2 furnace, in-line
fluxer and scrap dryer/delacquering kiln/decoating kiln that identifies
the applicable emission limits and means of compliance, including:
(1) The type of affected source or emission unit (e.g., scrap dryer/
delacquering kiln/decoating kiln, group 1 furnace, group 2 furnace, in-
line fluxer).
(2) The applicable operational standard(s) and control method(s)
(work practice or control device). This includes, but is not limited to,
the type of charge to be used for a furnace (e.g., clean scrap only, all
scrap, etc.), flux materials and addition practices, and the applicable
operating parameter ranges and requirements as incorporated in the OM&M
plan.
(3) The afterburner operating temperature and design residence time
for a scrap dryer/delacquering kiln/decoating kiln.
(c) Capture/collection systems. For each affected source or emission
unit equipped with an add-on air pollution control device, the owner or
operator must:
(1) Design and install a system for the capture and collection of
emissions to meet the engineering standards for minimum exhaust rates as
published by the American Conference of Governmental Industrial
Hygienists in chapters 3 and 5 of ``Industrial Ventilation: A Manual of
Recommended Practice'' (incorporated by reference in Sec. 63.1502 of
this subpart);
(2) Vent captured emissions through a closed system, except that
dilution air may be added to emission streams for the purpose of
controlling temperature at the inlet to a fabric filter; and
(3) Operate each capture/collection system according to the
procedures and requirements in the OM&M plan.
(d) Feed/charge weight. The owner or operator of each affected
source or emission unit subject to an emission limit in kg/Mg (lb/ton)
of feed/charge must:
(1) Except as provided in paragraph (d)(3) of this section, install
and operate a device that measures and records or otherwise determine
the weight of feed/charge (or throughput) for each operating cycle or
time period used in the performance test; and
(2) Operate each weight measurement system or other weight
determination procedure in accordance with the OM&M plan.
(3) The owner or operator may chose to measure and record aluminum
production weight from an affected source or emission unit rather than
feed/charge weight to an affected source or emission unit, provided
that:
(i) The aluminum production weight, rather than feed/charge weight
is measured and recorded for all emission units within a SAPU; and
(ii) All calculations to demonstrate compliance with the emission
limits for SAPUs are based on aluminum production weight rather than
feed/charge weight.
(e) Aluminum scrap shredder. The owner or operator of a scrap
shredder with emissions controlled by a fabric filter must operate a bag
leak detection system, or a continuous opacity monitor, or conduct
visible emissions observations.
(1) If a bag leak detection system is used to meet the monitoring
requirements in Sec. 63.1510, the owner or operator must:
(i) Initiate corrective action within 1-hour of a bag leak detection
system alarm and complete the corrective action procedures in accordance
with the OM&M plan.
(ii) Operate each fabric filter system such that the bag leak
detection system alarm does not sound more than 5 percent of the
operating time during a 6-month block reporting period. In calculating
this operating time fraction, if inspection of the fabric filter
demonstrates that no corrective action is required, no alarm time is
counted. If corrective action is required, each alarm shall be counted
as a minimum of 1 hour. If the owner or operator takes longer than 1
hour to initiate corrective action, the alarm time shall be counted as
the actual amount of time taken by the owner or operator to initiate
corrective action.
(2) If a continuous opacity monitoring system is used to meet the
monitoring requirements in Sec. 63.1510, the
[[Page 62]]
owner or operator must initiate corrective action within 1-hour of any
6-minute average reading of 5 percent or more opacity and complete the
corrective action procedures in accordance with the OM&M plan.
(3) If visible emission observations are used to meet the monitoring
requirements in Sec. 63.1510, the owner or operator must initiate
corrective action within 1-hour of any observation of visible emissions
during a daily visible emissions test and complete the corrective action
procedures in accordance with the OM&M plan.
(f) Thermal chip dryer. The owner or operator of a thermal chip
dryer with emissions controlled by an afterburner must:
(1) Maintain the 3-hour block average operating temperature of each
afterburner at or above the average temperature established during the
performance test.
(2) Operate each afterburner in accordance with the OM&M plan.
(3) Operate each thermal chip dryer using only unpainted aluminum
chips as the feedstock.
(g) Scrap dryer/delacquering kiln/decoating kiln. The owner or
operator of a scrap dryer/delacquering kiln/decoating kiln with
emissions controlled by an afterburner and a lime-injected fabric filter
must:
(1) For each afterburner,
(i) Maintain the 3-hour block average operating temperature of each
afterburner at or above the average temperature established during the
performance test.
(ii) Operate each afterburner in accordance with the OM&M plan.
(2) If a bag leak detection system is used to meet the fabric filter
monitoring requirements in Sec. 63.1510,
(i) Initiate corrective action within 1-hour of a bag leak detection
system alarm and complete any necessary corrective action procedures in
accordance with the OM&M plan.
(ii) Operate each fabric filter system such that the bag leak
detection system alarm does not sound more than 5 percent of the
operating time during a 6-month block reporting period. In calculating
this operating time fraction, if inspection of the fabric filter
demonstrates that no corrective action is required, no alarm time is
counted. If corrective action is required, each alarm shall be counted
as a minimum of 1 hour. If the owner or operator takes longer than 1
hour to initiate corrective action, the alarm time shall be counted as
the actual amount of time taken by the owner or operator to initiate
corrective action.
(3) If a continuous opacity monitoring system is used to meet the
monitoring requirements in Sec. 63.1510, initiate corrective action
within 1-hour of any 6-minute average reading of 5 percent or more
opacity and complete the corrective action procedures in accordance with
the OM&M plan.
(4) Maintain the 3-hour block average inlet temperature for each
fabric filter at or below the average temperature established during the
performance test, plus 14 [deg]C (plus 25 [deg]F).
(5) For a continuous injection device, maintain free-flowing lime in
the hopper to the feed device at all times and maintain the lime feeder
setting at the same level established during the performance test.
(h) Sweat furnace. The owner or operator of a sweat furnace with
emissions controlled by an afterburner must:
(1) Maintain the 3-hour block average operating temperature of each
afterburner at or above:
(i) The average temperature established during the performance test;
or
(ii) 1600 [deg]F if a performance test was not conducted, and the
afterburner meets the specifications of Sec. 63.1505(f)(1).
(2) Operate each afterburner in accordance with the OM&M plan.
(i) Dross-only furnace. The owner or operator of a dross-only
furnace with emissions controlled by a fabric filter must:
(1) If a bag leak detection system is used to meet the monitoring
requirements in Sec. 63.1510,
(i) Initiate corrective action within 1-hour of a bag leak detection
system alarm and complete the corrective action procedures in accordance
with the OM&M plan.
(ii) Operate each fabric filter system such that the bag leak
detection system alarm does not sound more than 5 percent of the
operating time during a
[[Page 63]]
6-month block reporting period. In calculating this operating time
fraction, if inspection of the fabric filter demonstrates that no
corrective action is required, no alarm time is counted. If corrective
action is required, each alarm shall be counted as a minimum of 1 hour.
If the owner or operator takes longer than 1 hour to initiate corrective
action, the alarm time shall be counted as the actual amount of time
taken by the owner or operator to initiate corrective action.
(2) If a continuous opacity monitoring system is used to meet the
monitoring requirements in Sec. 63.1510, initiate corrective action
within 1-hour of any 6-minute average reading of 5 percent or more
opacity and complete the corrective action procedures in accordance with
the OM&M plan.
(3) Operate each furnace using dross as the sole feedstock.
(j) Rotary dross cooler. The owner or operator of a rotary dross
cooler with emissions controlled by a fabric filter must:
(1) If a bag leak detection system is used to meet the monitoring
requirements in Sec. 63.1510,
(i) Initiate corrective action within 1-hour of a bag leak detection
system alarm and complete the corrective action procedures in accordance
with the OM&M plan.
(ii) Operate each fabric filter system such that the bag leak
detection system alarm does not sound more than 5 percent of the
operating time during a 6-month block reporting period. In calculating
this operating time fraction, if inspection of the fabric filter
demonstrates that no corrective action is required, no alarm time is
counted. If corrective action is required, each alarm shall be counted
as a minimum of 1 hour. If the owner or operator takes longer than 1
hour to initiate corrective action, the alarm time shall be counted as
the actual amount of time taken by the owner or operator to initiate
corrective action.
(2) If a continuous opacity monitoring system is used to meet the
monitoring requirements in Sec. 63.1510, initiate corrective action
within 1 hour of any 6-minute average reading of 5 percent or more
opacity and complete the corrective action procedures in accordance with
the OM&M plan.
(k) In-line fluxer. The owner or operator of an in-line fluxer with
emissions controlled by a lime-injected fabric filter must:
(1) If a bag leak detection system is used to meet the monitoring
requirements in Sec. 63.1510,
(i) Initiate corrective action within 1-hour of a bag leak detection
system alarm and complete the corrective action procedures in accordance
with the OM&M plan.
(ii) Operate each fabric filter system such that the bag leak
detection system alarm does not sound more than 5 percent of the
operating time during a 6-month block reporting period. In calculating
this operating time fraction, if inspection of the fabric filter
demonstrates that no corrective action is required, no alarm time is
counted. If corrective action is required, each alarm shall be counted
as a minimum of 1 hour. If the owner or operator takes longer than 1
hour to initiate corrective action, the alarm time shall be counted as
the actual amount of time taken by the owner or operator to initiate
corrective action.
(2) If a continuous opacity monitoring system is used to meet the
monitoring requirements in Sec. 63.1510, initiate corrective action
within 1 hour of any 6-minute average reading of 5 percent or more
opacity and complete the corrective action procedures in accordance with
the OM&M plan.
(3) For a continuous injection system, maintain free-flowing lime in
the hopper to the feed device at all times and maintain the lime feeder
setting at the same level established during the performance test.
(4) Maintain the total reactive chlorine flux injection rate for
each operating cycle or time period used in the performance test at or
below the average rate established during the performance test.
(l) In-line fluxer using no reactive flux material. The owner or
operator of a new or existing in-line fluxer using no reactive flux
materials must operate each in-line fluxer using no reactive flux
materials.
(m) Group 1 furnace with add-on air pollution control devices. The
owner or
[[Page 64]]
operator of a group 1 furnace with emissions controlled by a lime-
injected fabric filter must:
(1) If a bag leak detection system is used to meet the monitoring
requirements in Sec. 63.1510, the owner or operator must:
(i) Initiate corrective action within 1 hour of a bag leak detection
system alarm.
(ii) Complete the corrective action procedures in accordance with
the OM&M plan.
(iii) Operate each fabric filter system such that the bag leak
detection system alarm does not sound more than 5 percent of the
operating time during a 6-month block reporting period. In calculating
this operating time fraction, if inspection of the fabric filter
demonstrates that no corrective action is required, no alarm time is
counted. If corrective action is required, each alarm shall be counted
as a minimum of 1 hour. If the owner or operator takes longer than 1
hour to initiate corrective action, the alarm time shall be counted as
the actual amount of time taken by the owner or operator to initiate
corrective action.
(2) If a continuous opacity monitoring system is used to meet the
monitoring requirements in Sec. 63.1510, the owner or operator must:
(i) Initiate corrective action within 1 hour of any 6-minute average
reading of 5 percent or more opacity; and
(ii) Complete the corrective action procedures in accordance with
the OM&M plan.
(3) Maintain the 3-hour block average inlet temperature for each
fabric filter at or below the average temperature established during the
performance test, plus 14 [deg]C (plus 25 [deg]F).
(4) For a continuous lime injection system, maintain free-flowing
lime in the hopper to the feed device at all times and maintain the lime
feeder setting at the same level established during the performance
test.
(5) Maintain the total reactive chlorine flux injection rate for
each operating cycle or time period used in the performance test at or
below the average rate established during the performance test.
(6) Operate each sidewell furnace such that:
(i) The level of molten metal remains above the top of the passage
between the sidewell and hearth during reactive flux injection, unless
emissions from both the sidewell and the hearth are included in
demonstrating compliance with all applicable emission limits.
(ii) Reactive flux is added only in the sidewell, unless emissions
from both the sidewell and the hearth are included in demonstrating
compliance with all applicable emission limits.
(n) Group 1 furnace without add-on air pollution control devices.
The owner or operator of a group 1 furnace (including a group 1 furnace
that is part of a secondary aluminum processing unit) without add-on air
pollution control devices must:
(1) Maintain the total reactive chlorine flux injection rate for
each operating cycle or time period used in the performance test at or
below the average rate established during the performance test.
(2) Operate each furnace in accordance with the work practice/
pollution prevention measures documented in the OM&M plan and within the
parameter values or ranges established in the OM&M plan.
(3) Operate each group 1 melting/holding furnace subject to the
emission standards in Sec. 63.1505(i)(2) using only clean charge as the
feedstock.
(o) Group 2 furnace. The owner or operator of a new or existing
group 2 furnace must:
(1) Operate each furnace using only clean charge as the feedstock.
(2) Operate each furnace using no reactive flux.
(p) Corrective action. When a process parameter or add-on air
pollution control device operating parameter deviates from the value or
range established during the performance test and incorporated in the
OM&M plan, the owner or operator must initiate corrective action.
Corrective action must restore operation of the affected source or
emission unit (including the process or control device) to its normal or
usual mode of operation as expeditiously as practicable in accordance
with good air pollution control practices for minimizing emissions.
Corrective actions taken must include follow-up actions necessary to
return the
[[Page 65]]
process or control device parameter level(s) to the value or range of
values established during the performance test and steps to prevent the
likely recurrence of the cause of a deviation.
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 59792, Sept. 24, 2002;
67 FR 79816, Dec. 30, 2002]
Secs. 63.1507-63.1509 [Reserved]
Monitoring and Compliance Requirements
Sec. 63.1510 Monitoring requirements.
(a) Summary. On and after the compliance date established by
Sec. 63.1501, the owner or operator of a new or existing affected source
or emission unit must monitor all control equipment and processes
according to the requirements in this section. Monitoring requirements
for each type of affected source and emission unit are summarized in
Table 3 to this subpart.
(b) Operation, maintenance, and monitoring (OM&M) plan. The owner or
operator must prepare and implement for each new or existing affected
source and emission unit, a written operation, maintenance, and
monitoring (OM&M) plan. The owner or operator of an existing affected
source must submit the OM&M plan to the responsible permitting authority
no later than the compliance date established by Sec. 63.1501(a). The
owner or operator of any new affected source must submit the OM&M plan
to the responsible permitting authority within 90 days after a
successful initial performance test under Sec. 63.1511(b), or within 90
days after the compliance date established by Sec. 63.1501(b) if no
initial performance test is required. The plan must be accompanied by a
written certification by the owner or operator that the OM&M plan
satisfies all requirements of this section and is otherwise consistent
with the requirements of this subpart. The owner or operator must comply
with all of the provisions of the OM&M plan as submitted to the
permitting authority, unless and until the plan is revised in accordance
with the following procedures. If the permitting authority determines at
any time after receipt of the OM&M plan that any revisions of the plan
are necessary to satisfy the requirements of this section or this
subpart, the owner or operator must promptly make all necessary
revisions and resubmit the revised plan. If the owner or operator
determines that any other revisions of the OM&M plan are necessary, such
revisions will not become effective until the owner or operator submits
a description of the changes and a revised plan incorporating them to
the permitting authority. Each plan must contain the following
information:
(1) Process and control device parameters to be monitored to
determine compliance, along with established operating levels or ranges,
as applicable, for each process and control device.
(2) A monitoring schedule for each affected source and emission
unit.
(3) Procedures for the proper operation and maintenance of each
process unit and add-on control device used to meet the applicable
emission limits or standards in Sec. 63.1505.
(4) Procedures for the proper operation and maintenance of
monitoring devices or systems used to determine compliance, including:
(i) Calibration and certification of accuracy of each monitoring
device, at least once every 6 months, according to the manufacturer's
instructions; and
(ii) Procedures for the quality control and quality assurance of
continuous emission or opacity monitoring systems as required by the
general provisions in subpart A of this part.
(5) Procedures for monitoring process and control device parameters,
including procedures for annual inspections of afterburners, and if
applicable, the procedure to be used for determining charge/feed (or
throughput) weight if a measurement device is not used.
(6) Corrective actions to be taken when process or operating
parameters or add-on control device parameters deviate from the value or
range established in paragraph (b)(1) of this section, including:
(i) Procedures to determine and record the cause of an deviation or
excursion, and the time the deviation or excursion began and ended; and
(ii) Procedures for recording the corrective action taken, the time
corrective action was initiated, and the time/date corrective action was
completed.
[[Page 66]]
(7) A maintenance schedule for each process and control device that
is consistent with the manufacturer's instructions and recommendations
for routine and long-term maintenance.
(8) Documentation of the work practice and pollution prevention
measures used to achieve compliance with the applicable emission limits
and a site-specific monitoring plan as required in paragraph (o) of this
section for each group 1 furnace not equipped with an add-on air
pollution control device.
(c) Labeling. The owner or operator must inspect the labels for each
group 1 furnace, group 2 furnace, in-line fluxer and scrap dryer/
delacquering kiln/decoating kiln at least once per calendar month to
confirm that posted labels as required by the operational standard in
Sec. 63.1506(b) are intact and legible.
(d) Capture/collection system. The owner or operator must:
(1) Install, operate, and maintain a capture/collection system for
each affected source and emission unit equipped with an add-on air
pollution control device; and
(2) Inspect each capture/collection and closed vent system at least
once each calendar year to ensure that each system is operating in
accordance with the operating requirements in Sec. 63.1506(c) and record
the results of each inspection.
(e) Feed/charge weight. The owner or operator of an affected source
or emission unit subject to an emission limit in kg/Mg (lb/ton) or
[mu]g/Mg (gr/ton) of feed/charge must install, calibrate, operate, and
maintain a device to measure and record the total weight of feed/charge
to, or the aluminum production from, the affected source or emission
unit over the same operating cycle or time period used in the
performance test. Feed/charge or aluminum production within SAPUs must
be measured and recorded on an emission unit-by-emission unit basis. As
an alternative to a measurement device, the owner or operator may use a
procedure acceptable to the applicable permitting authority to determine
the total weight of feed/charge or aluminum production to the affected
source or emission unit.
(1) The accuracy of the weight measurement device or procedure must
be [plusmn]1 percent of the weight being measured. The owner or operator
may apply to the permitting agency for approval to use a device of
alternative accuracy if the required accuracy cannot be achieved as a
result of equipment layout or charging practices. A device of
alternative accuracy will not be approved unless the owner or operator
provides assurance through data and information that the affected source
will meet the relevant emission standard.
(2) The owner or operator must verify the calibration of the weight
measurement device in accordance with the schedule specified by the
manufacturer, or if no calibration schedule is specified, at least once
every 6 months.
(f) Fabric filters and lime-injected fabric filters. The owner or
operator of an affected source or emission unit using a fabric filter or
lime-injected fabric filter to comply with the requirements of this
subpart must install, calibrate, maintain, and continuously operate a
bag leak detection system as required in paragraph (f)(1) of this
section or a continuous opacity monitoring system as required in
paragraph (f)(2) of this section. The owner or operator of an aluminum
scrap shredder must install and operate a bag leak detection system as
required in paragraph (f)(1) of this section, install and operate a
continuous opacity monitoring system as required in paragraph (f)(2) of
this section, or conduct visible emission observations as required in
paragraph (f)(3) of this section.
(1) These requirements apply to the owner or operator of a new or
existing affected source or existing emission unit using a bag leak
detection system.
(i) The owner or operator must install and operate a bag leak
detection system for each exhaust stack of a fabric filter.
(ii) Each triboelectric bag leak detection system must be installed,
calibrated, operated, and maintained according to the ``Fabric Filter
Bag Leak Detection Guidance,'' (September 1997). This document is
available from the U.S. Environmental Protection Agency; Office of Air
Quality Planning and Standards; Emissions, Monitoring and
[[Page 67]]
Analysis Division; Emission Measurement Center (MD-19), Research
Triangle Park, NC 27711. This document also is available on the
Technology Transfer Network (TTN) under Emission Measurement Technical
Information (EMTIC), Continuous Emission Monitoring. Other bag leak
detection systems must be installed, operated, calibrated, and
maintained in a manner consistent with the manufacturer's written
specifications and recommendations.
(iii) The bag leak detection system must be certified by the
manufacturer to be capable of detecting PM emissions at concentrations
of 10 milligrams per actual cubic meter (0.0044 grains per actual cubic
foot) or less.
(iv) The bag leak detection system sensor must provide output of
relative or absolute PM loadings.
(v) The bag leak detection system must be equipped with a device to
continuously record the output signal from the sensor.
(vi) The bag leak detection system must be equipped with an alarm
system that will sound automatically when an increase in relative PM
emissions over a preset level is detected. The alarm must be located
where it is easily heard by plant operating personnel.
(vii) For positive pressure fabric filter systems, a bag leak
detection system must be installed in each baghouse compartment or cell.
For negative pressure or induced air fabric filters, the bag leak
detector must be installed downstream of the fabric filter.
(viii) Where multiple detectors are required, the system's
instrumentation and alarm may be shared among detectors.
(ix) The baseline output must be established by adjusting the range
and the averaging period of the device and establishing the alarm set
points and the alarm delay time.
(x) Following initial adjustment of the system, the owner or
operator must not adjust the sensitivity or range, averaging period,
alarm set points, or alarm delay time except as detailed in the OM&M
plan. In no case may the sensitivity be increased by more than 100
percent or decreased more than 50 percent over a 365-day period unless
such adjustment follows a complete fabric filter inspection which
demonstrates that the fabric filter is in good operating condition.
(2) These requirements apply to the owner or operator of a new or
existing affected source or an existing emission unit using a continuous
opacity monitoring system.
(i) The owner or operator must install, calibrate, maintain, and
operate a continuous opacity monitoring system to measure and record the
opacity of emissions exiting each exhaust stack.
(ii) Each continuous opacity monitoring system must meet the design
and installation requirements of Performance Specification 1 in appendix
B to 40 CFR part 60.
(3) These requirements apply to the owner or operator of a new or
existing aluminum scrap shredder who conducts visible emission
observations. The owner or operator must:
(i) Perform a visible emissions test for each aluminum scrap
shredder using a certified observer at least once a day according to the
requirements of Method 9 in appendix A to 40 CFR part 60. Each Method 9
test must consist of five 6-minute observations in a 30-minute period;
and
(ii) Record the results of each test.
(g) Afterburner. These requirements apply to the owner or operator
of an affected source using an afterburner to comply with the
requirements of this subpart.
(1) The owner or operator must install, calibrate, maintain, and
operate a device to continuously monitor and record the operating
temperature of the afterburner consistent with the requirements for
continuous monitoring systems in subpart A of this part.
(2) The temperature monitoring device must meet each of these
performance and equipment specifications:
(i) The temperature monitoring device must be installed at the exit
of the combustion zone of each afterburner.
(ii) The monitoring system must record the temperature in 15-minute
block averages and determine and record the average temperature for each
3-hour block period.
[[Page 68]]
(iii) The recorder response range must include zero and 1.5 times
the average temperature established according to the requirements in
Sec. 63.1512(m).
(iv) The reference method must be a National Institute of Standards
and Technology calibrated reference thermocouple-potentiometer system or
alternate reference, subject to approval by the Administrator.
(3) The owner or operator must conduct an inspection of each
afterburner at least once a year and record the results. At a minimum,
an inspection must include:
(i) Inspection of all burners, pilot assemblies, and pilot sensing
devices for proper operation and clean pilot sensor;
(ii) Inspection for proper adjustment of combustion air;
(iii) Inspection of internal structures (e.g., baffles) to ensure
structural integrity;
(iv) Inspection of dampers, fans, and blowers for proper operation;
(v) Inspection for proper sealing;
(vi) Inspection of motors for proper operation;
(vii) Inspection of combustion chamber refractory lining and clean
and replace lining as necessary;
(viii) Inspection of afterburner shell for corrosion and/or hot
spots;
(ix) Documentation, for the burn cycle that follows the inspection,
that the afterburner is operating properly and any necessary adjustments
have been made; and
(x) Verification that the equipment is maintained in good operating
condition.
(xi) Following an equipment inspection, all necessary repairs must
be completed in accordance with the requirements of the OM&M plan.
(h) Fabric filter inlet temperature. These requirements apply to the
owner or operator of a scrap dryer/delacquering kiln/decoating kiln or a
group 1 furnace using a lime-injected fabric filter to comply with the
requirements of this subpart.
(1) The owner or operator must install, calibrate, maintain, and
operate a device to continuously monitor and record the temperature of
the fabric filter inlet gases consistent with the requirements for
continuous monitoring systems in subpart A of this part.
(2) The temperature monitoring device must meet each of these
performance and equipment specifications:
(i) The monitoring system must record the temperature in 15-minute
block averages and calculate and record the average temperature for each
3-hour block period.
(ii) The recorder response range must include zero and 1.5 times the
average temperature established according to the requirements in
Sec. 63.1512(n).
(iii) The reference method must be a National Institute of Standards
and Technology calibrated reference thermocouple-potentiometer system or
alternate reference, subject to approval by the Administrator.
(i) Lime injection. These requirements apply to the owner or
operator of an affected source or emission unit using a lime-injected
fabric filter to comply with the requirements of this subpart.
(1) The owner or operator of a continuous lime injection system must
verify that lime is always free-flowing by either:
(i) Inspecting each feed hopper or silo at least once each 8-hour
period and recording the results of each inspection. If lime is found
not to be free-flowing during any of the 8-hour periods, the owner or
operator must increase the frequency of inspections to at least once
every 4-hour period for the next 3 days. The owner or operator may
return to inspections at least once every 8 hour period if corrective
action results in no further blockages of lime during the 3-day period;
or
(ii) Subject to the approval of the permitting agency, installing,
operating and maintaining a load cell, carrier gas/lime flow indicator,
carrier gas pressure drop measurement system or other system to confirm
that lime is free-flowing. If lime is found not to be free-flowing, the
owner or operator must promptly initiate and complete corrective action,
or
(iii) Subject to the approval of the permitting agency, installing,
operating and maintaining a device to monitor the concentration of HCl
at the outlet of the fabric filter. If an increase in the concentration
of HCl indicates that the lime is not free-flowing, the
[[Page 69]]
owner or operator must promptly initiate and complete corrective action.
(2) The owner or operator of a continuous lime injection system must
record the lime feeder setting once each day of operation.
(3) An owner or operator who intermittently adds lime to a lime
coated fabric filter must obtain approval from the permitting authority
for a lime addition monitoring procedure. The permitting authority will
not approve a monitoring procedure unless data and information are
submitted establishing that the procedure is adequate to ensure that
relevant emission standards will be met on a continuous basis.
(j) Total reactive flux injection rate. These requirements apply to
the owner or operator of a group 1 furnace (with or without add-on air
pollution control devices) or in-line fluxer. The owner or operator
must:
(1) Install, calibrate, operate, and maintain a device to
continuously measure and record the weight of gaseous or liquid reactive
flux injected to each affected source or emission unit.
(i) The monitoring system must record the weight for each 15-minute
block period, during which reactive fluxing occurs, over the same
operating cycle or time period used in the performance test.
(ii) The accuracy of the weight measurement device must be [plusmn]1
percent of the weight of the reactive component of the flux being
measured. The owner or operator may apply to the permitting authority
for permission to use a weight measurement device of alternative
accuracy in cases where the reactive flux flow rates are so low as to
make the use of a weight measurement device of [plusmn]1 percent
impracticable. A device of alternative accuracy will not be approved
unless the owner or operator provides assurance through data and
information that the affected source will meet the relevant emission
standards.
(iii) The owner or operator must verify the calibration of the
weight measurement device in accordance with the schedule specified by
the manufacturer, or if no calibration schedule is specified, at least
once every 6 months.
(2) Calculate and record the gaseous or liquid reactive flux
injection rate (kg/Mg or lb/ton) for each operating cycle or time period
used in the performance test using the procedure in Sec. 63.1512(o).
(3) Record, for each 15-minute block period during each operating
cycle or time period used in the performance test during which reactive
fluxing occurs, the time, weight, and type of flux for each addition of:
(i) Gaseous or liquid reactive flux other than chlorine; and
(ii) Solid reactive flux.
(4) Calculate and record the total reactive flux injection rate for
each operating cycle or time period used in the performance test using
the procedure in Sec. 63.1512(o).
(5) The owner or operator of a group 1 furnace or in-line fluxer
performing reactive fluxing may apply to the Administrator for approval
of an alternative method for monitoring and recording the total reactive
flux addition rate based on monitoring the weight or quantity of
reactive flux per ton of feed/charge for each operating cycle or time
period used in the performance test. An alternative monitoring method
will not be approved unless the owner or operator provides assurance
through data and information that the affected source will meet the
relevant emission standards on a continuous basis.
(k) Thermal chip dryer. These requirements apply to the owner or
operator of a thermal chip dryer with emissions controlled by an
afterburner. The owner or operator must:
(1) Record the type of materials charged to the unit for each
operating cycle or time period used in the performance test.
(2) Submit a certification of compliance with the applicable
operational standard for charge materials in Sec. 63.1506(f)(3) for each
6-month reporting period. Each certification must contain the
information in Sec. 63.1516(b)(2)(i).
(l) Dross-only furnace. These requirements apply to the owner or
operator of a dross-only furnace. The owner or operator must:
(1) Record the materials charged to each unit for each operating
cycle or
[[Page 70]]
time period used in the performance test.
(2) Submit a certification of compliance with the applicable
operational standard for charge materials in Sec. 63.1506(i)(3) for each
6-month reporting period. Each certification must contain the
information in Sec. 63.1516(b)(2)(ii).
(m) In-line fluxers using no reactive flux. The owner or operator of
an in-line fluxer that uses no reactive flux materials must submit a
certification of compliance with the operational standard for no
reactive flux materials in Sec. 63.1506(l) for each 6-month reporting
period. Each certification must contain the information in
Sec. 63.1516(b)(2)(vi).
(n) Sidewell group 1 furnace with add-on air pollution control
devices. These requirements apply to the owner or operator of a sidewell
group 1 furnace using add-on air pollution control devices. The owner or
operator must:
(1) Record in an operating log for each charge of a sidewell furnace
that the level of molten metal was above the top of the passage between
the sidewell and hearth during reactive flux injection, unless the
furnace hearth was also equipped with an add-on control device.
(2) Submit a certification of compliance with the operational
standards in Sec. 63.1506(m)(7) for each 6-month reporting period. Each
certification must contain the information in Sec. 63.1516(b)(2)(iii).
(o) Group 1 furnace without add-on air pollution control devices.
These requirements apply to the owner or operator of a group 1 furnace
that is not equipped with an add-on air pollution control device.
(1) The owner or operator must develop, in consultation with the
responsible permitting authority, a written site-specific monitoring
plan. The site-specific monitoring plan must be submitted to the
permitting authority as part of the OM&M plan. The site-specific
monitoring plan must contain sufficient procedures to ensure continuing
compliance with all applicable emission limits and must demonstrate,
based on documented test results, the relationship between emissions of
PM, HCl, and D/F and the proposed monitoring parameters for each
pollutant. Test data must establish the highest level of PM, HCl, and D/
F that will be emitted from the furnace. This may be determined by
conducting performance tests and monitoring operating parameters while
charging the furnace with feed/charge materials containing the highest
anticipated levels of oils and coatings and fluxing at the highest
anticipated rate. If the permitting authority determines that any
revisions of the site-specific monitoring plan are necessary to meet the
requirements of this section or this subpart, the owner or operator must
promptly make all necessary revisions and resubmit the revised plan to
the permitting authority.
(i) The owner or operator of an existing affected source must submit
the site-specific monitoring plan to the applicable permitting authority
for review at least 6 months prior to the compliance date.
(ii) The permitting authority will review and approve or disapprove
a proposed plan, or request changes to a plan, based on whether the plan
contains sufficient provisions to ensure continuing compliance with
applicable emission limits and demonstrates, based on documented test
results, the relationship between emissions of PM, HCl, and D/F and the
proposed monitoring parameters for each pollutant. Test data must
establish the highest level of PM, HCl, and D/F that will be emitted
from the furnace. Subject to permitting agency approval of the OM&M
plan, this may be determined by conducting performance tests and
monitoring operating parameters while charging the furnace with feed/
charge materials containing the highest anticipated levels of oils and
coatings and fluxing at the highest anticipated rate.
(2) Each site-specific monitoring plan must document each work
practice, equipment/design practice, pollution prevention practice, or
other measure used to meet the applicable emission standards.
(3) Each site-specific monitoring plan must include provisions for
unit labeling as required in paragraph (c) of this section, feed/charge
weight measurement (or production weight measurement) as required in
paragraph (e) of
[[Page 71]]
this section and flux weight measurement as required in paragraph (j) of
this section.
(4) Each site-specific monitoring plan for a melting/holding furnace
subject to the clean charge emission standard in Sec. 63.1505(i)(3) must
include these requirements:
(i) The owner or operator must record the type of feed/ charge
(e.g., ingot, thermally dried chips, dried scrap, etc.) for each
operating cycle or time period used in the performance test; and
(ii) The owner or operator must submit a certification of compliance
with the applicable operational standard for clean charge materials in
Sec. 63.1506(n)(3) for each 6-month reporting period. Each certification
must contain the information in Sec. 63.1516(b)(2)(iv).
(5) If a continuous emission monitoring system is included in a
site-specific monitoring plan, the plan must include provisions for the
installation, operation, and maintenance of the system to provide
quality-assured measurements in accordance with all applicable
requirements of the general provisions in subpart A of this part.
(6) If a continuous opacity monitoring system is included in a site-
specific monitoring plan, the plan must include provisions for the
installation, operation, and maintenance of the system to provide
quality-assured measurements in accordance with all applicable
requirements of this subpart.
(7) If a site-specific monitoring plan includes a scrap inspection
program for monitoring the scrap contaminant level of furnace feed/
charge materials, the plan must include provisions for the demonstration
and implementation of the program in accordance with all applicable
requirements in paragraph (p) of this section.
(8) If a site-specific monitoring plan includes a calculation method
for monitoring the scrap contaminant level of furnace feed/charge
materials, the plan must include provisions for the demonstration and
implementation of the program in accordance with all applicable
requirements in paragraph (q) of this section.
(p) Scrap inspection program for group 1 furnace without add-on air
pollution control devices. A scrap inspection program must include:
(1) A proven method for collecting representative samples and
measuring the oil and coatings content of scrap samples;
(2) A scrap inspector training program;
(3) An established correlation between visual inspection and
physical measurement of oil and coatings content of scrap samples;
(4) Periodic physical measurements of oil and coatings content of
randomly-selected scrap samples and comparison with visual inspection
results;
(5) A system for assuring that only acceptable scrap is charged to
an affected group 1 furnace; and
(6) Recordkeeping requirements to document conformance with plan
requirements.
(q) Monitoring of scrap contamination level by calculation method
for group 1 furnace without add-on air pollution control devices. The
owner or operator of a group 1 furnace dedicated to processing a
distinct type of furnace feed/charge composed of scrap with a uniform
composition (such as rejected product from a manufacturing process for
which the coating-to-scrap ratio can be documented) may include a
program in the site-specific monitoring plan for determining,
monitoring, and certifying the scrap contaminant level using a
calculation method rather than a scrap inspection program. A scrap
contaminant monitoring program using a calculation method must include:
(1) Procedures for the characterization and documentation of the
contaminant level of the scrap prior to the performance test.
(2) Limitations on the furnace feed/charge to scrap of the same
composition as that used in the performance test. If the performance
test was conducted with a mixture of scrap and clean charge, limitations
on the proportion of scrap in the furnace feed/charge to no greater than
the proportion used during the performance test.
(3) Operating, monitoring, recordkeeping, and reporting requirements
to ensure that no scrap with a contaminant level higher than that used
in the performance test is charged to the furnace.
[[Page 72]]
(r) Group 2 furnace. These requirements apply to the owner or
operator of a new or existing group 2 furnace. The owner or operator
must:
(1) Record a description of the materials charged to each furnace,
including any nonreactive, non-HAP-containing/non-HAP-generating fluxing
materials or agents.
(2) Submit a certification of compliance with the applicable
operational standard for charge materials in Sec. 63.1506(o) for each 6-
month reporting period. Each certification must contain the information
in Sec. 63.1516(b)(2)(v).
(s) Site-specific requirements for secondary aluminum processing
units. (1) An owner or operator of a secondary aluminum processing unit
at a facility must include, within the OM&M plan prepared in accordance
with Sec. 63.1510(b), the following information:
(i) The identification of each emission unit in the secondary
aluminum processing unit;
(ii) The specific control technology or pollution prevention measure
to be used for each emission unit in the secondary aluminum processing
unit and the date of its installation or application;
(iii) The emission limit calculated for each secondary aluminum
processing unit and performance test results with supporting
calculations demonstrating initial compliance with each applicable
emission limit;
(iv) Information and data demonstrating compliance for each emission
unit with all applicable design, equipment, work practice or operational
standards of this subpart; and
(v) The monitoring requirements applicable to each emission unit in
a secondary aluminum processing unit and the monitoring procedures for
daily calculation of the 3-day, 24-hour rolling average using the
procedure in Sec. 63.1510(t).
(2) The SAPU compliance procedures within the OM&M plan may not
contain any of the following provisions:
(i) Any averaging among emissions of differing pollutants;
(ii) The inclusion of any affected sources other than emission units
in a secondary aluminum processing unit;
(iii) The inclusion of any emission unit while it is shutdown; or
(iv) The inclusion of any periods of startup, shutdown, or
malfunction in emission calculations.
(3) To revise the SAPU compliance provisions within the OM&M plan
prior to the end of the permit term, the owner or operator must submit a
request to the applicable permitting authority containing the
information required by paragraph (s)(1) of this section and obtain
approval of the applicable permitting authority prior to implementing
any revisions.
(t) Secondary aluminum processing unit. Except as provided in
paragraph (u) of this section, the owner or operator must calculate and
record the 3-day, 24-hour rolling average emissions of PM, HCl, and D/F
for each secondary aluminum processing unit on a daily basis. To
calculate the 3-day, 24-hour rolling average, the owner or operator
must:
(1) Calculate and record the total weight of material charged to
each emission unit in the secondary aluminum processing unit for each
24-hour day of operation using the feed/charge weight information
required in paragraph (e) of this section. If the owner or operator
chooses to comply on the basis of weight of aluminum produced by the
emission unit, rather than weight of material charged to the emission
unit, all performance test emissions results and all calculations must
be conducted on the aluminum production weight basis.
(2) Multiply the total feed/charge weight to the emission unit, or
the weight of aluminum produced by the emission unit, for each emission
unit for the 24-hour period by the emission rate (in lb/ton of feed/
charge) for that emission unit (as determined during the performance
test) to provide emissions for each emission unit for the 24-hour
period, in pounds.
(3) Divide the total emissions for each SAPU for the 24-hour period
by the total material charged to the SAPU, or the weight of aluminum
produced by the SAPU over the 24-hour period to provide the daily
emission rate for the SAPU.
(4) Compute the 24-hour daily emission rate using Equation 4:
[[Page 73]]
[GRAPHIC] [TIFF OMITTED] TR23MR00.003
Where,
Eday = The daily PM, HCl, or D/F emission rate for the
secondary aluminum processing unit for the 24-hour period;
Ti = The total amount of feed, or aluminum produced, for
emission unit i for the 24-hour period (tons);
ERi = The measured emission rate for emission unit i as
determined in the performance test (lb/ton or [mu]g/Mg of feed/charge);
and
n = The number of emission units in the secondary aluminum processing
unit.
(5) Calculate and record the 3-day, 24-hour rolling average for each
pollutant each day by summing the daily emission rates for each
pollutant over the 3 most recent consecutive days and dividing by 3.
(u) Secondary aluminum processing unit compliance by individual
emission unit demonstration. As an alternative to the procedures of
paragraph (t) of this section, an owner or operator may demonstrate,
through performance tests, that each individual emission unit within the
secondary aluminum production unit is in compliance with the applicable
emission limits for the emission unit.
(v) Alternative monitoring method for lime addition. The owner or
operator of a lime-coated fabric filter that employs intermittent or
noncontinuous lime addition may apply to the Administrator for approval
of an alternative method for monitoring the lime addition schedule and
rate based on monitoring the weight of lime added per ton of feed/charge
for each operating cycle or time period used in the performance test. An
alternative monitoring method will not be approved unless the owner or
operator provides assurance through data and information that the
affected source will meet the relevant emission standards on a
continuous basis.
(w) Alternative monitoring methods. If an owner or operator wishes
to use an alternative monitoring method to demonstrate compliance with
any emission standard in this subpart, other than those alternative
monitoring methods which may be authorized pursuant to
Sec. 63.1510(j)(5) and Sec. 63.1510(v), the owner or operator may submit
an application to the Administrator. Any such application will be
processed according to the criteria and procedures set forth in
paragraphs (w)(1) through (6) of this section.
(1) The Administrator will not approve averaging periods other than
those specified in this section.
(2) The owner or operator must continue to use the original
monitoring requirement until necessary data are submitted and approval
is received to use another monitoring procedure.
(3) The owner or operator shall submit the application for approval
of alternate monitoring methods no later than the notification of the
performance test. The application must contain the information specified
in paragraphs (w)(3) (i) through (iii) of this section:
(i) Data or information justifying the request, such as the
technical or economic infeasibility, or the impracticality of using the
required approach;
(ii) A description of the proposed alternative monitoring
requirements, including the operating parameters to be monitored, the
monitoring approach and technique, and how the limit is to be
calculated; and
(iii) Data and information documenting that the alternative
monitoring requirement(s) would provide equivalent or better assurance
of compliance with the relevant emission standard(s).
(4) The Administrator will not approve an alternate monitoring
application unless it would provide equivalent or better assurance of
compliance with the relevant emission standard(s). Before disapproving
any alternate monitoring application, the Administrator will provide:
(i) Notice of the information and findings upon which the intended
disapproval is based; and
(ii) Notice of opportunity for the owner or operator to present
additional supporting information before final action is taken on the
application. This notice will specify how much additional time is
allowed for the owner or
[[Page 74]]
operator to provide additional supporting information.
(5) The owner or operator is responsible for submitting any
supporting information in a timely manner to enable the Administrator to
consider the application prior to the performance test. Neither
submittal of an application nor the Administrator's failure to approve
or disapprove the application relieves the owner or operator of the
responsibility to comply with any provisions of this subpart.
(6) The Administrator may decide at any time, on a case-by-case
basis, that additional or alternative operating limits, or alternative
approaches to establishing operating limits, are necessary to
demonstrate compliance with the emission standards of this subpart.
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 59792, Sept. 24, 2002;
67 FR 79816, Dec. 30, 2002]
Sec. 63.1511 Performance test/compliance demonstration general requirements.
(a) Site-specific test plan. Prior to conducting any performance
test required by this subpart, the owner or operator must prepare a
site-specific test plan which satisfies all of the requirements, and
must obtain approval of the plan pursuant to the procedures, set forth
in Sec. 63.7(c).
(b) Initial performance test. Following approval of the site-
specific test plan, the owner or operator must demonstrate initial
compliance with each applicable emission, equipment, work practice, or
operational standard for each affected source and emission unit, and
report the results in the notification of compliance status report as
described in Sec. 63.1515(b). The owner or operator of any existing
affected source for which an initial performance test is required to
demonstrate compliance must conduct this initial performance test no
later than the date for compliance established by Sec. 63.1501(a). The
owner or operator of any new affected source for which an initial
performance test is required must conduct this initial performance test
within 90 days after the date for compliance established by
Sec. 63.1501(b). Except for the date by which the performance test must
be conducted, the owner or operator must conduct each performance test
in accordance with the requirements and procedures set forth in
Sec. 63.7(c). Owners or operators of affected sources located at
facilities which are area sources are subject only to those performance
testing requirements pertaining to D/F. Owners or operators of sweat
furnaces meeting the specifications of Sec. 63.1505(f)(1) are not
required to conduct a performance test.
(1) The owner or operator must conduct each test while the affected
source or emission unit is operating at the highest production level
with charge materials representative of the range of materials processed
by the unit and, if applicable, at the highest reactive fluxing rate.
(2) Each performance test for a continuous process must consist of 3
separate runs; pollutant sampling for each run must be conducted for the
time period specified in the applicable method or, in the absence of a
specific time period in the test method, for a minimum of 3 hours.
(3) Each performance test for a batch process must consist of three
separate runs; pollutant sampling for each run must be conducted over
the entire process operating cycle.
(4) Where multiple affected sources or emission units are exhausted
through a common stack, pollutant sampling for each run must be
conducted over a period of time during which all affected sources or
emission units complete at least 1 entire process operating cycle or for
24 hours, whichever is shorter.
(5) Initial compliance with an applicable emission limit or standard
is demonstrated if the average of three runs conducted during the
performance test is less than or equal to the applicable emission limit
or standard.
(c) Test methods. The owner or operator must use the following
methods in appendix A to 40 CFR part 60 to determine compliance with the
applicable emission limits or standards:
(1) Method 1 for sample and velocity traverses.
(2) Method 2 for velocity and volumetric flow rate.
(3) Method 3 for gas analysis.
(4) Method 4 for moisture content of the stack gas.
[[Page 75]]
(5) Method 5 for the concentration of PM.
(6) Method 9 for visible emission observations.
(7) Method 23 for the concentration of D/F.
(8) Method 25A for the concentration of THC, as propane.
(9) Method 26A for the concentration of HCl. Where a lime-injected
fabric filter is used as the control device to comply with the 90
percent reduction standard, the owner or operator must measure the
fabric filter inlet concentration of HCl at a point before lime is
introduced to the system.
(d) Alternative methods. The owner or operator may use an
alternative test method, subject to approval by the Administrator.
(e) Repeat tests. The owner or operator of new or existing affected
sources and emission units located at secondary aluminum production
facilities that are major sources must conduct a performance test every
5 years following the initial performance test.
(f) Testing of representative emission units. With the prior
approval of the permitting authority, an owner or operator may utilize
emission rates obtained by testing a particular type of group 1 furnace
which is not controlled by any add-on control device, or by testing an
in-line flux box which is not controlled by any add-on control device,
to determine the emission rate for other units of the same type at the
same facility. Such emission test results may only be considered to be
representative of other units if all of the following criteria are
satisfied:
(1) The tested emission unit must use feed materials and charge
rates which are comparable to the emission units that it represents;
(2) The tested emission unit must use the same type of flux
materials in the same proportions as the emission units it represents;
(3) The tested emission unit must be operated utilizing the same
work practices as the emission units that it represents;
(4) The tested emission unit must be of the same design as the
emission units that it represents; and
(5) The tested emission unit must be tested under the highest load
or capacity reasonably expected to occur for any of the emission units
that it represents.
(g) Establishment of monitoring and operating parameter values. The
owner or operator of new or existing affected sources and emission units
must establish a minimum or maximum operating parameter value, or an
operating parameter range for each parameter to be monitored as required
by Sec. 63.1510 that ensures compliance with the applicable emission
limit or standard. To establish the minimum or maximum value or range,
the owner or operator must use the appropriate procedures in this
section and submit the information required by Sec. 63.1515(b)(4) in the
notification of compliance status report. The owner or operator may use
existing data in addition to the results of performance tests to
establish operating parameter values for compliance monitoring provided
each of the following conditions are met to the satisfaction of the
applicable permitting authority:
(1) The complete emission test report(s) used as the basis of the
parameter(s) is submitted.
(2) The same test methods and procedures as required by this subpart
were used in the test.
(3) The owner or operator certifies that no design or work practice
changes have been made to the source, process, or emission control
equipment since the time of the report.
(4) All process and control equipment operating parameters required
to be monitored were monitored as required in this subpart and
documented in the test report.
(h) Testing of commonly-ducted units within a secondary aluminum
processing unit. When group 1 furnaces and/or in-line fluxers are
included in a single existing SAPU or new SAPU, and the emissions from
more than one emission unit within that existing SAPU or new SAPU are
manifolded to a single control device, compliance for all units within
the SAPU is demonstrated if the total measured emissions from all
controlled and uncontrolled units in the SAPU do not exceed the emission
limits calculated for that SAPU based on the applicable equation in
Sec. 63.1505(k).
[[Page 76]]
(i) Testing of commonly-ducted units not within a secondary aluminum
processing unit. With the prior approval of the permitting authority, an
owner or operator may do combined performance testing of two or more
individual affected sources or emission units which are not included in
a single existing SAPU or new SAPU, but whose emissions are manifolded
to a single control device. Any such performance testing of commonly-
ducted units must satisfy the following basic requirements:
(1) All testing must be designed to verify that each affected source
or emission unit individually satisfies all emission requirements
applicable to that affected source or emission unit;
(2) All emissions of pollutants subject to a standard must be tested
at the outlet from each individual affected source or emission unit
while operating under the highest load or capacity reasonably expected
to occur, and prior to the point that the emissions are manifolded
together with emissions from other affected sources or emission units;
(3) The combined emissions from all affected sources and emission
units which are manifolded to a single emission control device must be
tested at the outlet of the emission control device;
(4) All tests at the outlet of the emission control device must be
conducted with all affected sources and emission units whose emissions
are manifolded to the control device operating simultaneously under the
highest load or capacity reasonably expected to occur; and
(5) For purposes of demonstrating compliance of a commonly-ducted
unit with any emission limit for a particular type of pollutant, the
emissions of that pollutant by the individual unit shall be presumed to
be controlled by the same percentage as total emissions of that
pollutant from all commonly-ducted units are controlled at the outlet of
the emission control device.
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 59792, Sept. 24, 2002;
67 FR 79817, Dec. 30, 2002]
Sec. 63.1512 Performance test/compliance demonstration requirements and procedures.
(a) Aluminum scrap shredder. The owner or operator must conduct
performance tests to measure PM emissions at the outlet of the control
system. If visible emission observations is the selected monitoring
option, the owner or operator must record visible emission observations
from each exhaust stack for all consecutive 6-minute periods during the
PM emission test according to the requirements of Method 9 in appendix A
to 40 CFR part 60.
(b) Thermal chip dryer. The owner or operator must conduct a
performance test to measure THC and D/F emissions at the outlet of the
control device while the unit processes only unpainted aluminum chips.
(c) Scrap dryer/delacquering kiln/decoating kiln. The owner or
operator must conduct performance tests to measure emissions of THC, D/
F, HCl, and PM at the outlet of the control device.
(1) If the scrap dryer/delacquering kiln/decoating kiln is subject
to the alternative emission limits in Sec. 63.1505(e), the average
afterburner operating temperature in each 3-hour block period must be
maintained at or above 760 [deg]C (1400 [deg]F) for the test.
(2) The owner or operator of a scrap dryer/delacquering kiln/
decoating kiln subject to the alternative limits in Sec. 63.1505(e) must
submit a written certification in the notification of compliance status
report containing the information required by Sec. 63.1515(b)(7).
(d) Group 1 furnace with add-on air pollution control devices. (1)
The owner or operator of a group 1 furnace that processes scrap other
than clean charge materials with emissions controlled by a lime-injected
fabric filter must conduct performance tests to measure emissions of PM
and D/F at the outlet of the control device and emissions of HCl at the
outlet (for the emission limit) or the inlet and the outlet (for the
percent reduction standard).
(2) The owner or operator of a group 1 furnace that processes only
clean charge materials with emissions controlled by a lime-injected
fabric filter must conduct performance tests to
[[Page 77]]
measure emissions of PM at the outlet of the control device and
emissions of HCl at the outlet (for the emission limit) or the inlet and
the outlet (for the percent reduction standard).
(3) The owner or operator may choose to determine the rate of
reactive flux addition to the group 1 furnace and assume, for the
purposes of demonstrating compliance with the SAPU emission limit, that
all reactive flux added to the group 1 furnace is emitted. Under these
circumstances, the owner or operator is not required to conduct an
emission test for HCl.
(4) The owner or operator of a sidewell group 1 furnace that
conducts reactive fluxing (except for cover flux) in the hearth, or that
conducts reactive fluxing in the sidewell at times when the level of
molten metal falls below the top of the passage between the sidewell and
the hearth, must conduct the performance tests required by paragraph
(d)(1) or (d)(2) of this section, to measure emissions from both the
sidewell and the hearth.
(e) Group 1 furnace (including melting holding furnaces) without
add-on air pollution control devices. In the site-specific monitoring
plan required by Sec. 63.1510(o), the owner or operator of a group 1
furnace (including a melting/holding furnaces) without add-on air
pollution control devices must include data and information
demonstrating compliance with the applicable emission limits.
(1) If the group 1 furnace processes other than clean charge
material, the owner or operator must conduct emission tests to measure
emissions of PM, HCl, and D/F at the furnace exhaust outlet.
(2) If the group 1 furnace processes only clean charge, the owner or
operator must conduct emission tests to simultaneously measure emissions
of PM and HCl at the furnace exhaust outlet. A D/F test is not required.
Each test must be conducted while the group 1 furnace (including a
melting/holding furnace) processes only clean charge.
(3) The owner or operator may choose to determine the rate of
reactive flux addition to the group 1 furnace and assume, for the
purposes of demonstrating compliance with the SAPU emission limit, that
all reactive flux added to the group 1 furnace is emitted. Under these
circumstances, the owner or operator is not required to conduct an
emission test for HCl.
(f) Sweat furnace. Except as provided in Sec. 63.1505(f)(1), the
owner or operator must measure emissions of D/F from each sweat furnace
at the outlet of the control device.
(g) Dross-only furnace. The owner or operator must conduct a
performance test to measure emissions of PM from each dross-only furnace
at the outlet of each control device while the unit processes only
dross.
(h) In-line fluxer. (1) The owner or operator of an in-line fluxer
that uses reactive flux materials must conduct a performance test to
measure emissions of HCl and PM or otherwise demonstrate compliance in
accordance with paragraph (h)(2) of this section. If the in-line fluxer
is equipped with an add-on control device, the emissions must be
measured at the outlet of the control device.
(2) The owner or operator may choose to limit the rate at which
reactive chlorine flux is added to an in-line fluxer and assume, for the
purposes of demonstrating compliance with the SAPU emission limit, that
all chlorine in the reactive flux added to the in-line fluxer is emitted
as HCl. Under these circumstances, the owner or operator is not required
to conduct an emission test for HCl. If the owner or operator of any in-
line flux box which has no ventilation ductwork manifolded to any outlet
or emission control device chooses to demonstrate compliance with the
emission limit for HCl by limiting use of reactive chlorine flux and
assuming that all chlorine in the flux is emitted as HCl, compliance
with the HCl limit shall also constitute compliance with the emission
limit for PM, and no separate emission test for PM is required. In this
case, the owner or operator of the unvented in-line flux box must
utilize the maximum permissible PM emission rate for the in-line flux
boxes when determining the total emissions for any SAPU which includes
the flux box.
(i) Rotary dross cooler. The owner or operator must conduct a
performance test to measure PM emissions at the outlet of the control
device.
[[Page 78]]
(j) Secondary aluminum processing unit. The owner or operator must
conduct performance tests as described in paragraphs (j)(1) through (3)
of this section. The results of the performance tests are used to
establish emission rates in lb/ton of feed/charge for PM and HCl and
[mu]g TEQ/Mg of feed/charge for D/F emissions from each emission unit.
These emission rates are used for compliance monitoring in the
calculation of the 3-day, 24-hour rolling average emission rates using
the equation in Sec. 63.1510(t). A performance test is required for:
(1) Each group 1 furnace processing only clean charge to measure
emissions of PM and either:
(i) Emissions of HCl (for the emission limit); or
(ii) The mass flow rate of HCl at the inlet to and outlet from the
control device (for the percent reduction standard).
(2) Each group 1 furnace that processes scrap other than clean
charge to measure emissions of PM and D/F and either:
(i) Emissions of HCl (for the emission limit); or
(ii) The mass flow rate of HCl at the inlet to and outlet from the
control device (for the percent reduction standard).
(3) Each in-line fluxer to measure emissions of PM and HCl.
(k) Feed/charge weight measurement. During the emission test(s)
conducted to determine compliance with emission limits in a kg/Mg (lb/
ton) format, the owner or operator of an affected source or emission
unit, subject to an emission limit in a kg/Mg (lb/ton) of feed/charge
format, must measure (or otherwise determine) and record the total
weight of feed/charge to the affected source or emission unit for each
of the three test runs and calculate and record the total weight. An
owner or operator that chooses to demonstrate compliance on the basis of
the aluminum production weight must measure the weight of aluminum
produced by the emission unit or affected source instead of the feed/
charge weight.
(l) Continuous opacity monitoring system. The owner or operator of
an affected source or emission unit using a continuous opacity
monitoring system must conduct a performance evaluation to demonstrate
compliance with Performance Specification 1 in appendix B to 40 CFR part
60. Following the performance evaluation, the owner or operator must
measure and record the opacity of emissions from each exhaust stack for
all consecutive 6-minute periods during the PM emission test.
(m) Afterburner. These requirements apply to the owner or operator
of an affected source using an afterburner to comply with the
requirements of this subpart.
(1) Prior to the initial performance test, the owner or operator
must conduct a performance evaluation for the temperature monitoring
device according to the requirements of Sec. 63.8.
(2) The owner or operator must use these procedures to establish an
operating parameter value or range for the afterburner operating
temperature.
(i) Continuously measure and record the operating temperature of
each afterburner every 15 minutes during the THC and D/F performance
tests;
(ii) Determine and record the 15-minute block average temperatures
for the three test runs; and
(iii) Determine and record the 3-hour block average temperature
measurements for the 3 test runs.
(n) Inlet gas temperature. The owner or operator of a scrap dryer/
delacquering kiln/decoating kiln or a group 1 furnace using a lime-
injected fabric filter must use these procedures to establish an
operating parameter value or range for the inlet gas temperature.
(1) Continuously measure and record the temperature at the inlet to
the lime-injected fabric filter every 15 minutes during the HCl and D/F
performance tests;
(2) Determine and record the 15-minute block average temperatures
for the 3 test runs; and
(3) Determine and record the 3-hour block average of the recorded
temperature measurements for the 3 test runs.
(o) Flux injection rate. The owner or operator must use these
procedures to establish an operating parameter value or range for the
total reactive chlorine flux injection rate.
(1) Continuously measure and record the weight of gaseous or liquid
reactive flux injected for each 15 minute period
[[Page 79]]
during the HCl and D/F tests, determine and record the 15-minute block
average weights, and calculate and record the total weight of the
gaseous or liquid reactive flux for the 3 test runs;
(2) Record the identity, composition, and total weight of each
addition of solid reactive flux for the 3 test runs;
(3) Determine the total reactive chlorine flux injection rate by
adding the recorded measurement of the total weight of chlorine in the
gaseous or liquid reactive flux injected and the total weight of
chlorine in the solid reactive flux using Equation 5:
[GRAPHIC] [TIFF OMITTED] TR23MR00.013
Where,
Wt = Total chlorine usage, by weight;
F1 = Fraction of gaseous or liquid flux that is chlorine;
W1 = Weight of reactive flux gas injected;
F2 = Fraction of solid reactive chloride flux that is
chlorine (e.g., F = 0.75 for magnesium chloride; and
W2 = Weight of solid reactive flux;
(4) Divide the weight of total chlorine usage (Wt) for
the 3 test runs by the recorded measurement of the total weight of feed
for the 3 test runs; and
(5) If a solid reactive flux other than magnesium chloride is used,
the owner or operator must derive the appropriate proportion factor
subject to approval by the applicable permitting authority.
(p) Lime injection. The owner or operator of an affected source or
emission unit using a lime-injected fabric filter system must use these
procedures during the HCl and D/F tests to establish an operating
parameter value for the feeder setting for each operating cycle or time
period used in the performance test.
(1) For continuous lime injection systems, ensure that lime in the
feed hopper or silo is free-flowing at all times; and
(2) Record the feeder setting for the 3 test runs. If the feed rate
setting varies during the runs, determine and record the average feed
rate from the 3 runs.
(q) Bag leak detection system. The owner or operator of an affected
source or emission unit using a bag leak detection system must submit
the information described in Sec. 63.1515(b)(6) as part of the
notification of compliance status report to document conformance with
the specifications and requirements in Sec. 63.1510(f).
(r) Labeling. The owner or operator of each scrap dryer/delacquering
kiln/decoating kiln, group 1 furnace, group 2 furnace and in-line fluxer
must submit the information described in Sec. 63.1515(b)(3) as part of
the notification of compliance status report to document conformance
with the operational standard in Sec. 63.1506(b).
(s) Capture/collection system. The owner or operator of a new or
existing affected source or emission unit with an add-on control device
must submit the information described in Sec. 63.1515(b)(2) as part of
the notification of compliance status report to document conformance
with the operational standard in Sec. 63.1506(c).
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 79817, Dec. 30, 2002]
Sec. 63.1513 Equations for determining compliance.
(a) THC emission limit. Use Equation 6 to determine compliance with
an emission limit for THC:
[GRAPHIC] [TIFF OMITTED] TR23MR00.004
Where,
E = Emission rate of measured pollutant, kg/Mg (lb/ton) of feed;
C = Measured volume fraction of pollutant, ppmv;
MW = Molecular weight of measured pollutant, g/g-mole (lb/lb-mole): THC
(as propane) = 44.11;
Q = Volumetric flow rate of exhaust gases, dscm/hr (dscf/hr);
K1 = Conversion factor, 1 kg/1,000 g (1 lb/lb);
K2 = Conversion factor, 1,000 L/m\3\ (1 ft\3\/ft\3\);
Mv = Molar volume, 24.45 L/g-mole (385.3 ft\3\/lb-mole); and
P = Production rate, Mg/hr (ton/hr).
(b) PM, HCl and D/F emission limits. Use Equation 7 to determine
compliance with an emission limit for PM, HCl, and D/F:
[GRAPHIC] [TIFF OMITTED] TR23MR00.005
Where,
[[Page 80]]
E = Emission rate of PM, HCl, or D/F, kg/Mg (lb/ton) of feed;
C = Concentration of PM, HCl, or D/F, g/dscm (gr/dscf);
Q = Volumetric flow rate of exhaust gases, dscm/hr (dscf/hr);
K1 = Conversion factor, 1 kg/1,000 g (1 lb/7,000 gr); and
P = Production rate, Mg/hr (ton/hr).
(c) HCl percent reduction standard. Use Equation 8 to determine
compliance with an HCl percent reduction standard:
[GRAPHIC] [TIFF OMITTED] TR23MR00.006
Where,
%R = Percent reduction of the control device;
Li = Inlet loading of pollutant, kg/Mg (lb/ton); and
Lo = Outlet loading of pollutant, kg/Mg (lb/ton).
(d) Conversion of D/F measurements to TEQ units. To convert D/F
measurements to TEQ units, the owner or operator must use the procedures
and equations in ``Interim Procedures for Estimating Risks Associated
with Exposures to Mixtures of Chlorinated Dibenzo-p-Dioxins and -
Dibenzofurans (CDDs and CDFs) and 1989 Update'' (EPA-625/3-89-016),
incorporated by reference in Sec. 63.1502 of this subpart, available
from the National Technical Information Service (NTIS), 5285 Port Royal
Road, Springfield, Virginia, NTIS no. PB 90-145756.
(e) Secondary aluminum processing unit. Use the procedures in
paragraphs (e)(1), (2), and (3) or the procedure in paragraph (e)(4) of
this section to determine compliance with emission limits for a
secondary aluminum processing unit.
(1) Use Equation 9 to compute the mass-weighted PM emissions for a
secondary aluminum processing unit. Compliance is achieved if the mass-
weighted emissions for the secondary aluminum processing unit
(EcPM) is less than or equal to the emission limit for the
secondary aluminum processing unit (LcPM) calculated using
Equation 1 in Sec. 63.1505(k).
[GRAPHIC] [TIFF OMITTED] TR23MR00.007
Where,
EcPM = The mass-weighted PM emissions for the secondary
aluminum processing unit;
EtiPM = Measured PM emissions for individual emission unit i;
Tti = The average feed rate for individual emission unit i
during the operating cycle or performance test period; and
n=The number of emission units in the secondary aluminum processing
unit.
(2) Use Equation 10 to compute the aluminum mass-weighted HCl
emissions for the secondary aluminum processing unit. Compliance is
achieved if the mass-weighted emissions for the secondary aluminum
processing unit (EcHCl) is less than or equal to the emission
limit for the secondary aluminum processing unit (LcHCl)
calculated using Equation 2 in Sec. 63.1505(k).
[GRAPHIC] [TIFF OMITTED] TR23MR00.008
Where,
EcHCl = The mass-weighted HCl emissions for the secondary
aluminum processing unit; and
EtiHCl = Measured HCl emissions for individual emission unit
i.
(3) Use Equation 11 to compute the aluminum mass-weighted D/F
emissions for the secondary aluminum processing unit. Compliance is
achieved if the mass-weighted emissions for the secondary aluminum
processing unit is less than or equal to the emission limit for the
secondary aluminum processing unit (LcD/F) calculated using
Equation 3 in Sec. 63.1505(k).
[GRAPHIC] [TIFF OMITTED] TR23MR00.009
[[Page 81]]
Where,
EcD/F = The mass-weighted D/F emissions for the secondary
aluminum processing unit; and
EtiD/F = Measured D/F emissions for individual emission unit
i.
(4) As an alternative to using the equations in paragraphs (e)(1),
(2), and (3) of this section, the owner or operator may demonstrate
compliance for a secondary aluminum processing unit by demonstrating
that each existing group 1 furnace is in compliance with the emission
limits for a new group 1 furnace in Sec. 63.1505(i) and that each
existing in-line fluxer is in compliance with the emission limits for a
new in-line fluxer in Sec. 63.1505(j).
Sec. 63.1514 [Reserved]
Notifications, Reports, And Records
Sec. 63.1515 Notifications.
(a) Initial notifications. The owner or operator must submit initial
notifications to the applicable permitting authority as described in
paragraphs (a)(1) through (7) of this section.
(1) As required by Sec. 63.9(b)(1), the owner or operator must
provide notification for an area source that subsequently increases its
emissions such that the source is a major source subject to the
standard.
(2) As required by Sec. 63.9(b)(3), the owner or operator of a new
or reconstructed affected source, or a source that has been
reconstructed such that it is an affected source, that has an initial
startup after the effective date of this subpart and for which an
application for approval of construction or reconstruction is not
required under Sec. 63.5(d), must provide notification that the source
is subject to the standard.
(3) As required by Sec. 63.9(b)(4), the owner or operator of a new
or reconstructed major affected source that has an initial startup after
the effective date of this subpart and for which an application for
approval of construction or reconstruction is required by Sec. 63.5(d)
must provide the following notifications:
(i) Intention to construct a new major affected source, reconstruct
a major source, or reconstruct a major source such that the source
becomes a major affected source;
(ii) Date when construction or reconstruction was commenced
(submitted simultaneously with the application for approval of
construction or reconstruction if construction or reconstruction was
commenced before the effective date of this subpart, or no later than 30
days after the date construction or reconstruction commenced if
construction or reconstruction commenced after the effective date of
this subpart);
(iii) Anticipated date of startup; and
(iv) Actual date of startup.
(4) As required by Sec. 63.9(b)(5), after the effective date of this
subpart, an owner or operator who intends to construct a new affected
source or reconstruct an affected source subject to this subpart, or
reconstruct a source such that it becomes an affected source subject to
this subpart, must provide notification of the intended construction or
reconstruction. The notification must include all the information
required for an application for approval of construction or
reconstruction as required by Sec. 63.5(d). For major sources, the
application for approval of construction or reconstruction may be used
to fulfill these requirements.
(i) The application must be submitted as soon as practicable before
the construction or reconstruction is planned to commence (but no sooner
than the effective date) if the construction or reconstruction commences
after the effective date of this subpart; or
(ii) The application must be submitted as soon as practicable before
startup but no later than 90 days after the effective date of this
subpart if the construction or reconstruction had commenced and initial
startup had not occurred before the effective date.
(5) As required by Sec. 63.9(d), the owner or operator must provide
notification of any special compliance obligations for a new source.
(6) As required by Sec. 63.9(e) and (f), the owner or operator must
provide notification of the anticipated date for conducting performance
tests and visible emission observations. The owner or
[[Page 82]]
operator must notify the Administrator of the intent to conduct a
performance test at least 60 days before the performance test is
scheduled; notification of opacity or visible emission observations for
a performance test must be provided at least 30 days before the
observations are scheduled to take place.
(7) As required by Sec. 63.9(g), the owner or operator must provide
additional notifications for sources with continuous emission monitoring
systems or continuous opacity monitoring systems.
(b) Notification of compliance status report. Each owner or operator
of an existing affected source must submit a notification of compliance
status report within 60 days after the compliance date established by
Sec. 63.1501(a). Each owner or operator of a new affected source must
submit a notification of compliance status report within 90 days after
conducting the initial performance test required by Sec. 63.1511(b), or
within 90 days after the compliance date established by Sec. 63.1501(b)
if no initial performance test is required. The notification must be
signed by the responsible official who must certify its accuracy. A
complete notification of compliance status report must include the
information specified in paragraphs (a)(1) through (10) of this section.
The required information may be submitted in an operating permit
application, in an amendment to an operating permit application, in a
separate submittal, or in any combination. In a State with an approved
operating permit program where delegation of authority under section
112(l) of the CAA has not been requested or approved, the owner or
operator must provide duplicate notification to the applicable Regional
Administrator. If an owner or operator submits the information specified
in this section at different times or in different submittals, later
submittals may refer to earlier submittals instead of duplicating and
resubmitting the information previously submitted. A complete
notification of compliance status report must include:
(1) All information required in Sec. 63.9(h). The owner or operator
must provide a complete performance test report for each affected source
and emission unit for which a performance test is required. A complete
performance test report includes all data, associated measurements, and
calculations (including visible emission and opacity tests).
(2) The approved site-specific test plan and performance evaluation
test results for each continuous monitoring system (including a
continuous emission or opacity monitoring system).
(3) Unit labeling as described in Sec. 63.1506(b), including process
type or furnace classification and operating requirements.
(4) The compliant operating parameter value or range established for
each affected source or emission unit with supporting documentation and
a description of the procedure used to establish the value (e.g., lime
injection rate, total reactive chlorine flux injection rate, afterburner
operating temperature, fabric filter inlet temperature), including the
operating cycle or time period used in the performance test.
(5) Design information and analysis, with supporting documentation,
demonstrating conformance with the requirements for capture/collection
systems in Sec. 63.1506(c).
(6) If applicable, analysis and supporting documentation
demonstrating conformance with EPA guidance and specifications for bag
leak detection systems in Sec. 63.1510(f).
(7) Manufacturer's specification or analysis documenting the design
residence time of no less than 1 second for each afterburner used to
control emissions from a scrap dryer/delacquering kiln/decoating kiln
subject to alternative emission standards in Sec. 63.1505(e).
(8) Manufacturer's specification or analysis documenting the design
residence time of no less than 0.8 seconds and design operating
temperature of no less than 1,600 [deg]F for each afterburner used to
control emissions from a sweat furnace that is not subject to a
performance test.
(9) The OM&M plan (including site-specific monitoring plan for each
group 1 furnace with no add-on air pollution control device).
[[Page 83]]
(10) Startup, shutdown, and malfunction plan, with revisions.
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 59793, Sept. 24, 2002;
67 FR 79818, Dec. 30, 2002]
Sec. 63.1516 Reports.
(a) Startup, shutdown, and malfunction plan/reports. The owner or
operator must develop and implement a written plan as described in
Sec. 63.6(e)(3) that contains specific procedures to be followed for
operating and maintaining the source during periods of startup,
shutdown, and malfunction, and a program of corrective action for
malfunctioning process and air pollution control equipment used to
comply with the standard. The owner or operator shall also keep records
of each event as required by Sec. 63.10(b) and record and report if an
action taken during a startup, shutdown, or malfunction is not
consistent with the procedures in the plan as described in
Sec. 63.6(e)(3). In addition to the information required in
Sec. 63.6(e)(3), the plan must include:
(1) Procedures to determine and record the cause of the malfunction
and the time the malfunction began and ended; and
(2) Corrective actions to be taken in the event of a malfunction of
a process or control device, including procedures for recording the
actions taken to correct the malfunction or minimize emissions.
(b) Excess emissions/summary report. As required by
Sec. 63.10(e)(3), the owner or operator must submit semiannual reports
within 60 days after the end of each 6-month period. Each report must
contain the information specified in Sec. 63.10(c). When no deviations
of parameters have occurred, the owner or operator must submit a report
stating that no excess emissions occurred during the reporting period.
(1) A report must be submitted if any of these conditions occur
during a 6-month reporting period:
(i) The corrective action specified in the OM&M plan for a bag leak
detection system alarm was not initiated within 1 hour.
(ii) The corrective action specified in the OM&M plan for a
continuous opacity monitoring deviation was not initiated within 1 hour.
(iii) The corrective action specified in the OM&M plan for visible
emissions from an aluminum scrap shredder was not initiated within 1
hour.
(iv) An excursion of a compliant process or operating parameter
value or range (e.g., lime injection rate or screw feeder setting, total
reactive chlorine flux injection rate, afterburner operating
temperature, fabric filter inlet temperature, definition of acceptable
scrap, or other approved operating parameter).
(v) An action taken during a startup, shutdown, or malfunction was
not consistent with the procedures in the plan as described in
Sec. 63.6(e)(3).
(vi) An affected source (including an emission unit in a secondary
aluminum processing unit) was not operated according to the requirements
of this subpart.
(vii) A deviation from the 3-day, 24-hour rolling average emission
limit for a secondary aluminum processing unit.
(2) Each report must include each of these certifications, as
applicable:
(i) For each thermal chip dryer: ``Only unpainted aluminum chips
were used as feedstock in any thermal chip dryer during this reporting
period.''
(ii) For each dross-only furnace: ``Only dross was used as the
charge material in any dross-only furnace during this reporting
period.''
(iii) For each sidewell group 1 furnace with add-on air pollution
control devices: ``Each furnace was operated such that the level of
molten metal remained above the top of the passage between the sidewell
and hearth during reactive fluxing, and reactive flux, except for cover
flux, was added only to the sidewell or to a furnace hearth equipped
with an add-on air pollution control device for PM, HCl, and D/F
emissions during this reporting period.''
(iv) For each group 1 melting/holding furnace without add-on air
pollution control devices and using pollution prevention measures that
processes only clean charge material: ``Each group 1 furnace without
add-on air pollution control devices subject to emission limits in
Sec. 63.1505(i)(2) processed only clean charge during this reporting
period.''
[[Page 84]]
(v) For each group 2 furnace: ``Only clean charge materials were
processed in any group 2 furnace during this reporting period, and no
fluxing was performed or all fluxing performed was conducted using only
nonreactive, non-HAP-containing/non-HAP-generating fluxing gases or
agents, except for cover fluxes, during this reporting period.''
(vi) For each in-line fluxer using no reactive flux: ``Only
nonreactive, non-HAP-containing, non-HAP-generating flux gases, agents,
or materials were used at any time during this reporting period.''
(3) The owner or operator must submit the results of any performance
test conducted during the reporting period, including one complete
report documenting test methods and procedures, process operation, and
monitoring parameter ranges or values for each test method used for a
particular type of emission point tested.
(c) Annual compliance certifications. For the purpose of annual
certifications of compliance required by 40 CFR part 70 or 71, the owner
or operator must certify continuing compliance based upon, but not
limited to, the following conditions:
(1) Any period of excess emissions, as defined in paragraph (b)(1)
of this section, that occurred during the year were reported as required
by this subpart; and
(2) All monitoring, recordkeeping, and reporting requirements were
met during the year.
Sec. 63.1517 Records
(a) As required by Sec. 63.10(b), the owner or operator shall
maintain files of all information (including all reports and
notifications) required by the general provisions and this subpart.
(1) The owner or operator must retain each record for at least 5
years following the date of each occurrence, measurement, maintenance,
corrective action, report, or record. The most recent 2 years of records
must be retained at the facility. The remaining 3 years of records may
be retained off site.
(2) The owner or operator may retain records on microfilm, computer
disks, magnetic tape, or microfiche; and
(3) The owner or operator may report required information on paper
or on a labeled computer disk using commonly available and EPA-
compatible computer software.
(b) In addition to the general records required by Sec. 63.10(b),
the owner or operator of a new or existing affected source (including an
emission unit in a secondary aluminum processing unit) must maintain
records of:
(1) For each affected source and emission unit with emissions
controlled by a fabric filter or a lime-injected fabric filter:
(i) If a bag leak detection system is used, the number of total
operating hours for the affected source or emission unit during each 6-
month reporting period, records of each alarm, the time of the alarm,
the time corrective action was initiated and completed, and a brief
description of the cause of the alarm and the corrective action(s)
taken.
(ii) If a continuous opacity monitoring system is used, records of
opacity measurement data, including records where the average opacity of
any 6-minute period exceeds 5 percent, with a brief explanation of the
cause of the emissions, the time the emissions occurred, the time
corrective action was initiated and completed, and the corrective action
taken.
(iii) If an aluminum scrap shredder is subject to visible emission
observation requirements, records of all Method 9 observations,
including records of any visible emissions during a 30-minute daily
test, with a brief explanation of the cause of the emissions, the time
the emissions occurred, the time corrective action was initiated and
completed, and the corrective action taken.
(2) For each affected source with emissions controlled by an
afterburner:
(i) Records of 15-minute block average afterburner operating
temperature, including any period when the average temperature in any 3-
hour block period falls below the compliant operating parameter value
with a brief explanation of the cause of the excursion and the
corrective action taken; and
(ii) Records of annual afterburner inspections.
[[Page 85]]
(3) For each scrap dryer/delacquering kiln/decoating kiln and group
1 furnace, subject to D/F and HCl emission standards with emissions
controlled by a lime-injected fabric filter, records of 15-minute block
average inlet temperatures for each lime-injected fabric filter,
including any period when the 3-hour block average temperature exceeds
the compliant operating parameter value +14 [deg]C (+25 [deg]F), with a
brief explanation of the cause of the excursion and the corrective
action taken.
(4) For each affected source and emission unit with emissions
controlled by a lime-injected fabric filter:
(i) Records of inspections at least once every 8-hour period
verifying that lime is present in the feeder hopper or silo and flowing,
including any inspection where blockage is found, with a brief
explanation of the cause of the blockage and the corrective action
taken, and records of inspections at least once every 4-hour period for
the subsequent 3 days. If flow monitors, pressure drop sensors or load
cells are used to verify that lime is present in the hopper and flowing,
records of all monitor or sensor output including any event where
blockage was found, with a brief explanation of the cause of the
blockage and the corrective action taken;
(ii) If lime feeder setting is monitored, records of daily
inspections of feeder setting, including records of any deviation of the
feeder setting from the setting used in the performance test, with a
brief explanation of the cause of the deviation and the corrective
action taken.
(iii) If lime addition rate for a noncontinuous lime injection
system is monitored pursuant to the approved alternative monitoring
requirements in Sec. 63.1510(v), records of the time and mass of each
lime addition during each operating cycle or time period used in the
performance test and calculations of the average lime addition rate (lb/
ton of feed/charge).
(5) For each group 1 furnace (with or without add-on air pollution
control devices) or in-line fluxer, records of 15-minute block average
weights of gaseous or liquid reactive flux injection, total reactive
flux injection rate and calculations (including records of the identity,
composition, and weight of each addition of gaseous, liquid or solid
reactive flux), including records of any period the rate exceeds the
compliant operating parameter value and corrective action taken.
(6) For each continuous monitoring system, records required by
Sec. 63.10(c).
(7) For each affected source and emission unit subject to an
emission standard in kg/Mg (lb/ton) of feed/charge, records of feed/
charge (or throughput) weights for each operating cycle or time period
used in the performance test.
(8) Approved site-specific monitoring plan for a group 1 furnace
without add-on air pollution control devices with records documenting
conformance with the plan.
(9) Records of all charge materials for each thermal chip dryer,
dross-only furnace, and group 1 melting/holding furnaces without air
pollution control devices processing only clean charge.
(10) Operating logs for each group 1 sidewell furnace with add-on
air pollution control devices documenting conformance with operating
standards for maintaining the level of molten metal above the top of the
passage between the sidewell and hearth during reactive flux injection
and for adding reactive flux only to the sidewell or a furnace hearth
equipped with a control device for PM, HCl, and D/F emissions.
(11) For each in-line fluxer for which the owner or operator has
certified that no reactive flux was used:
(i) Operating logs which establish that no source of reactive flux
was present at the in-line fluxer;
(ii) Labels required pursuant to Sec. 63.1506(b) which establish
that no reactive flux may be used at the in-line fluxer; or
(iii) Operating logs which document each flux gas, agent, or
material used during each operating cycle.
(12) Records of all charge materials and fluxing materials or agents
for a group 2 furnace.
(13) Records of monthly inspections for proper unit labeling for
each affected source and emission unit subject to labeling requirements.
(14) Records of annual inspections of emission capture/collection
and closed vent systems.
[[Page 86]]
(15) Records for any approved alternative monitoring or test
procedure.
(16) Current copy of all required plans, including any revisions,
with records documenting conformance with the applicable plan,
including:
(i) Startup, shutdown, and malfunction plan;
(ii) OM&M plan; and
(iii) Site-specific secondary aluminum processing unit emission plan
(if applicable).
(17) For each secondary aluminum processing unit, records of total
charge weight, or if the owner or operator chooses to comply on the
basis of aluminum production, total aluminum produced for each 24-hour
period and calculations of 3-day, 24-hour rolling average emissions.
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 79818, Dec. 30, 2002]
Other
Sec. 63.1518 Applicability of general provisions.
The requirements of the general provisions in subpart A of this part
that are applicable to the owner or operator subject to the requirements
of this subpart are shown in appendix A to this subpart.
Sec. 63.1519 Delegation of authority.
(a) In delegating implementation and enforcement authority to a
State under section 112(d) of the CAA, the authorities contained in
paragraph (b) of this section are retained by the Administrator and are
not transferred to a State.
(b) Applicability determinations pursuant to Sec. 63.1.
Effective Date Note: At 68 FR 37359, June 23, 2003, Sec. 63.1519 was
revised effective August 22, 2003. For the convenience of the user, the
revised text is set forth as follows:
Sec. 63.1519 Implementation and enforcement.
(a) This subpart can be implemented and enforced by the U.S. EPA, or
a delegated authority such as the applicable State, local, or Tribal
agency. If the U.S. EPA Administrator has delegated authority to a
State, local, or Tribal agency, then that agency, in addition to the
U.S. EPA, has the authority to implement and enforce this regulation.
Contact the applicable U.S. EPA Regional Office to find out if this
subpart is delegated to a State, local, or Tribal agency.
(b) In delegating implementation and enforcement authority of this
regulation to a State, local, or Tribal agency under subpart E of this
part, the authorities contained in paragraph (c) of this section are
retained by the Administrator of U.S. EPA and cannot be transferred to
the State, local, or Tribal agency.
(c) The authorities that cannot be delegated to State, local, or
Tribal agencies are as specified in paragraphs (c)(1) through (4) of
this section.
(1) Approval of alternatives to the requirements in Secs. 63.1500
through 63.1501 and 63.1505 through 63.1506.
(2) Approval of major alternatives to test methods for under
Sec. 63.7(e)(2)(ii) and (f), as defined in Sec. 63.90, and as required
in this subpart.
(3) Approval of major alternatives to monitoring under Sec. 63.8(f),
as defined in Sec. 63.90, and as required in this subpart.
(4) Approval of major alternatives to recordkeeping and reporting
under Sec. 63.10(f), as defined in Sec. 63.90, and as required in this
subpart.
Sec. 63.1520 [Reserved]
[[Page 87]]
Table 1 to Subpart RRR of Part 63
[GRAPHIC] [TIFF OMITTED] TR23MR00.010
[[Page 88]]
[GRAPHIC] [TIFF OMITTED] TR23MR00.011
[[Page 89]]
[GRAPHIC] [TIFF OMITTED] TR23MR00.012
[[Page 90]]
Table 2 to Subpart RRR of Part 63--Summary of Operating Requirements for
New and Existing Affected Sources and Emission Units
----------------------------------------------------------------------------------------------------------------
Monitor type/operation/
Affected source/emission unit process Operating requirements
----------------------------------------------------------------------------------------------------------------
All affected sources and emission units Emission capture and Design and install in accordance with
with an add-on air pollution control collection system. Industrial Ventilation: A Handbook of
device. Recommended Practice; operate in
accordance with OM&M plan.b
All affected sources and emission units Charge/feed weight or Operate a device that records the weight
subject to production-based (lb/ton of Production weight. of each charge; Operate in accordance
feed) emission limits a. with OM&M plan.b
Group 1 furnace, group 2 furnace, in-line Labeling................... Identification, operating parameter
fluxer and scrap dryer/delacquering kiln/ ranges and operating requirements
decoating kiln. posted at affected sources and emission
units; control device temperature and
residence time requirements posted at
scrap dryer/delacquering kiln/decoating
kiln.
Aluminum scrap shredder with fabric Bag leak detector or....... Initiate corrective action within 1-hr
filter. of alarm and complete in accordance
with OM&M plan b; operate such that
alarm does not sound more than 5% of
operating time in 6-month period.
COM or..................... Initiate corrective action within 1-hr
of a 6-minute average opacity reading
of 5% or more and complete in
accordance with OM&M plan.b
VE......................... Initiate corrective action within 1-hr
of any observed VE and complete in
accordance with the OM&M plan.b
Thermal chip dryer with afterburner...... Afterburner operating Maintain average temperature for each 3-
temperature. hr period at or above average operating
temperature during the performance
test.
Afterburner operation...... Operate in accordance with OM&M plan.b
Feed material.............. Operate using only unpainted aluminum
chips.
Scrap dryer/delacquering kiln/decoating Afterburner operating Maintain average temperature for each 3-
kiln with afterburner and lime-injected temperature. hr period at or above average operating
fabric filter. temperature during the performance
test.
Afterburner operation...... Operate in accordance with OM&M plan.b
Bag leak detector or....... Initiate corrective action within 1-hr
of alarm and complete in accordance
with the OM&M plan; b operate such that
alarm does not sound more than 5% of
operating time in 6-month period.
COM........................ Initiate corrective action within 1-hr
of a 6-minute average opacity reading
of 5% or more and complete in
accordance with the OM&M plan.b
Fabric filter inlet Maintain average fabric filter inlet
temperature. temperature for each 3-hr period at or
below average temperature during the
performance test +14 [deg]C (+25
[deg]F).
Lime injection rate........ Maintain free-flowing lime in the feed
hopper or silo at all times for
continuous injection systems; maintain
feeder setting at level established
during the performance test for
continuous injection systems.
Sweat furnace with afterburner........... Afterburner operating If a performance test was conducted,
temperature. maintain average temperature for each 3-
hr period at or above average operating
temperature during the performance
test; if a performance test was not
conducted, and afterburner meets
specifications of Sec. 63.1505(f)(1),
maintain average temperature for each 3-
hr period at or above 1600 [deg]F.
Afterburner operation...... Operate in accordance with OM&M plan.b
Dross-only furnace with fabric filter.... Bag leak detector or....... Initiate corrective action within 1-hr
of alarm and complete in accordance
with the OM&M plan; b operate such that
alarm does not sound more than 5% of
operating time in 6-month period.
COM........................ Initiate corrective action within 1-hr
of a 6-minute average opacity reading
of 5% or more and complete in
accordance with the OM&M plan.b
Feed/charge material....... Operate using only dross as the feed
material.
Rotary dross cooler with fabric filter... Bag leak detector or....... Initiate corrective action within 1-hr
of alarm and complete in accordance
with the OM&M plan; b operate such that
alarm does not sound more than 5% of
operating time in 6-month period.
COM........................ Initiate corrective action within 1-hr
of a 6-minute average opacity reading
of 5% or more and complete in
accordance with the OM&M plan.b
In-line fluxer with lime-injected fabric Bag leak detector or....... Initiate corrective action within 1-hr
filter (including those that are part of of alarm and complete in accordance
a secondary aluminum processing unit). with the OM&M plan; b operate such that
alarm does not sound more than 5% of
operating time in 6-month period.
[[Page 91]]
COM........................ Initiate corrective action within 1-hr
of a 6-minute average opacity reading
of 5% or more and complete in
accordance with the OM&M plan.b
Lime injection rate........ Maintain free-flowing lime in the feed
hopper or silo at all times for
continuous injection systems; maintain
feeder setting at level established
during performance test for continuous
injection systems.
Reactive flux injection Maintain reactive flux injection rate at
rate. or below rate used during the
performance test for each operating
cycle or time period used in the
performance test.
In-line fluxer (using no reactive flux Flux materials............. Use no reactive flux.
material).
Group 1 furnace with lime-injected fabric Bag leak detector or....... Initiate corrective action within 1-hr
filter (including those that are part of of alarm; operate such that alarm does
a secondary aluminum processing unit). not sound more than 5% of operating
time in 6-month period; complete
corrective action in accordance with
the OM&M plan.b
COM........................ Initiate corrective action within 1-hr
of a 6-minute average opacity reading
of 5% or more; complete corrective
action in accordance with the OM&M
plan.b
Fabric filter inlet Maintain average fabric filter inlet
temperature. temperature for each 3-hour period at
or below average temperature during the
performance test +14 [deg]C (+25
[deg]F).
Reactive flux injection Maintain reactive flux injection rate
rate. (lb/hr) at or below rate used during
the performance test for each furnace
cycle.
Lime injection rate........ Maintain free-flowing lime in the feed
hopper or silo at all times for
continuous injection systems; maintain
feeder setting at level established at
performance test for continuous
injection systems.
Maintain molten aluminum Operate side-well furnaces such that the
level. level of molten metal is above the top
of the passage between sidewell and
hearth during reactive flux injection,
unless the hearth is also controlled.
Fluxing in sidewell furnace Add reactive flux only to the sidewell
hearth. of the furnace unless the hearth is
also controlled.
Group 1 furnace without add-on controls Reactive flux injection Maintain reactive flux injection rate
(including those that are part of a rate. (lb/hr) at or below rate used during
secondary aluminum processing unit). the performance test for each operating
cycle or time period used in the
performance test.
Site-specific monitoring Operate furnace within the range of
plan c. charge materials, contaminant levels,
and parameter values established in the
site-specific monitoring plan.
Feed material (melting/ Use only clean charge.
holding furnace).
Clean (group 2) furnace.................. Charge and flux materials.. Use only clean charge. Use no reactive
flux.
----------------------------------------------------------------------------------------------------------------
a Thermal chip dryers, scrap dryers/delacquering kilns/decoating kilns, dross-only furnaces, in-line fluxers and
group 1 furnaces including melting/holding furnaces.
b OM&M plan--Operation, maintenance, and monitoring plan.
c Site-specific monitoring plan. Owner/operators of group 1 furnaces without control devices must include a
section in their OM&M plan that documents work practice and pollution prevention measures, including
procedures for scrap inspection, by which compliance is achieved with emission limits and process or feed
parameter-based operating requirements. This plan and the testing to demonstrate adequacy of the monitoring
plan must be developed in coordination with and approved by the permitting authority.
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 79818, Dec. 30, 2002]
Table 3 to Subpart RRR of Part 63--Summary of Monitoring Requirements
for New and Existing Affected Sources and Emission Units
----------------------------------------------------------------------------------------------------------------
Monitor type/Operation/
Affected source/Emission unit Process Monitoring requirements
----------------------------------------------------------------------------------------------------------------
All affected sources and emission units Emission capture and Annual inspection of all emission
with an add-on air pollution control collection system. capture, collection, and transport
device. systems to ensure that systems continue
to operate in accordance with ACGIH
standards.
All affected sources and emission units Feed/charge weight......... Record weight of each feed/charge,
subject to production-based (lb/ton of weight measurement device or other
feed/charge) emission limits a. procedure accuracy of [plusmn]1% b;
calibrate according to manufacturers
specifications, or at least once every
6 months.
Group 1 furnace, group 2 furnace, in-line Labeling................... Check monthly to confirm that labels are
fluxer, and scrap dryer/delacquering intact and legible.
kiln/decoating kiln.
[[Page 92]]
Aluminum scrap shredder with fabric Bag leak detector or....... Install and operate in accordance with
filter. ``Fabric Filter Bag Leak Detection
Guidance'' c; record voltage output
from bag leak detector.
COM or..................... Design and install in accordance with PS-
1; collect data in accordance with
subpart A of 40 CFR part 63; determine
and record 6-minute block averages.
VE......................... Conduct and record results of 30-minute
daily test in accordance with Method 9.
Thermal chip dryer with afterburner...... Afterburner operating Continuous measurement device to meet
temperature. specifications in Sec. 63.1510(g)(1);
record average temperature for each 15-
minute block; determine and record 3-hr
block averages.
Afterburner operation...... Annual inspection of afterburner
internal parts; complete repairs in
accordance with the OM&M plan.
Feed/charge material....... Record identity of each feed/charge;
certify feed/charge materials every 6
months.
Scrap dryer/ delacquering kiln/ decoating Afterburner operating Continuous measurement device to meet
kiln with afterburner and lime injected temperature. specifications in Sec. 63.1510(g)(1);
fabric filter. record temperatures in 15-minute block
averages; determine and record 3-hr
block averages.
Afterburner operation...... Annual inspection of afterburner
internal parts; complete repairs in
accordance with the OM&M plan.
Bag leak detector or....... Install and operate in accordance with
``Fabric Filter Bag Leak Detection
Guidance'' c; record voltage output
from bag leak detector.
COM........................ Design and install in accordance with PS-
1; collect data in accordance with
subpart A of 40 CFR part 63; determine
and record 6-minute block averages.
Lime injection rate........ For continuous injection systems,
inspect each feed hopper or silo every
8 hrs to verify that lime is free-
flowing; record results of each
inspection. If blockage occurs, inspect
every 4 hrs for 3 days; return to 8-hr
inspections if corrective action
results in no further blockage during 3-
day periode; record feeder setting
daily.
Fabric filter inlet Continuous measurement device to meet
temperature. specifications in Sec. 63.1510(h)(2);
record temperatures in 15-minute block
averages; determine and record 3-hr
block averages.
Sweat furnace with afterburner........... Afterburner operating Continuous measurement device to meet
temperature. specifications in Sec. 63.1510(g)(1);
record temperatures in 15-minute block
averages; determine and record 3-hr
block averages.
Afterburner operation...... Annual inspection of afterburner
internal parts; complete repairs in
accordance with the OM&M plan.
Dross-only furnace with fabric filter.... Bag leak detector or....... Install and operate in accordance with
``Fabric Filter Bag Leak Detection
Guidance'' c; record output voltage
from bag leak detector.
COM........................ Design and install in accordance with PS-
1; collect data in accordance with
subpart A of 40 CFR part 63; determine
and record 6-minute block averages.
Feed/charge material....... Record identity of each feed/charge;
certify charge materials every 6
months.
Rotary dross cooler with fabric filter... Bag leak detector or....... Install and operate in accordance with
``Fabric Filter Bag Leak Detection
Guidance'' c; record output voltage
from bag leak detector.
COM........................ Design and install in accordance with PS-
1; collect data in accordance with
subpart A of 40 CFR part 63; determine
and record 6-minute block averages.
In-line fluxer with lime-injected fabric Bag leak detector or....... Install and operate in accordance with
filter. ``Fabric Filter Bag Leak Detection
Guidance''c; record output voltage from
bag leak detector.
COM........................ Design and install in accordance with PS-
1; collect data in accordance with
subpart A of 40 CFR part 63; determine
and record 6-minute block averages
Reactive flux injection Weight measurement device accuracy of
rate. [plusmn]1% b; calibrate according to
manufacturer's specifications or at
least once every 6 months; record time,
weight and type of reactive flux added
or injected for each 15-minute block
period while reactive fluxing occurs;
calculate and record total reactive
flux injection rate for each operating
cycle or time period used in
performance test; or
Alternative flux injection rate
determination procedure per Sec.
63.1510(j)(5).
[[Page 93]]
Lime injection rate........ For continuous injection systems, record
feeder setting daily and inspect each
feed hopper or silo every 8 hrs to
verify that lime is free-flowing;
record results of each inspection. If
blockage occurs, inspect every 4 hrs
for 3 days; return to 8-hour
inspections if corrective action
results in no further blockage during 3-
day period.d
In-line fluxer using no reactive flux.... Flux materials............. Record flux materials; certify every 6
months for no reactive flux.
Group 1 furnace with lime-injected fabric Bag leak detector or....... Install and operate in accordance with
filter. ``Fabric Filter Bag Leak Detection
Guidance'' c; record output voltage
from bag leak detector.
COM........................ Design and install in accordance with PS-
1; collect data in accordance with
subpart A of 40 part CFR 63; determine
and record 6-minute block averages.
Lime injection rate........ For continuous injection systems, record
feeder setting daily and inspect each
feed hopper or silo every 8 hours to
verify that lime is free-flowing;
record results of each inspection. If
blockage occurs, inspect every 4 hours
for 3 days; return to 8-hour
inspections if corrective action
results in no further blockage during 3-
day period.d
Reactive flux injection Weight measurement device accuracy of
rate. [plusmn]1%\b\; calibrate every 3
months; record weight and type of
reactive flux added or injected for
each 15-minute block period while
reactive fluxing occurs; calculate and
record total reactive flux injection
rate for each operating cycle or time
period used in performance test; or
Alternative flux injection rate
determination procedure per Sec.
63.1510(j)(5).
Fabric filter inlet Continuous measurement device to meet
temperature. specifications in Sec. 63.1510(h)(2);
record temperatures in 15-minute block
averages; determine and record 3-hour
block averages.
Maintain molten aluminum Maintain aluminum level operating log;
level in sidewell furnace. certify every 6 months.
Group 1 furnace without add-on controls.. Fluxing in sidewell furnace Maintain flux addition operating log;
hearth. certify every 6 months.
Reactive flux injection Weight measurement device accuracy of
rate. +1% b; calibrate according to
manufacturers specifications or at
least once every six months; record
weight and type of reactive flux added
or injected for each 15-minute block
period while reactive fluxing occurs;
calculate and record total reactive
flux injection rate for each operating
cycle or time period used in
performance test.
OM&M plan (approved by Demonstration of site-specific
permitting agency). monitoring procedures to provide data
and show correlation of emissions
across the range of charge and flux
materials and furnace operating
parameters.
Feed material (melting/ Record type of permissible feed/charge
holding furnace). material; certify charge materials
every 6 months.
Clean (group 2) furnace.................. Charge and flux materials.. Record charge and flux materials;
certify every 6 months for clean charge
and no reactive flux.
----------------------------------------------------------------------------------------------------------------
a Thermal chip dryers, scrap dryers/delacquering kilns/decoating kilns, dross-only furnaces, in-line fluxers and
group 1 furnaces or melting/holding furnaces.
b Permitting agency may approve measurement devices of alternative accuracy, for example in cases where flux
rates are very low and costs of meters of specified accuracy are prohibitive; or where feed/charge weighing
devices of specified accuracy are not practicable due to equipment layout or charging practices.
c Non-triboelectric bag leak detectors must be installed and operated in accordance with manufacturers'
specifications.
d Permitting agency may approve other alternatives including load cells for lime hopper weight, sensors for
carrier gas pressure, or HCl monitoring devices at fabric filter outlet.
Appendix A to Subpart RRR of Part 63--General Provisions Applicability
to Subpart RRR
----------------------------------------------------------------------------------------------------------------
Citation Requirement Applies to RRR Comment
----------------------------------------------------------------------------------------------------------------
Sec. 63.1(a)(1)-(4).................... General Applicability. Yes. .....................
Sec. 63.1(a)(5)........................ ...................... No..................... [Reserved].
Sec. 63.1(a)(6)-(8).................... ...................... Yes. .....................
Sec. 63.1(a)(9)........................ ...................... No..................... [Reserved].
Sec. 63.1(a) (10)-(14)................. ...................... Yes. .....................
Sec. 63.1(b)........................... Initial Applicability Yes.................... EPA retains approval
Determination. authority.
Sec. 63.1(c)(1)........................ Applicability After Yes. .....................
Standard Established.
[[Page 94]]
Sec. 63.1(c)(2)........................ ...................... Yes.................... States have option to
exclude area sources
from title V permit
program.
Sec. 63.1(c)(3)........................ ...................... No..................... [Reserved].
Sec. 63.1(c)(4)-(5).................... ...................... Yes. .....................
Sec. 63.1(d)........................... ...................... No..................... [Reserved].
Sec. 63.1(e)........................... Applicability of Yes. .....................
Permit Program.
Sec. 63.2.............................. Definitions........... Yes.................... Additional
definitions in Sec.
63.1503.
Sec. 63.3.............................. Units and Yes.................... .....................
Abbreviations.
Sec. 63.4(a)(1)-(3).................... Prohibited Activities. Yes. .....................
Sec. 63.4(a)(4)........................ ...................... No..................... [Reserved]
Sec. 63.4(a)(5)........................ ...................... Yes. .....................
Sec. 63.4(b)-(c)....................... Circumvention/ Yes. .....................
Severability.
Sec. 63.5(a)........................... Construction and Yes. .....................
Reconstruction--
Applicability.
Sec. 63.5(b)(1)........................ Existing, New, Yes. .....................
Reconstructed Sources-
-Requirements.
Sec. 63.5(b)(2)........................ ...................... No..................... [Reserved].
Sec. 63.5(b)(3)-(6).................... ...................... Yes. .....................
Sec. 63.5(c)........................... ...................... No..................... [Reserved].
Sec. 63.5(d)........................... Application for Yes. .....................
Approval of
Construction/
Reconstruction.
Sec. 63.5(e)........................... Approval of Yes. .....................
Construction/
Reconstruction.
Sec. 63.5(f)........................... Approval of Yes. .....................
Construction/
Reconstruction Based
on State Review.
Sec. 63.6(a)........................... Compliance with Yes. .....................
Standards and
Maintenance--
Applicability.
Sec. 63.6(b)(1)-(5).................... New and Reconstructed Yes. .....................
Sources--Dates.
Sec. 63.6(b)(6)........................ ...................... No..................... [Reserved].
Sec. 63.6(b)(7)........................ ...................... Yes. .....................
Sec. 63.6(c)(1)........................ Existing Sources Dates Yes.................... Sec. 63.1501
specifies dates.
Sec. 63.6(c)(2)........................ ...................... Yes. .....................
Sec. 63.6(c)(3)-(4).................... ...................... No..................... [Reserved].
Sec. 63.6(c)(5)........................ ...................... Yes. .....................
Sec. 63.6(d)........................... ...................... No..................... [Reserved].
Sec. 63.6(e)(1)-(2).................... Operation & Yes.................... Sec. 63.1510
Maintenance requires plan.
Requirements.
Sec. 63.6(e)(3)........................ Startup, Shutdown, and Yes. .....................
Malfunction Plan.
Sec. 63.6(f)........................... Compliance with Yes. .....................
Emission Standards.
Sec. 63.6(g)........................... Alternative Standard.. No..................... .....................
Sec. 63.6(h)........................... Compliance with Yes. .....................
Opacity/VE Standards.
Sec. 63.6(i)(1)-(14)................... Extension of Yes. .....................
Compliance.
Sec. 63.6(i)(15)....................... ...................... No..................... [Reserved].
Sec. 63.6(i)(16)....................... ...................... Yes. .....................
Sec. 63.6(j)........................... Exemption from Yes. .....................
Compliance.
Sec. 63.7(a)-(h)....................... Performance Test Yes.................... Except Sec. 63.1511
Requirements- establishes dates
Applicability and for initial
Dates. performance tests.
Sec. 63.7(b)........................... Notification.......... Yes. .....................
Sec. 63.7(c)........................... Quality Assurance/Test Yes. .....................
Plan.
Sec. 63.7(d)........................... Testing Facilities.... Yes. .....................
Sec. 63.7(e)........................... Conduct of Tests...... Yes. .....................
Sec. 63.7(f)........................... Alternative Test Yes. .....................
Method.
Sec. 63.7(g)........................... Data Analysis......... Yes. .....................
Sec. 63.7(h)........................... Waiver of Tests....... Yes. .....................
Sec. 63.8(a)(1)........................ Monitoring Yes. .....................
Requirements--
Applicability.
Sec. 63.8(a)(2)........................ ...................... Yes. .....................
Sec. 63.8(a)(3)........................ ...................... No..................... [Reserved]
Sec. 63.8(a)(4)........................ ...................... Yes.................... .....................
Sec. 63.8(b)........................... Conduct of Monitoring. Yes. .....................
Sec. 63.8(c)(1)-(3).................... CMS Operation and Yes. .....................
Maintenance.
Sec. 63.8(c)(4)-(8).................... ...................... Yes. .....................
Sec. 63.8(d)........................... Quality Control....... Yes. .....................
Sec. 63.8(e)........................... CMS Performance Yes. .....................
Evaluation.
Sec. 63.8(f)(1)-(5).................... Alternative Monitoring No..................... Sec. 63.1510(w)
Method. includes provisions
for monitoring
alternatives.
[[Page 95]]
Sec. 63.8(f)(6)........................ Alternative to RATA Yes. .....................
Test.
Sec. 63.8(g)(1)........................ Data Reduction........ Yes. .....................
Sec. 63.8(g)(2)........................ ...................... No..................... Sec. 63.1512
requires five 6-
minute averages for
an aluminum scrap
shredder.
Sec. 63.8(g)(3)-(5).................... ...................... Yes. .....................
Sec. 63.9(a)........................... Notification Yes. .....................
Requirements--
Applicability.
Sec. 63.9(b)........................... Initial Notifications. Yes. .....................
Sec. 63.9(c)........................... Request for Compliance Yes. .....................
Extension.
Sec. 63.9(d)........................... New Source Yes. .....................
Notification for
Special Compliance
Requirements.
63.9(e)................................. Notification of Yes. .....................
Performance Test.
Sec. 63.9(f)........................... Notification of VE/ Yes. .....................
Opacity Test.
Sec. 63.9(g)........................... Additional CMS Yes. .....................
Notifications.
Sec. 63.9(h)(1)-(3).................... Notification of Yes.................... Except Sec. 63.1515
Compliance Status. establishes dates
for notification of
compliance status
reports.
Sec. 63.9(h)(4)........................ ...................... No..................... [Reserved].
Sec. 63.9(h)(5)-(6).................... ...................... Yes. .....................
Sec. 63.9(i)........................... Adjustment of Yes. .....................
Deadlines.
Sec. 63.9(j)........................... Change in Previous Yes. .....................
Information.
Sec. 63.10(a).......................... Recordkeeping/ Yes. .....................
Reporting--
Applicability.
Sec. 63.10(b).......................... General Requirements.. Yes.................... Sec. 63.1517
includes additional
requirements.
Sec. 63.10(c)(1)....................... Additional CMS Yes. .....................
Recordkeeping.
Sec. 63.10(c)(2)-(4)................... ...................... No..................... [Reserved].
Sec. 63.10(c)(5)....................... ...................... Yes. .....................
Sec. 63.10(c)(6)....................... ...................... Yes. .....................
Sec. 63.10(c)(7)-(8)................... ...................... Yes. .....................
Sec. 63.10(c)(9)....................... ...................... No..................... [Reserved].
Sec. 63.10(c)(10)-(13)................. ...................... Yes. .....................
Sec. 63.10(c)(14)...................... ...................... Yes. .....................
Sec. 63.10(d)(1)....................... General Reporting Yes. .....................
Requirements.
Sec. 63.10(d)(2)....................... Performance Test Yes. .....................
Results.
Sec. 63.10(d)(3)....................... Opacity or VE Yes. .....................
Observations.
Sec. 63.10(d)(4) -(5).................. Progress Reports/ Yes. .....................
Startup, Shutdown,
and Malfunction
Reports.
Sec. 63.10(e)(1)-(2)................... Additional CMS Reports Yes. .....................
Sec. 63.10(e)(3)....................... Excess Emissions/CMS Yes. .....................
Performance Reports.
Sec. 63.10(e)(4)....................... COMS Data Reports..... Yes. .....................
Sec. 63.10(f).......................... Recordkeeping/ Yes. .....................
Reporting Waiver.
Sec. 63.11(a)-(b)...................... Control Device No..................... Flares not
Requirements. applicable.
Sec. 63.12(a)-(c)...................... State Authority and Yes. EPA retains authority
Delegations. for applicability
determinations.
Sec. 63.13............................. Addresses............. Yes. .....................
Sec. 63.14............................. Incorporation by Yes.................... Chapters 3 and 5 of
Reference. ACGIH Industrial
Ventilation Manual
for capture/
collection systems;
and Interim
Procedures for
Estimating Risk
Associated with
Exposure to Mixtures
of Chlorinated
Dibenzofurans (CDDs
and CDFs) and 1989
Update (incorporated
by reference in Sec.
63.1502).
Sec. 63.15............................. Availability of Yes. .....................
Information/
Confidentiality.
----------------------------------------------------------------------------------------------------------------
[[Page 96]]
[65 FR 15710, Mar. 23, 2000, as amended at 67 FR 59793, Sept. 24, 2002;
67 FR 79818, Dec. 30, 2002]
Subpart SSS [Reserved]
Subpart TTT--National Emission Standards for Hazardous Air Pollutants
for Primary Lead Smelting
Source: 64 FR 30204, June 4, 1999, unless othewise noted.
Sec. 63.1541 Applicability.
(a) The provisions of this subpart apply to the following affected
sources at primary lead smelters: sinter machine, blast furnace, dross
furnace, process fugitive sources, and fugitive dust sources. The
provisions of this subpart do not apply to secondary lead smelters, lead
refiners, or lead remelters.
(b) Table 1 of this subpart specifies the provisions of subpart A
that apply and those that do not apply to owners and operators of
primary lead smelters. The following sections of part 63 apply to this
subpart as stated in subpart A and Table 1: Sec. 63.1 (Applicability),
Sec. 63.2 (Definitions), Sec. 63.3 (Units and abbreviations), Sec. 63.4
(Prohibited activities and circumvention), Sec. 63.5 (Construction and
reconstruction), Sec. 63.7 (Performance testing requirements), Sec. 63.8
(Monitoring requirements), Sec. 63.12 (State authority and delegations),
Sec. 63.13 (Addresses of State air pollution control agencies and EPA
Regional Offices), Sec. 63.14 (Incorporations by reference), and
Sec. 63.15 (Availability of information confidentiality). The following
sections of part 63 apply to the extent specified in this subpart and
Table 1: Sec. 63.6 (Compliance with standards and maintenance
requirements), Sec. 63.9 (Notification requirements), and Sec. 63.10
(Recordkeeping and reporting requirements). Section Sec. 63.11 (Control
device requirements) does not apply to this subpart.
Sec. 63.1542 Definitions.
Terms used in this subpart are defined in the Act, in subpart A of
this part, or in this section as follows:
Bag leak detection system means a system that is capable of
continuously monitoring relative particulate matter (dust) loadings in
the exhaust of a baghouse in order to detect bag leaks and other upset
conditions. A bag leak detection system includes, but is not limited to,
an instrument that operates on triboelectric, light scattering, light
transmittance, or other effect to continuously monitor relative
particulate matter loadings.
Blast furnace means any reduction furnace to which sinter is charged
and which forms separate layers of molten slag and lead bullion.
Building means a roofed and walled structure with limited openings
to allow access and egress for people and vehicles.
Charging location means the physical opening through which raw
materials are introduced into a sinter machine, blast furnace, or dross
furnace.
Dross furnace means any smelting furnace to which drosses are
charged and which chemically and physically separates lead from other
impurities.
Drossing and refining kettle means an open-top vessel that is
constructed of cast iron or steel and is indirectly heated from below
and contains molten lead for the purpose of drossing, refining, or
alloying lead. Included are pot furnaces, receiving kettles, and holding
kettles.
Fugitive dust source means a stationary source of hazardous air
pollutant emissions at a primary lead smelter resulting from the
handling, storage, transfer, or other management of lead-bearing
materials where the source is not associated with a specific process,
process vent, or stack. Fugitive dust sources include roadways, storage
piles, materials handling transfer points, and materials transport
areas.
Furnace area means any area of a primary lead smelter in which a
blast furnace or dross furnace is located.
Malfunction means any sudden, infrequent, and not reasonably
preventable failure of air pollution control equipment, process
equipment, or a process to operate in a normal or usual manner. Failures
that are caused in part by poor maintenance or careless operation are
not malfunctions.
Materials storage and handling area means any area of a primary lead
[[Page 97]]
smelter in which lead-bearing materials (including ore concentrate,
sinter, granulated lead, dross, slag, and flue dust) are stored or
handled between process steps, including areas in which materials are
stored in piles, bins, or tubs, and areas in which material is prepared
for charging to a sinter machine or smelting furnace.
Operating time means the period of time in hours that an affected
source is in operation beginning at a startup and ending at the next
shutdown.
Plant operating time means the period of time in hours that either a
sinter machine or blast furnace is in operation.
Plant roadway means any area of a primary lead smelter that is
subject to vehicle traffic, including traffic by fork lifts, front-end
loaders, or vehicles carrying ore concentrates or cast lead ingots.
Excluded from this definition are employee and visitor parking areas,
provided they are not subject to traffic by vehicles carrying lead-
bearing materials.
Primary lead smelter means any facility engaged in the production of
lead metal from lead sulfide ore concentrates through the use of
pyrometallurgical techniques.
Process fugitive source means a source of hazardous air pollutant
emissions at a primary lead smelter that is associated with lead
smelting or refining but is not the primary exhaust stream and is not a
fugitive dust source. Process fugitive sources include sinter machine
charging locations, sinter machine discharge locations, sinter crushing
and sizing equipment, furnace charging locations, furnace taps, drossing
kettles, and refining kettles.
Refining and casting area means any area of a primary lead smelter
in which drossing or refining operations occur, or casting operations
occur.
Shutdown means the cessation of operation of an affected source for
any purpose.
Sinter machine means any device in which a lead sulfide ore
concentrate charge is heated in the presence of air to eliminate sulfur
contained in the charge and to agglomerate the charge into a hard porous
mass called sinter.
Sinter machine area means any area of a primary lead smelter where a
sinter machine, or sinter crushing and sizing equipment is located.
Sinter machine discharge end means the physical opening at the end
of a sinter machine where the sinter exits the sinter machine.
Startup means the setting in operation of an affected source for any
purpose.
Tapping location means the opening thru which lead and slag are
removed from the furnace.
Sec. 63.1543 Standards for process and process fugitive sources.
(a) No owner or operator of any existing, new, or reconstructed
primary lead smelter shall discharge or cause to be discharged into the
atmosphere lead compounds in excess of 500 grams of lead per megagram of
lead metal produced (1.0 pounds of lead per ton of lead metal produced)
from the aggregation of emissions discharged from the air pollution
control devices used to control emissions from the sources listed in
paragraphs (a)(1) through (a)(9) of this section.
(1) Sinter machine;
(2) Blast furnace;
(3) Dross furnace;
(4) Dross furnace charging location;
(5) Blast furnace and dross furnace tapping location;
(6) Sinter machine charging location;
(7) Sinter machine discharge end;
(8) Sinter crushing and sizing equipment; and
(9) Sinter machine area.
(b) The process fugitive sources listed in paragraphs (a)(4) through
(a)(8) of this section shall be equipped with a hood and shall be
ventilated to a baghouse or equivalent control device. The hood design
and ventilation rate shall be consistent with American Conference of
Governmental Industrial Hygienists recommended practices.
(c) The sinter machine area shall be enclosed in a building that is
ventilated to a baghouse or equivalent control device at a rate that
maintains a positive in-draft through any doorway opening.
(d) Except as provided in paragraph (e) of this section, following
the initial test to demonstrate compliance with paragraph (a) of this
section, the owner or operator of a primary lead smelter
[[Page 98]]
shall conduct a compliance test for lead compounds on an annual basis
(no later than 12 calendar months following any previous compliance
test).
(e) If the three most recent compliance tests demonstrate compliance
with the emission limit specified in paragraph (a) of this section, the
owner or operator of a primary lead smelter shall be allowed up to 24
calendar months from the last compliance test to conduct the next
compliance test for lead compounds.
(f) The owner or operator of a primary lead smelter shall maintain
and operate each baghouse used to control emissions from the sources
listed in paragraphs (a)(1) through (a)(9) of this section such that the
alarm on a bag leak detection system required under Sec. 63.1547(c)(9)
does not sound for more than five percent of the total operating time in
a 6-month reporting period.
(g) The owner or operator of a primary lead smelter shall record the
date and time of a bag leak detection system alarm and initiate
procedures to determine the cause of the alarm according to the
corrective action plan required under Sec. 63.1547(c)(9) within 1 hour
of the alarm. The cause of the alarm shall be corrected as soon as
practicable.
Sec. 63.1544 Standards for fugitive dust sources.
(a) Each owner or operator of a primary lead smelter shall prepare,
and at all times operate according to, a standard operating procedures
manual that describes in detail the measures that will be put in place
to control fugitive dust emissions from the sources listed in paragraphs
(a)(1) through (a)(5) of this section:
(1) Plant roadways;
(2) Material storage and handling area(s);
(3) Sinter machine area(s);
(4) Furnace area(s); and
(5) Refining and casting area(s).
(b) Not withstanding paragraph (c) of this section, the standard
operating procedures manual shall be submitted to the Administrator or
delegated authority for review and approval.
(c) Existing manuals that describe the measures in place to control
fugitive dust sources required as part of a State implementation plan
for lead shall satisfy the requirements of paragraph (a) of this section
provided they address the sources listed in paragraphs (a)(1) through
(a)(5) of this section.
Sec. 63.1545 Compliance dates.
(a) Each owner or operator of an existing primary lead smelter shall
achieve compliance with the requirements of this subpart no later than
May 4, 2001.
(b) Each owner or operator of a primary lead smelter that commences
construction or reconstruction after April 17, 1998, shall achieve
compliance with the requirements of this subpart by June 4, 1999 or upon
startup of operations, whichever is later.
Sec. 63.1546 Test methods.
(a) The following procedure shall be used to determine compliance
with the emissions standard for lead compounds under Sec. 63.1543(a):
(1) The lead compound emission rate, in units of grams of lead per
hour, for each source listed in Sec. 63.1543(a)(1) through
Sec. 63.1543(a)(9) shall be determined according to the following test
methods in appendix A of part 60 of this chapter:
(i) Method 1 shall be used to select the sampling port location and
the number of traverse points.
(ii) Method 2 shall be used to measure volumetric flow rate.
(iii) Method 3 shall be used for gas analysis.
(iv) Method 4 shall be used to determine moisture content of the
stack gas
(v) Method 12 shall be used to measure the lead emission rate of the
stack gas. The minimum sample volume shall be 0.85 dry standard cubic
meters (30 dry standard cubic feet) and the minimum sampling time shall
be 60 minutes for each run. Three runs shall be performed and the
average of the three runs shall be used to determine compliance.
(2) The lead production rate, in units of megagrams per hour, shall
be determined based on production data for the previous 12 calendar
months according to the procedures detailed in paragraphs (a)(2)(i)
through (a)(2)(v) of this section:
[[Page 99]]
(i) Total lead products production multiplied by the fractional lead
content shall be determined in units of megragrams.
(ii) Total copper matte production multiplied by the fractional lead
content shall be determined in units of megragrams.
(iii) Total copper speiss production multiplied by the fractional
lead content shall be determined in units of megragrams.
(iv) Total lead production shall be determined by summing the values
obtained in paragraphs (a)(2)(i) through (a)(2)(iii) of this section.
(v) The lead production rate, in units of megragrams per hours,
shall be calculated based on the total lead production, as determined in
accordance with paragraph (a)(2)(iv) of this section, divided by the
total plant operating time, in hours, for the previous 12 months.
(3) The sum of lead compound emission rates for the sources in
Sec. 63.1543(a)((1) through (a)(9), as determined in accordance with
paragraph (a)(1) of this section, shall be divided by the lead
production rate, as determined in accordance with paragraph (a)(2)(v) of
this section, to obtain a production-based, lead compound emission rate
in units of grams of lead per megagram of lead metal produced. The
production-based, lead compound emission rate shall be used to determine
compliance with the emissions standard for lead compounds under
Sec. 63.1543(a).
(b) Owner and operators shall perform an initial compliance test to
demonstrate compliance with the sinter building in-draft requirements of
Sec. 63.1543(c) at each doorway opening in accordance with paragraphs
(b)(1) through (b)(4) of this section.
(1) Use a propeller anemometer or equivalent device.
(2) Determine doorway in-draft by placing the anemometer in the
plane of the doorway opening near its center.
(3) Determine doorway in-draft for each doorway that is open during
normal operation with all remaining doorways in their customary position
during normal operation.
(4) Do not determine doorway in-draft when ambient wind speed
exceeds 2 meters per second.
Sec. 63.1547 Monitoring requirements.
(a) Owners and operators of primary lead smelters shall prepare, and
at all times operate according to, a standard operating procedures
manual that describes in detail the procedures for inspection,
maintenance, and bag leak detection and corrective action for all
baghouses that are used to control process, process fugitive, or
fugitive dust emissions from any source subject to the lead emission
standards in Secs. 63.1543 and 63.1544, including those used to control
emissions from general ventilation systems.
(b) The standard operating procedures manual for baghouses required
by paragraph (a) of this section shall be submitted to the Administrator
or delegated authority for review and approval.
(c) The procedures specified in the standard operating procedures
manual for inspections and routine maintenance shall, at a minimum,
include the requirements of paragraphs (c)(1) through (c)(9) of this
section.
(1) Daily monitoring of pressure drop across each baghouse cell to
ensure pressure drop is within the normal operating range identified in
the standard operating procedures manual.
(2) Weekly confirmation that dust is being removed from hoppers
through visual inspection or equivalent means of ensuring the proper
functioning of removal mechanisms.
(3) Daily check of compressed air supply for pulse-jet baghouses.
(4) An appropriate methodology for monitoring cleaning cycles to
ensure proper operation.
(5) Monthly check of bag cleaning mechanisms for proper functioning
through visual inspection or equivalent means.
(6) Quarterly visual check of bag tension on reverse air and shaker-
type baghouses to ensure that bags are not kinked (kneed or bent) or
laying on their sides. Such checks are not required for shaker-type
baghouses using self-tensioning (spring loaded) devices.
(7) Quarterly confirmation of the physical integrity of the baghouse
[[Page 100]]
through visual inspection of the baghouse interior for air leaks.
(8) Quarterly inspection of fans for wear, material buildup, and
corrosion through visual inspection, vibration detectors, or equivalent
means.
(9) Except as provided in paragraph (h) of this section, continuous
operation of a bag leak detection system.
(d) The procedures specified in the standard operating procedures
manual for maintenance shall, at a minimum, include a preventative
maintenance schedule that is consistent with the baghouse manufacturer's
instructions for routine and long-term maintenance.
(e) The bag leak detection system required by paragraph (c)(9) of
this section shall meet the specifications and requirements of (e)(1)
through (e)(8) of this section.
(1) The bag leak detection system must be certified by the
manufacturer to be capable of detecting particulate matter emissions at
concentrations of 10 milligram per actual cubic meter (0.0044 grains per
actual cubic foot) or less.
(2) The bag leak detection system sensor must provide output of
relative particulate matter loadings, and the owner or operator shall
continuously record the output from the bag leak detection system.
(3) The bag leak detection system must be equipped with an alarm
system that will sound when an increase in relative particulate loading
is detected over a preset level, and the alarm must be located such that
it can be heard by the appropriate plant personnel.
(4) Each bag leak detection system that works based on the
triboelectric effect shall be installed, calibrated, and maintained in a
manner consistent with guidance provided in the U.S. Environmental
Protection Agency guidance document ``Fabric Filter Bag Leak Detection
Guidance'' (EPA-454/R-98-015). Other bag leak detection systems shall be
installed, calibrated, and maintained in a manner consistent with the
manufacturer's written specifications and recommendations.
(5) The initial adjustment of the system shall, at a minimum,
consist of establishing the baseline output by adjusting the sensitivity
(range) and the averaging period of the device, and establishing the
alarm set points and the alarm delay time.
(6) Following initial adjustment, the owner or operator shall not
adjust the sensitivity or range, averaging period, alarm set points, or
alarm delay time, except as detailed in the approved SOP required under
paragraph (a) of this section. In no event shall the sensitivity be
increased by more than 100 percent or decreased more than 50 percent
over a 365-day period unless a responsible official certifies that the
baghouse has been inspected and found to be in good operating condition.
(7) For negative pressure, induced air baghouses, and positive
pressure baghouses that are discharged to the atmosphere through a
stack, the bag leak detector must be installed downstream of the
baghouse and upstream of any wet acid gas scrubber.
(8) Where multiple detectors are required, the system's
instrumentation and alarm may be shared among detectors.
(f) The standard operating procedures manual required by paragraph
(a) of this section shall include a corrective action plan that
specifies the procedures to be followed in the event of a bag leak
detection system alarm. The corrective action plan shall include, at a
minimum, procedures to be used to determine the cause of an alarm, as
well as actions to be taken to minimize emissions, which may include,
but are not limited to, the following.
(1) Inspecting the baghouse for air leaks, torn or broken bags or
filter media, or any other condition that may cause an increase in
emissions.
(2) Sealing off defective bags or filter media.
(3) Replacing defective bags or filter media, or otherwise repairing
the control device.
(4) Sealing off a defective baghouse compartment.
(5) Cleaning the bag leak detection system probe, or otherwise
repairing the bag leak detection system.
(6) Shutting down the process producing the particulate emissions.
[[Page 101]]
(g) The percentage of total operating time the alarm on the bag leak
detection system sounds in a 6-month reporting period shall be
calculated in order to determine compliance with the five percent
operating limit in Sec. 63.1543(f). The percentage of time the alarm on
the bag leak detection system sounds shall be determined according to
paragraphs (g)(1) through (g)(5) of this section.
(1) Alarms that occur due solely to a malfunction of the bag leak
detection system shall not be included in the calculation.
(2) Alarms that occur during startup, shutdown, or malfunction shall
not be included in the calculation if the condition is described in the
startup, shutdown, and malfunction plan and the owner or operator
follows all the procedures in the plan defined for this condition.
(3) For each alarm where the owner or operator initiates procedures
to determine the cause of an alarm within 1 hour of the alarm, 1 hour of
alarm time shall be counted.
(4) For each alarm where the owner or operator does not initiate
procedures to determine the cause of the alarm within 1 hour of the
alarm, alarm time will be counted as the actual amount of time taken by
the owner or operator to initiate procedures to determine the cause of
the alarm.
(5) The percentage of time the alarm on the bag leak detection
system sounds shall be calculated as the ratio of the sum of alarm times
to the total operating time multiplied by 100.
(h) Baghouses equipped with HEPA filters as a secondary filter used
to control process or process fugitive sources subject to the lead
emission standards in Sec. 63.1543 are exempt from the requirement in
Sec. 63.1543(c)(9) to be equipped with a bag leak detector. The owner or
operator of an affected source that uses a HEPA filter shall monitor and
record the pressure drop across the HEPA filter system daily. If the
pressure drop is outside the limit(s) specified by the filter
manufacturer, the owner or operator must take appropriate corrective
measures, which may include, but not be limited to, the following:
(1) Inspecting the filter and filter housing for air leaks and torn
or broken filters.
(2) Replacing defective filter media, or otherwise repairing the
control device.
(3) Sealing off a defective control device by routing air to other
control devices.
(4) Shutting down the process producing the particulate emissions.
(i) Owners and operators shall monitor sinter machine building in-
draft to demonstrate continued compliance with the operating standard
specified in Sec. 63.1543(c) in accordance with either paragraph (i)(1),
(i)(2), or (i)(3) of this section.
(1) Owners and operators shall check and record on a daily basis
doorway in-draft at each doorway in accordance with the methodology
specified in Sec. 63.1546(b).
(2) Owners and operators shall establish and maintain baseline
ventilation parameters which result in a positive in-draft according to
paragraphs (i)(2)(i) through (i)(2)(iv) of this section.
(i) Owners and operators shall install, calibrate, maintain, and
operate a monitoring device that continuously records the actual
volumetric flow rate through each separately ducted hood; or install,
calibrate, maintain, and operate a monitoring device that continuously
records the volumetric flow rate at the control device inlet of each
exhaust system ventilating the building. The flow rate monitoring
device(s) can be installed in any location in the exhaust duct such that
reproducible flow rate monitoring will result. The flow rate monitoring
device(s) shall have an accuracy of plus or minus 10 percent over its
normal operating range and shall be calibrated according to
manufacturer's instructions.
(ii) During the initial demonstration of sinter building in-draft,
and at any time the owner or operator wishes to re-establish the
baseline ventilation parameters, the owner or operator shall
continuously record the volumetric flow rate through each separately
ducted hood, or continuously record the volumetric flow rate at the
control device inlet of each exhaust system ventilating the building and
[[Page 102]]
record exhaust system damper positions. The owner or operator shall
determine the average volumetric flow rate(s) corresponding to the
period of time the in-draft compliance determinations are being
conducted.
(iii) The owner or operator shall maintain the volumetric flow
rate(s) at or above the value(s) established during the most recent in-
draft determination at all times the sinter machine is in operation.
Volumetric flow rate(s) shall be calculated as a 15-minute average.
(iv) If the volumetric flow rate is monitored at the control device
inlet, the owner or operator shall check and record damper positions
daily to ensure they are in the positions they were in during the most
recent in-draft determination.
(3) An owner or operator may request an alternative monitoring
method by following the procedures and requirements in Sec. 63.8(f) of
the General Provisions.
Sec. 63.1548 Notification requirements.
(a) The owner or operator of a primary lead smelter shall comply
with all of the notification requirements of Sec. 63.9 of subpart A,
General Provisions.
(b) The owner or operator of a primary lead smelter shall submit the
fugitive dust control standard operating procedures manual required
under Sec. 63.1544(a) and the standard operating procedures manual for
baghouses required under Sec. 63.1547(a) to the Administrator or
delegated authority along with a notification that the smelter is
seeking review and approval of these plans and procedures. Owners or
operators of existing primary lead smelters shall submit this
notification no later than November 6, 2000. The owner or operator of a
primary lead smelter that commences construction or reconstruction after
April 17, 1998, shall submit this notification no later than 180 days
before startup of the constructed or reconstructed primary lead smelter,
but no sooner than September 2, 1999.
Sec. 63.1549 Recordkeeping and reporting requirements.
(a) The owner or operator of a primary lead smelter shall comply
with all of the recordkeeping requirements of Sec. 63.10 of subpart A,
General Provisions.
(b) In addition to the general records required by paragraph (a) of
this section, each owner or operator of a primary lead smelter shall
maintain for a period of 5 years, records of the information listed in
paragraphs (b)(1) through (b)(8) of this section.
(1) Production records of the weight and lead content of lead
products, copper matte, and copper speiss.
(2) Records of the bag leak detection system output.
(3) An identification of the date and time of all bag leak detection
system alarms, the time that procedures to determine the cause of the
alarm were initiated, the cause of the alarm, an explanation of the
actions taken, and the date and time the cause of the alarm was
corrected.
(4) Any recordkeeping required as part of the practices described in
the standard operating procedures manual required under Sec. 63.1544(a)
for the control of fugitive dust emissions.
(5) Any recorkeeping required as part of the practices described in
the standard operating procedures manual for baghouses required under
Sec. 63.1547(a).
(6) If an owner or operator chooses to demonstrate continuous
compliance with the sinter building in-draft requirement under
Sec. 63.1543(c) by employing the method allowed in Sec. 63.1546(i)(1),
the records of the daily doorway in-draft checks, an identification of
the periods when there was not a positive in-draft, and an explanation
of the corrective actions taken.
(7) If an owner or operator chooses to demonstrate continuous
compliance with the sinter building in-draft requirement under
Sec. 63.1543(c) by employing the method allowed in Sec. 63.1546(i)(2),
the records of the output from the continuous volumetric flow
monitor(s), an identification of the periods when the 15-minute
volumetric flow rate dropped below the minimum established during the
most recent in-draft determination, and an explanation of the corrective
actions taken.
(8) If an owner or operator chooses to demonstrate continuous
compliance with the sinter building in-draft requirement under
Sec. 63.1543(c) by employing the method allowed in Sec. 63.1546(i)(2),
[[Page 103]]
and volumetric flow rate is monitored at the baghouse inlet, records of
the daily checks of damper positions, an identification of the days that
the damper positions were not in the positions established during the
most recent in-draft determination, and an explanation of the corrective
actions taken.
(c) Records for the most recent 2 years of operation must be
maintained on site. Records for the previous 3 years may be maintained
off site.
(d) The owner or operator of a primary lead smelter shall comply
with all of the reporting requirements of Sec. 63.10 of subpart A,
General Provisions.
(e) In addition to the information required under Sec. 63.10 of the
General Provisions, the owner or operator shall provide semi-annual
reports containing the information specified in paragraphs (e)(1)
through (e)(7) of this section to the Administrator or designated
authority.
(1) The reports shall include records of all alarms from the bag
leak detection system specified in Sec. 63.1547(e).
(2) The reports shall include a description of the actions taken
following each bag leak detection system alarm pursuant to
Sec. 63.1547(f).
(3) The reports shall include a calculation of the percentage of
time the alarm on the bag leak detection system sounded during the
reporting period pursuant to Sec. 63.1547(g).
(4) If an owner or operator chooses to demonstrate continuous
compliance with the sinter building in-draft requirement under
Sec. 63.1543(c) by employing the method allowed in Sec. 63.1546(i)(1),
the reports shall contain an identification of the periods when there
was not a positive in-draft, and an explanation of the corrective
actions taken.
(5) If an owner or operator chooses to demonstrate continuous
compliance with the sinter building in-draft requirement under
Sec. 63.1543(c) by employing the method allowed in Sec. 63.1546(i)(2),
the reports shall contain an identification of the periods when the 15-
minute volumetric flow rate(s) dropped below the minimum established
during the most recent in-draft determination, and an explanation of the
corrective actions taken.
(6) If an owner or operator chooses to demonstrate continuous
compliance with the sinter building in-draft requirement under
Sec. 63.1543(c) by employing the method allowed in Sec. 63.1546(i)(2),
and volumetric flow rate is monitored at the baghouse inlet, the reports
shall contain an identification of the days that the damper positions
were not in the positions established during the most recent in-draft
determination, and an explanation of the corrective actions taken.
(7) The reports shall contain a summary of the records maintained as
part of the practices described in the standard operating procedures
manual for baghouses required under Sec. 63.1547(a), including an
explanation of the periods when the procedures were not followed and the
corrective actions taken.
(8) The reports shall contain a summary of the fugitive dust control
measures performed during the required reporting period, including an
explanation of any periods when the procedures outlined in the standard
operating procedures manual required by Sec. 63.1544(a) were not
followed and the corrective actions taken. The reports shall not contain
copies of the daily records required to demonstrate compliance with the
requirements of the standard operating procedures manuals required under
Secs. 63.1544(a) and Sec. 63.1547(a).
Sec. 63.1550 Delegation of authority
(a) In delegating implementation and enforcement authority to a
State under section 112(1) of the act, the authorities contained in
paragraph (b) of this section shall be retained by the Administrator and
not transferred to a State.
(b) Authorities which will not be delegated to States: no
restrictions.
Effective Date Note: At 68 FR 37360, June 23, 2003, Sec. 63.1550 was
revised effective August 22, 2003. For the convenience of the user, the
revised text is set forth as follows:
Sec. 63.1550 Implementation and enforcement.
(a) This subpart will be implemented and enforced by the U.S. EPA,
or a delegated authority such as the applicable State, local, or Tribal
agency. If the U.S. EPA Administrator has delegated authority to a
State, local, or Tribal agency, then that agency, in addition to the
U.S. EPA, has the authority
[[Page 104]]
to implement and enforce this subpart. Contact the applicable U.S. EPA
Regional Office to find out if this subpart is delegated to a State,
local, or Tribal agency.
(b) In delegating implementation and enforcement authority of this
subpart to a State, local, or Tribal agency under subpart E of this
part, the authorities contained in paragraph (c) of this section are
retained by the Administrator of U.S. EPA and cannot be transferred to
the State, local, or Tribal agency.
(c) The authorities that cannot be delegated to State, local, or
Tribal agencies are as specified in paragraphs (c)(1) through (4) of
this section.
(1) Approval of alternatives to the requirements in Secs. 63.1541,
63.1543(a) through (c), (f) through (g), and 63.1544 through 63.1545.
(2) Approval of major alternatives to test methods under
Sec. 63.7(e)(2)(ii) and (f), as defined in Sec. 63.90, and as required
in this subpart.
(3) Approval of major alternatives to monitoring under Sec. 63.8(f),
as defined in Sec. 63.90, and as required in this subpart.
(4) Approval of major alternatives to recordkeeping and reporting
under Sec. 63.10(f), as defined in Sec. 63.90, and as required in this
subpart.
Table 1 to Subpart TTT of Part 63--Summary of Monitoring Requirements
for New and Existing Affected Sources and Emission Units
------------------------------------------------------------------------
Applies to subpart
Reference TTT Comment
------------------------------------------------------------------------
Sec. 63.1................... Yes
Sec. 63.2................... Yes
Sec. 63.3................... Yes
Sec. 63.4................... Yes
Sec. 63.5................... Yes
Sec. 63.6(a), (b), (c), (e), Yes
(f), (g), (i) and (j).
Sec. 63.6(d) and (h)........ No No opacity limits in
rule.
Sec. 63.7................... Yes
Sec. 63.8................... Yes
Sec. 63.9 (a), (b), (c), Yes
(d), (e), (g), (h)(1)
through (3), (h)(5) and (6),
(i) and (j).
Sec. 63.9(f) and (h)(4)..... No No opacity or visible
emission limits in
rule.
Sec. 63.10.................. Yes
Sec. 63.11.................. No Flares will not be
used to comply with
the emission limits.
Sec. 63.12 through 63.15.... Yes
------------------------------------------------------------------------
Subpart UUU--National Emission Standards for Hazardous Air Pollutants
for Petroleum Refineries: Catalytic Cracking Units, Catalytic Reforming
Units, and Sulfur Recovery Units
Source: 67 FR 17773, Apr. 11, 2002, unless otherwise noted.
What This Subpart Covers
Sec. 63.1560 What is the purpose of this subpart?
This subpart establishes national emission standards for hazardous
air pollutants (HAP) emitted from petroleum refineries. This subpart
also establishes requirements to demonstrate initial and continuous
compliance with the emission limitations and work practice standards.
Sec. 63.1561 Am I subject to this subpart?
(a) You are subject to this subpart if you own or operate a
petroleum refinery that is located at a major source of HAP emissions.
(1) A petroleum refinery is an establishment engaged primarily in
petroleum refining as defined in the Standard Industrial Classification
(SIC) code 2911 and the North American Industry Classification (NAIC)
code 32411, and used mainly for:
(i) Producing transportation fuels (such as gasoline, diesel fuels,
and jet fuels), heating fuels (such as kerosene, fuel gas distillate,
and fuel oils), or lubricants;
(ii) Separating petroleum; or
[[Page 105]]
(iii) Separating, cracking, reacting, or reforming an intermediate
petroleum stream, or recovering a by-product(s) from the intermediate
petroleum stream (e.g., sulfur recovery).
(2) A major source of HAP is a plant site that emits or has the
potential to emit any single HAP at a rate of 9.07 megagrams (10 tons)
or more per year or any combination of HAP at a rate of 22.68 megagrams
(25 tons) or more per year.
(b) [Reserved]
Sec. 63.1562 What parts of my plant are covered by this subpart?
(a) This subpart applies to each new, reconstructed, or existing
affected source at a petroleum refinery.
(b) The affected sources are:
(1) Each catalytic cracking unit that regenerates catalyst.
(2) Each catalytic reforming unit that regenerates catalyst.
(3) Each sulfur recovery unit and the tail gas treatment unit
serving it.
(4) Each bypass line serving a new, existing, or reconstructed
catalytic cracking unit, catalytic reforming unit, or sulfur recovery
unit. This means each vent system that contains a bypass line (e.g.,
ductwork) that could divert an affected vent stream away from a control
device used to comply with the requirements of this subpart.
(c) An affected source is a new affected source if you commence
construction of the affected source after September 11, 1998, and you
meet the applicability criteria in Sec. 63.1561 at the time you
commenced construction.
(d) Any affected source is reconstructed if you meet the criteria in
Sec. 63.2.
(e) An affected source is existing if it is not new or
reconstructed.
(f) This subpart does not apply to:
(1) A thermal catalytic cracking unit.
(2) A sulfur recovery unit that does not recover elemental sulfur or
where the modified reaction is carried out in a water solution which
contains a metal ion capable of oxidizing the sulfide ion to sulfur
(e.g., the LO-CAT II process).
(3) A redundant sulfur recovery unit not located at a petroleum
refinery and used by the refinery only for emergency or maintenance
backup.
(4) Equipment associated with bypass lines such as low leg drains,
high point bleed, analyzer vents, open-ended valves or lines, or
pressure relief valves needed for safety reasons.
(5) Gaseous streams routed to a fuel gas system.
Sec. 63.1563 When do I have to comply with this subpart?
(a) If you have a new or reconstructed affected source, you must
comply with this subpart according to the requirements in paragraphs
(a)(1) and (2) of this section.
(1) If you startup your affected source before April 11, 2002, then
you must comply with the emission limitations and work practice
standards for new and reconstructed sources in this subpart no later
than April 11, 2002.
(2) If you startup your affected source after April 11, 2002, you
must comply with the emission limitations and work practice standards
for new and reconstructed sources in this subpart upon startup of your
affected source.
(b) If you have an existing affected source, you must comply with
the emission limitations and work practice standards for existing
affected sources in this subpart by no later than April 11, 2005 except
as specified in paragraph (c) of this section.
(c) We will grant an extension of compliance for an existing
catalytic cracking unit allowing additional time to meet the emission
limitations and work practice standards for catalytic cracking units in
Secs. 63.1564 and 63.1565 if you commit to hydrotreating the catalytic
cracking unit feedstock and to meeting the emission limitations of this
subpart on the same date that your facility meets the final Tier 2
gasoline sulfur control standard (40 CFR part 80, subpart J). To obtain
an extension, you must submit a written notification to your permitting
authority according to the requirements in Sec. 63.1574(e). Your
notification must include the information in paragraphs (c)(1) and (2)
of this section.
(1) Identification of the affected source with a brief description
of the controls to be installed (if needed) to
[[Page 106]]
comply with the emission limitations for catalytic cracking units in
this subpart.
(2) A compliance schedule, including the information in paragraphs
(c)(2)(i) through (iv) of this section.
(i) The date by which onsite construction or the process change is
to be initiated.
(ii) The date by which onsite construction or the process change is
to be completed.
(iii) The date by which your facility will achieve final compliance
with both the final Tier 2 gasoline sulfur control standard as specified
in Sec. 80.195, and the emission limitations and work practice standards
for catalytic cracking units in this subpart. In no case will your
permitting authority grant an extension beyond the date you are required
to meet the Tier 2 gasoline sulfur control standard or December 31,
2009, whichever comes first. If you don't comply with the emission
limitations and work practice standards for existing catalytic cracking
units by the specified date, you will be out-of-compliance with the
requirements for catalytic cracking units beginning April 11, 2005.
(iv) A brief description of interim emission control measures that
will be taken to ensure proper operation and maintenance of the process
equipment during the period of the compliance extension.
(d) If you have an area source that increases its emissions or its
potential to emit such that it becomes a major source of HAP, the
requirements in paragraphs (d)(1) and (2) of this section apply.
(1) Any portion of the existing facility that is a new affected
source or a new reconstructed source must be in compliance with the
requirements of this subpart upon startup.
(2) All other parts of the source must be in compliance with the
requirements of this subpart by no later than 3 years after it becomes a
major source or, if applicable, the extended compliance date granted
according to the requirements in paragraph (c) of this section.
(e) You must meet the notification requirements in Sec. 63.1574
according to the schedule in Sec. 63.1574 and in 40 CFR part 63, subpart
A. Some of the notifications must be submitted before the date you are
required to comply with the emission limitations and work practice
standards in this subpart.
Catalytic Cracking Units, Catalytic Reforming Units, Sulfur Recovery
Units, and Bypass Lines
Sec. 63.1564 What are my requirements for metal HAP emissions from catalytic cracking units?
(a) What emission limitations and work practice standards must I
meet? You must:
(1) Meet each emission limitation in Table 1 of this subpart that
applies to you. If your catalytic cracking unit is subject to the NSPS
for PM in Sec. 60.102 of this chapter, you must meet the emission
limitations for NSPS units. If your catalytic cracking unit isn't
subject to the NSPS for PM, you can choose from the four options in
paragraphs (a)(1)(i) through (iv) of this section:
(i) You can elect to comply with the NSPS requirements (Option 1);
(ii) You can elect to comply with the PM emission limit (Option 2);
(iii) You can elect to comply with the Nickel (Ni) lb/hr emission
limit (Option 3); or
(iv) You can elect to comply with the Ni lb/1,000 lbs of coke burn-
off emission limit (Option 4).
(2) Comply with each operating limit in Table 2 of this subpart that
applies to you.
(3) Prepare an operation, maintenance, and monitoring plan according
to the requirements in Sec. 63.1574(f) and operate at all times
according to the procedures in the plan.
(4) The emission limitations and operating limits for metal HAP
emissions from catalytic cracking units required in paragraphs (a)(1)
and (2) of this section do not apply during periods of planned
maintenance preapproved by the applicable permitting authority according
to the requirements in Sec. 63.1575(j).
(b) How do I demonstrate initial compliance with the emission
limitations and work practice standard? You must:
[[Page 107]]
(1) Install, operate, and maintain a continuous monitoring system(s)
according to the requirements in Sec. 63.1572 and Table 3 of this
subpart.
(2) Conduct a performance test for each catalytic cracking unit not
subject to the NSPS for PM according to the requirements in Sec. 63.1571
and under the conditions specified in Table 4 of this subpart.
(3) Establish each site-specific operating limit in Table 2 of this
subpart that applies to you according to the procedures in Table 4 of
this subpart.
(4) Use the procedures in paragraphs (b)(4)(i) through (iv) of this
section to determine initial compliance with the emission limitations.
(i) If you elect Option 1 in paragraph (a)(1)(i) of ths section, the
NSPS requirements, compute the PM emission rate (lb/1,000 lbs of coke
burn-off) for each run using Equations 1, 2, and 3 (if applicable) of
this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.000
Where:
Rc = Coke burn-off rate, kg/hr (lb/hr);
Qr = Volumetric flow rate of exhaust gas from catalyst
regenerator before adding air or gas streams. Example: You may measure
after an electrostatic precipitator, but you must measure before a
carbon monoxide boiler, dscm/min (dscf/min);
Qa = Volumetric flow rate of air to catalytic cracking unit
catalyst regenerator, as determined from instruments in the catalytic
cracking unit control room, dscm/min (dscf/min);
%CO2 = Carbon dioxide concentration in regenerator exhaust,
percent by volume (dry basis);
%CO = Carbon monoxide concentration in regenerator exhaust, percent by
volume (dry basis);
%O2 = Oxygen concentration in regenerator exhaust, percent by
volume (dry basis);
K1 = Material balance and conversion factor, 0.2982 (kg-min)/
(hr-dscm-%) (0.0186 (lb-min)/(hr-dscf-%));
K2 = Material balance and conversion factor, 2.088 (kg-min)/
(hr-dscm) (0.1303 (lb-min)/(hr-dscf));
K3 = Material balance and conversion factor, 0.0994 (kg-min)/
(hr-dscm-%) (0.0062 (lb-min)/(hr-dscf-%));
Qoxy = Volumetric flow rate of oxygen-enriched air stream to
regenerator, as determined from instruments in the catalytic cracking
unit control room, dscm/min (dscf/min); and
%Oxy = Oxygen concentration in oxygen-enriched air stream,
percent by volume (dry basis).
[GRAPHIC] [TIFF OMITTED] TR11AP02.001
Where:
E = Emission rate of PM, kg/1,000 kg (lb/1,000 lb) of coke burn-off;
Cs = Concentration of PM, g/dscm (lb/dscf);
Qsd = Volumetric flow rate of the catalytic cracking unit
catalyst regenerator flue gas as measured by Method 2 in appendix A to
part 60 of this chapter, dscm/hr (dscf/hr);
Rc = Coke burn-off rate, kg coke/hr (1,000 lb coke/hr); and
K = Conversion factor, 1.0 (kg\2\/g)/(1,000 kg) (1,000 lb/(1,000 lb)).
[GRAPHIC] [TIFF OMITTED] TR11AP02.002
Where:
Es = Emission rate of PM allowed, kg/1,000 kg (1b/1,000 lb)
of coke burn-off in catalyst regenerator;
1.0 = Emission limitation, kg coke/1,000 kg (lb coke/1,000 lb);
A = Allowable incremental rate of PM emissions, 0.18 g/million cal (0.10
lb/million Btu); and
H = Heat input rate from solid or liquid fossil fuel, million cal/hr
(million Btu/hr). Make sure your permitting authority approves
procedures for determining the heat input rate.
Rc = Coke burn-off rate, kg coke/hr (1,000 lb coke/hr)
determined using Equation 1 of this section; and
K' = Conversion factor to units to standard, 1.0 (kg\2\/g)/(1,000 kg)
(10\3\ lb/(1,000 lb)).
(ii) If you elect Option 2 in paragraph (a)(1)(ii) of this section,
the PM emission limit, compute your PM emission rate (lb/1,000 lbs of
coke burn-off) using Equations 1 and 2 of this section and your site-
specific opacity operating limit (if you use a continuous opacity
monitoring system) using Equation 4 of this section as follows:
[[Page 108]]
[GRAPHIC] [TIFF OMITTED] TR11AP02.003
Where:
Opacity limit = Maximum permissible hourly average opacity, percent, or
10 percent, whichever is greater;
Opacityst = Hourly average opacity measured during the source
test runs, percent; and
PMEmRst = PM emission rate measured during the source test,
lb/1,000 lbs coke burn.
[GRAPHIC] [TIFF OMITTED] TR11AP02.004
(iii) If you elect Option 3 in paragraph (a)(1)(iii) of this
section, the Ni lb/hr emission limit, compute your Ni emission rate
using Equation 5 of this section and your site-specific Ni operating
limit (if you use a continuous opacity monitoring system) using
Equations 6 and 7 of this section as follows:
Where:
ENi1 = Mass emission rate of Ni, mg/hr (lb/hr); and
CNi = Ni concentration in the catalytic cracking unit
catalyst regenerator flue gas as measured by Method 29 in appendix A to
part 60 of this chapter, mg/dscm (lbs/dscf).
[GRAPHIC] [TIFF OMITTED] TR11AP02.005
Where:
Opacityl = Opacity value for use in Equation 7 of this
section, percent, or 10 percent, whichever is greater; and
NiEmR1st = Average Ni emission rate calculated as the
arithmetic average Ni emission rate using Equation 5 of this section for
each of the performance test runs, g Ni/hr.
[GRAPHIC] [TIFF OMITTED] TR11AP02.006
Where:
Ni operating limit1 = Maximum permissible hourly average Ni
operating limit, percent-acfm-ppmw, i.e., your site-specific Ni
operating limit;
Qmon,st = Hourly average actual gas flow rate as measured by
the continuous parameter monitoring system during the performance test
or using the alternative procedure in Sec. 63.1573, acfm; and
E-Catst = Ni concentration on equilibrium catalyst measured
during source test, ppmw.
(iv) If you elect Option 4 in paragraph (a)(1)(iv) of this section,
the Ni lbs/1,000 lbs of coke burn-off emission limit, compute your Ni
emission rate using Equations 1 and 8 of this section and your site-
specific Ni operating limit (if you use a continuous opacity monitoring
system) using Equations 9 and 10 of this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.007
Where:
ENi2 = Normalized mass emission rate of Ni, mg/kg coke (lb/
1,000 lbs coke).
[[Page 109]]
[GRAPHIC] [TIFF OMITTED] TR11AP02.008
Where:
Opacity2 = Opacity value for use in Equation 10 of this
section, percent, or 10 percent, whichever is greater; and
NiEmR2st = Average Ni emission rate calculated as the
arithmetic average Ni emission rate using Equation 8 of this section for
each of the performance test runs, mg/kg coke.
[GRAPHIC] [TIFF OMITTED] TR11AP02.009
Where:
Ni operating limit2 = Maximum permissible hourly average Ni
operating limit, percent-ppmw-acfm-hr/kg coke, i.e., your site-specific
Ni operating limit; and
Rc,st = Coke burn rate from Equation 1 of this section, as
measured during the initial performance test, kg coke/hr.
(5) Demonstrate initial compliance with each emission limitation
that applies to you according to Table 5 of this subpart.
(6) Demonstrate initial compliance with the work practice standard
in paragraph (a)(3) of this section by submitting your operation,
maintenance, and monitoring plan to your permitting authority as part of
your Notification of Compliance Status.
(7) Submit the Notification of Compliance Status containing the
results of the initial compliance demonstration according to the
requirements in Sec. 63.1574.
(c) How do I demonstrate continuous compliance with the emission
limitations and work practice standards? You must:
(1) Demonstrate continuous compliance with each emission limitation
in Tables 1 and 2 of this subpart that applies to you according to the
methods specified in Tables 6 and 7 of this subpart.
(2) Demonstrate continuous compliance with the work practice
standard in paragraph (a)(3) of this section by maintaining records to
document conformance with the procedures in your operation, maintenance,
and monitoring plan.
(3) If you use a continuous opacity monitoring system and elect to
comply with Option 3 in paragraph (a)(1)(iii) of this section, determine
continuous compliance with your site-specific Ni operating limit by
using Equation 11 of this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.010
Where:
Ni operating value1 = Maximum permissible hourly average Ni
standard operating value, %-acfm-ppmw;
Opacity = Hourly average opacity, percent;
Qmon = Hourly average actual gas flow rate as measured by
continuous parameter monitoring system or calculated by alternative
procedure in Sec. 63.1573, acfm; and
E-Cat = Ni concentration on equilibrium catalyst from weekly or more
recent measurement, ppmw.
(4) If you use a continuous opacity monitoring system and elect to
comply with Option 4 in paragraph (a)(1)(iv) of this section, determine
continuous
[[Page 110]]
compliance with your site-specific Ni operating limit by using Equation
12 of this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.011
Where:
Ni operating value2 = Maximum permissible hourly average Ni
standard operating value, percent-acfm-ppmw-hr/kg coke.
Sec. 63.1565 What are my requirements for organic HAP emissions from catalytic cracking units?
(a) What emission limitations and work practice standards must I
meet? You must:
(1) Meet each emission limitation in Table 8 of this subpart that
applies to you. If your catalytic cracking unit is subject to the NSPS
for carbon monoxide (CO) in Sec. 60.103 of this chapter, you must meet
the emission limitations for NSPS units. If your catalytic cracking unit
isn't subject to the NSPS for CO, you can choose from the two options in
paragraphs (a)(1)(i) through (ii) of this section:
(i) You can elect to comply with the NSPS requirements (Option 1);
or
(ii) You can elect to comply with the CO emission limit (Option 2).
(2) Comply with each site-specific operating limit in Table 9 of
this subpart that applies to you.
(3) Prepare an operation, maintenance, and monitoring plan according
to the requirements in Sec. 63.1574(f) and operate at all times
according to the procedures in the plan.
(4) The emission limitations and operating limits for organic HAP
emissions from catalytic cracking units required in paragraphs (a)(1)
and (2) of this section do not apply during periods of planned
maintenance preapproved by the applicable permitting authority according
to the requirements in Sec. 63.1575(j).
(b) How do I demonstrate initial compliance with the emission
limitations and work practice standards? You must:
(1) Install, operate, and maintain a continuous monitoring system
according to the requirements in Sec. 63.1572 and Table 10 of this
subpart. Except:
(i) Whether or not your catalytic cracking unit is subject to the
NSPS for CO in Sec. 60.103 of this chapter, you don't have to install
and operate a continuous emission monitoring system if you show that CO
emissions from your vent average less than 50 parts per million (ppm),
dry basis. You must get an exemption from your permitting authority,
based on your written request. To show that the emissions average is
less than 50 ppm (dry basis), you must continuously monitor CO emissions
for 30 days using a CO continuous emission monitoring system that meets
the requirements in Sec. 63.1572.
(ii) If your catalytic cracking unit isn't subject to the NSPS for
CO, you don't have to install and operate a continuous emission
monitoring system or a continuous parameter monitoring system if you
vent emissions to a boiler (including a ``CO boiler'') or process heater
that has a design heat input capacity of at least 44 megawatts (MW).
(iii) If your catalytic cracking unit isn't subject to the NSPS for
CO, you don't have to install and operate a continuous emission
monitoring system or a continuous parameter monitoring system if you
vent emissions to a boiler or process heater in which all vent streams
are introduced into the flame zone.
(2) Conduct each performance test for a catalytic cracking unit not
subject to the NSPS for CO according to the requirements in Sec. 63.1571
and under the conditions specified in Table 11 of this subpart.
(3) Establish each site-specific operating limit in Table 9 of this
subpart that applies to you according to the procedures in Table 11 of
this subpart.
[[Page 111]]
(4) Demonstrate initial compliance with each emission limitation
that applies to you according to Table 12 of this subpart.
(5) Demonstrate initial compliance with the work practice standard
in paragraph (a)(3) of this section by submitting the operation,
maintenance, and monitoring plan to your permitting authority as part of
your Notification of Compliance Status according to Sec. 63.1574.
(6) Submit the Notification of Compliance Status containing the
results of the initial compliance demonstration according to the
requirements in Sec. 63.1574.
(c) How do I demonstrate continuous compliance with the emission
limitations and work practice standards? You must:
(1) Demonstrate continuous compliance with each emission limitation
in Tables 8 and 9 of this subpart that applies to you according to the
methods specified in Tables 13 and 14 of this subpart.
(2) Demonstrate continuous compliance with the work practice
standard in paragraph (a)(3) of this section by complying with the
procedures in your operation, maintenance, and monitoring plan.
Sec. 63.1566 What are my requirements for organic HAP emissions from catalytic reforming units?
(a) What emission limitations and work practice standards must I
meet? You must:
(1) Meet each emission limitation in Table 15 of this subpart that
applies to you. You can choose from the two options in paragraphs
(a)(1)(i) through (ii) of this section:
(i) You can elect to vent emissions of total organic compounds (TOC)
to a flare that meets the control device requirements in Sec. 63.11(b)
(Option 1); or
(ii) You can elect to use a control device to meet a TOC percent
reduction standard or concentration limit, whichever is less stringent
(Option 2).
(2) Comply with each site-specific operating limit in Table 16 of
this subpart that applies to you.
(3) The emission limitations in Tables 15 and 16 of this subpart
apply to emissions from catalytic reforming unit process vents that
occur during depressuring and purging operations. These process vents
include those used during unit depressurization, purging, coke burn,
catalyst rejuvenation, and reduction or activation purge.
(4) The emission limitations in Tables 15 and 16 of this subpart do
not apply to emissions from process vents during depressuring and
purging operations when the reactor vent pressure is 5 pounds per square
inch gauge (psig) or less.
(5) Prepare an operation, maintenance, and monitoring plan according
to the requirements in Sec. 63.1574(f) and operate at all times
according to the procedures in the plan.
(b) How do I demonstrate initial compliance with the emission
limitations and work practice standard? You must:
(1) Install, operate, and maintain a continuous monitoring system(s)
according to the requirements in Sec. 63.1572 and Table 17 of this
subpart.
(2) Conduct each performance test for a catalytic reforming unit
according to the requirements in Sec. 63.1571 and under the conditions
specified in Table 18 of this subpart.
(3) Establish each site-specific operating limit in Table 16 of this
subpart that applies to you according to the procedures in Table 18 of
this subpart.
(4) Use the procedures in paragraph (b)(4)(i) or (ii) of this
section to determine initial compliance with the emission limitations.
(i) If you elect the percent reduction standard under Option 2,
calculate the emission rate of TOC using Equation 1 of this section (if
you use Method 25) or Equation 2 of this section (if you use Method
25A); then calculate the mass emission reduction using Equation 3 of
this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.012
Where:
E = Emission rate of TOC in the vent stream, kilograms-C per hour;
K 4 = Constant, 6.0 x 10-5 (kilograms per
milligram)(minutes per hour);
M c = Mass concentration of total gaseous nonmethane organic
as measured and calculated using Method 25 in appendix A to part 60 of
this chapter, mg/dscm; and
[[Page 112]]
Q s = Vent stream flow rate, dscm/min, at a temperature of 20
degrees Celsius (C).
[GRAPHIC] [TIFF OMITTED] TR11AP02.013
Where:
E = Emission rate of TOC in the vent stream, kilograms-C per hour;
K 5 = Constant, 9.0x10-5(parts per million)
-1 (gram-mole per standard cubic meter) (gram-C per gram-
mole-propane) (kilogram per gram) (minutes per hour), where the standard
temperature (standard cubic meter) is at 20 degrees C (uses 36g-C/g.mole
propane);
C TOC = Concentration of TOC on a dry basis in ppmv as
propane as measured by Method 25A in appendix A to part 60 of this
chapter; and
Q s = Vent stream flow rate, dry standard cubic meters per
minute, at a temperature of 20 degrees C.
[GRAPHIC] [TIFF OMITTED] TR11AP02.014
Where:
E i = Mass emission rate of TOC at control device inlet, kg/
hr; and
E o = Mass emission rate of TOC at control device outlet, kg/
hr.
(5) If you elect the 20 parts per million by volume (ppmv)
concentration limit, correct the measured TOC concentration for oxygen
(O2) content in the gas stream using Equation 4 of this
section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.015
(6) You are not required to do a TOC performance test if:
(i) You elect to vent emissions to a flare as provided in paragraph
(a)(1)(i) of this section (Option 1); or
(ii) You elect the TOC percent reduction or concentration limit in
paragraph (a)(1)(ii) of this section (Option 2), and you use a boiler or
process heater with a design heat input capacity of 44 MW or greater or
a boiler or process heater in which all vent streams are introduced into
the flame zone.
(7) Demonstrate initial compliance with each emission limitation
that applies to you according to Table 19 of this subpart.
(8) Demonstrate initial compliance with the work practice standard
in paragraph (a)(5) of this section by submitting the operation,
maintenance, and monitoring plan to your permitting authority as part of
your Notification of Compliance Status.
(9) Submit the Notification of Compliance Status containing the
results of the initial compliance demonstration according to the
requirements in Sec. 63.1574.
(c) How do I demonstrate continuous compliance with the emission
limitations and work practice standards? You must:
(1) Demonstrate continuous compliance with each emission limitation
in Tables 15 and 16 of this subpart that applies to you according to the
methods specified in Tables 20 and 21 of this subpart.
(2) Demonstrate continuous compliance with the work practice
standards in paragraph (a)(3) of this section by complying with the
procedures in your operation, maintenance, and monitoring plan.
[[Page 113]]
Sec. 63.1567 What are my requirements for inorganic HAP emissions from catalytic reforming units?
(a) What emission limitations and work practice standards must I
meet? You must:
(1) Meet each emission limitation in Table 22 of this subpart that
applies to you. These emission limitations apply during coke burn-off
and catalyst rejuvenation. You can choose from the two options in
paragraphs (a)(1)(i) through (ii) of this section:
(i) You can elect to use a control device to meet either a percent
reduction standard for hydrogen chloride (HCl) emissions (Option 1); or
(ii) You can elect to meet an HCl concentration limit (Option 2).
(2) Meet each site-specific operating limit in Table 23 of this
subpart that applies to you. These operating limits apply during coke
burn-off and catalyst rejuvenation.
(3) Prepare an operation, maintenance, and monitoring plan according
to the requirements in Sec. 63.1574(f) and operate at all times
according to the procedures in the plan.
(b) How do I demonstrate initial compliance with the emission
limitations and work practice standard? You must:
(1) Install, operate, and maintain a continuous monitoring system(s)
according to the requirements in Sec. 63.1572 and Table 24 of this
subpart.
(2) Conduct each performance test for a catalytic reforming unit
according to the requirements in Sec. 63.1571 and the conditions
specified in Table 25 of this subpart.
(3) Establish each site-specific operating limit in Table 23 of this
subpart that applies to you according to the procedures in Table 25 of
this subpart.
(4) Demonstrate initial compliance with each emission limitation
that applies to you according to Table 26 of this subpart.
(5) Demonstrate initial compliance with the work practice standard
in paragraph (a)(3) of this section by submitting the operation,
maintenance, and monitoring plan to your permitting authority as part of
your Notification of Compliance Status.
(6) Submit the Notification of Compliance Status containing the
results of the initial compliance demonstration according to the
requirements in Sec. 63.1574.
(c) How do I demonstrate continuous compliance with the emission
limitations and work practice standard? You must:
(1) Demonstrate continuous compliance with each emission limitation
in Tables 22 and 23 of this subpart that applies to you according to the
methods specified in Tables 27 and 28 of this subpart.
(2) Demonstrate continuous compliance with the work practice
standard in paragraph (a)(3) of this section by maintaining records to
document conformance with the procedures in your operation, maintenance
and monitoring plan.
Sec. 63.1568 What are my requirements for HAP emissions from sulfur recovery units?
(a) What emission limitations and work practice standard must I
meet? You must:
(1) Meet each emission limitation in Table 29 of this subpart that
applies to you. If your sulfur recovery unit is subject to the NSPS for
sulfur oxides in Sec. 60.104 of this chapter, you must meet the emission
limitations for NSPS units. If your sulfur recovery unit isn't subject
to the NSPS for sulfur oxides, you can choose from the options in
paragraphs (a)(1)(i) through (ii) of this section:
(i) You can elect to meet the NSPS requirements (Option 1); or
(ii) You can elect to meet the total reduced sulfur (TRS) emission
limitation (Option 2).
(2) Meet each operating limit in Table 30 of this subpart that
applies to you.
(3) Prepare an operation, maintenance, and monitoring plan according
to the requirements in Sec. 63.1574(f) and operate at all times
according to the procedures in the plan.
(b) How do I demonstrate initial compliance with the emission
limitations and work practice standards? You must:
(1) Install, operate, and maintain a continuous monitoring system
according to the requirements in Sec. 63.1572 and Table 31 of this
subpart.
(2) Conduct each performance test for a sulfur recovery unit not
subject to the NSPS for sulfur oxides according to the requirements in
Sec. 63.1571 and under
[[Page 114]]
the conditions specified in Table 32 of this subpart.
(3) Establish each site-specific operating limit in Table 30 of this
subpart that applies to you according to the procedures in Table 32 of
this subpart.
(4) Correct the reduced sulfur samples to zero percent excess air
using Equation 1 of this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.016
Where:
Cadj = pollutant concentration adjusted to zero percent
oxygen, ppm or g/dscm;
Cmeas = pollutant concentration measured on a dry basis, ppm
or g/dscm;
20.9c = 20.9 percent oxygen--0.0 percent oxygen (defined
oxygen correction basis), percent;
20.9 = oxygen concentration in air, percent;
%O2 = oxygen concentration measured on a dry basis, percent.
(5) Demonstrate initial compliance with each emission limitation
that applies to you according to Table 33 of this subpart.
(6) Demonstrate initial compliance with the work practice standard
in paragraph (a)(3) of this section by submitting the operation,
maintenance, and monitoring plan to your permitting authority as part of
your notification of compliance status.
(7) Submit the notification of compliance status containing the
results of the initial compliance demonstration according to the
requirements in Sec. 63.1574.
(c) How do I demonstrate continuous compliance with the emission
limitations and work practice standards? You must:
(1) Demonstrate continuous compliance with each emission limitation
in Tables 29 and 30 of this subpart that applies to you according to the
methods specified in Tables 34 and 35 of this subpart.
(2) Demonstrate continuous compliance with the work practice
standard in paragraph (a)(3) of this section by complying with the
procedures in your operation, maintenance, and monitoring plan.
Sec. 63.1569 What are my requirements for HAP emissions from bypass lines?
(a) What work practice standards must I meet? (1) You must meet each
work practice standard in Table 36 of this subpart that applies to you.
You can choose from the four options in paragraphs (a)(1)(i) through
(iv) of this section:
(i) You can elect to install an automated system (Option 1);
(ii) You can elect to use a manual lock system (Option 2);
(iii) You can elect to seal the line (Option 3); or
(iv) You can elect to vent to a control device (Option 4).
(2) As provided in Sec. 63.6(g), we, the EPA, may choose to grant
you permission to use an alternative to the work practice standard in
paragraph (a)(1) of this section.
(3) You must prepare an operation, maintenance, and monitoring plan
according to the requirements in Sec. 63.1574(f) and operate at all
times according to the procedures in the plan.
(b) How do I demonstrate initial compliance with the work practice
standards? You must:
(1) If you elect the option in paragraph (a)(1)(i) of this section,
conduct each performance test for a bypass line according to the
requirements in Sec. 63.1571 and under the conditions specified in Table
37 of this subpart.
(2) Demonstrate initial compliance with each work practice standard
in Table 36 of this subpart that applies to you according to Table 38 of
this subpart.
(3) Demonstrate initial compliance with the work practice standard
in paragraph (a)(3) of this section by submitting the operation,
maintenance,
[[Page 115]]
and monitoring plan to your permitting authority as part of your
notification of compliance status.
(4) Submit the notification of compliance status containing the
results of the initial compliance demonstration according to the
requirements in Sec. 63.1574.
(c) How do I demonstrate continuous compliance with the work
practice standards? You must:
(1) Demonstrate continuous compliance with each work practice
standard in Table 36 of this subpart that applies to you according to
the requirements in Table 39 of this subpart.
(2) Demonstrate continuous compliance with the work practice
standard in paragraph (a)(2) of this section by complying with the
procedures in your operation, maintenance, and monitoring plan.
General Compliance Requirements
Sec. 63.1570 What are my general requirements for complying with this subpart?
(a) You must be in compliance with all of the non-opacity standards
in this subpart during the times specified in Sec. 63.6(f)(1).
(b) You must be in compliance with the opacity and visible emission
limits in this subpart during the times specified in Sec. 63.6(h)(1).
(c) You must always operate and maintain your affected source,
including air pollution control and monitoring equipment, according to
the provisions in Sec. 63.6(e)(1)(i). During the period between the
compliance date specified for your affected source and the date upon
which continuous monitoring systems have been installed and validated
and any applicable operating limits have been set, you must maintain a
log detailing the operation and maintenance of the process and emissions
control equipment.
(d) You must develop and implement a written startup, shutdown, and
malfunction plan (SSMP) according to the provisions in Sec. 63.6(e)(3).
(e) During periods of startup, shutdown, and malfunction, you must
operate in accordance with your SSMP.
(f) You must report each instance in which you did not meet each
emission limitation and each operating limit in this subpart that
applies to you. This includes periods of startup, shutdown, and
malfunction. You also must report each instance in which you did not
meet the work practice standards in this subpart that apply to you.
These instances are deviations from the emission limitations and work
practice standards in this subpart. These deviations must be reported
according to the requirements in Sec. 63.1575.
(g) Consistent with Secs. 63.6(e) and 63.7(e)(1), deviations that
occur during a period of startup, shutdown, or malfunction are not
violations if you demonstrate to the Administrator's satisfaction that
you were operating in accordance with the SSMP. The SSMP must require
that good air pollution control practices are used during those periods.
The plan must also include elements designed to minimize the frequency
of such periods (i.e., root cause analysis). The Administrator will
determine whether deviations that occur during a period of startup,
shutdown, or malfunction are violations, according to the provisions in
Sec. 63.6(e) and the contents of the SSMP.
Sec. 63.1571 How and when do I conduct a performance test or other initial compliance demonstration?
(a) When must I conduct a performance test? You must conduct
performance tests and report the results by no later than 150 days after
the compliance date specified for your source in Sec. 63.1563 and
according to the provisions in Sec. 63.7(a)(2). If you are required to
do a performance evaluation or test for a semi-regenerative catalytic
reforming unit catalyst regenerator vent, you may do them at the first
regeneration cycle after your compliance date and report the results in
a followup Notification of Compliance Status report due no later than
150 days after the test.
(1) For each emission limitation or work practice standard where
initial compliance is not demonstrated using a performance test, opacity
observation, or visible emission observation, you must conduct the
initial compliance demonstration within 30 calendar days after the
compliance date that is specified for your source in Sec. 63.1563.
(2) For each emission limitation where the averaging period is 30
days,
[[Page 116]]
the 30-day period for demonstrating initial compliance begins at 12:00
a.m. on the compliance date that is specified for your source in
Sec. 63.1563 and ends at 11:59 p.m., 30 calendar days after the
compliance date that is specified for your source in Sec. 63.1563.
(3) If you commenced construction or reconstruction between
September 11, 1998 and April 11, 2002, you must demonstrate initial
compliance with either the proposed emission limitation or the
promulgated emission limitation no later than October 8, 2002 or within
180 calendar days after startup of the source, whichever is later,
according to Sec. 63.7(a)(2)(ix).
(4) If you commenced construction or reconstruction between
September 11, 1998 and April 11, 2002, and you chose to comply with the
proposed emission limitation when demonstrating initial compliance, you
must conduct a second compliance demonstration for the promulgated
emission limitation by October 10, 2005, or after startup of the source,
whichever is later, according to Sec. 63.7(a)(2)(ix).
(b) What are the general requirements for performance test and
performance evaluations? You must:
(1) Conduct each performance test according to the requirements in
Sec. 63.7(e)(1).
(2) Except for opacity and visible emission observations, conduct
three separate test runs for each performance test as specified in
Sec. 63.7(e)(3). Each test run must last at least 1 hour.
(3) Conduct each performance evaluation according to the
requirements in Sec. 63.8(e).
(4) Not conduct performance tests during periods of startup,
shutdown, or malfunction, as specified in Sec. 63.7(e)(1).
(5) Calculate the average emission rate for the performance test by
calculating the emission rate for each individual test run in the units
of the applicable emission limitation using Equation 2, 5, or 8 of
Sec. 63.1564, and determining the arithmetic average of the calculated
emission rates.
(c) What procedures must I use for an engineering assessment? You
may choose to use an engineering assessment to calculate the process
vent flow rate, net heating value, TOC emission rate, and total organic
HAP emission rate expected to yield the highest daily emission rate when
determining the emission reduction or outlet concentration for the
organic HAP standard for catalytic reforming units. If you use an
engineering assessment, you must document all data, assumptions, and
procedures to the satisfaction of the applicable permitting authority.
An engineering assessment may include the approaches listed in
paragraphs (c)(1) through (c)(4) of this section. Other engineering
assessments may be used but are subject to review and approval by the
applicable permitting authority.
(1) You may use previous test results provided the tests are
representative of current operating practices at the process unit, and
provided EPA methods or approved alternatives were used;
(2) You may use bench-scale or pilot-scale test data representative
of the process under representative operating conditions;
(3) You may use maximum flow rate, TOC emission rate, organic HAP
emission rate, or organic HAP or TOC concentration specified or implied
within a permit limit applicable to the process vent; or
(4) You may use design analysis based on engineering principles,
measurable process parameters, or physical or chemical laws or
properties. Examples of analytical methods include, but are not limited
to:
(i) Use of material balances based on process stoichiometry to
estimate maximum TOC concentrations;
(ii) Calculation of hourly average maximum flow rate based on
physical equipment design such as pump or blower capacities; and
(iii) Calculation of TOC concentrations based on saturation
conditions.
(d) Can I adjust the process or control device measured values when
establishing an operating limit? If you do a performance test to
demonstrate compliance, you must base the process or control device
operating limits for continuous parameter monitoring systems on the
results measured during the performance test. You may adjust the values
measured during the performance test according to the criteria in
paragraphs (d)(1) through (3) of this section.
[[Page 117]]
(1) If you must meet the HAP metal emission limitations in
Sec. 63.1564, you elect the option in paragraph (a)(1)(iii) in
Sec. 63.1564 (Ni lb/hr), and you use continuous parameter monitoring
systems, you must establish an operating limit for the equilibrium
catalyst Ni concentration based on the laboratory analysis of the
equilibrium catalyst Ni concentration from the initial performance test.
Section 63.1564(b)(2) allows you to adjust the laboratory measurements
of the equilibrium catalyst Ni concentration to the maximum level. You
must make this adjustment using Equation 1 of this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.017
Where:
Ecat-Limit = Operating limit for equilibrium catalyst Ni concentration,
mg/kg;
NiEmR1st = Average Ni emission rate calculated as the
arithmetic average Ni emission rate using Equation 5 of this section for
each performance test run, g Ni/hr; and
Ecatst = Average equilibrium Ni concentration from laboratory
test results, mg/kg.
(2) If you must meet the HAP metal emission limitations in
Sec. 63.1564, you elect the option in paragraph (a)(1)(iv) in
Sec. 63.1564 (Ni lb/1,000 lb of coke burn-off), and you use continuous
parameter monitoring systems, you must establish an operating limit for
the equilibrium catalyst Ni concentration based on the laboratory
analysis of the equilibrium catalyst Ni concentration from the initial
performance test. Section 63.1564(b)(2) allows you to adjust the
laboratory measurements of the equilibrium catalyst Ni concentration to
the maximum level. You must make this adjustment using Equation 2 of
this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.018
Where:
NiEmR2st = Average Ni emission rate calculated as the
arithmetic average Ni emission rate using Equation 8 of Sec. 63.1564 for
each performance test run, mg/kg coke burn-off.
(3) If you choose to adjust the equilibrium catalyst Ni
concentration to the maximum level, you can't adjust any other monitored
operating parameter (i.e., gas flow rate, voltage, pressure drop,
liquid-to-gas ratio).
(4) Except as specified in paragraph (d)(3) of this section, if you
use continuous parameter monitoring systems, you may adjust one of your
monitored operating parameters (flow rate, voltage and secondary
current, pressure drop, liquid-to-gas ratio) from the average of
measured values during the performance test to the maximum value (or
minimum value, if applicable) representative of worst-case operating
conditions, if necessary. This adjustment of measured values may be done
using control device design specifications, manufacturer
recommendations, or other applicable information. You must provide
supporting documentation and rationale in your Notification of
Compliance Status, demonstrating to the satisfaction of your permitting
authority, that your affected source complies with the applicable
emission limit at the operating limit based on adjusted values.
(e) Can I change my operating limit? You may change the established
operating limit by meeting the requirements in paragraphs (e)(1) through
(3) of this section.
[[Page 118]]
(1) You may change your established operating limit for a continuous
parameter monitoring system by doing an additional performance test, a
performance test in conjunction with an engineering assessment, or an
engineering assessment to verify that, at the new operating limit, you
are in compliance with the applicable emission limitation.
(2) You must establish a revised operating limit for your continuous
parameter monitoring system if you make any change in process or
operating conditions that could affect control system performance or you
change designated conditions after the last performance or compliance
tests were done. You can establish the revised operating limit as
described in paragraph (e)(1) of this section.
(3) You may change your site-specific opacity operating limit or Ni
operating limit only by doing a new performance test.
Sec. 63.1572 What are my monitoring installation, operation, and maintenance requirements?
(a) You must install, operate, and maintain each continuous emission
monitoring system according to the requirements in paragraphs (a)(1)
through (4) of this section.
(1) You must install, operate, and maintain each continuous emission
monitoring system according to the requirements in Table 40 of this
subpart.
(2) If you use a continuous emission monitoring system to meet the
NSPS CO or SO2 limit, you must conduct a performance
evaluation of each continuous emission monitoring system according to
the requirements in Sec. 63.8 and Table 40 of this subpart. This
requirement does not apply to an affected source subject to the NSPS
that has already demonstrated initial compliance with the applicable
performance specification.
(3) As specified in Sec. 63.8(c)(4)(ii), each continuous emission
monitoring system must complete a minimum of one cycle of operation
(sampling, analyzing, and data recording) for each successive 15-minute
period.
(4) Data must be reduced as specified in Sec. 63.8(g)(2).
(b) You must install, operate, and maintain each continuous opacity
monitoring system according to the requirements in paragraphs (b)(1)
through (3) of this section.
(1) Each continuous opacity monitoring system must be installed,
operated, and maintained according to the requirements in Table 40 of
this subpart.
(2) If you use a continuous opacity monitoring system to meet the
NSPS opacity limit, you must conduct a performance evaluation of each
continuous opacity monitoring system according to the requirements in
Sec. 63.8 and Table 40 of this subpart. This requirement does not apply
to an affected source subject to the NSPS that has already demonstrated
initial compliance with the applicable performance specification.
(3) As specified in Sec. 63.8(c)(4)(i), each continuous opacity
monitoring system must complete a minimum of one cycle of sampling and
analyzing for each successive 10-second period and one cycle of data
recording for each successive 6-minute period.
(c) You must install, operate, and maintain each continuous
parameter monitoring system according to the requirements in paragraphs
(c)(1) through (7) of this section.
(1) Each continuous parameter monitoring system must be installed,
operated, and maintained according to the requirements in Table 41 of
this subpart and in a manner consistent with the manufacturer's
specifications or other written procedures that provide adequate
assurance that the equipment will monitor accurately.
(2) The continuous parameter monitoring system must complete a
minimum of one cycle of operation for each successive 15-minute period.
You must have a minimum of four successive cycles of operation to have a
valid hour of data (or at least two if a calibration check is performed
during that hour or if the continuous parameter monitoring system is
out-of-control).
(3) Each continuous parameter monitoring system must have valid
hourly average data from at least 75 percent of the hours during which
the process operated.
[[Page 119]]
(4) Each continuous parameter monitoring system must determine and
record the hourly average of all recorded readings and if applicable,
the daily average of all recorded readings for each operating day. The
daily average must cover a 24-hour period if operation is continuous or
the number of hours of operation per day if operation is not continuous.
(5) Each continuous parameter monitoring system must record the
results of each inspection, calibration, and validation check.
(d) You must monitor and collect data according to the requirements
in paragraphs (d)(1) and (2) of this section.
(1) Except for monitoring malfunctions, associated repairs, and
required quality assurance or control activities (including as
applicable, calibration checks and required zero and span adjustments),
you must conduct all monitoring in continuous operation (or collect data
at all required intervals) at all times the affected source is
operating.
(2) You may not use data recorded during monitoring malfunctions,
associated repairs, and required quality assurance or control activities
for purposes of this regulation, including data averages and
calculations, for fulfilling a minimum data availability requirement, if
applicable. You must use all the data collected during all other periods
in assessing the operation of the control device and associated control
system.
Sec. 63.1573 What are my monitoring alternatives?
(a) What is the approved alternative for monitoring gas flow rate?
You can elect to use this alternative to a continuous parameter
monitoring system for the catalytic regenerator exhaust gas flow rate
for your catalytic cracking unit if the unit does not introduce any
other gas streams into the catalyst regeneration vent (i.e., complete
combustion units with no additional combustion devices). If you select
this alternative, you must use the same procedure for the performance
test and for monitoring after the performance test.
(1) Install and operate a continuous parameter monitoring system to
measure and record the hourly average volumetric air flow rate to the
catalytic cracking unit regenerator. Or, you can determine and record
the hourly average volumetric air flow rate to the catalytic cracking
unit regenerator using the catalytic cracking unit control room
instrumentation.
(2) Install and operate a continuous parameter monitoring system to
measure and record the temperature of the gases entering the control
device (or exiting the catalyst regenerator if you do not use an add-on
control device).
(3) Calculate and record the hourly average actual exhaust gas flow
rate using Equation 1 of this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.019
Where:
Qgas = Hourly average actual gas flow rate, acfm;
1.12 = Default correction factor to convert gas flow from dry standard
cubic feet per minute (dscfm) to standard cubic feet per minute (scfm);
Qair = Volumetric flow rate of air to regenerator, as
determined from the catalytic cracking unit control room
instrumentations, dscfm;
Qoxy = Volumetric flow rate of oxygen-enriched air stream to
regenerator, as determined from the catalytic cracking unit control room
instrumentations, dscfm;
Tempgas = Temperature of gas stream in vent measured as near
as practical to the control device or opacity monitor, [deg]K. For wet
scrubbers, temperature of gas prior to the wet scrubber; and
[[Page 120]]
Pvent = Absolute pressure in the vent measured as near as
practical to the control device or opacity monitor, atm. When used in
conjunction with opacity in the final vent stack, you can assume
Pvent = 1 atm.
(b) What is the approved alternative for monitoring pH levels? If
you use a wet scrubber to control inorganic HAP emissions from your vent
on a catalytic reforming unit, you can measure and record the pH of the
water (or scrubbing liquid) exiting the scrubber at least once an hour
during coke burn-off and catalyst rejuvenation using pH strips as an
alternative to a continuous parameter monitoring system. The pH strips
must meet the requirements in Table 41 of this subpart.
(c) Can I use another type of monitoring system? You may request
approval from your permitting authority to use an automated data
compression system. An automated data compression system does not record
monitored operating parameter values at a set frequency (e.g., once
every hour) but records all values that meet set criteria for variation
from previously recorded values. Your request must contain a description
of the monitoring system and data recording system, including the
criteria used to determine which monitored values are recorded and
retained, the method for calculating daily averages, and a demonstration
that the system meets all of the criteria in paragraphs (c)(1) through
(5) of this section:
(1) The system measures the operating parameter value at least once
every hour;
(2) The system records at least 24 values each day during periods of
operation;
(3) The system records the date and time when monitors are turned
off or on;
(4) The system recognizes unchanging data that may indicate the
monitor is not functioning properly, alerts the operator, and records
the incident; and
(5) The system computes daily average values of the monitored
operating parameter based on recorded data.
(d) Can I monitor other process or control device operating
parameters? You may request approval to monitor parameters other than
those required in this subpart. You must request approval if:
(1) You use a control device other than a thermal incinerator,
boiler, process heater, flare, electrostatic precipitator, or wet
scrubber;
(2) You use a combustion control device (e.g., incinerator, flare,
boiler or process heater with a design heat capacity of at least 44 MW,
boiler or process heater where the vent stream is introduced into the
flame zone), electrostatic precipitator, or scrubber but want to monitor
a parameter other than those specified; or
(3) You wish to use another type of continuous emission monitoring
system that provides direct measurement of a pollutant (i.e., a PM or
multi-metals HAP continuous emission monitoring system, a carbonyl
sulfide/carbon disulfide continuous emission monitoring system, a TOC
continuous emission monitoring system, or HCl continuous emission
monitoring system).
(e) How do I request to monitor alternative parameters? You must
submit a request for review and approval or disapproval to the
Administrator. The request must include the information in paragraphs
(e)(1) through (5) of this section.
(1) A description of each affected source and the parameter(s) to be
monitored to determine whether the affected source will continuously
comply with the emission limitations and an explanation of the criteria
used to select the parameter(s).
(2) A description of the methods and procedures that will be used to
demonstrate that the parameter can be used to determine whether the
affected source will continuously comply with the emission limitations
and the schedule for this demonstration. You must certify that you will
establish an operating limit for the monitored parameter(s) that
represents the conditions in existence when the control device is being
properly operated and maintained to meet the emission limitation.
(3) The frequency and content of monitoring, recording, and
reporting, if monitoring and recording are not continuous. You also must
include the rationale for the proposed monitoring, recording, and
reporting requirements.
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(4) Supporting calculations.
(5) Averaging time for the alternative operating parameter.
Notifications, Reports, and Records
Sec. 63.1574 What notifications must I submit and when?
(a) Except as allowed in paragraphs (a)(1) through (3) of this
section, you must submit all of the notifications in Secs. 63.6(h),
63.7(b) and (c), 63.8(e), 63.8(f)(4), 63.8(f)(6), and 63.9(b) through
(h) that apply to you by the dates specified.
(1) You must submit the notification of your intention to construct
or reconstruct according to Sec. 63.9(b)(5) unless construction or
reconstruction had commenced and initial startup had not occurred before
April 11, 2002. In this case, you must submit the notification as soon
as practicable before startup but no later than July 10, 2002. This
deadline also applies to the application for approval of construction or
reconstruction and approval of construction or reconstruction based on
State preconstruction review required in Secs. 63.5(d)(1)(i) and
63.5(f)(2).
(2) You must submit the notification of intent to conduct a
performance test required in Sec. 63.7(b) at least 30 calendar days
before the performance test is scheduled to begin (instead of 60 days).
(3) If you are required to conduct a performance test, performance
evaluation, design evaluation, opacity observation, visible emission
observation, or other initial compliance demonstration, you must submit
a notification of compliance status according to Sec. 63.9(h)(2)(ii).
You can submit this information in an operating permit application, in
an amendment to an operating permit application, in a separate
submission, or in any combination. In a State with an approved operating
permit program where delegation of authority under section 112(l) of the
CAA has not been requested or approved, you must provide a duplicate
notification to the applicable Regional Administrator. If the required
information has been submitted previously, you do not have to provide a
separate notification of compliance status. Just refer to the earlier
submissions instead of duplicating and resubmitting the previously
submitted information.
(i) For each initial compliance demonstration that does not include
a performance test, you must submit the Notification of Compliance
Status no later than 30 calendar days following completion of the
initial compliance demonstration.
(ii) For each initial compliance demonstration that includes a
performance test, you must submit the notification of compliance status,
including the performance test results, no later than 150 calendar days
after the compliance date specified for your affected source in
Sec. 63.1573.
(b) As specified in Sec. 63.9(b)(2), if you startup your new
affected source before April 11, 2002, you must submit the initial
notification no later than August 9, 2002.
(c) As specified in Sec. 63.9(b)(3), if you start your new or
reconstructed affected source on or after April 11, 2002, you must
submit the initial notification no later than 120 days after you become
subject to this subpart.
(d) You also must include the information in Table 42 of this
subpart in your notification of compliance status.
(e) If you request an extension of compliance for an existing
catalytic cracking unit as allowed in Sec. 63.1563(c), you must submit a
notification to your permitting authority containing the required
information by October 13, 2003.
(f) As required by this subpart, you must prepare and implement an
operation, maintenance, and monitoring plan for each affected source,
control system, and continuous monitoring system. The purpose of this
plan is to detail the operation, maintenance, and monitoring procedures
you will follow.
(1) You must submit the plan to your permitting authority for review
and approval along with your notification of compliance status. While
you do not have to include the entire plan in your part 70 or 71 permit,
you must include the duty to prepare and implement the plan as an
applicable requirement in your part 70 or 71 operating permit. You must
submit any changes to your permitting authority for review and approval
and comply with the plan until the change is approved.
[[Page 122]]
(2) Each plan must include, at a minimum, the information specified
in paragraphs (f)(2)(i) through (x) of this section.
(i) Process and control device parameters to be monitored for each
affected source, along with established operating limits.
(ii) Procedures for monitoring emissions and process and control
device operating parameters for each affected source.
(iii) Procedures that you will use to determine the coke burn-rate,
the volumetric flow rate (if you use process data rather than direct
measurement), and the rate of combustion of liquid or solid fossil fuels
if you use an incinerator-waste heat boiler to burn the exhaust gases
from a catalyst regenerator.
(iv) Procedures and analytical methods you will use to determine the
equilibrium catalyst Ni concentration, the equilibrium catalyst Ni
concentration monthly rolling average, and the hourly or hourly average
Ni operating value.
(v) Procedures you will use to determine the pH of the water (or
scrubbing liquid) exiting a wet scrubber if you use pH strips.
(vi) Procedures you will use to determine the HCl concentration of
gases from a semi-regenerative catalytic reforming unit with an internal
scrubbing system (i.e., no add-on control device) when you use a
colormetric tube sampling system, including procedures for correcting
for pressure (if applicable to the sampling equipment).
(vii) Procedures you will use to determine the gas flow rate for a
catalytic cracking unit if you use the alternative procedure based on
air flow rate and temperature.
(viii) Monitoring schedule, including when you will monitor and when
you will not monitor an affected source (e.g., during the coke burn-off,
regeneration process).
(ix) Quality control plan for each continuous opacity monitoring
system and continuous emission monitoring system you use to meet an
emission limit in this subpart. This plan must include procedures you
will use for calibrations, accuracy audits, and adjustments to the
system needed to meet applicable requirements for the system.
(x) Maintenance schedule for each affected source, monitoring
system, and control device that is generally consistent with the
manufacturer's instructions for routine and long-term maintenance.
Sec. 63.1575 What reports must I submit and when?
(a) You must submit each report in Table 43 of this subpart that
applies to you.
(b) Unless the Administrator has approved a different schedule, you
must submit each report by the date in Table 43 of this subpart and
according to the requirements in paragraphs (b)(1) through (5) of this
section.
(1) The first compliance report must cover the period beginning on
the compliance date that is specified for your affected source in
Sec. 63.1563 and ending on June 30 or December 31, whichever date is the
first date following the end of the first calendar half after the
compliance date that is specified for your affected source in
Sec. 63.1563.
(2) The first compliance report must be postmarked or delivered no
later than July 31 or January 31, whichever date follows the end of the
first calendar half after the compliance date that is specified for your
affected source in Sec. 63.1563.
(3) Each subsequent compliance report must cover the semiannual
reporting period from January 1 through June 30 or the semiannual
reporting period from July 1 through December 31.
(4) Each subsequent compliance report must be postmarked or
delivered no later than July 31 or January 31, whichever date is the
first date following the end of the semiannual reporting period.
(5) For each affected source that is subject to permitting
regulations pursuant to part 70 or 71 of this chapter, and if the
permitting authority has established dates for submitting semiannual
reports pursuant to Sec. 70.6(a)(3)(iii)(A) or Sec. 71.6(a)(3)(iii)(A)
of this chapter, you may submit the first
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and subsequent compliance reports according to the dates the permitting
authority has established instead of according to the dates in
paragraphs (b)(1) through (4) of this section.
(c) The compliance report must contain the information required in
paragraphs (c)(1) through (4) of this section.
(1) Company name and address.
(2) Statement by a responsible official, with that official's name,
title, and signature, certifying the accuracy of the content of the
report.
(3) Date of report and beginning and ending dates of the reporting
period.
(4) If there are no deviations from any emission limitation that
applies to you and there are no deviations from the requirements for
work practice standards, a statement that there were no deviations from
the emission limitations or work practice standards during the reporting
period and that no continuous emission monitoring system or continuous
opacity monitoring system was inoperative, inactive, malfunctioning,
out-of-control, repaired, or adjusted.
(d) For each deviation from an emission limitation and for each
deviation from the requirements for work practice standards that occurs
at an affected source where you are not using a continuous opacity
monitoring system or a continuous emission monitoring system to comply
with the emission limitation or work practice standard in this subpart,
the compliance report must contain the information in paragraphs (c)(1)
through (3) of this section and the information in paragraphs (d)(1)
through (3) of this section.
(1) The total operating time of each affected source during the
reporting period.
(2) Information on the number, duration, and cause of deviations
(including unknown cause, if applicable), as applicable, and the
corrective action taken.
(3) Information on the number, duration, and cause for monitor
downtime incidents (including unknown cause, if applicable, other than
downtime associated with zero and span and other daily calibration
checks).
(e) For each deviation from an emission limitation occurring at an
affected source where you are using a continuous opacity monitoring
system or a continuous emission monitoring system to comply with the
emission limitation, you must include the information in paragraphs
(d)(1) through (3) of this section and the information in paragraphs
(e)(1) through (13) of this section.
(1) The date and time that each malfunction started and stopped.
(2) The date and time that each continuous opacity monitoring system
or continuous emission monitoring system was inoperative, except for
zero (low-level) and high-level checks.
(3) The date and time that each continuous opacity monitoring system
or continuous emission monitoring system was out-of-control, including
the information in Sec. 63.8(c)(8).
(4) The date and time that each deviation started and stopped, and
whether each deviation occurred during a period of startup, shutdown, or
malfunction or during another period.
(5) A summary of the total duration of the deviation during the
reporting period (recorded in minutes for opacity and hours for gases
and in the averaging period specified in the regulation for other types
of emission limitations), and the total duration as a percent of the
total source operating time during that reporting period.
(6) A breakdown of the total duration of the deviations during the
reporting period and into those that are due to startup, shutdown,
control equipment problems, process problems, other known causes, and
other unknown causes.
(7) A summary of the total duration of downtime for the continuous
opacity monitoring system or continuous emission monitoring system
during the reporting period (recorded in minutes for opacity and hours
for gases and in the averaging time specified in the regulation for
other types of standards), and the total duration of downtime for the
continuous opacity monitoring system or continuous emission monitoring
system as a percent of the total source operating time during that
reporting period.
(8) A breakdown of the total duration of downtime for the continuous
opacity monitoring system or continuous emission monitoring system
during the reporting period into periods that are due
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to monitoring equipment malfunctions, non-monitoring equipment
malfunctions, quality assurance/quality control calibrations, other
known causes, and other unknown causes.
(9) An identification of each HAP that was monitored at the affected
source.
(10) A brief description of the process units.
(11) The monitoring equipment manufacturer(s) and model number(s).
(12) The date of the latest certification or audit for the
continuous opacity monitoring system or continuous emission monitoring
system.
(13) A description of any change in the continuous emission
monitoring system or continuous opacity monitoring system, processes, or
controls since the last reporting period.
(f) You also must include the information required in paragraphs
(f)(1) through (2) of this section in each compliance report, if
applicable.
(1) A copy of any performance test done during the reporting period
on any affected unit. The report may be included in the next semiannual
report. The copy must include a complete report for each test method
used for a particular kind of emission point tested. For additional
tests performed for a similar emission point using the same method, you
must submit the results and any other information required, but a
complete test report is not required. A complete test report contains a
brief process description; a simplified flow diagram showing affected
processes, control equipment, and sampling point locations; sampling
site data; description of sampling and analysis procedures and any
modifications to standard procedures; quality assurance procedures;
record of operating conditions during the test; record of preparation of
standards; record of calibrations; raw data sheets for field sampling;
raw data sheets for field and laboratory analyses; documentation of
calculations; and any other information required by the test method.
(2) Any requested change in the applicability of an emission
standard (e.g., you want to change from the PM standard to the Ni
standard for catalytic cracking units or from the HCl concentration
standard to percent reduction for catalytic reforming units) in your
periodic report. You must include all information and data necessary to
demonstrate compliance with the new emission standard selected and any
other associated requirements.
(g) You may submit reports required by other regulations in place of
or as part of the compliance report if they contain the required
information.
(h) The reporting requirements in paragraphs (h)(1) and (2) of this
section apply to startups, shutdowns, and malfunctions:
(1) When actions taken to respond are consistent with the plan, you
are not required to report these events in the semiannual compliance
report and the reporting requirements in Secs. 63.6(e)(3)(iii) and
63.10(d)(5) do not apply.
(2) When actions taken to respond are not consistent with the plan,
you must report these events and the response taken in the semiannual
compliance report. In this case, the reporting requirements in
Secs. 63.6(e)(3)(iv) and 63.10(d)(5) do not apply.
(i) If the applicable permitting authority has approved a period of
planned maintenance for your catalytic cracking unit according to the
requirements in paragraph (j) of this section, you must include the
following information in your compliance report.
(1) In the compliance report due for the 6-month period before the
routine planned maintenance is to begin, you must include a full copy of
your written request to the applicable permitting authority and written
approval received from the applicable permitting authority.
(2) In the compliance report due after the routine planned
maintenance is complete, you must include a description of the planned
routine maintenance that was performed for the control device during the
previous 6-month period, and the total number of hours during those 6
months that the control device did not meet the emission limitations and
monitoring requirements as a result of the approved routine planned
maintenance.
(j) If you own or operate multiple catalytic cracking units that are
served by a single wet scrubber emission control device (e.g., a Venturi
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scrubber), you may request the applicable permitting authority to
approve a period of planned routine maintenance for the control device
needed to meet requirements in your operation, maintenance, and
monitoring plan. You must present data to the applicable permitting
authority demonstrating that the period of planned maintenance results
in overall emissions reductions. During this pre-approved time period,
the emission control device may be taken out of service while
maintenance is performed on the control device and/or one of the process
units while the remaining process unit(s) continue to operate. During
the period the emission control device is unable to operate, the
emission limits, operating limits, and monitoring requirements
applicable to the unit that is operating and the wet scrubber emission
control device do not apply. The applicable permitting authority may
require that you take specified actions to minimize emissions during the
period of planned maintenance.
(1) You must submit a written request to the applicable permitting
authority at least 6 months before the planned maintenance is scheduled
to begin with a copy to the EPA Regional Administrator.
(2) Your written request must contain the information in paragraphs
(j)(2)(i) through (v) of this section.
(i) A description of the planned routine maintenance to be performed
during the next 6 months and why it is necessary.
(ii) The date the planned maintenance will begin and end.
(iii) A quantified estimate of the HAP and criteria pollutant
emissions that will be emitted during the period of planned maintenance.
(iv) An analysis showing the emissions reductions resulting from the
planned maintenance as opposed to delaying the maintenance until the
next unit turnaround.
(v) Actions you will take to minimize emissions during the period of
planned maintenance.
Sec. 63.1576 What records must I keep, in what form, and for how long?
(a) You must keep the records specified in paragraphs (a)(1) through
(3) of this section.
(1) A copy of each notification and report that you submitted to
comply with this subpart, including all documentation supporting any
initial notification or Notification of Compliance Status that you
submitted, according to the requirements in Sec. 63.10(b)(2)(xiv).
(2) The records in Sec. 63.6(e)(1)(iii) through (v) related to
startup, shutdown, and malfunction.
(3) Records of performance tests, performance evaluations, and
opacity and visible emission observations as required in
Sec. 63.10(b)(2)(viii).
(b) For each continuous emission monitoring system and continuous
opacity monitoring system, you must keep the records required in
paragraphs (b)(1) through (5) of this section.
(1) Records described in Sec. 63.10(b)(2)(vi) through (xi).
(2) Monitoring data for continuous opacity monitoring systems during
a performance evaluation as required in Sec. 63.6(h)(7)(i) and (ii).
(3) Previous (i.e., superceded) versions of the performance
evaluation plan as required in Sec. 63.8(d)(3).
(4) Requests for alternatives to the relative accuracy test for
continuous emission monitoring systems as required in
Sec. 63.8(f)(6)(i).
(5) Records of the date and time that each deviation started and
stopped, and whether the deviation occurred during a period of startup,
shutdown, or malfunction or during another period.
(c) You must keep the records in Sec. 63.6(h) for visible emission
observations.
(d) You must keep records required by Tables 6, 7, 13, and 14 of
this subpart (for catalytic cracking units); Tables 20, 21, 27 and 28 of
this subpart (for catalytic reforming units); Tables 34 and 35 of this
subpart (for sulfur recovery units); and Table 39 of this subpart (for
bypass lines) to show continuous compliance with each emission
limitation that applies to you.
[[Page 126]]
(e) You must keep a current copy of your operation, maintenance, and
monitoring plan onsite and available for inspection. You also must keep
records to show continuous compliance with the procedures in your
operation, maintenance, and monitoring plan.
(f) You also must keep the records of any changes that affect
emission control system performance including, but not limited to, the
location at which the vent stream is introduced into the flame zone for
a boiler or process heater.
(g) Your records must be in a form suitable and readily available
for expeditious review according to Sec. 63.10(b)(1).
(h) As specified in Sec. 63.10(b)(1), you must keep each record for
5 years following the date of each occurrence, measurement, maintenance,
corrective action, report, or record.
(i) You must keep each record on site for at least 2 years after the
date of each occurrence, measurement, maintenance, corrective action,
report, or record, according to Sec. 63.10(b)(1). You can keep the
records offsite for the remaining 3 years.
Other Requirements and Information
Sec. 63.1577 What parts of the General Provisions apply to me?
Table 44 of this subpart shows which parts of the General Provisions
in Secs. 63.1 through 63.15 apply to you.
Sec. 63.1578 Who implements and enforces this subpart?
(a) This subpart can be implemented and enforced by us, the U.S.
EPA, or a delegated authority such as your State, local, or tribal
agency. If the U.S. EPA Administrator has delegated authority to your
State, local, or tribal agency, then that Agency has the authority to
implement and enforce this subpart. You should contact your U.S. EPA
Regional Office to find out if this subpart is delegated to your State,
local, or tribal agency.
(b) In delegating implementation and enforcement authority of this
subpart to a State, local, or tribal agency under 40 CFR part 63,
subpart E, the authorities contained in paragraph (c) of this section
are retained by the Administrator of the U.S. EPA and are not
transferred to the State, local, or tribal agency.
(c) The authorities that will not be delegated to State, local, or
tribal agencies are listed in paragraphs (c)(1) through (5) of this
section.
(1) Approval of alternatives to the non-opacity emission limitations
and work practice standards in Secs. 63.1564 through 63.1569 under
Sec. 63.6(g).
(2) Approval of alternative opacity emission limitations in
Secs. 63.1564 through 63.1569 under Sec. 63.6(h)(9).
(3) Approval of major alternatives to test methods under
Sec. 63.7(e)(2)(ii) and (f) and as defined in Sec. 63.90.
(4) Approval of major alternatives to monitoring under Sec. 63.8(f)
and as defined in Sec. 63.90.
(5) Approval of major alternatives to recordkeeping and reporting
under Sec. 63.10(f) and as defined in Sec. 63.90.
Sec. 63.1579 What definitions apply to this subpart?
Terms used in this subpart are defined in the Clean Air Act (CAA),
in 40 CFR 63.2, the General Provisions of this part (Secs. 63.1 through
63.15), and in this section as listed.
Boiler means any enclosed combustion device that extracts useful
energy in the form of steam and is not an incinerator.
Catalytic cracking unit means a refinery process unit in which
petroleum derivatives are continuously charged; hydrocarbon molecules in
the presence of a catalyst suspended in a fluidized bed are fractured
into smaller molecules, or react with a contact material suspended in a
fluidized bed to improve feedstock quality for additional processing;
and the catalyst or contact material is continuously regenerated by
burning off coke and other deposits. The unit includes, but is not
limited to, the riser, reactor, regenerator, air blowers, spent catalyst
or contact material stripper, catalyst or contact material recovery
equipment, and regenerator equipment for controlling air pollutant
emissions and equipment used for heat recovery.
Catalytic cracking unit catalyst regenerator means one or more
regenerators (multiple regenerators) which comprise that portion of the
catalytic cracking
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unit in which coke burn-off and catalyst or contact material
regeneration occurs and includes the regenerator combustion air
blower(s).
Catalytic reforming unit means a refinery process unit that reforms
or changes the chemical structure of naphtha into higher octane
aromatics through the use of a metal catalyst and chemical reactions
that include dehydrogenation, isomerization, and hydrogenolysis. The
catalytic reforming unit includes the reactor, regenerator (if
separate), separators, catalyst isolation and transport vessels (e.g.,
lock and lift hoppers), recirculation equipment, scrubbers, and other
ancillary equipment.
Catalytic reforming unit regenerator means one or more regenerators
which comprise that portion of the catalytic reforming unit and
ancillary equipment in which the following regeneration steps typically
are performed: depressurization, purge, coke burn-off, catalyst
rejuvenation with a chloride (or other halogenated) compound(s), and a
final purge. The catalytic reforming unit catalyst regeneration process
can be done either as a semi-regenerative, cyclic, or continuous
regeneration process.
Coke burn-off means the coke removed from the surface of the
catalytic cracking unit catalyst or the catalytic reforming unit
catalyst by combustion in the catalyst regenerator. The rate of coke
burn-off is calculated using Equation 2 in Sec. 63.1564.
Combustion device means an individual unit of equipment such as a
flare, incinerator, process heater, or boiler used for the destruction
of organic HAP or VOC.
Combustion zone means the space in an enclosed combustion device
(e.g., vapor incinerator, boiler, furnace, or process heater) occupied
by the organic HAP and any supplemental fuel while burning. The
combustion zone includes any flame that is visible or luminous as well
as that space outside the flame envelope in which the organic HAP
continues to be oxidized to form the combustion products.
Contact material means any substance formulated to remove metals,
sulfur, nitrogen, or any other contaminants from petroleum derivatives.
Continuous regeneration reforming means a catalytic reforming
process characterized by continuous flow of catalyst material through a
reactor where it mixes with feedstock, and a portion of the catalyst is
continuously removed and sent to a special regenerator where it is
regenerated and continuously recycled back to the reactor.
Control device means any equipment used for recovering, removing, or
oxidizing HAP in either gaseous or solid form. Such equipment includes,
but is not limited to, condensers, scrubbers, electrostatic
precipitators, incinerators, flares, boilers, and process heaters.
Cyclic regeneration reforming means a catalytic reforming process
characterized by continual batch regeneration of catalyst in situ in any
one of several reactors (e.g., 4 or 5 separate reactors) that can be
isolated from and returned to the reforming operation while maintaining
continuous reforming process operations (i.e., feedstock continues
flowing through the remaining reactors without change in feed rate or
product octane).
Deviation means any instance in which an affected source subject to
this subpart, or an owner or operator of such a source:
(1) Fails to meet any requirement or obligation established by this
subpart, including but not limited to any emission limit, operating
limit, or work practice standard;
(2) Fails to meet any term or condition that is adopted to implement
an applicable requirement in this subpart and that is included in the
operating permit for any affected source required to obtain such a
permit; or
(3) Fails to meet any emission limit, operating limit, or work
practice standard in this subpart during startup, shutdown, or
malfunction, regardless of whether or not such failure is permitted by
this subpart.
Emission limitation means any emission limit, opacity limit,
operating limit, or visible emission limit.
Flame zone means the portion of a combustion chamber of a boiler or
process heater occupied by the flame envelope created by the primary
fuel.
Flow indicator means a device that indicates whether gas is flowing,
or
[[Page 128]]
whether the valve position would allow gas to flow, in or through a
line.
Fuel gas system means the offsite and onsite piping and control
system that gathers gaseous streams generated by the source, may blend
them with sources of gas, if available, and transports the blended
gaseous fuel at suitable pressures for use as fuel in heaters, furnaces,
boilers, incinerators, gas turbines, and other combustion devices
located within or outside of the refinery. The fuel is piped directly to
each individual combustion device, and the system typically operates at
pressures over atmospheric. The gaseous streams can contain a mixture of
methane, light hydrocarbons, hydrogen, and other miscellaneous species.
HCl means for the purposes of this subpart, gaseous emissions of
hydrogen chloride that serve as a surrogate measure for total emissions
of hydrogen chloride and chlorine as measured by Method 26 or 26A in
appendix A to part 60 of this chapter or an approved alternative method.
Incinerator means an enclosed combustion device that is used for
destroying organic compounds, with or without heat recovery. Auxiliary
fuel may be used to heat waste gas to combustion temperatures. An
incinerator may use a catalytic combustion process where a substance is
introduced into an exhaust stream to burn or oxidize contaminants while
the substances itself remains intact, or a thermal process which uses
elevated temperatures as a primary means to burn or oxidize
contaminants.
Ni means, for the purposes of this subpart, particulate emissions of
nickel that serve as a surrogate measure for total emissions of metal
HAP, including but not limited to: antimony, arsenic, beryllium,
cadmium, chromium, cobalt, lead, manganese, nickel, and selenium as
measured by Method 29 in appendix A to part 60 of this chapter or by an
approved alternative method.
Oxidation control system means an emission control system which
reduces emissions from sulfur recovery units by converting these
emissions to sulfur dioxide.
PM means, for the purposes of this subpart, emissions of particulate
matter that serve as a surrogate measure of the total emissions of
particulate matter and metal HAP contained in the particulate matter,
including but not limited to: antimony, arsenic, beryllium, cadmium,
chromium, cobalt, lead, manganese, nickel, and selenium as measured by
Methods 5B or 5F in appendix A to part 60 of this chapter or by an
approved alternative method.
Process heater means an enclosed combustion device that primarily
transfers heat liberated by burning fuel directly to process streams or
to heat transfer liquids other than water.
Process vent means, for the purposes of this subpart, a gas stream
that is continuously or periodically discharged during normal operation
of a catalytic cracking unit, catalytic reforming unit, or sulfur
recovery unit, including gas streams that are discharged directly to the
atmosphere, gas streams that are routed to a control device prior to
discharge to the atmosphere, or gas streams that are diverted through a
product recovery device line prior to control or discharge to the
atmosphere.
Reduced sulfur compounds means hydrogen sulfide, carbonyl sulfide,
and carbon disulfide.
Reduction control system means an emission control system which
reduces emissions from sulfur recovery units by converting these
emissions to hydrogen sulfide.
Responsible official means responsible official as defined in 40 CFR
70.2.
Semi-regenerative reforming means a catalytic reforming process
characterized by shutdown of the entire reforming unit (e.g., which may
employ three to four separate reactors) at specified intervals or at the
owner's or operator's convenience for in situ catalyst regeneration.
Sulfur recovery unit means a process unit that recovers elemental
sulfur from gases that contain reduced sulfur compounds and other
pollutants, usually by a vapor-phase catalytic reaction of sulfur
dioxide and hydrogen sulfide. This definition does not include a unit
where the modified reaction is carried out in a water solution which
contains a metal ion capable of oxidizing the sulfide ion to sulfur,
e.g., the LO-CAT II process.
[[Page 129]]
TOC means, for the purposes of this subpart, emissions of total
organic compounds, excluding methane and ethane, that serve as a
surrogate measure of the total emissions of organic HAP compounds,
including but not limited to, acetaldehyde, benzene, hexane, phenol,
toluene, and xylenes and non-HAP VOC as measured by Method 25 or 25A in
appendix A to part 60 of this chapter or an approved alternative method.
TRS means, for the purposes of this subpart, emissions of total
reduced sulfur compounds, expressed as an equivalent sulfur dioxide
concentration, that serve as a surrogate measure of the total emissions
of sulfide HAP carbonyl sulfide and carbon disulfide as measured by
Method 15 in appendix A to part 60 of this chapter or by an approved
alternative method.
Work practice standard means any design, equipment, work practice,
or operational standard, or combination thereof, that is promulgated
pursuant to section 112(h) of the CAA.
Table 1 to Subpart UUU of Part 63--Metal HAP Emission Limits for
Catalytic Cracking Units
[As stated in Sec. 63.1564(a)(1), you must meet each emission
limitation in the following table that applies to you]
------------------------------------------------------------------------
You must meet the following emission
For each new or existing catalytic limits for each catalyst regenerator
cracking unit * * * vent * * *
------------------------------------------------------------------------
1. Subject to the new source PM emissions must not exceed 1.0
performance standard (NSPS) for kilogram (kg) per 1,000 kg (1.0 lb/
PM in 40 CFR 60.102. 1,000 lb) of coke burn-off in the
catalyst regenerator; if the
discharged gases pass through an
incinerator or waste heat boiler in
which you burn auxiliary or
supplemental liquid or solid fossil
fuel, you must limit the
incremental rate of PM to no more
than 43.0 grams per Megajoule (g/
MJ) or 0.10 pounds per million
British thermal units (lb/million
Btu) of heat input attributable to
the liquid or solid fossil fuel;
and the opacity of emissions must
not exceed 30 percent, except for
one 6-minute average opacity
reading in any 1-hour period.
2. Option 1: NSPS requirements not PM emissions must not exceed 1.0 kg/
subject to the NSPS for PM in 40 1,000 kg (1.0 lb/1,000 lb) of coke
CFR 60.102. burn-off in the catalyst
regenerator; if the discharged
gases pass through an incinerator
or waste heat boiler in which you
burn auxiliary or in supplemental
liquid or solid fossil fuel, you
must limit the incremental rate of
PM to no more than 43.0 g/MJ or lb/
million Btu of heat input
attributable to the liquid or solid
fossil fuel; and the opacity of
emissions must not exceed 30
percent, except for one 6-minute
average opacity reading in any 1-
hour period.
3. Option 2: PM limit not subject PM emissions must not exceed 1.0 kg/
to the NSPS for PM in 40 CFR 1,000 kg (1.0 lb/1,000 lbs) of coke
60.102. burn-off in the catalyst
regenerator.
4. Option 3: Ni lb/hr not subject Nickel (Ni) emissions must not
to the NSPS for PM in 40 CFR exceed 13,000 milligrams per hour
60.102. (mg/hr) (0.029 lb/hr).
5. Option 4: Ni Lb/1,000 lbs of Ni emissions must not exceed 1.0 mg/
coke burn-off not subject to the kg (0.001 lb/1,000 lbs) of coke
NSPS for PM in 40 CFR 60.102. burn-off in the catalyst
regenerator.
------------------------------------------------------------------------
Table 2 to Subpart UUU of Part 63--Operating Limits for Metal HAP
Emissions From Catalytic Cracking Units
[As stated in Sec. 63.1564(a)(2), you must meet each operating limit in the following table that applies to
you]
----------------------------------------------------------------------------------------------------------------
For this type of
For each new or existing catalytic continuous monitoring For this type of You must meet this
cracking unit * * * system * * * control device * * * operating limit * * *
----------------------------------------------------------------------------------------------------------------
1. Subject to the NSPS for PM in 40 Continuous opacity Not applicable......... Not applicable.
CFR 60.102. monitoring system.
2. Option 1: NSPS requirements not Continuous opacity Not applicable......... Not applicable.
subject to the NSPS for PM in 40 CFR monitoring system.
60.102.
3. Option 2: PM limit not subject to a. Continuous opacity Electrostatic Maintain the hourly
the NSPS for PM in 40 CFR 60.102. monitoring system. precipitator. average opacity of
emissions from your
catalyst regenerator
vent no higher than
the site-specific
opacity limit
established during the
performance test.
[[Page 130]]
b. Continuous parameter Electrostatic Maintain the daily
monitoring systems. precipitator. average gas flow rate
no higher than the
limit established in
the performance test;
and maintain the daily
average voltage and
secondary current (or
total power input)
above the limit
established in the
performance test.
c. Continuous parameter Wet scrubber........... Maintain the daily
monitoring systems. average pressure drop
above the limit
established in the
performance test (not
applicable to a wet
scrubber of the non-
venturi jet-ejector
design); and maintain
the daily average
liquid-to-gas ratio
above the limit
established in the
performance test.
4. Option 3: Ni lb/hr not subject to a. Continuous opacity Electrostatic Maintain the daily
the NSPS for PM in 40 CFR 60.102. monitoring system. precipitator. average Ni operating
value no higher than
the limit established
during the performance
test.
b. Continuous parameter i. Electrostatic Maintain the daily
monitoring systems. precipitator. average gas flow rate
no higher than the
limit established
during the performance
test; maintain the
monthly rolling
average of the
equilibrium catalyst
Ni concentration no
higher than the limit
established during the
performance test; and
maintain the daily
average voltage and
secondary current (or
total power input)
above the established
during the performance
test.
ii. Wet scrubber....... Maintain the monthly
rolling average of the
equilibrium catalyst
Ni concentration no
higher than the limit
established during the
performance test;
maintain the daily
average pressure drop
above the limit
established during the
performance test (not
applicable to a non-
venturi wet scrubber
of the jet-ejector
design); and maintain
the daily average
liquid-to-gas ratio
above the limit
established during the
performance test.
5. Option 4: Ni lb/1,000 lbs of coke a. Continuous opacity Electrostatic Maintain the daily
burn-off not subject to the NSPS for monitoring system precipitator. average Ni operating
PM in 40 CFR 60.102. value no higher than
the Ni operating limit
established during the
performance test.
[[Page 131]]
b. Continuous parameter i. Electrostatic Maintain the monthly
monitoring systems. precipitator. rolling average of the
equilibrium catalyst
Ni concentration no
higher than the limit
established during the
performance test; and
maintain the daily
average voltage and
secondary current for
total power input)
above the limit
established during the
performance test.
ii. Wet scrubber....... Maintain the monthly
rolling average of the
equilibrium catalyst
Ni concentration no
higher than the limit
established during the
performance test;
maintain the daily
average pressure drop
above the limit
established during the
performance test (not
applicable to a non-
venturi wet scrubber
of the jet-ejector
design); and maintain
the daily average
liquid-to-gas ratio
above the limit
established during the
performance test.
----------------------------------------------------------------------------------------------------------------
Table 3 to Subpart UUU of Part 63--Continous Monitoring Systems for
Metal HAP Emissions From Catalytic Cracking Units
[As stated in Sec. 63.1564(b)(1), you must meet each requirement in the following table that applies to you]
----------------------------------------------------------------------------------------------------------------
And you use this type You must install,
For each new or existing catalytic If your catalytic of control device for operate, and maintain a
cracking unit * * * cracking unit is * * * your vent * * * * * *
----------------------------------------------------------------------------------------------------------------
1. Subject to the NSPS for PM in 40 Any size............... Electrostatic Continous opacity
CFR 60.102. precipitator or wet monitoring system to
scrubber or no control measure and record the
device. opacity of emissions
from each catalyst
regenerator vent.
2. Option 1: NSPS limits not subject Any size............... Electrostatic Continuous opacity
to the NSPS for PM in 40 CFR 60.102. precipitator or wet monitoring system to
scrubber or no control measure and record the
device. opacity of emissions
from each catalyst
regenerator vent.
3. Option 2: PM limit not subject to a. Over 20,000 barrels Electrostatic Continous opacity
the NSPS for PM in 40 CFR 60.102. per day fresh feed precipitator. monitoring system to
capacity. measure and record the
opacity of emissions
from each catalyst
regenerator vent.
b. Up to 20,000 barrels Electrostatic Continuous opacity
per day fresh feed precipitator. monitoring system to
capacity. measure and record the
opacity of emissions
from each catalyst
regenerator vent; or
continuous parameter
monitoring systems to
measure and record the
gas flow rate to the
control device and the
voltage and secondary
current (or total
power input) to the
control device.
c. Any size............ i. Wet scrubber........ (1) Continuous
parameter monitoring
system to measure and
record the pressure
drop across the
scrubber, gas flow
rate to the scrubber,
and total liquid (or
scrubbing liquor) flow
rate to the scrubber.
(2) If you use a wet
scrubber of the non-
venturi jet-ejector
design, you're not
required to install
and operate a
continuous parameter
monitoring system for
pressure drop.
[[Page 132]]
d. Any size............ No electrostatic Continous opacity
precipitator or wet monitoring system to
scrubber. measure and record the
opacity of emissions
from each catalyst
regenerator vent.
4. Option 3: Ni lb/hr not subject to a. Over 20,000 barrels Electrostatic Continous opacity
the NSPS for PM in 40 CFR 60.102. per day fresh feed precipitator. monitoring system to
capacity. measure and record the
opacity of emissions
from each catalyst
regenerator vent and
continuous parameter
monitoring system to
measure and record the
gas flow rate.
b. Up to 20,000 barrels Electrostatic Continuous opacity
per day fresh feed precipitator. monitoring system to
capacity. measure and record the
opacity of emissions
from each catalyst
regenerator vent and
continuous parameter
monitoring system to
measure and record the
gas flow rate; or
continuous parameter
monitoring systems to
measure and record the
gas flow rate and the
voltage and secondary
current (or total
power input) to the
control device.
c. Any size............ Wet scrubber........... (1) Continuous
parameter monitoring
system to measure and
record the pressure
drop across the
scrubber, gas flow
rate to the scrubber,
and total liquid (or
scrubbing liquor) flow
rate to the scrubber.
(2) If you use a wet
scrubber of the non-
venturi jet-ejector,
design, you're not
required to install
and operate a
continuous parameter
monitoring system for
pressure drop.
d. Any size............ No electrostatic Continuous opacity
precipitator or wet monitoring system to
scrubber. measure and record the
opacity of emissions
from each catalyst
regenerator vent and
continuous parameter
monitoring system to
measure and record the
gas flow rate.
5. Option 4: Ni lb/1,000 lbs of coke a. Over 20,000 barrels Electrostatic Continuous opacity
burn-off not subject to the NSPS for per day fresh feed precipitator. monitoring system to
PM in 40 CFR 60.102. capacity. measure and record the
opacity of emissions
from each catalyst
regenerator vent and
continuous parameter
monitoring system to
measure and record the
gas flow rate.
b. Up to 20,000 barrels Electrostatic Continuous opacity
per day fresh feed precipitator. monitoring system to
capacity. measure and record the
opacity of emissions
from each catalyst
regenerator vent and
continuous parameter
monitoring system to
measure and record the
gas flow rate; or
continuous parameter
monitoring systems to
measure and record the
gas flow rate and the
voltage and secondary
current (or total
power input) to the
control device.
c. Any size............ Wet scrubber........... Continuous parameter
monitoring system to
measure and record the
pressure drop across
the scrubber, gas flow
rate to the scrubber,
and total liquid (or
scrubbing liquor) flow
rate to the scrubber.
d. Any size............ No electrostatic Continuous opacity
precipitator or wet monitoring system to
scrubber measure and record the
opacity of emissions
from each catalyst
regenerator vent and
continuous parameter
monitoring system to
measure and record the
gas flow rate.
----------------------------------------------------------------------------------------------------------------
[[Page 133]]
Table 4 to Subpart UUU of Part 63--Requirements for Performance Tests
for Metal HAP Emissions From Catalytic Cracking Units Not Subject to the
New Source Performance Standard (NSPS) for Particulate Matter (PM)
[As stated in Sec. 63.1564(b)(2), you must meet each requirement in the following table that applies to you]
----------------------------------------------------------------------------------------------------------------
For each new or existing catalytic
cracking unit catalyst regenerator You must * * * Using * * * According to these
vent * * * requirements * * *
----------------------------------------------------------------------------------------------------------------
1. If you elect Option 1 in item 2 of a. Select sampling Method 1 or 1A in Sampling sites must be
Table 1, Option 2 in item 3 of Table port's location and appendix A to part 60 located at the outlet
1, Option 3 in item 4 of Table 1, or the number of traverse of this chapter. of the control device
Option 4 in item 5 of Table 1 of ports. or the outlet of the
this subpart. regenerator, as
applicable, and prior
to any releases to the
atmosphere.
b. Determine velocity Method 2, 2A, 2C, 2D, .......................
and volumetric flow 2F, or 2G in appendix
rate. A to part 60 of this
chapter, as
applicable.
c. Conduct gas Method 3, 3A, or 3B in .......................
molecular weight appendix A to part 60
analysis. of this chapter, as
applicable.
d. Measure moisture Method 4 in appendix A .......................
content of the stack to part 60 of this
gas. chapter.
e. If you use an .......................
electro-static
precipitator, record
the total number of
fields in the control
system and how many
operated during the
applicable performance
test.
f. If you use a wet .......................
scrubber, record the
total amount (rate) of
water (or scrubbing
liquid) and the amount
(rate) of make-up
liquid to the scrubber
during each test run.
2. Option 1: Elect NSPS.............. a. Measure PM emissions Method 5B or 5F (40 CFR You must maintain a
part 60, appendix A) sampling rate of at
to determine PM least 0.15 dry
emissions and standard cubic meters
associated moisture per minute (dscm/min)
content for units (0.53 dry standard
without wet scrubbers. cubic feet per minute
Method 5B (40 CFR part (dscf/min)).
60, appendix A) to
determine PM emissions
and associated
moisture content for
unit with wet scrubber.
b. Compute PM emission Equations 1, 2, and 3 .......................
rate (lbs/1,000 lbs) of Sec. 63.1564 (if
of coke burn-off. applicable).
c. Measure opacity of Continuous opacity You must collect
emissions.. monitoring system. opacity monitoring
data every 10 seconds
during the entire
period of the initial
Method 5 performance
test and reduce the
data to 6-minute
averages.
3. Option 2: PM limit................ a. Measure PM emissions See item 2. of this See item 2. of this
table. table.
b. Compute coke burn- Equations 1 and 2 of .......................
off rate and PM Sec. 63.1564
emission rate.
c. Establish your site- Data from the You must collect
specific opacity continuous opacity opacity monitoring
operating limit if you monitoring system. data every 10 seconds
use a continuous during the entire
opacity monitoring period of the initial
system. Method 5 performance
test and reduce the
data to 6-minute
averages; determine
and record the hourly
average opacity from
all the 6-minute
averages; and compute
the site-specific
limit using Equation 4
of Sec. 63.1564.
4. Option 3: Ni lb/hr................ a. Measure Method 29 (40 CFR part You must maintain a
concentration of Ni 60, appendix A). sampling rate of at
and total metal HAP. least 0.028 dscm/min
(0.74 dscf/min).
[[Page 134]]
b. Compute Ni emission Equation 5 of Sec. .......................
rate (lb/hr). 63.1564
c. Determine the EPA Method 6010B or You must obtain 1
equilibrium catalyst 6020 or EPA Method sample for each of the
Ni concentration. 7520 or 7521 in SW-846 3 runs; determine and
1; or, you can use an record the average
alternative method equilibrium catalyst
satisfactory to the Ni concentration for
Administrator. each of the 3 runs;
and you may adjust the
results for an
individual run to the
maximum value using
Equation 1 of Sec.
63.1571.
d. If you use a i. Equations 6 and 7 of (1) You must collect
continuous opacity Sec. 63.1564 using opacity monitoring
monitoring system, data from continuous data every 10 seconds
establish your site- opacity monitoring during the entire
specific Ni operating system, gas flow rate, period of the initial
limit. results of equilibrium Ni performance test;
catalyst Ni reduce the data to 6-
concentration minute averages; and
analysis, and Ni determine and record
emission rate from the hourly average
Method 29 test. opacity from all the 6-
minute averages.
(2) You must collect
gas flow rate
monitoring data every
15 minutes during the
entire period of the
initial Ni performance
test; measure the gas
flow as near as
practical to the
continuous opacity
monitoring system; and
determine and record
the hourly average
actual gas flow rate
from all the readings.
5. Option 4: Ni lbs/1,000 lbs of coke a. Measure Method 29 (40 CFR part You must maintain a
burn-off. concentration of Ni 60, appendix A). sampling rate of at
and total metal HAP. least 0.028 dscm/min
(0.74 dscf/min).
b. Compute Ni emission Equations 1 and 8 of .......................
rate (lb/1,000 lbs of Sec. 63.1564.
coke burn-off).
c. Determine the EPA Method 6010B or You must obtain 1
equilibrium catalyst 6020 or EPA Method sample for each of the
Ni concentration. 7520 or 7521 (SW-846) 3 runs; determine and
1; or, you can use an record the equilibrium
alternative method catalyst Ni
satisfactory to the concentration for each
Administrator. of the 3 samples; and
you may adjust the
laboratory results to
the maximum value
using Equation 2 of
Sec. 63.1571.
d. If you use a i. Equations 9 and 10 (1) You must collect
continuous opacity of Sec. 63.1564 with opacity monitoring
monitoring system, data from continuous data every 10 seconds
establish your site- opacity monitoring during the entire
specific Ni operating system, coke burn-off period of the initial
limit. rate, gas flow rate, Ni performance test;
results of equilibrium reduce the data to 6-
catalyst Ni minute averages; and
concentration determine and record
analysis, and Ni the hourly average
emission rate from opacity from all the 6-
Method 29 test. minute averages.
(2) You must collect
gas flow rate
monitoring data every
15 minutes during the
entire period of the
initial Ni performance
test; measure the gas
flow rate as near as
practical to the
continuous opacity
monitoring system; and
determine and record
the hourly average
actual gas flow rate
from all the readings.
[[Page 135]]
e. Record the catalyst
addition rate for each
test and schedule for
the 10-day period
prior to the test.
6. If you elect Option 2 in Entry 3 a. Establish each Data from the .......................
in Table 1, Option 3 in Entry 4 in operating limit in continuous parameter
Table 1, or Option 4 in Entry 5 in Table 2 of this monitoring systems and
Table 1 of this subpart and you use subpart that applies applicable performance
continuous parameter monitoring to you. test methods.
systems.
b. Electrostatic Data from the You must collect gas
precipitator or wet continuous parameter flow rate monitoring
scrubber: gas flow monitoring systems and data every 15 minutes
rate. applicable performance during the entire
test methods. period of the initial
performance test; and
determine and record
the maximum hourly
average gas flow rate
from all the readings.
c. Electrostatic Data from the You must collect
precipitator: voltage continuous parameter voltage and secondary
and secondary current monitoring systems and current (or total
(or total power applicable performance power input)
input). test methods. monitoring data every
15 minutes during the
entire period of the
initial performance
test; and determine
and record the minimum
hourly average voltage
and secondary current
(or total power input)
from all the readings.
d. Electrostatic Results of analysis for You must determine and
precipitator or wet equilibrium catalyst record the average
scrubber: equilibrium Ni concentration. equilibrium catalyst
catalyst Ni Ni concentration for
concentration. the 3 runs based on
the laboratory
results. You may
adjust the value using
Equation 1 or 2 of
Sec. 63.1571 as
applicable.
e. Wet scrubber: Data from the You must collect
pressure drop (not continuous parameter pressure drop
applicable to non- monitoring systems and monitoring data every
venturi scrubber of applicable performance 15 minutes during the
jet ejector design). test methods. entire period of the
initial performance
test; and determine
and record the minimum
hourly average
pressure drop from all
the readings.
f. Wet scrubber: liquid- Data from the You must collect gas
to-gas ratio. continuous parameter flow rate and total
monitoring systems and water (or scrubbing
applicable performance liquid) flow rate
test methods. monitoring data every
15 minutes during the
entire period of the
initial performance
test; determine and
record the hourly
average gas flow rate
and total water (or
scrubbing liquid) flow
rate from all the
readings; and
determine and record
the minimum liquid-to-
gas ratio.
[[Page 136]]
g. Alternative Data from the You must collect air
procedure for gas flow continuous parameter flow rate monitoring
rate. monitoring systems and data or determine the
applicable performance air flow rate using
test methods. control room
instrumentation every
15 minutes during the
entire period of the
initial performance
test; determine and
record the hourly
average rate of all
the readings; and
determine and record
the maximum gas flow
rate using Equation 1
of Sec. 63.1573.
----------------------------------------------------------------------------------------------------------------
\1\ EPA Method 6010B, Inductively Coupled Plasma-Atomic Emission Spectrometry, EPA Method 6020, Inductively
Coupled Plasma-Mass Spectrometry, EPA Method 7520, Nickel Atomic Absorption, Direct Aspiration, and EPA Method
7521, Nickel Atomic Absorption, Direct Aspiration are included in ``Test Methods for Evaluating Solid Waste,
Physical/Chemical Methods,'' EPA Publication SW-846, Revision 5 (April 1998). The SW-846 and Updates (document
number 955-001-00000-1) are available for purchase from the Superintendent of Documents, U.S. Government
Printing Office, Washington, DC 20402, (202) 512-1800; and from the National Technical Information Services
(NTIS), 5285 Port Royal Road, Springfield, VA 22161, (703) 487-4650. Copies may be inspected at the Air and
Radiation Docket and Information Center, U.S. Environmental Protection Agency, 401 M Street, SW, Washington,
DC; or at the Office of the Federal Register, 800 North Capitol Street, NW, Suite 700, Washington, DC.
Table 5 to Subpart UUU of Part 63--Initial Compliance With Metal HAP
Emission Limits for Catalytic Cracking Units
[As stated in Sec. 63.1564(b)(5), you must meet each requirement in the following table that applies to you]
----------------------------------------------------------------------------------------------------------------
For each new and existing catalytic
cracking unit catalyst regenerator vent For the following emission limit * You have demonstrated initial
* * * * * compliance if * * *
----------------------------------------------------------------------------------------------------------------
1. Subject to the NSPS for PM in 40 CFR PM emissions must not exceed 1.0 kg/ You have already conducted a
60.102. 1,000 kg (1.0 lb/1,000 lb) of coke performance test to demonstrate
burn-off in the catalyst initial compliance with the NSPS
regenerator; if the discharged and the measured PM emission rate
gases pass through an incinerator is less than or equal to 1.0 kg/
or waste heat boiler in which you 1,000 kg (1.0 lb/1,000 lb) of
burn auxiliary or supplemental coke burn-off in the catalyst
liquid or solid fossil fuel, you regenerator. As part of the
must limit the incremental rate of Notification of Compliance
PM to no more than 43.0 grams per Status, you must certify that
Megajoule (g/MJ) or 0.10 pounds your vent meets the PM limit. You
per million British thermal units are not required to do another
(lb/million Btu) of heat input performance test to demonstrate
attributable to the liquid or initial compliance. If
solid fossil fuel; and the opacity applicable, you have already
of emissions 30 percent, except conducted a performance test to
for one 6-minute average opacity demonstrate initial compliance
reading in any 1-hour period. with the NSPS and the measured PM
rate is less than or equal to
43.0 g/MJ or 0.010 lb/million Btu
of heat input attributable to the
liquid or solid fossil fuel. As
part of the Notification of
Compliance Status, you must
certify that your vent meets the
PM emission limit. You are not
required to do another
performance test to demonstrate
initial compliance. You have
already conducted a performance
test to demonstrate initial
compliance with the NSPS and the
average hourly opacity of
emissions is no more than 30
percent. Except: one 6-minute
average in any 1-hour period can
exceed 30 percent. As part of the
Notification of Compliance
Status, you must certify that
your vent meets the opacity
limit. You are not required to do
another performance test to
demonstrate initial compliance.
You have already conducted a
performance evaluation to
demonstrate initial compliance
with the applicable performance
specification. As part of your
Notification of Compliance
Status, you certify that your
continuous opacity monitoring
system meets the requirements in
Sec. 63.1572. You are not
required to do a performance
evaluation to demonstrate initial
compliance.
[[Page 137]]
2. Option 1: Elect NSPS not subject to PM emissions must not exceed 1.0 kg/ The average PM emission rate,
the NSPS for PM. 1,000 kg (1.0 lb/1,000 lb) of coke measured using EPA method 5 over
burn-off in the catalyst the period of the initial
regenerator; if the discharged performance test, is no higher
gases pass through an incinerator than 1.0 kg/1,000 kg (1.0 lb/
or waste heat boiler in which you 1,000 lbs) of coke burn-off in
burn auxiliary or supplemental the catalyst regenerator. The PM
liquid or solid fossil fuel, you emission rate is calculated using
must limit the incremental rate of Equations 1 and 2 of the Sec.
PM to no more than 43.0 grams per 63.1564. If applicable, the
Megajoule (g/MJ) or 0.10 pounds average PM emission rate,
per million British thermal units measured using EPA Method 5 over
(lb/million Btu) of heat input the period of the initial
attributable to the liquid or performance test, is no higher
solid fossil fuel; and the opacity than 43.0 g/MJ or 0.010 lb/
of emissions must not exceed 30 million Btu of heat input
percent, except for one 6-minute attributable to the liquid or
average opacity reading in any 1- solid fossil fuel. The PM
hour period. emission rate is calculated using
Equation 3 of Sec. 63.1564; no
more than one 6-minute average
measured by the continuous
opacity monitoring system exceeds
30 percent opacity in any 1-hour
period over the period of the
performance test; and your
performance evaluation shows the
continuous opacity monitoring
system meets the applicable
requirements in Sec. 63.1572.
3. Option 2: not subject to the NSPS PM emissions must not exceed 1.0 kg/ The average PM emission rate,
for PM. 1,000 kg (1.0 lb/1,000 lb) of coke measured using EPA Method 5 over
burn-off in the catalyst the period of the initial
regenerator. performance test, is less than or
equal to 1.0 kg/1,000 kg (1.0 lb/
1,000 lbs) of coke burn-off in
the catalyst regenerator. The PM
emission rate is calculated using
Equations 1 and 2 of Sec.
63.1564; and if you use a
continuous opacity monitoring
system, your performance
evaluation shows the system meets
the applicable requirements in
Sec. 63.1572.
4. Option 3: not subject to the NSPS Nickel (Ni) emissions from your The average Ni emission rate,
for PM. catalyst regenerator vent must not measured using Method 29 over the
exceed 13,000 mg/hr (0.029 lb/hr). period of the initial performance
test, is not more than 13,000 mg/
hr (0.029 lb/hr). The Ni emission
rate is calculated using Equation
5 of Sec. 63.1564; and if you
use a continuous opacity
monitoring system, your
performance evaluation shows the
system meets the applicable
requirements in Sec. 63.1572.
5. Option 4: Ni lb/1,000 lbs of coke Ni emissions from your catalyst The average Ni emission rate,
burn-off not subject to the NSPS for regenerator vent must not exceed measured using Method 29 over the
PM. 1.0 mg/kg (0.001 lb/1,000 lbs) of period of the initial performance
coke burn-off in the catalyst test, is not more than 1.0 mg/kg
regenerator. (0.001 lb/1,000 lbs) of coke burn-
off in the catalyst regenerator.
The Ni emission rate is
calculated using Equation 8 of
Sec. 63.1564; and if you use a
continuous opacity monitoring
system, your performance
evaluation shows the system meets
the applicable requirements in
Sec. 63.1572.
----------------------------------------------------------------------------------------------------------------
[[Page 138]]
Table 6 to Subpart UUU of Part 63--Continuous Compliance With Metal HAP
Emission Limits for Catalytic Cracking Units
[As stated in Sec. 63.1564(c)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
Subject to this
For each new and existing emission limit for You must demonstrate
catalytic cracking unit * * your catalyst continuous
* regenerator vent * * compliance by * * *
*
------------------------------------------------------------------------
1. Subject to the NSPS for a. PM emissions must i. Determining and
PM in 40 CFR 60.102. not exceed 1.0 lb/ recording each day
1,000 lbs of coke the average coke
burn-off in the burn-off rate
catalyst (thousands of
regenerator; if the kilograms per hour)
discharged gases using Equation 2 in
pass through an Sec. 63.1564 and
incinerator or the hours of
waste heat boiler operation for each
in which you burn catalyst
auxiliary or regenerator;
supplemental liquid maintaining PM
or solid fossil emission rate below
fuel, incremental 1.0 kg/1,000 kg
rate of PM can't (1.0 lb/1,000 lbs)
exceed 43.0 g/MJ of coke burn-off;
(0.10 lb/million if applicable,
Btu) of heat input determining and
attributable to the recording each day
liquid or solid the rate of
fossil fuel; and combustion of
opacity of liquid or solid
emissions can't fossil fuels
exceed 30 percent, (liters/hour or
except for one 6- kilograms/hour)
minute average using Equation 3 of
opacity reading in Sec. 63.1564 and
any 1-hour period. the hours of
operation during
which liquid or
solid fossil-fuels
are combusted in
the incinerator-
waste heat boiler;
if applicable,
maintaining PM rate
below 43 g/MJ (0.10
lb/million Btu) of
heat input
attributable to the
solid or liquid
fossil fuel;
collecting the
continuous opacity
monitoring data for
each catalyst
regenerator vent
according to Sec.
63.1572; and
maintaining each 6-
minute average at
or below 30 percent
except that one 6-
minute average
during a 1-hour
period can exceed
30 percent.
2. Option 1: Elect NSPS not See item 1.a. of See item 1.a.i. of
subject to the NSPS for PM this table. this table.
in 40 CFR 60.102.
3. Option 2: PM limit not PM emissions must Determining and
subject to the NSPS for PM. not exceed 1.0 lb/ recording each day
1,000 lbs of coke the average coke
burn-off in the burn-off rate
catalyst (thousands of
regenerator. kilograms per hour)
and the hours of
operation for each
catalyst
regenerator by
Equation 2 of Sec.
63.1564. You can
use process data to
determine the
volumetric flow
rate; and
maintaining PM
emission rate below
1.0 kg/1,000 kg
(1.0 lb/1,000 lbs)
of coke burn-off.
4. Option 3: Ni lb/hr not Ni emissions must Maintaining Ni
subject to the NSPS for PM. not exceed 13,000 emission rate below
mg/hr (0.029 lb/ 13,000 mg/hr (0.029
hr). lb/hr).
5. Option 4: Ni lb/1,000 lbs Ni emissions must Determining and
of coke burn-off not not exceed 1.0 mg/ recording each day
subject to the NSPS for PM. kg (0.001 lb/1,000 the average coke
lbs) of coke burn- burn-off rate
off in the catalyst (thousands of
regenerator. kilograms per hour)
and the hours of
operation for each
catalyst
regenerator by
Equation 2 of Sec.
63.1564. You can
use process data to
determine the
volumetric flow
rate; and
maintaining Ni
emission rate below
1.0 mg/kg (0.001 lb/
1,000 lbs) of coke
burn-off in the
catalyst
regenerator.
------------------------------------------------------------------------
Table 7 to Subpart UUU of Part 63--Continuous Compliance With Operating
Limits for Metal HAP Emissions From Catalytic Cracking Units
[As stated in Sec. 63.1564(c)(1), you must meet each requirement in the following table that applies to you]
----------------------------------------------------------------------------------------------------------------
You must demonstrate
For each new or existing catalytic If you use * * * For this operating continuous compliance
cracking unit * * * limit * * * by * * *
----------------------------------------------------------------------------------------------------------------
1. Subject to NSPS for PM in 40 CFR Continuous opacity Not applicable......... Complying with Table 6
60.102. monitoring system. of this subpart.
2. Option 1: Elect NSPS not subject Continuous opacity Not applicable......... Complying with Table 6
to the NSPS for PM in 40 CFR 60.102. monitoring system. of this subpart.
[[Page 139]]
3. Option 2: PM limit not subject to a. Continuous opacity The opacity of Collecting the hourly
the NSPS for PM in 40 CFR 60.102. monitoring system. emissions from your average continuous
catalyst regenerator opacity monitoring
vent must not exceed system data according
the site-specific to Sec. 63.1572; and
opacity operating maintaining each 6-
limit established minute average in each
during the performance 1-hour period at or
test below the site-
specific limit.
b. Continuous parameter i. The daily average Collecting the hourly
monitoring systems-- gas flow rate to the and daily average gas
electrostatic control device must flow rate monitoring
precipitator. not exceed the data according to Sec.
operating limit 63.1572 \1\; and
established during the maintaining the daily
performance test. average gas flow rate
at limit or below the
established during the
performance test.
ii. The daily average Collecting the hourly
voltage and secondary and daily average
current (or total voltage and secondary
power input) to the current (or total
control device must power input)
not fall below the monitoring data
operating limit according to Sec.
established during the 63.1572; and
performance test. maintaining the daily
average voltage and
secondary current (or
total power input) at
or above the limit
established during the
performance test.
c. Continuous parameter i. The daily average Collecting the hourly
monitoring systems-- pressure drop across and daily average
wet scrubber. the scrubber must not pressure drop
fall below the monitoring data
operating limit according to Sec.
established during the 63.1572; and
performance test. maintaining the daily
average press drop
above the limit
established during the
performance test.
ii. The daily average Collecting the hourly
liquid-to-gas ratio average gas flow rate
must not fall below and water (or
the operating limit scrubbing liquid) flow
established during the rate monitoring data
performance test. according to Sec.
63.1572 \1\;
determining and
recording the hourly
average liquid-to-gas
ratio; determining and
recording the daily
average liquid-to-gas
ratio; and maintaining
the daily average
liquid-to-gas ratio
above the limit
established during the
performance test.
[[Page 140]]
4. Option 3: Ni lb/hr not subject to a. Continuous opacity The daily average Ni Collecting the hourly
the NSPS for PM in 40 CFR 60.102. monitoring system. operating value must average continuous
not exceed the site- opacity monitoring
specific Ni operating system data according
limit established Sec. 63.1572;
during the performance determining and
test. recording equilibrium
catalyst Ni
concentration at least
once a week collecting
the hourly average gas
flow rate monitoring
data according to Sec.
63.1572 \1\;
determining and
recording the hourly
average Ni operating
value using Equation
11 of Sec. 63.1564;
determining and
recording the daily
average Ni operating
value; and maintaining
the daily average Ni
operating value below
the site-specific Ni
operating limit
established the
performance test.
b. Continuous parameter i. The daily average See item 3.b.i. of this
monitoring systems-- gas flow rate to the table.
electrostatic control device must
precipitator. notice exceed the
level established in
the performance test.
ii. The daily average See item 3.b.ii. of
voltage and secondary this table.
current (or total
power input) must not
fall below the level
established in the
performance test.
iii. The monthly Determining the
rolling average of recording the
equilibrium catalyst equilibrium catalyst
Ni concentration must Ni concentration at
not exceed the level least once a week;
established during the determining and
performance test. recording the monthly
rolling average of the
equilibrium catalyst
Ni concentration once
each week using the
weekly or most recent
value; and maintaining
the monthly rolling
average below the
limit established in
the performance test
c. Continuous parameter i. The daily average See item 3.c.i. of this
monitoring systems-- pressure drop must not table.
wet scrubber. fall below the
operating limit
established in the
performance test.
ii. The daily average See item 3.c.ii. of
liquid-to-gas ratio this table.
must not fall below
the operating limit
established during the
performance test.
iii. The monthly Determining and
rolling average recording the
equilibrium catalyst equilibrium catalyst
Ni concentration must Ni concentration at
not exceed the level least once a week;
established during the determining and
performance test. recording the monthly
rolling average of
equilibrium catalyst
Ni concentration once
each week using the
weekly or most recent
value; and maintaining
the monthly rolling
average below the
limit established in
the performance test.
[[Page 141]]
5. Option 4: Ni lb/ton of coke burn- a. Continuous opacity The daily average Ni Collecting the hourly
off not subject to the NSPS for PM monitoring system. operating value must average continuous
in 40 CFR 60.102 not exceed the site- opacity monitoring
specific Ni operating system data according
limit established to Sec. 63.1572;
during the performance collecting the hourly
test. average gas flow rate
monitoring data
according to Sec.
63.1572 \1\;
determining and
recording equilibrium
catalyst Ni
concentration at least
once a week;
determining and
recording the hourly
average Ni operating
value using Equation
12 of Sec. 63.1564;
determining and
recording the daily
average Ni operating
value; and maintaining
the daily average Ni
operating value below
the site-specific Ni
operating limit
established during the
performance test.
b. Continuous parameter i. The daily average See item 3.b.i. of this
monitoring systems-- gas flow rate to the table.
electrostatic control device must
precipitator. not exceed the level
established in the
performance test.
ii. The daily average See item 3.b.ii. of
voltage and secondary this table.
current (or total
power input) must not
fall below the level
established in the
performance test.
iii. The monthly See item 4.b.iii. of
rolling average this table.
equilibrium catalyst
Ni concentration must
not exceed the level
established during the
performance test.
c. Continuous parameter i. The daily average See item 3.c.i. of this
monitoring systems-- pressure drop must not table.
wet scrubber. fall below the
operating limit
established in the
performance test.
ii. The daily average
liquid-to-gas ratio
must not fall below
the operating limit
established during the
performance test. See
item 3.c.ii. of this
table.
iii. The monthly See item 4.c.iii. of
rolling average this table.
equilibrium catalyst
Ni concentration must
not exceed the level
established during the
performance test.
----------------------------------------------------------------------------------------------------------------
\1\ If applicable, you can use the alternative in Sec. 63.1573 for gas flow rate instead of a continuous
parameter monitoring system if you used the alternative method in the initial performance test. If so, you
must continuously monitor and record the air flow rate to the regenerator and the temperature of the gases
entering the control device as described in Sec. 63.1573. You must determine and record the hourly average
gas flow rate using Equation 1 of Sec. 63.1573 and the daily average gas flow rate. You must maintain the
daily average gas flow rate below the operating limit established during the performance test.
[[Page 142]]
Table 8 to Subpart UUU of Part 63--Organic HAP Emission Limits for
Catalytic Cracking Units
[As stated in Sec. 63.1565(a)(1), you must meet each emission
limitation in the following table that applies to you]
------------------------------------------------------------------------
You must meet the
following emission
For each new and existing catalytic cracking unit limit for each
* * * catalyst regenerator
vent * * *
------------------------------------------------------------------------
1. Subject to the NSPS for carbon monoxide (CO) in CO emissions from
40 CFR 60.103. the catalyst
regenerator vent or
CO boiler serving
the catalytic
cracking unit must
not exceed 500
parts per million
volume (ppmv) (dry
basis).
2. Not subject to the NSPS for CO in 40 CFR 60.103 a. CO emissions from
the catalyst
regenerator vent or
CO boiler serving
the catalytic
cracking unit must
not exceed 500 ppmv
(dry basis).
b. If you use a
flare to meet the
CO limit, the flare
must meet the
requirements for
control devices in
Sec. 63.11(b):
visible emissions
must not exceed a
total of 5 minutes
during any 2
consecutive hours.
------------------------------------------------------------------------
Table 9 to Subpart UUU of Part 63--Operating Limits for Organic HAP
Emissions From Catalytic Cracking Units
[As stated in Sec. 63.1565(a)(2), you must meet each operating limit in the following table that applies to
you]
----------------------------------------------------------------------------------------------------------------
For this type of
For each new or existing catalytic continuous monitoring For this type of You must meet this
cracking unit * * * system * * * control device * * * operating limit * * *
----------------------------------------------------------------------------------------------------------------
1. Subject to the NSPS for carbon Continuous emission Not applicable......... Not applicable.
monoxide (CO) in 40 CFR 60.103. monitoring system.
2. Not subject to the NSPS for CO in a. Continuous emission Not applicable......... Not applicable.
40 CFR 60.103. monitoring system.
b. Continuous parameter i. Thermal incinerator. Maintain the daily
monitoring systems. average combustion
zone temperature above
the limit established
during the performance
test; and maintain the
daily average oxygen
concentration in the
vent stream (percent,
dry basis) above the
limit established
during the performance
test.
ii. Boiler or process Maintain the daily
heater with a design average combustion
heat input capacity zone temperature above
under 44 MW or a the limit established
boiler or process in the performance
heater in which all test.
vent streams are not
introduced into the
flame zone.
iii. Flare............. The flare pilot light
must be present at all
times and the flare
must be operating at
all times that
emissions may be
vented to it.
----------------------------------------------------------------------------------------------------------------
Table 10 to Subpart UUU of Part 63--Continuous Monitoring Systems for
Organic HAP Emissions From Catalytic Cracking Units
[As stated in Sec. 63.1565(b)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You must install,
And you use this operate, and
For each new or existing type of control maintain this type
catalytic cracking unit * * device for your vent of continuous
* * * * monitoring system *
* *
------------------------------------------------------------------------
1. Subject to the NSPS for Not applicable...... Continuous emission
carbon monoxide (CO) in 40 monitoring system
CFR 60.103. to measure and
record the
concentration by
volume (dry basis)
of CO emissions
from each catalyst
regenerator vent.
[[Page 143]]
2. Not subject to the NSPS a. Thermal Continuous emission
for CO in 40 CFR 60.103. incinerator. monitoring system
to measure and
record the
concentration by
volume (dry basis)
of CO emissions
from each catalyst
regenerator vent;
or continuous
parameter
monitoring systems
to measure and
record the
combustion zone
temperature and
oxygen content
(percent, dry
basis) in the
incinerator vent
stream.
b. Process heater or Continuous emission
boiler with a monitoring system
design heat input to measure and
capacity under 44 record the
MW or process concentration by
heater or boiler in volume (dry basis)
which all vent of CO emissions
streams are not from each catalyst
introduced into the regenerator vent;
flame zone. or continuous
parameter
monitoring systems
to measure and
record the
combustion zone
temperature.
c. Flare............ Monitoring device
such as a
thermocouple, an
ultraviolet beam
sensor, or infrared
sensor to
continuously detect
the presence of a
pilot flame.
d. No control device Continuous emission
monitoring system
to measure and
record the
concentration by
volume (dry basis)
of CO emissions
from each catalyst
regenerator vent.
------------------------------------------------------------------------
Table 11 to Subpart UUU of Part 63--Requirements for Performance Tests
for Organic HAP Emissions From Catalytic Cracking Units Not Subject to
New Source Performance Standard (NSPS) for Carbon Monoxide (CO)
[As stated in Sec. 63.1565(b)(2) and (3), you must meet each requirement in the following table that applies to
you]
----------------------------------------------------------------------------------------------------------------
According to these
For * * * You must * * * Using * * * requirements * * *
----------------------------------------------------------------------------------------------------------------
1. Each new or existing catalytic a. Select sampling Method 1 or 1A in Sampling sites must be
cracking unit catalyst regenerator port's location and appendix A to part 60 located at the outlet
vent. the number of traverse of this chapter. of the control device
ports. or the outlet of the
regenerator, as
applicable, and prior
to any releases to the
atmosphere.
b. Determine velocity Method 2, 2A, 2D, 2F,
and volumetric flow or 2G in appendix A to
rate. part 60 of this
chapter, as
applicable.
c. Conduct gas Method 3, 3A, or 3B in
molecular weight appendix A to part 60
analysis. of this chapter, as
applicable.
d. Measure moisture Method 4 in appendix A
content of the stack to part 60 of this
gas. chapter.
2. For each new or existing catalytic Measure CO emissions... Data from your Collect CO monitoring
cracking unit catalyst regenerator continuous emission data for each vent for
vent if you use a continuous monitoring system. 24 consecutive
emission monitoring system. operating hours; and
reduce the continuous
emission monitoring
data to 1-hour
averages computed from
four or more data
points equally spaced
over each 1-hour
period.
3. Each catalytic cracking unit a. Measure the CO Method 10, 10A, or 10B
catalyst regenerator vent if you use concentration (dry in appendix A to part
continuous parameter monitoring basis) of emissions 60 of this chapter, as
systems. exiting the control applicable.
device.
b. Establish each Data from the
operating limit in continuous parameter
Table 9 of this monitoring systems.
subpart that applies
to you.
[[Page 144]]
c. Thermal incinerator Data from the Collect temperature
combustion zone continuous parameter monitoring data every
temperature. monitoring systems. 15 minutes during the
entire period of the
CO initial performance
test; and determine
and record the minimum
hourly average
combustion zone
temperature from all
the readings.
d. Thermal incinerator: Data from the Collect oxygen
oxygen, content continuous parameter concentration
(percent, dry basis) monitoring systems. (percent, dry basis)
in the incinerator monitoring data every
vent stream. 15 minutes during the
entire period of the
CO initial performance
test; and determine
and record the minimum
hourly average percent
excess oxygen
concentration from all
the readings.
e. If you use a process Data from the Collect the temperature
heater or boiler with continuous parameter monitoring data every
a design heat input monitoring systems. 15 minutes during the
capacity under 44 MW entire period of the
or process heater or CO initial performance
boiler in which all test; and determine
vent streams are not and record the minimum
introduced into the hourly average
flame zone, establish combustion zone
operating limit for temperature from all
combustion zone the readings.
temperature.
f. If you use a flare, Method 22 (40 CFR part Maintain a 2-hour
conduct visible 60, appendix A). observation period;
emission observations. and record the
presence of a flame at
the pilot light over
the full period of the
test.
g. If you use a flare, 40 CFR
determine that the 60.11(b)(6)through(8).
flare meets the
requirements for net
heating value of the
gas being combusted
and exit velocity.
----------------------------------------------------------------------------------------------------------------
Table 12 to Subpart UUU of Part 63--Initial Compliance With Organic HAP
Emission Limits for Catalytic Cracking Units
[As stated in Sec. 63.1565(b)(4), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
For each new and existing You have
catalytic cracking unit * * For the following demonstrated initial
* emission limit * * * compliance if * * *
------------------------------------------------------------------------
1. Subject to the NSPS for CO emissions from You have already
carbon monoxide (CO) in 40 your catalyst conducted a
CFR 60.103. regenerator vent or performance test to
CO boiler serving demonstrate initial
the catalytic compliance with the
cracking unit must NSPS and the
not exceed 500 ppmv measured CO
(dry basis). emissions are less
than or equal to
500 ppm (dry
basis). As part of
the Notification of
Compliance Status,
you must certify
that your vent
meets the CO limit.
You are not
required to conduct
another performance
test to demonstrate
initial compliance.
You have already
conducted a
performance
evaluation to
demonstrate initial
compliance with the
applicable
performance
specification. As
part of your
Notification of
Compliance Status,
you must certify
that your
continuous emission
monitoring system
meets the
applicable
requirements in
Sec. 63.1572. You
are not required to
conduct another
performance
evaluation to
demonstrate initial
compliance.
[[Page 145]]
2. Not subject to the NSPS a. CO emissions from i. If you use a
for CO in 40 CFR 60.103. your catalyst continuous
regenerator vent or parameter
CO boiler serving monitoring system,
the catalytic the average CO
cracking unit must emissions measured
not exceed 500 ppmv by Method 10 over
(dry basis). the period of the
initial performance
test are less than
or equal to 500
ppmv (dry basis).
ii. If you use a
continuous emission
monitoring system,
the hourly average
CO emissions over
the 24-hour period
for the initial
performance test
are not more than
500 ppmv (dry
basis); and your
performance
evaluation shows
your continuous
emission monitoring
system meets the
applicable
requirements in
Sec. 63.1572.
b. If you use a Visible emissions,
flare, visible measured by Method
emissions must not 22 during the 2-
exceed a total of 5 hour observation
minutes during any period during the
2 operating hours. initial performance
test, are no higher
than 5 minutes.
------------------------------------------------------------------------
Table 13 to Subpart UUU of Part 63--Continuous Compliance With Organic
HAP Emission Limits for Catalytic Cracking Units
[As stated in Sec. 63.1565(c)(1), you must meet each requirement in the following table that applies to you]
----------------------------------------------------------------------------------------------------------------
Subject to this
For each new and existing catalytic emission limit for your You must demonstrate
cracking unit * * ;* catalyst regenerator If you must * * * continuous compliance
vent * * * by * * *
----------------------------------------------------------------------------------------------------------------
1. Subject to the NSPS for carbon CO emissions from your Continuous emission Collecting the hourly
monoxide (CO) in 40 CFR 60.103. catalyst regenerator monitoring system. average CO monitoring
vent or CO boiler data according to Sec.
serving the catalytic 63.1572; and
cracking unit must not maintaining the hourly
exceed 500 ppmv (dry average CO
basis). concentration at or
below 500 ppmv (dry
basis).
2. Not subject to the NSPS for CO in i. CO emissions from Continuous emission Same as above.
40 CFR 60.103. your catalyst monitoring system.
regenerator vent or CO
boiler serving the
catalytic cracking
unit must not exceed
500 ppmv (dry basis).
ii. CO emissisons from Continuous parameter Maintaining the hourly
your catalyst monitoring system. average CO
regenerator vent or CO concentration below
boiler serving the 500 ppmv (dry basis).
catalytic cracking
unit must not exceed
500 ppmv (dry basis).
iii. Visible emissions Control device-flare... Maintaining visible
from a flare must not emissions below a
exceed a total of 5 total of 5 minutes
minutes during any 2- during any 2-hour
hour period. operating period.
----------------------------------------------------------------------------------------------------------------
Table 14 to Subpart UUU of Part 63--Continuous Compliance With Operating
Limits for Organic HAP Emissions From Catalytic Cracking Units
[As stated in Sec. 63.1565(c)(1), you must meet each requirement in the following table that applies to you]
----------------------------------------------------------------------------------------------------------------
You must demonstrate
For each new existing catalytic If you use * * * For this operating continuous compliance
cracking unit * * * limit * * * by * * *
----------------------------------------------------------------------------------------------------------------
1. Subject to NSPS for carbon Continuous emission Not applicable......... Complying with Table 13
monoxide (CO) in 40 CFR 60.103. monitoring system. of this subpart.
2. Not subject to the NSPS for CO in a. Continuous emission Not applicable......... Complying with Table 13
40 CFR 60.103. monitoring system. of this subpart.
[[Page 146]]
b. Continuous parameter i. The daily average Collecting the hourly
monitoring systems-- combustion zone and daily average
thermal incinerator. temperature must not temperature monitoring
fall below the level data according to Sec.
established during the 63.1572; and
performance test. maintaining the daily
average combustion
zone temperature above
the limit established
during the performance
test.
ii. The daily average Collecting the hourly
oxygen concentration and daily average
in the vent stream oxygen concentration
(percent, dry basis) monitoring data
must not fall below according to Sec.
the level established 63.1572; and
during the performance maintaining the daily
test. average oxygen
concentration above
the limit established
during the performance
test.
c. Continuous parameter The daily combustion Collecting the average
monitoring systems-- zone temperature must hourly and daily
boiler or process not fall below the temperature monitoring
heater with a design level established in data according to Sec.
heat input capacity the performance test. 63.1572; and
under 44 MW or boiler maintaining the daily
or process heater in average combustion
which all vent streams zone temperature above
are not introduced the limit established
into the flame zone. during the performance
test.
d. Continuous parameter The flare pilot light Collecting the flare
monitoring system-- must be present at all monitoring data
flare. times and the flare according to Sec.
must be operating at 63.1572; and recording
all times that for each 1-hour period
emissions may be whether the monitor
vented to it. was continuously
operating and the
pilot light was
continuously present
during each 1-hour
period.
----------------------------------------------------------------------------------------------------------------
Table 15 to Subpart UUU of Part 63--Organic HAP Emission Limits for
Catalytic Reforming Units
[As stated in Sec. 63.1566(a)(1), you must meet each emission
limitation in the following table that applies to you]
------------------------------------------------------------------------
You must meet this emission
For each new or existing catalytic limit for each process vent
reforming unit * * * during depressuring and
purging operation * * *
------------------------------------------------------------------------
1. Option 1............................... Vent emissions to a flare
that meets the requirements
for control devices in Sec.
63.11(b). Visible
emissions from a flare must
not exceed a total of 5
minutes during any 2-hour
operating period.
2. Option 2............................... Using a control device,
reduce uncontrolled
emissions of total organic
compounds (TOC) from your
process vent by 98 percent
by weight or to a
concentration of 20 ppmv
(dry basis), corrected to 3
percent oxygen, whichever
is less stringent. If you
vent emissions to a boiler
or process heater to comply
with the percent reduction
or concentration emission
limitation, the vent stream
must be introduced into the
flame zone, or any other
location that will achieve
the percent reduction or
concentration standard.
------------------------------------------------------------------------
Table 16 to Subpart UUU of Part 63--Operating Limits for Organic HAP
Emissions From Catalytic Reforming Units
[As stated in Sec. 63.1566(a)(2), you must meet each operating limit in
the following table that applies to you]
------------------------------------------------------------------------
You must meet this
For each new or existing operating limit
catalytic reforming unit * * For this type of during depressuring
* control device * * * and purging
operations * * *
------------------------------------------------------------------------
1. Option 1: vent to flare.. Flare that meets the The flare pilot
requirements for light must be
control devices in present at all
Sec. 63.11(b). times and the flare
must be operating
at all times that
emissions may be
vented to it.
[[Page 147]]
2. Option 2: percent Thermal incinerator, The daily average
reduction or concentration boiler or process combustion zone
limit. heater with a temperature must
design heat input not fall below the
capacity under 44 limit established
MW, or boiler or during the
process heater in performance test.
which all vent
streams are not
introduced into the
flame zone.
------------------------------------------------------------------------
Table 17 to Subpart UUU of Part 63--Continuous Monitoring Systems for
Organic HAP Emissions From Catalytic Reforming Units
[As stated in Sec. 63.1566(b)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You must install and
For each new or exiting If you use this type operate this type of
catalytic reforming unit * * of control device * continuous
* * * monitoring system *
* *
------------------------------------------------------------------------
1. Option 1: vent to a flare Flare that meets the Monitoring device
requirements for such as a
control devices in thermocouple, an
Sec. 63.11(b). ultraviolet beam
sensor, or infrared
sensor to
continuously detect
the presence of a
pilot flame.
2. Option 2: percent Thermal incinerator, Continuous parameter
reduction or concentration process heater or monitoring systems
limit. boiler with a to measure and
design heat input record the
capacity under 44 combustion zone
MW, or process temperature.
heater or boiler in
which all vent
streams are not
introduced into the
flame zone.
------------------------------------------------------------------------
Table 18 to Subpart UUU of Part 63--Requirements for Performance Tests
for Organic HAP Emissions From Catalytic Reforming Units
[As stated in Sec. 63.1566(b)(2) and (3), you must meet each requirement in the following table that applies to
you]
----------------------------------------------------------------------------------------------------------------
For each new or exiting catalytic According to these
reforming unit * * * You must * * * Using * * * requirements * * *
----------------------------------------------------------------------------------------------------------------
1. Option 1: vent to a flare......... a. Conduct visible Method 22 (40 CFR 60, 2-hour observation
emission observations. appendix A). period. Record the
presence of a flame at
the pilot light over
the full period of the
test.
b. Determine that the Not applicable......... 40 CFR 60.11(b)(6)
flare meets the through (8).
requirements for net
heating value of the
gas being combusted
and exit velocity.
2. Option 2: percent reduction or a. Select sampling site Method 1 or 1A (40 CFR Sampling sites must be
concentration limit. part 60, appendix A). located at the inlet
No traverse site (if you elect the
selection method is emission reduction
needed for vents standard) and outlet
smaller than 0.10 of the control device
meter in diameter. and prior to any
releases to the
atmosphere.
b. Measure gas Method 2, 2A, 2C, 2D, .......................
volumetric flow rate. 2F, or 2G (40 CFR part
60, appendix A), as
applicable.
c. Measure TOC Method 25 (40 CFR part Take either an
concentration (for 60, appendix A) to integrated sample or
percent reduction measure TOC four grab samples
standard). concentration at the during each run. If
inlet and outlet of you use a grab
the control device. If sampling technique,
the TOC outlet take the samples at
concentration is approximately equal
expected to be less intervals in time,
than 50 ppm, you can such as 15-minute
use Method 25A to intervals during the
measure TOC run.
concentration at the
inlet and the outlet
of the control device.
[[Page 148]]
d. Calculate TOC Calculate emission rate .......................
emission rate and mass by Equation 1 of Sec.
emission reduction. 63.1566 (if you use
Method 25) or Equation
2 of Sec. 63.1566 (if
you use Method 25A).
Calculate mass
emission reduction by
Equation 3 of Sec.
63.1566.
e. Measure TOC Method 25A (40 CFR
concentration (for part 60, appendix A)
concentration to measure TOC
standard). concentration at the
outlet of the control
device.
f. Determine oxygen Method 3A or 3B (40
content in the gas CFR part 60, appendix
stream at the outlet A), as applicable.
of the control device.
g. Correct the measured Equation 4 of Sec.
TOC concentration for 63.1566
oxygen content.
h. Established each Data from the Collect the temperature
operating limit in continuous parameter monitoring data every
Table 16 of this monitoring systems. 15 minutes during the
subpart that applies entire period of the
to you for a thermal initial TOC
incinerator, or performance test.
process heater or Determine and record
boiler with a design the minimum hourly
heat input capacity average combustion
under 44 MW, or zone temperature.
process heater or
boiler in which all
vent streams are not
introduced into the
flame zone.
----------------------------------------------------------------------------------------------------------------
Table 19 to Subpart UUU of Part 63--Initial Compliance With Organic HAP
Emission Limits for Catalytic Reforming Units
[As stated in Sec. 63.1566(b)(7), you must meet each requirement in the following table that applies to you.]
----------------------------------------------------------------------------------------------------------------
For the following emission limit . You have demonstrated initial
For . . . . . compliance if . . .
----------------------------------------------------------------------------------------------------------------
1. Each new and existing catalytic a. Visible emissions from a flare Visible emissions, measured using
reforming unit. must not exceed a total of 5 Method 22 over the 2-hour
minutes during any 2 consecutive observation period of the
hours. performance test do not exceed a
total of 5 minutes.
b. Reduce uncontrolled emissions of The mass emission reduction
TOC from your process vent using a measured using Method 25 over the
control device, by 98 percent by period of the performance test, is
weight or to a concentration of 20 at least 98 percent by weight. The
ppmv, on a dry basis, corrected to mass emission reduction is
3 percent oxygen, whichever is calculated using Equations 1 (or
less stringent. 2) and 3 of Sec. 63.1566 or the
TOC concentration, measured by
Method 25A over the period of the
performance test, does not exceed
20 ppmv (dry basis), corrected to
3 percent oxygen using Equation 4
of Sec. 63.1566.
----------------------------------------------------------------------------------------------------------------
Table 20 to Subpart UUU of Part 63--Continuous Compliance With Organic
HAP Emission Limits for Catalytic Reforming Units
[As stated in Sec. 63.1566(c)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You must demonstrate
continuous
For * * * For this emission compliance during
limit * * * depressuring and
purging by * * *
------------------------------------------------------------------------
1. Option 1: Each new or Vent emissions from Maintaining visible
existing catalytic your process vent emissions from a
reforming unit. to a flare that flare below a total
meets the of 5 minutes during
requirements in any 2 consecutive
Sec. 63.11(b). hours.
2. Option 2: Each new or Using a control Maintaining a 98
existing catalytic device, reduce percent by weight
reforming unit. uncontrolled TOC emission
emissions of TOC reduction; or
from your process maintaining a TOC
vent by 98 percent concentration of
by weight or to a not more than 20
concentration of 20 ppmv (dry basis),
ppmv, (dry basis), corrected to 3
corrected to 3 percent oxygen,
percent oxygen, whichever is less
whichever is less stringent.
stringent.
------------------------------------------------------------------------
[[Page 149]]
Table 21 to Subpart UUU of Part 63--Continuous Compliance With Operating
Limits for Organic HAP Emissions From Catalytic Reforming Units
[As stated in Sec. 63.1566(c)(1), you must meet each requirement in the following table that applies to you]
----------------------------------------------------------------------------------------------------------------
You must demonstrate
For this operating continuous compliance
For * * * If you use * * * limit * * * during depressuring and
purging by * * *
----------------------------------------------------------------------------------------------------------------
1. Each new or existing catalytic a. Flare that meets the The flare pilot light Collecting flare
reforming unit. requirements in Sec. must be present at all monitoring data
63.11(b). times and the flare according to Sec.
must be operating at 63.1572; and recording
all times that for each 1-hour period
emissions may be whether the monitor
vented to it. was continuously
operating and the
pilot light was
continuously present
during each 1-hour
period.
b. Thermal incinerator, Maintain the daily Collecting the hourly
boiler or process average combustion and daily temperature
heater with a design zone temperature above monitoring data
input capacity under the limit established according to Sec.
44 MW or boiler or during the performance 63.1572; and
process heater in test. maintaining the daily
which all vent streams average combustion
are not introduced zone temperature above
into the flame zone. the limit established
during the performance
test.
----------------------------------------------------------------------------------------------------------------
Table 22 to Subpart UUU of Part 63--Inorganic HAP Emission Limits for
Catalytic Reforming Units
[As stated in Sec. 63.1567(a)(1), you must meet each emission
limitation in the following table that applies to you]
------------------------------------------------------------------------
You must meet this
emission limit for
your process vent
For * * * during coke burn-off
and catalyst
rejuvenation * * *
------------------------------------------------------------------------
1. Each existing semi-regenerative catalytic Reduce uncontrolled
reforming unit. emissions of
hydrogen chloride
(HC1) by 92 percent
by weight using a
control device or
to a concentration
of 30 ppmv (dry
basis), corrected
to 3 percent
oxygen.
2. Each existing cyclic or continuous catalytic Reduce uncontrolled
reforming unit. emissions of HC1 by
97 percent by
weight using a
control device or
to a concentration
of 10 ppmv (dry
basis), corrected
to 3 percent
oxygen.
3. Each new semi-regenerative, cyclic, or Reduce uncontrolled
continuous catalytic reforming unit. emissions of HC1 by
97 percent by
weight using a
control device or
to a concentration
of 10 ppmv (dry
basis), corrected
to 3 percent
oxygen.
------------------------------------------------------------------------
Table 23 to Subpart UUU of Part 63--Operating Limits for Inorganic HAP
Emission Limitations for Catalytic Reforming Units
[As stated in Sec. 63.1567(a)(2), you must meet each operating limit in the following table that applies to
you]
----------------------------------------------------------------------------------------------------------------
You must meet this operating limit
For * * * If you use this type of control during coke burn-off and catalytst
device * * * rejuvenation . . .
----------------------------------------------------------------------------------------------------------------
1. Each new or existing catalytic a. Wet scrubber................. The daily average pH of the water
reforming unit. (or scrubbing liquid) exiting the
scrubber must not fall below the
limit established during the
performance test; and the daily
average liquid-to-gas ratio must
not fall below the limit
established during the performance
test.
b. Internal scrubbing system The HCl concentration in the
(i.e., no add-on control catalyst regenerator exhaust gas
device). must not exceed the limit
established during the performance
test.
----------------------------------------------------------------------------------------------------------------
[[Page 150]]
Table 24 to Subpart UUU of Part 63--Continuous Monitoring Systems for
Inorganic HAP Emissions From Catalytic Reforming Units
[As stated in Sec. 63.1567(b)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You must install and operate this
If you use this type of control type of continuous monitoring system
device for your vent * * * * * *
------------------------------------------------------------------------
1. Wet scrubber................... Continuous parameter monitoring
system to measure and record the pH
of the water (or scrubbing liquid)
exiting the scrubber during coke
burn-off and catalyst rejuvenation.
If applicable, you can use the
alternative in Sec. 63.1573
instead of a continuous parameter
monitoring system for pH of the
water (or scrubbing liquid); and
continuous parameter monitoring
systems to measure and record the
gas flow rate to the scrubber and
the total water (or scrubbing
liquid) flow rate to the scrubber
during coke burn-off and catalyst
rejuvenation.
2. Internal scrubbing system Colormetric tube sampling system to
(i.e., no add-on control device). measure the HCl concentration in
the catalyst regenerator exhaust
gas during coke burn-off and
catalyst rejuvenation.
------------------------------------------------------------------------
Table 25 to Subpart UUU of Part 63--Requirements for Performance Tests
for Inorganic HAP Emissions From Catalytic Reforming Units
[As stated in Sec. 63.1567(b)(2) and (3), you must meet each requirement in the following table that applies to
you]
----------------------------------------------------------------------------------------------------------------
If you use this type of control According to these
device or system * * * You must * * * Using * * * requirements * * *
----------------------------------------------------------------------------------------------------------------
1. Wet scrubber...................... a. Measure the HCl i. Method 26A (40 CFR (1) Sampling rate must
concentration at the part 60, appendix A). be at least 0.014 dscm/
outlet of the control min (0.5 dscf/min).
device (for the You must do the test
concentration during the coke burn-
standard) or at the off and catalyst
inlet and outlet of rejuvenation cycle,
the control d4evice but don't make any
(for the percent test runs during the
reduction standard). first hour or the last
6 hours of the cycle.
(2) Record the total
amount (rate) of
scrubbing liquid or
solution and the
amount (rate) of make-
up liquid to the
scrubber during each
test run.
b. Establish operating ....................... (1) Measure and record
limit for pH level. the pH of the water
(or scrubbing liquid)
exiting the scrubber
every 15 minutes
during the entire
period of the
performance test.
Determine and record
the hourly average pH
level from the
recorded values.
(2) If you use the
alternative method in
Sec. 63.1573, measure
and record the pH of
the water (or
scrubbing liquid)
exiting the scrubber
during coke burn-off
and catalyst
rejuvenation using pH
strips at least three
times during each run.
Determine and record
the average pH level.
c. Establish operating Data from the Measure and record the
limit for liquid-to- continuous parameter gas flow rate to the
gas ratio. monitoring systems. scrubber and the total
water (or scrubbing
liquid) flow rate to
the scrubber every 15
minutes during the
entire period of the
performance test.
Determine and record
the hourly average gas
flow rate and total
water (or scrubbing
liquid) flow rate.
Determine and record
the minimum liquid-to-
gas ratio.
[[Page 151]]
2. Internal scrubbing system (i.e., a. Measure the Method 26 (40 CFR part Sampling rate must be
no add-on control device). concentration of HCl 60, appendix A). at least 0.014 dscm/
in the catalyst min (0.5 dscf/min).
regenerator exhaust You must do the test
gas. during the coke burn-
off and catalyst
rejuvenation cycle,
but don't make any
test runs during the
first hour or the last
6 hours of the cycle.
b. Establish operating Measure and record the
limit for HCl HCl concentration in
concentration. the catalyst
regenerator exhaust
gas using the
colorimetric tube
sampling system at
least three times
during each test run.
Determine and record
the average HCl
concentration.
----------------------------------------------------------------------------------------------------------------
Table 26 to Subpart UUU of Part 63--Initial Compliance With Inorganic
HAP Emission Limits for Catalytic Reforming Units
[As stated in Sec. 63.1567(b)(4), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You have
For* * * For the following demonstrated initial
emission limit * * * compliance if * * *
------------------------------------------------------------------------
1. Each existing semi- Reduce uncontrolled Average emissions of
regenerative catalytic emissions of HCl by HCl measured using
reforming unit. 92 percent by Method 26 or 26A,
weight using a as applicable over
control device or the period of the
to a concentration performance test,
of 30 ppmv, (dry are reduced by 92
basis), corrected percent or to a
to 3 percent concentration less
oxygen. than or equal to 30
ppmv (dry basis)
corrected to 3
percent oxygen.
2. Each existing cyclic or Reduce uncontrolled Average emissions of
continuous catalytic emissions of HCl by HCl measured using
reforming unit and each new 97 percent by Method 26 or 26A,
semi-regenerative, cyclic, weight using a as applicable over
or continuous catalytic control device, or the period of the
reforming unit. to a concentration performance test,
of 10 ppmv (dry are reduced by 97
basis), corrected percent or to a
to 3 percent concentration less
oxygen. than or equal to 10
ppmv (dry basis)
corrected to 3
percent oxygen.
------------------------------------------------------------------------
Table 27 to Subpart UUU of Part 63--Continuous Compliance With Inorganic
HAP Emission Limits for Catalytic Reforming Units
[As stated in Sec. 63.1567(c)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You must demonstrate
continuous
compliance during
For * * * For this emission coke burn-off and
limit * * * catalyst
rejuvenation by * *
*
------------------------------------------------------------------------
1. Each existing semi- Reduce uncontrolled Maintaining a 92
regenerative catalytic emissions of HCl by percent HCl
reforming unit. 92 percent by emission reduction
weight using a or an HCl
control device or concentration no
to a concentration more than 30 ppmv
of 30 ppmv (dry (dry basis),
basis), corrected corrected to 3
to 3 percent oxygen. percent oxygen.
2. Each existing cyclic or Reduce uncontrolled Maintaining a 97
continuous catalytic emissions of HCl by percent HCl control
reforming unit. 97 percent by efficiency or an
weight using a HCl concentration
control device, or no more than 10
to a concentration ppmv (dry basis),
of 10 ppmv (dry corrected to 3
basis), corrected percent oxygen.
to 3 percent
oxygen.
3. Each new semi- Reduce uncontrolled Maintaining a 97
regenerative, cyclic, or emissions of HCl by percent HCl control
continuous catalytic 97 percent by efficiency or an
reforming unit. weight using a HCl concentration
control device, or no more than 10
to a concentration ppmv (dry basis),
of 10 ppmv (dry corrected to 3
basis), corrected percent oxygen.
to 3 percent
oxygen.
------------------------------------------------------------------------
[[Page 152]]
Table 28 to Subpart UUU of Part 63--Continuous Compliance With Operating
Limits for Inorganic HAP Emissions From Catalytic Reforming Units
[As stated in Sec. 63.1567(c)(1), you must meet each requirement in the following table that applies to you]
----------------------------------------------------------------------------------------------------------------
You must demonstrate
continuous compliance
For * * * For this operating If you use this type of during coke burn-off
limit * * * control device * * * and catalyst
rejuvenation by * * *
----------------------------------------------------------------------------------------------------------------
1. Each new or existing catalytic a. The daily average pH i. Wet scrubber........ (1) Collecting the
reforming unit. of the water (or hourly and daily
scrubbing and liquid) average pH monitoring
exiting the scrubber data according to Sec.
must not fall below 63.1572; and
the level established maintaining the daily
during the performance average the pH above
test. the operating limit
established during the
performance test.
(2) If you use the
alternative in Sec.
63.1573, measuring and
recording the pH of
the water (or
scrubbing liquid)
exiting the scrubber
every hour according
to Sec. 63.1572;
determining and
recording the daily
average pH; and
maintaining the daily
average pH above the
operating limit
established during the
performance test.
b. The daily average Wet scrubber........... Collecting the hourly
liquid-to-gas ratio average gas flow rate
must not fall below and total water (or
the level established scrubbing liquid) flow
during the performance rate monitoring data;
test. determining and
recording the hourly
average liquid-to-gas
ratio; determining and
recording the daily
average liquid-to-gas
ratio; and maintaining
the daily average
liquid-to-gas ratio
above the limit
established during the
performance test.
c. The HCl Internal scrubbing Measuring and recording
concentration in the system (e.g., no add- the concentration of
catalyst regenerator on control device). HCl every 4 hours
exhaust gas must not using a colormetric
exceed the applicable tube sampling system;
operating limit and maintaining the
established during the HCl concentration
performance test. below the applicable
operating limit.
----------------------------------------------------------------------------------------------------------------
Table 29 to Subpart UUU of Part 63--HAP Emission Limits for Sulfur
Recovery Units
[As stated in Sec. 63.1568(a)(1), you must meet each emission
limitation in the following table that applies to you]
------------------------------------------------------------------------
You must meet this emission
For * * * limit for each process vent * *
*
------------------------------------------------------------------------
1. Each new or existing Claus sulfur a. 250 ppmv (dry basis) of
recovery unit part of a sulfur sulfur dioxide (SO2) at zero
recovery plant of 20 long tons per day percent excess air if you use
or more and subject to the NSPS for an oxidation or reduction
sulfur oxides in 40 CFR 60.104(a)(2). control system followed by
incineration.
b. 300 ppmv of reduced sulfur
compounds calculated as ppmv
SO2 (dry basis) at zero
percent excess air if you use
a reduction control system
without incineration.
2. Each new or existing sulfur recovery a. 250 ppmv (dry basis) of SO2
unit (Claus or other type, regardless at zero percent excess air if
of size) not subject to the NSPS for you use an oxidation or
sulfur oxides in 40 CFR 60.104(a)(2): reduction control system
Option 1 (Elect NSPS). followed by incineration.
b. 300 ppmv of reduced sulfur
compounds calculated as ppmv
SO2 (dry basis) at zero
percent excess air if you use
a reduction control system
without incineration.
[[Page 153]]
3. Each new or existing sulfur recovery 300 ppmv of total reduced
unit (Claus or other type, regardless sulfur (TRS) compounds,
of size) not subject to the NSPS for expressed as an equivalent SO2
sulfur oxides in paragraph (a)(2) of concentration (dry basis) at
40 CFR 60.104: Option 2 (TRS limit). zero percent oxygen.
------------------------------------------------------------------------
Table 30 to Subpart UUU of Part 63--Operating Limits for HAP Emissions
From Sulfur Recovery Units
[As stated in Sec. 63.1568(a)(2), you must meet each operating limit in
the following table that applies to you]
------------------------------------------------------------------------
If use this type of You must meet this
For * * * control device operating limit* * *
------------------------------------------------------------------------
1. Each new or existing Not applicable...... Not applicable.
Claus sulfur recovery unit
part of a sulfur recovery
plant of 20 long tons per
day or more and subject to
the NSPS for sulfur oxides
in 40 CFR 60.104(a)(2).
2. Each new or existing Not applicable...... Not applicable.
sulfur recovery unit (Claus
or other type, regardless
of size) not subject to the
NSPS for sulfur oxides in
40 CFR 60.104(a)(2): Option
1 (Elect NSPS).
3. Each new or existing Thermal incinerator. Maintain the daily
sulfur recovery unit (Claus average combustion
or other type, regardless zone temperature
of size) not subject to the above the limit
NSPS for sulfur oxides in established during
40 CFR 60.104(a)(2): Option the performance
2 (TRS limit). test; and maintain
the daily average
oxygen
concentration in
the vent stream
(percent, dry
basis) above the
limit established
during the
performance test.
------------------------------------------------------------------------
Table 31 to Subpart UUU of Part 63--Continuous Monitoring Systems for
HAP Emissions From Sulfur Recovery Units
[As stated in Sec. 63.1568(b)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You must install and
operate this
For * * * For this limit * * * continuous
monitoring system *
* *
------------------------------------------------------------------------
1. Each new or existing a. 250 ppmv (dry Continuous emission
Claus sulfur recovery unit basis) of SO2 at monitoring system
part to a sulfur recovery zero percent excess to measure and
plant of 20 long tons per air if you use an record the hourly
day and subject to the NSPS oxidation or average
for sulfur oxides in 40 CFR reduction control concentration of
60.104 (1) (2). system followed by SO2 (dry basis) at
incineration. zero percent excess
air for each
exhaust stack. This
system must include
an oxygen monitor
for correcting the
data for excess
air.
b. 300 ppmv of Continuous emission
reduced sulfur monitoring system
compounds to measure and
calculated as ppmv record the hourly
SO2 (dry basis) at average
zero percent excess concentration of
air if you use a reduced sulfur and
reduction control oxygen (O2)
system without emissions.
incineration. Calculate the
reduced sulfur
emissions as SO2
(dry basis) at zero
percent excess air.
Exception: You can
use an instrument
having an air or
SO2 dilution and
oxidation system to
convert the reduced
sulfur to SO2 for
continuously
monitoring and
recording the
concentration (dry
basis) at zero
percent excess air
of the resultant
SO2 instead of the
reduced sulfur
monitor. The
monitor must
include an oxygen
monitor for
correcting the data
for excess oxygen.
2. Option 1: Elect NSPS. a. 250 ppmv (dry Continuous emission
Each new or existing sulfur basis) of SO2 at monitoring system
recovery unit (Claus or zero percent excess to measure and
other type, regardless of air if you use an record the hourly
size) not subject to the oxidation or average
NSPS for sulfur oxides in reduction control concentration of
paragraph (a) (2) of 40 CFR system followed by SO2 (dry basis), at
60.104. incineration. zero percent excess
air for each
exhaust stack. This
system must include
an oxygen monitor
for correcting the
data for excess
air.
[[Page 154]]
b. 300 ppmv of Continuous emission
reduced sulfur monitoring system
compounds to measure and
calculated as ppmv record the hourly
SO2 (dry basis) at average
zero percent excess concentration of
air if you use a reduced sulfur and
reduction control O2 emissions for
system without each exhaust stack.
incineration. Calculate the
reduced sulfur
emissions as SO2
(dry basis), at
zero percent excess
air. Exception: You
can use an
instrument having
an air or O2
dilution and
oxidation system to
convert the reduced
sulfur to SO2 for
continuously
monitoring and
recording the
concentration (dry
basis) at zero
percent excess air
of the resultant
SO2 instead of the
reduced sulfur
monitor. The
monitor must
include an oxygen
monitor for
correcting the data
for excess oxygen.
3. Option 2: TRS limit Each 300 ppmv of total Continuous emission
new or existing sulfur reduced sulfur monitoring system
recovery unit (Claus or (TRS) compounds, to measure and
Other type, regardless or expressed as an record the hourly
size) not subject to the equivalent SO2 average
NSPS for sulfur oxides in concentration (dry concentration of
40 CFR 60.104 (a) (2). basis) at zero TRS for each
percent oxygen. exhaust stack. This
monitor must
include an oxygen
monitor for
correcting the data
for excess oxygen;
or continuous
parameter
monitoring systems
to measure and
record the
combustion zone
temperature of each
thermal incinerator
and the oxygen
content (percent,
dry basis) in the
vent stream of the
incinerator.
------------------------------------------------------------------------
Table 32 to Subpart UUU of Part 63--Requirements for Performance Tests
for HAP Emissions From Sulfur Recovery Units Not Subject to the New
Source Performance Standards for Sulfur Oxides
[As stated in Sec. 63.1568(b)(2) and (3), you must meet each requirement in the following table that applies to
you]
----------------------------------------------------------------------------------------------------------------
According to these
For * * * You must * * * Using * * * requirements * * *
----------------------------------------------------------------------------------------------------------------
1. Each new and existing sulfur Measure SO2 Data from continuous Collect SO2 monitoring
recovery unit: Option 1 (Elect concentration (for an emission monitoring data every 15 minutes
NSPS). oxidation or reduction system. for 24 consecutive
system followed by operating hours.
incineration) or the Reduce the data to 1-
concentration of hour averages computed
reduced sulfur (or SO2 from four or more data
if you use an points equally spaced
instrument to convert over each 1-hour
the reduced sulfur to period.
SO2) for a reduction
control system without
incineration.
2. Each new and existing sulfur a. Select sampling Method 1 or 1A appendix Sampling sites must be
recovery unit: Option 2 (TRS limit). port's location and A to part 60 of this located at the outlet
the number of traverse chapter. of the control device
ports. and prior to any
releases to the
atmosphere.
b. Determine velocity Method 2, 2A, 2C, 2D,
and volumetric flow 2F, or 2G in appendix
rate. A to part 60 of this
chapter, as
applicable.
c. Conduct gas Method 3, 3A, or 3B in Take the samples
molecular weight appendix A to part 60 simultaneously with
analysis; obtain the of this chapter, as reduced sulfur or
oxygen concentration applicable. moisture samples.
needed to correct the
emission rate for
excess air.
d. Measure moisture Method 4 in appendix A Make your sampling time
content of the stack to part 60 of this for each Method 4
gas. chapter. sample equal to that
for 4 Method 15
samples.
[[Page 155]]
e. Measure the Method 15 or 15A in If the cross-sectional
concentration of TRS. appendix A to part 60 area of the duct is
of this chapter, as less than 5 square
applicable. meters (m2) or 54
square feet, you must
use the centroid of
the cross section as
the sampling point. If
the cross-sectional
area is 5 m2 or more
and the centroid is
more than 1 meter (m)
from the wall, your
sampling point may be
at a point no closer
to the walls than 1 m
or 39 inches. Your
sampling rate must be
at least 3 liters per
minute or 0.10 cubic
feet per minute to
ensure minimum
residence time for the
sample inside the
sample lines.
f. Calculate the SO2 The arithmetic average
equivalent for each of the SO2 equivalent
run after correcting for each sample during
for moisture and the run.
oxygen.
g. Correct the reduced Equation 1 of Sec.
sulfur samples to zero 63.1568.
percent excess air.sa
h. Establish each Data from the
operating limit in continuous parameter
Table 30 of this monitoring system.
subpart that applies
to you.
i. Measure thermal Data from the Collect temperature
incinerator: continuous parameter monitoring data every
combustion zone monitoring system. 15 minutes during the
temperature. entire period of the
performance test; and
determine and record
the minimum hourly
average temperature
from all the readings.
j. Measure thermal Data from the Collect oxygen
incinerator: oxygen continuous parameter concentration
concentration monitoring system. (percent, dry basis)
(percent, dry basis) data every 15 minutes
in the vent stream. during the entire
period of the
performance test; and
determine and record
the minimum hourly
average percent excess
oxygen concentration.
k. If you use a Data from continuous Collect TRS data every
continuous emission emission monitoring 15 minutes for 24
monitoring system, system. consecutive operating
measure TRS hours. Reduce the data
concentration. to 1-hour averages
computed from four or
more data points
equally spaced over
each 1-hour period.
----------------------------------------------------------------------------------------------------------------
[[Page 156]]
Table 33 to Subpart UUU of Part 63--Initial Compliance With HAP Emission
Limits for Sulfur Recovery Units
[As stated in Sec. 63.1568(b)(5), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You have
For * * * For the following demonstrated initial
emission limit * * * compliance if * * *
------------------------------------------------------------------------
1. Each new or existing a. 250 ppmv (dry You have already
Clause sulfur recovery unit basis) SO2 at zero conducted a
part of a sulfur recovery percent excess air performance test to
plant of 20 long tons per if you use an demonstrate initial
day and subject to the NSPS oxidation or compliance with the
for sulfur oxides in 40 CFR reduction control NSPS and the hourly
60.104(a)(2). system followed by average SO2
incineration. emissions measured
by the continuous
emission monitoring
system are less
than or equal to
250 ppmv (dry
basis) at zero
percent excess air.
As part of the
Notification of
Compliance Status,
you must certify
that your vent
meets the SO2
limit. You are not
required to do
another performance
test to demonstrate
initial compliance.
You have already
conducted a
performance
evaluation to
demonstrate initial
compliance with the
applicable
performance
specification. As
part of your
Notification of
Compliance Status,
you must certify
that your
continuous emission
monitoring system
meets the
applicable
requirements in
Sec. 63.1572. You
are not required to
do another
performance
evaluation to
demonstrate initial
compliance.
b. 300 ppmv of You have already
reduced sulfur conducted a
compounds performance test to
calculated as ppmv demonstrate initial
SO2 (dry basis) at compliance with the
zero percent excess NSPS and the hourly
air if you use a average SO2
reduction control emissions measured
system without by your continuous
incineration. emission monitoring
system are less
than or equal to
250 ppmv (dry
basis) at zero
percent excess air.
As part of the
Notification of
Compliance Status,
you must certify
that your vent
meets the SO2
limit. You are not
required to do
another performance
test do demonstrate
initial compliance.
You have already
conducted a
performance
evaluation to
demonstrate initial
compliance with the
applicable
performance
specification. As
part of your
Notification of
Compliance Status,
you must certify
that your
continuous emission
monitoring system
meets the
applicable
requirements in
Sec. 63.1572. You
are not required to
do another
performance
evaluation to
demonstrate initial
compliance.
2. Option 1: Elect NSPS. a. 250 ppmv (dry The hourly average
Each new or existing sulfur basis) of SO2 at SO2 emissions
recovery unit (Claus or zero percent excess measured by the
other type, regardless of air if you use an continuous emission
size) not subject to the oxidation control monitoring system
NSPS for sulfur oxides in system followed by over the 24-hour
40 CFR 60.104(a)(2). incineration. period of the
initial performance
test are not more
than 250 ppvm (dry
basis) at zero
percent excess air;
and your
performance
evaluation shows
the monitoring
system meets the
applicable
requirements in
Sec. 63.1572.
b. 300 ppmv of The hourly average
reduced sulfur reduced sulfur
compounds emissions measured
calculated as ppmv by the continuous
SO2 (dry basis) at emission monitoring
zero percent excess system over the 24-
air if you use a hour period of the
reduction control performance test no
system without more than 300 ppmv,
incineration. calculated as ppmv
SO2 (dry basis) at
zero percent excess
air; and your
performance
evaluation shows
the continuous
emission monitoring
system meets the
applicable
requirements in
Sec. 63.1572.
[[Page 157]]
3. Option 2: TRS limit. Each 300 ppmv of TRS If you do not use a
new or existing sulfur compounds expressed continuous emission
recovery unit (Claus or as an equivalent monitoring system,
other type, regardless of SO2 concentration the average TRS
size) not subject to the (dry basis) at zero emissions measured
NSPS for sulfur oxides in percent oxygen. using Method 15
40 CFR 60.104(a)(2). over the period of
the initial
performance test
are less than or
equal to 300 ppmv
expressed as
equivalent SO2
concentration (dry
basis) at zero
percent oxygen. If
you use a
continuous emission
monitoring system
the hourly average
TRS emissions
measured by the
continuous emission
monitoring system
over the 24-hour
period of the
performance test
are no more than
300 ppmv expressed
as an equivalent
SO2 concentration
(dry basis) at zero
percent oxygen; and
your performance
evaluation shows
the continuous
emission monitoring
system meets the
applicable
requirements in
Sec. 63.1572.
------------------------------------------------------------------------
Table 34 to Subpart UUU of Part 63--Continuous Compliance With HAP
Emission Limits for Sulfur Recovery Units
[As stated in Sec. 63.1568(c)(1), you must meet each requirement in the
following table that applies to you.]
------------------------------------------------------------------------
You must demonstrate
For * * * For this emission continuous
limit * * * compliance by * * *
------------------------------------------------------------------------
1. Each new or existing a. 250 ppmv (dry Collecting the
Claus sulfur recovery unit basis) SO2 at zero hourly average SO2
part of a sulfur recovery percent excess air monitoring data
plant of 20 long tons per if you use an (dry basis, percent
or more and subject to the oxidation or excess air)
NSPS for sulfur oxides in reduction control according to Sec.
40 CFR 60.104(a)(2). system followed by 63.1572;
incineration. maintaining the
hourly average SO2
concentration at or
below the
applicable limit;
determining and
recording each 12-
hour average SO2
day concentration;
and reporting any
12-hour average SO2
concentration
greater than the
applicable emission
limitation in the
compliance report
required in Sec.
63.1575.
b. 300 ppmv of Collecting the
reduced sulfur hourly average
compounds reduced sulfur and
calculated as ppmv O2 data according
(dry basis) SO2 at to Sec. 63.1572;
zero percent excess and maintaining the
air if you use a hourly average
reduction control concentration of
system without reduced sulfur at
incineration. or below the
applicable limit;
and determining and
recording each 12-
hour average
concentration of
reduced sulfur; and
reporting any 12-
hour average
concentration of
reduced sulfur
greater than the
applicable emission
limitation in the
compliance report
required in Sec.
63.1575.
2. Option 1: Elect NSPS Each a. 250 ppmv (dry Collecting the
new or existing sulfur basis) of SO2 at hourly average SO2
recovery unit (Claus or zero percent excess monitoring data
other type, regardless of air (for oxidation (dry basis, percent
size) not subject to the or reduction system excess air)
NSPS for sulfur oxides in followed by according to Sec.
40 CFR 60.104(a)(2). incineration). 63.1572;
maintaining the
hourly average SO2
concentration at or
below the
applicable limit;
determining and
recording each 12-
hour average SO2
concentration; and
reporting any 12-
hour average SO2
concentration
greater than the
applicable emission
limitation in the
compliance report
required in Sec.
63.1575.
[[Page 158]]
b. 300 ppmv of Collecting the
reduced sulfur hourly average
compounds reduced sulfur (and
calculated as ppmv air or O2 dilution
SO2 (dry basis) at and oxidation data)
zero percent excess according to Sec.
air (for reduction 63.1572;
control system maintaining the
without hourly average SO2
incineration). concentration at or
below the
applicable limit;
reducing the
monitoring data to
12-hour averages;
and reporting any
12-hour average SO2
concentration
greater than the
applicable limit in
the compliance
report required by
Sec. 63.1575.
3. Option 2: TRS limit Each 300 ppmv of TRS Collecting the
new or existing sulfur compounds, hourly average TRS
recovery unit (Claus or expressed as an SO2 monitoring data
other type, regardless of concentration (dry according to Sec.
size) not subject to the basis) at zero 63.1572, if you use
NSPS for sulfur oxides in percent oxygen or a continuous
40 CFR 60.104(a)(2). reduced sulfur emission monitoring
compounds system; maintaining
calculated as ppmv the hourly average
SO2 (dry basis) at concentration of
zero percent excess TRS at or below the
air. applicable limit;
reducing the TRS
monitoring data to
12-hour averages;
reporting any 12-
hour average TRS
greater than the
applicable limit in
the compliance
report required by
Sec. 63.1575; and
maintaining the
hourly average
concentration of
TRS below the
applicable limit if
you use continuous
parameter
monitoring systems.
------------------------------------------------------------------------
Table 35 to Subpart UUU of Part 63--Continuous Compliance With Operating
Limits for HAP Emissions From Sulfur Recovery Units
[As stated in Sec. 63.1568(c)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You must demonstrate
For * * * For this operating continuous
limit * * * compliance by * * *
------------------------------------------------------------------------
1. Each new or existing Not applicable...... Meeting the
Claus sulfur recovery unit requirements of
part of a sulfur recovery Table 34 of this
plant of 20 long tons per subpart.
day or more and subject to
the NSPS for sulfur oxides
in paragraph 40 CFR
60.104(a)(2).
2. Option 1: Elect NSPS Each Not applicable...... Meeting the
new or existing sulfur requirements of
recovery unit (Claus or Table 34 of this
other type, regardless of subpart.
size) not subject to the
NSPS for sulfur oxides in
40 CFR 60.104(a)(2).
3. Option 2: TRS limit Each a. Maintain the Collecting the
new or existing sulfur daily average hourly and daily
recovery unit (Claus or combustion zone average temperature
other type, regardless of temperature above monitoring data
size) not subject to the the level according to Sec.
NSPS for sulfur oxides in established during 63.1572; and
40 CFR 60.104(a)(2) the performance maintaining the
test. daily average
combustion zone
temperature at or
above the limit
established during
the performance
test.
b. The daily average Collecting the
oxygen hourly and daily
concentration in average O2
the vent stream monitoring data
(percent, dry according to Sec.
basis) must not 63.1572; and
fall below the maintaining the
level established average O2
during the concentration above
performance test. the level
established during
the performance
test.
------------------------------------------------------------------------
Table 36 to Subpart UUU of Part 63--Work Practice Standards for HAP
Emissions From Bypass Lines
[As stated in Sec. 63.1569(a)(1), you must meet each work practice
standard in the following table that applies to you]
------------------------------------------------------------------------
You must meet one of these equipment
Option standards * * *
------------------------------------------------------------------------
1. Option 1..................... Install and operate a device
(including a flow indicator, level
recorder, or electronic valve
position monitor) to continuously
detect, at least every hour, whether
flow is present in the bypass line.
Install the device at or as near as
practical to the entrance to any
bypass line that could divert the
vent stream away from the control
device to the atmosphere.
[[Page 159]]
2. Option 2..................... Install a car-seal or lock-and-key
device placed on the mechanism by
which the bypass device flow position
is controlled (e.g., valve handle,
damper level) when the bypass device
is in the closed position such that
the bypass line valve cannot be
opened without breaking the seal or
removing the device.
3. Option 3..................... Seal the bypass line by installing a
solid blind between piping flanges.
4. Option 4..................... Vent the bypass line to a control
device that meets the appropriate
requirements in this subpart.
------------------------------------------------------------------------
Table 37 to Subpart UUU of Part 63--Requirements for Performance Tests
for Bypass Lines
[As stated in Sec. 63.1569(b)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
For this standard . . . You must . . .
------------------------------------------------------------------------
1. Option 1: Install and operate a flow Record during the performance
indicator, level recorder, or test for each type of control
electronic valve position monitor. device whether the flow
indicator, level recorder, or
electronic valve position
monitor was operating and
whether flow was detected at
any time during each hour of
level the three runs
comprising the performance
test.
------------------------------------------------------------------------
Table 38 to Subpart UUU of Part 63--Initial Compliance With Work
Practice Standards for HAP Emissions from Bypass Lines
[As stated in Sec. 63.1569(b)(2), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
For this work You have
For * * * practice standard * demonstrated initial
* * compliance if * * *
------------------------------------------------------------------------
1. Each new or existing a. Option 1: Install The installed
bypass line associated with and operate a equipment operates
a catalytic cracking unit, device (including a properly during
catalylic reforming unit, flow indicator, each run of the
or sulfur recovery unit. level recorder, or performance test
electronic valve and no flow is
position monitor) present in the line
to continuously during the test.
detect, at least
every hour, whether
flow is present in
the bypass line.
Install the device
at or as near as
practical to the
entrance to any
bypass line that
could divert the
vent stream away
from the control
device to the
atmosphere.
b. Option 2: Install As part of the
a car-seal or lock- notification of
and-key device compliance status,
placed on the you certify that
mechanism by which you installed the
the bypass device equipment, the
flow position is equipment was
controlled (e.g., operational by your
valve handle, compliance date,
damper level) when and you identify
the bypass device what equipment was
is in the closed installed.
position such that
the bypass line
valve cannot be
opened without
breaking the seal
or removing the
device.
c. Option 3: Seal See item 1.b. of
the bypass line by this table.
installing a solid
blind between
piping flanges.
d. Option 4: Vent See item 1.b. of
the bypass line to this table.
a control device
that meets the
appropriate
requirements in
this subpart.
------------------------------------------------------------------------
Table 39 to Subpart UUU of Part 63--Continuous Compliance With Work
Practice Standards for HAP Emissions From Bypass Lines
[As stated in Sec. 63.1569(c)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You must demonstrate continuous
If you elect this standard * * * compliance by * * *
------------------------------------------------------------------------
1. Option 1: Flow indicator, level Continuously monitoring and
recorder, or electronic valve position recording whether flow is
monitor. present in the bypass line;
visually inspecting the device
at least once every hour if
the device is not equipped
with a recording system that
provides a continuous record;
and recording whether the
device is operating properly
and whether flow is present in
the bypass line.
2. Option 2: Car-seal or lock-and-key Visually inspecting the seal or
device. closure mechanism at least
once every month; and
recording whether the bypass
line valve is maintained in
the closed position and
whether flow is present in the
line.
[[Page 160]]
3. Option 3: Solid blind flange........ Visually inspecting the blind
at least once a month; and
recording whether the blind is
maintained in the correct
position such that the vent
stream cannot be diverted
through the bypass line.
4. Option 4: Vent to control device.... Monitoring the control device
according to appropriate
subpart requirements.
5. Option 1, 2, 3, or 4................ Recording and reporting the
time and duration of any
bypass.
------------------------------------------------------------------------
Table 40 to Subpart UUU of Part 63--Requirements for Installation,
Operation, and Maintenance of Continuous Opacity Monitoring Systems and
Continuous Emission Monitoring Systems
[As stated in Sec. 63.1572(a)(1) and (b)(1), you must meet each
requirement in the following table that applies to you]
------------------------------------------------------------------------
This type of continuous opacity or Must meet these requirements *
emission monitoring system * * * * *
------------------------------------------------------------------------
1. Continuous opacity monitoring system Performance specification 1 (40
CFR part 60, appendix B).
2. CO continuous emission monitoring Performance specification 4 (40
system. CFR part 60, appendix B); span
value of 1,000 ppm; and
procedure 1 (40 CFR part 60,
appendix F) except relative
accuracy test audits are
required annually instead of
quarterly.
3. CO continuous emission monitoring Performance specification 4 (40
system used to demonstrate emissions CFR part 60, appendix B); and
average under 50 ppm (dry basis). span value of 100 ppm.
4. SO2 continuous emission monitoring Performance specification 2 (40
for sulfur recovery unit with CFR part 60, appendix B); span
oxidation control system or reduction values of 500 ppm SO2 and 10
control system; this monitor must percent O2; use Methods 6 or
include an O2 monitor for correcting 6C and 3A or 3B (40 CFR part
the data for excess air. 60, appendix A) for certifying
O2 monitor; and procedure 1
(40 CFR part 60, appendix F)
except relative accuracy test
audits are required annually
instead of quarterly.
5. Reduced sulfur and O2 continuous Performance specification 5 (40
emission monitoring system for sulfur CFR part 60, appendix B),
recovery unit with reduction control except calibration drift
system not followed by incineration; specification is 2.5 percent
this monitor must include an O2 of the span value instead of 5
monitor for correcting the data for percent; 450 ppm reduced
excess air unless exempted. sulfur and 10 percent O2; use
Methods 15 or 15A and 3A or 3B
(40 CFR part 60, appendix A)
for certifying O2 monitor; if
Method 3A or 3B yields O2
concentrations below 0.25
percent during the performance
evaluation, the O2
concentration can be assumed
to be zero and the O2 monitor
is not required; and procedure
1 (40 CFR part 60, appendix
F), except relative accuracy
test audits, are required
annually instead of quarterly.
6. Instrument with an air or O2 Performance specification 5 (40
dilution and oxidation system to CFR part 60, appendix B); span
convert reduced sulfur to SO2 for value of 375 ppm SO2 and 10
continuously monitoring the percent O2; use Methods 15 or
concentration of SO2 instead of 15A and 3A or 3B for
reduced sulfur monitor and O2 monitor. certifying O2 monitor; and
procedure 1 (40 CFR part 60,
appendix F), except relative
accuracy test audits, are
required annually instead of
quarterly.
7. TRS continuous emission monitoring Performance specification 5 (40
system for sulfur recovery unit; this CFR part 60, appendix B).
monitor must include an O2 monitor for
correcting the data for excess air.
8. O2 monitor for oxygen concentration. If necessary due to
interferences, locate the
oxygen sensor prior to the
introduction of any outside
gas stream; performance
specification 3 (40 CFR part
60, appendix B; span value for
O2 sensor is 10 percent; and
procedure 1 (40 CFR part 60,
appendix F), except relative
accuracy test audits, are
required annually instead of
quarterly.
------------------------------------------------------------------------
Table 41 to Subpart UUU of Part 63--Requirements for Installation,
Operation, and Maintenance of Continuous Parameter Monitoring Systems
[As stated in Sec. 63.1572(c)(1), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
If you use a continuous
parameter monitoring system You must * * *
to measure and record * * *
------------------------------------------------------------------------
1. Voltage and secondary At least monthly, inspect all components
current or total power of the continuous parameter monitoring
input. system for integrity and all electrical
connections for continuity; and record
the results of each inspection.
[[Page 161]]
2. Pressure drop 1........... Locate the pressure sensor(s) in a
position that provides a representative
measurement of the pressure; minimize or
eliminate pulsating pressure, vibration,
and internal and external corrosion; use
a gauge with an accuracy [plusmn] 2
percent over the operating range; check
pressure tap for plugs at least once a
week; using a manometer, check gauge
calibration quarterly and transducer
calibration monthly; for a semi-
regenerative catalytic reforming unit,
you can check the calibration quarterly
and monthly or prior to regeneration,
whichever is longer; record the results
of each calibration; conduct calibration
checks any time the sensor exceeds the
manufacturer's specified maximum
operating pressure range, or install a
new pressure sensor; at least monthly,
inspect all components for integrity,
all electrical connections for
continuity, and all mechanical
connections for leakage; and record the
results of each inspection.
3. Air flow rate, gas flow Locate the flow sensor(s) and other
rate, or total water (or necessary equipment such as
scrubbing liquid) flow rate. straightening vanes in a position that
provides representative flow; use a flow
rate sensor with an accuracy within
[plusmn]5 percent; reduce swirling flow
or abnormal velocity distributions due
to upstream and downstream disturbances;
conduct a flow sensor calibration check
at least semiannually;
for a semi-regenerative catalytic
reforming unit, you can check the
calibration at least semiannually or
prior to regeneration, whichever is
longer; record the results of each
calibration; if you elect to comply with
Option 3 (Ni lb/hr) or Option 4 (Ni lb/
1,000 lbs of coke burn-off) for the HAP
metal emission limitations in Sec.
63.1564, install the continuous
parameter monitoring system for gas flow
rate as close as practical to the
continuous opacity monitoring system;
and if you don't use a continuous
opacity monitoring system, install the
continuous parameter monitoring system
for gas flow rate as close as practical
to the control device.
4. Combustion zone Install the temperature sensor in the
temperature. combustion zone or in the ductwork
immediately downstream of the combustion
zone before any substantial heat
exchange occurs; locate the temperature
sensor in a position that provides a
representative temperature;
use a temperature sensor with an accuracy
of [plusmn]1 percent of the temperature
being measured, expressed in degrees
Celsius (C) or [plusmn]0.5 degrees C,
whichever is greater; shield the
temperature sensor system from
electromagnetic interference and
chemical contaminants; if you use a
chart recorder, it must have a
sensitivity in the minor division of at
least 20 degrees Fahrenheit; perform an
electronic calibration at least
semiannually according to the procedures
in the manufacturer's owners manual;
following the electronic calibration,
conduct a temperature sensor validation
check, in which a second or redundant
temperature sensor placed nearby the
process temperature sensor must yield a
reading within 16.7 degrees C of the
process temperature sensor's reading;
record the results of each calibration
and validation check; conduct
calibration and validation checks any
time the sensor exceeds the
manufacturer's specified maximum
operating temperature range, or install
a new temperature sensor; and at least
monthly, inspect all components for
integrity and all electrical connections
for continuity, oxidation, and galvanic
corrosion.
5. pH........................ Locate the pH sensor in a position that
provides a representative measurement of
pH; ensure the sample is properly mixed
and representative of the fluid to be
measured; check the pH meter's
calibration on at least two points every
8 hours of process operation;
at least monthly, inspect all components
for integrity and all electrical
components for continuity; record the
results of each inspection; and if you
use pH strips to measure the pH of the
water exiting a wet scrubber as an
alternative to a continuous parameter
monitoring system, you must use pH
strips with an accuracy of [plusmn]10
percent.
6. HCl concentration......... Use a colormetric tube sampling system
with a printed numerical scale in ppmv,
a standard measurement range of 1 to 10
ppmv (or 1 to 30 ppmv if applicable),
and a standard deviation for measured
values of no more than [plusmn]15
percent. System must include a gas
detection pump and hot air probe if
needed for the measurement range.
------------------------------------------------------------------------
1 Not applicable to non-venturi wet scrubbers of the jet-ejector design.
[[Page 162]]
Table 42 to Subpart UUU of Part 63--Additional Information for Initial
Notification of Compliance Status
[As stated in Sec. 63.1574(d), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
You must provide this additional
For * * * information * * *
------------------------------------------------------------------------
1. Identification of affected Nature, size, design, method of
sources and emission points. operation, operating design capacity of
each affected source; identify each
emission point for each HAP; identify
any affected source or vent associated
with an affected source not subject to
the requirements of subpart UUU.
2. Initial compliance........ Identification of each emission
limitation you will meet for each
affected source, including any option
you select (i.e., NSPS, PM or Ni, flare,
percent reduction, concentration,
options for bypass lines); if
applicable, certification that you have
already conducted a performance test to
demonstrate initial compliance with the
NSPS for an affected source;
certification that the vents meet the
applicable emission limit and the
continuous opacity or that the emission
monitoring system meets the applicable
performance specification; if
applicable, certification that you have
installed and verified the operational
status of equipment by your compliance
date for each bypass line that meets the
requirements of Option 2, 3, or 4 in
Sec. 63.1569 and what equipment you
installed; identification of the
operating limit for each affected
source, including supporting
documentation; if your affected source
is subject to the NSPS, certification of
compliance with NSPS emission
limitations and performance
specifications; a brief description of
performance test conditions (capacity,
feed quality, catalyst, etc.); an
engineering assessment (if applicable);
and if applicable, the flare design
(e.g., steam-assisted, air-assisted, or
non-assisted), all visible emission
readings, heat content determinations,
flow rate measurements, and exit
velocity determinations made during the
Method 22 test.
3. Continuous compliance..... Each monitoring option you elect; and
identification of any unit or vent for
which monitoring is not required; and
the definition of ``operating day.''
(This definition, subject to approval by
the applicable permitting authority,
must specify the times at which a 24-hr
operating day begins and ends.)
------------------------------------------------------------------------
Table 43 to Subpart UUU of Part 63--Requirements for Reports
[As stated in Sec. 63.1575(a), you must meet each requirement in the
following table that applies to you]
------------------------------------------------------------------------
The report must You must submit
You must submit a(n) * * * contain * * * the report * * *
------------------------------------------------------------------------
1. Compliance report.......... If there are not Semiannually
deviations from any according to
emission limitation the
or work practice requirements in
standard that applies Sec. 63.1575(b
to you, a statement ).
that there were no
deviations from the
standards during the
reporting period and
that no continuous
opacity monitoring
system or continuous
emission monitoring
system was
inoperative,
inactive, out-of-
control, repaired, or
adjusted;
and if you have a
deviation from any
emission limitation
or work practice
standard during the
reporting period, the
report must contain
the information in
Sec. 63.1575(d) or
(e)
------------------------------------------------------------------------
Table 44 to Subpart UUU of Part 63--Applicability of NESHAP General
Provisions to Subpart UUU
[As stated in Sec. 63.1577, you must meet each requirement in the following table that applies to you]
----------------------------------------------------------------------------------------------------------------
Citation Subject Applies to subpart UUU Explanation
----------------------------------------------------------------------------------------------------------------
Sec. 63.1........................... Applicability.......... Yes. Except that subpart UUU
specifies calendar or
operating day.
Sec. 63.2........................... Definitions............ Yes.
Sec. 63.3........................... Units and Abbreviations Yes.
Sec. 63.4........................... Prohibited Activities.. Yes.
Sec. 63.5(a)-(c).................... Construction and Yes.................... In Sec. 63.5(b)(4),
Reconstruction. replace the reference
to Sec. 63.9 with
Sec. 63.9(b)(4) and
(5).
Sec. 63.5(d)(1)(i).................. Application for Yes.................... Except, subpart UUU
Approval of specifies the
Construction or application is
Reconstruction-- submitted as soon as
General Application practicable before
Requirements. startup but no later
than 90 days (rather
than 60) after the
promulgation date
where construction or
reconstruction had
commenced and initial
startup had not
occurred before
promulgation.
Sec. 63.5(d)(1)(ii)................. ....................... Yes.................... Except that emission
estimates specified in
Sec. 63.5(d)(1)(ii)(H
) are not required.
[[Page 163]]
Sec. 63.5(d)(1)(iii)................ ....................... No..................... Subpart UUU specifies
submission of
notification of
compliance status.
Sec. 63.5(d)(2)..................... ....................... No.
Sec. 63.5(d)(3)..................... ....................... Yes.................... Except that Sec.
63.5(d)(3)(ii) does
not apply.
Sec. 63.5(d)(4)..................... ....................... Yes.
Sec. 63.5(e)........................ Approval of
Construction or
Reconstruction.
Sec. 63.5(f)(1)..................... Approval of Yes....................
Construction or
Reconstruction Based
on State Review.
Sec. 63.5(f)(2)..................... ....................... Yes.................... Except that 60 days is
changed to 90 days and
cross-reference to
Sec. 63.9(b)(2) does
not apply.
Sec. 63.6(a)........................ Compliance with Yes....................
Standards and
Maintenance--
Applicability.
Sec. 63.6(b)(1)-(4)................. Compliance Dates for Yes....................
New and Reconstructed
Sources.
Sec. 63.6(b)(5)..................... ....................... Yes.................... Except that subpart UUU
specifies different
compliance dates for
sources.
Sec. 63.6(b)(6)..................... [Reserved]............. Not applicable.........
Sec. 63.6(b)(7)..................... Compliance Dates for Yes....................
New and Reconstructed
Area Sources That
Become Major.
Sec. 63.6(c)(1)-(2)................. Compliance Dates for Yes.................... Except that for subpart
Existing Sources. UUU specifies
different compliance
dates for sources
subject to Tier II
gasoline sulfur
control requirements.
Sec. 63.6(c)(3)-(4)................. [Reserved]............. Not applicable.........
Sec. 63.6(c)(5)..................... Compliance Dates for Yes....................
Existing Area Sources
That Become Major.
Sec. 63.6(d)........................ [Reserved]............. Not applicable.........
Sec. 63.6(e)(1)-(2)................. Operation and Yes....................
Maintenance
Requirements.
Sec. 63.6(e)(3)(i)-(iii)............ Startup, Shutdown, and Yes....................
Malfunction Plan.
Sec. 63.6(e)(3)(iv)................. ....................... Yes.................... Except that reports of
actions not consistent
with plan are not
required within 2 and
7 days of action but
rather must be
included in next
periodic report.
Sec. 63.6(e)(3)(v)-(viii)........... ....................... Yes.................... The owner or operator
is only required to
keep the latest
version of the plan.
Sec. 63.6(f)(1)-(2)(iii)(C)......... Compliance with Yes....................
Emission Standards.
Sec. 63.6(f)(2)-(iii)(D)............ ....................... No.....................
Sec. 63.6(f)(2)(iv)-(v)............. ....................... Yes....................
Sec. 63.6(f)(3)..................... ....................... Yes....................
Sec. 63.6(g)........................ Alternative Standard... Yes....................
Sec. 63.6(h)........................ Opacity/VE Standards... Yes....................
Sec. 63.6(h)(2)(i).................. Determining Compliance No..................... Subpart UUU specifies
with Opacity/VE methods.
Standards.
Sec. 63.6(h)(2)(ii)................. [Reserved]............. Not applicable.........
Sec. 63.6(h)(2)(iii)................ ....................... Yes....................
Sec. 63.6(h)(3)..................... [Reserved]............. Not applicable.........
Sec. 63.6(h)(4)..................... Notification of Opacity/ Yes.................... Applies to Method 22
VE Observation Date. tests.
Sec. 63.6(h)(5)..................... Conducting Opacity/VE No.....................
Observations.
Sec. 63.6(h)(6)..................... Records of Conditions Yes.................... Applies to Method 22
During Opacity/VE observations.
Observations.
Sec. 63.6(h)(7)(i).................. Report COM Monitoring Yes....................
Data from Performance
Test.
Sec. 63.6(h)(7)(ii)................. Using COM Instead of No.....................
Method 9.
Sec. 63.6(h)(7)(iii)................ Averaging Time for COM Yes....................
during Performance
Test.
Sec. 63.6(h)(7)(iv)................. COM Requirements....... Yes....................
Sec. 63.6(h)(8)..................... Determining Compliance Yes....................
with Opacity/VE
Standards.
Sec. 63.6(h)(9)..................... Adjusted Opacity Yes....................
Standard.
[[Page 164]]
Sec. 63.6(i)(1)-(14)................ Extension of Compliance Yes.................... Not applicable to an
affected source with
Tier II compliance
date. May be
applicable to an
affected source exempt
from Tier II rule.
Sec. 63.6(i)(15).................... [Reserved]............. Not applicable.........
Sec. 63.6(i)(16).................... ....................... Yes....................
----------------------------------------------------------------------------------------------------------------
Subpart VVV--National Emission Standards for Hazardous Air Pollutants:
Publicly Owned Treatment Works
Source: 64 FR 57579, Oct. 26, 1999, unless otherwise noted.
Applicability
Sec. 63.1580 Am I subject to this subpart?
(a) You are subject to this subpart if the following are all true:
(1) You own or operate a publicly owned treatment works (POTW) that
includes an affected source (Sec. 63.1595);
(2) The affected source is located at a POTW which is a major source
of HAP emissions, or at any industrial POTW regardless of whether or not
it is a major source of HAP; and
(3) Your POTW is required to develop and implement a pretreatment
program as defined by 40 CFR 403.8 (for a POTW owned or operated by a
municipality, State, or intermunicipal or interstate agency), or your
POTW would meet the general criteria for development and implementation
of a pretreatment program (for a POTW owned or operated by a department,
agency, or instrumentality of the Federal government).
(b) If your existing POTW treatment plant is not located at a major
source as of October 26, 1999, but thereafter becomes a major source for
any reason other than reconstruction, then, for the purpose of this
subpart, your POTW treatment plant would be considered an existing
source. Note to Paragraph (b): See Sec. 63.2 of the national emission
standards for hazardous air pollutants (NESHAP) General Provisions in
subpart A of this part for the definitions of major source and area
source.
(c) If you reconstruct your POTW treatment plant, then the
requirements for a new or reconstructed POTW treatment plant, as defined
in Sec. 63.1595, apply.
[67 FR 64745, Oct. 21, 2002]
Sec. 63.1581 Does the subpart distinguish between different types of POTW treatment plants?
Yes, POTW treatment plants are divided into two subcategories. A
POTW treatment plant which does not meet the characteristics of an
industrial POTW treatment plant belongs in the non-industrial POTW
treatment plant subcategory as defined in Sec. 63.1595.
Industrial POTW Treatment Plant Description and Requirements
Sec. 63.1582 What are the characteristics of an industrial POTW treatment plant?
(a) Your POTW is an industrial POTW treatment plant if an industrial
discharger complies with its NESHAP by using the treatment and controls
located at your POTW. Your POTW accepts the regulated waste stream and
provides treatment and controls as an agent for the industrial
discharger. Industrial POTW treatment plant is defined in Sec. 63.1595.
(b) If, in the future, an industrial discharger begins complying
with its NESHAP by using the treatment and controls at your POTW, then
on the date that the industrial discharger certifies compliance, your
POTW treatment plant will be considered an industrial POTW treatment
plant.
(c) If your POTW treatment plant accepts one or more specific
regulated industrial waste streams as part of compliance with one or
more other NESHAP, then you are subject to all the requirements of each
appropriate
[[Page 165]]
NESHAP for each waste stream, as described in the following section. In
the case of overlapping NESHAP requirements, the more stringent of the
requirements will apply.
Sec. 63.1583 What are the emission points and control requirements for an industrial POTW treatment plant?
(a) The emission points and control requirements for an existing
industrial POTW treatment plant are specified in the appropriate
NESHAP(s) for the industrial user(s) (see Sec. 63.1582). For example, an
existing industrial POTW treatment plant that provides treatment for a
facility subject to subpart FF of this part, the National Emission
Standard for Benzene Waste Operations, must meet the treatment and
control requirements specified in Sec. 61.348(d)(4) of this chapter.
(b) The emission points and control requirements for a new or
reconstructed industrial POTW treatment plant are either those specified
by the particular NESHAP(s) which apply to the industrial user(s) who
discharge their waste for treatment to the POTW, or those emission
points and control requirements set forth in Sec. 63.1586. The set of
control requirements which applies to a particular new or reconstructed
POTW is that set which requires the most stringent overall control of
HAP emissions. If you are uncertain which set of requirements is more
stringent, this determination should be made in consultation with the
permitting authority. Reconstruction is defined in Sec. 63.1595.
Sec. 63.1584 When do I have to comply?
(a) Existing industrial POTW treatment plant. If you have an
existing industrial POTW treatment plant, the appropriate NESHAP(s) for
the industrial user(s) sets the compliance date, or the compliance date
is 60 days after October 26, 1999, whichever is later.
(b) New industrial POTW treatment plant. If you have a new
industrial POTW treatment plant, you must be in compliance as soon as
you begin accepting the waste stream(s) for treatment. If you begin
accepting a specific regulated industrial waste stream(s) for treatment,
you must be in compliance by the time specified in the appropriate
NESHAP(s) for the industrial user(s).
Sec. 63.1585 How does an industrial POTW treatment plant demonstrate compliance?
(a) An existing industrial POTW treatment plant demonstrates
compliance by operating treatment and control devices which meet all
requirements specified in the appropriate industrial NESHAP(s).
Requirements may include performance tests, routine monitoring,
recordkeeping, and reporting.
(b) If you have a new or reconstructed industrial POTW plant, you
must first determine whether the control requirements set forth in the
applicable industrial NESHAP(s) or the control requirements applicable
to a new or reconstructed nonindustrial POTW under Sec. 63.1586 would
require more stringent overall control of HAP emissions. You must then
meet whichever set of requirements is more stringent. If you determine
that the controls required by the applicable industrial NESHAP(s) are
more stringent, you demonstrate compliance by operating treatment and
control devices which meet all requirements specified in those
industrial NESHAP(s). If you determine that the controls required for a
new or reconstructed nonindustrial POTW are more stringent, you
demonstrate compliance by meeting all requirements in Secs. 63.1586
through 63.1590.
Non-industrial POTW Treatment Plant Requirements
Sec. 63.1586 What are the emission points and control requirements for a non-industrial POTW treatment plant?
There are no control requirements for an existing non-industrial
POTW treatment plant. There are no control requirements for any new or
reconstructed area source non-industrial POTW treatment plant which is
not a major source of HAP. The control requirements for a new or
reconstructed major source non-industrial POTW treatment plant which is
a major source of HAP are as follows:
[[Page 166]]
(a) Covers on the emission points up to, but not including, the
secondary influent pumping station or the secondary treatment units.
These emission points are treatment units that include, but are not
limited to, influent waste stream conveyance channels, bar screens, grit
chambers, grinders, pump stations, aerated feeder channels, primary
clarifiers, primary effluent channels, and primary screening stations.
In addition, all covered units, except primary clarifiers, must have the
air in the headspace ducted to a control device in accordance with the
standards for closed-vent systems and control devices in Sec. 63.693 of
subpart DD of this part, except you may substitute visual inspections
for leak checks rather than Method 21 of Appendix A of part 60 of this
chapter. Reconstruction is defined in Sec. 63.1595.
(1) Covers must be tightly fitted and designed and operated to
minimize exposure of the wastewater to the atmosphere. This includes,
but is not limited to, the absence of visible cracks, holes, or gaps in
the roof sections or between the roof and the supporting wall; broken,
cracked, or otherwise damaged seals or gaskets on closure devices; and
broken or missing hatches, access covers, caps, or other closure
devices.
(2) If wastewater is in a treatment unit, each opening must be
maintained in a closed, sealed position, unless plant personnel are
present and conducting wastewater or sludge sampling, or equipment
inspection, maintenance, or repair.
(b) As an alternative to the requirements in paragraph (a) of this
section, you may comply by demonstrating, for all units up to the
secondary influent pumping station or the secondary treatment units,
that the fraction emitted does not exceed 0.014. You must demonstrate
that for your POTW, the sum of all HAP emissions from those units
divided by the sum of all HAP mass loadings results in a annual rolling
average of the fraction emitted no greater than 0.014. You may use any
combination of pretreatment, wastewater treatment plant modifications,
and control devices to achieve this performance standard; however, you
must demonstrate, to the Administrator's satisfaction that:
(1) You have accurately determined your POTW's annual HAP mass
loadings and your POTW's annual HAP emissions as of the date of start-
up;
(2) Your POTW meets the fraction emitted standard of 0.014 or less;
and
(3) Your POTW has established procedures to demonstrate continuous
compliance which are consistent with the criteria set forth in
Sec. 63.1588(c)(4).
[64 FR 57579, Oct. 26, 1999, as amended at 66 FR 16142, Mar. 23, 2001;
67 FR 64746, Oct. 21, 2002]
Sec. 63.1587 When do I have to comply?
If your POTW treatment plant began construction on or after December
1, 1998, you must comply with all provisions of this subpart either
immediately upon startup, or by six months after October 26, 1999,
whichever date is later.
Sec. 63.1588 What inspections must I conduct?
(a) If your treatment units are required to have covers, you must
conduct the following inspections:
(1) You must visually check the cover and its closure devices for
defects that could result in air emissions. Defects include, but are not
limited to, visible cracks, holes, or gaps in the roof sections or
between the roof and the supporting wall; broken, cracked, or otherwise
damaged seals or gaskets on closure devices; and broken or missing
hatches, access covers, caps, or other closure devices.
(2) You must perform an initial visual inspection with follow-up
inspections at least once per year.
(3) In the event that you find a defect on a treatment unit in use,
you must repair the defect within 45 days. If you cannot repair within
45 days, you must notify the EPA or the designated State authority
immediately and report the reason for the delay and the date you expect
to complete the repair. If you find a defect on a treatment unit that is
not in service, you must repair the defect prior to putting the
treatment unit back in wastewater service.
(b) If you own or operate a control device used to meet the
requirements for Sec. 63.1586, you must comply with the
[[Page 167]]
inspection and monitoring requirements of Sec. 63.695(c) of subpart DD
of this part.
(c) To comply with the performance standard specified in
Sec. 63.1586(b), you must develop an inspection and monitoring plan.
This inspection and monitoring plan must include, at a minimum, the
following:
(1) A method to determine, to the satisfaction of the Administrator,
the influent HAP mass loading, i.e., the annual mass quantity for each
HAP entering the wastewater treatment plant.
(2) A method to determine, to the satisfaction of the Administrator,
your POTW's annual HAP emissions for all units up to and including the
secondary influent pumping station or up to and not including the
secondary treatment units as of October 26, 1999. The method you use to
determine your HAP emissions, such as modeling or direct source
measurement, must:
(i) Be approved by your EPA Regional Office, State, or local
regulatory agency for use at your POTW;
(ii) Account for all factors affecting emissions from your plant
including, but not limited to, emissions from wastewater treatment
units; emissions resulting from inspection, maintenance, and repair
activities; fluctuations (e.g., daily, monthly, annual, seasonal) in
your influent wastewater HAP concentrations; annual industrial loading;
performance of control devices; or any other factors that could affect
your annual HAP emissions; and
(iii) Include documentation that the values and sources of all data,
operating conditions, assumptions, etc., used in your method result in
an accurate estimation of annual emissions from your plant.
(3) Documentation, to the satisfaction of the Administrator, that
your POTW meets the fraction emitted standard of 0.014 or less, i.e.,
the sum of all HAP emissions from paragraph (c)(2) of this section
divided by the sum of all HAP mass loadings from paragraph (c)(1) of
this section results in a fraction emitted of 0.014 or less as described
in paragraph (c)(4) of this section.
(4) A method to demonstrate, to the satisfaction of the
Administrator, that your POTW is in continuous compliance with the
requirements of Sec. 63.1586(b). Continuous compliance means that your
emissions, when averaged over the course of a year, do not exceed the
level of emissions that allows your POTW to comply with Sec. 63.1586(b).
For example, you may identify a parameter(s) that you can monitor that
assures your emissions, when averaged over the entire year, will meet
the requirements in Sec. 63.1586(b). Some example parameters that may be
considered for monitoring include your wastewater influent HAP
concentration and flow, industrial loading from your permitted
industrial dischargers, and your control device performance criteria.
Where emission reductions are due to proper operation of equipment, work
practices, or other operational procedures, your demonstration must
specify the frequency of inspections and the number of days to
completion of repairs. You must, at a minimum, perform the following
each month to demonstrate that your annual rolling average of the
fraction emitted is 0.014 or less:
(i) Determine the average daily flow of the wastewater entering your
POTW treatment plant for the month;
(ii) Determine the flow-weighted monthly concentration of each HAP
in your influent listed in Table 1 to subpart DD of this part;
(iii) Using the current month's information in paragraphs (c)(4)(i)
and (ii) of this section, determine a total annual loading (Mg/year) of
each HAP entering your POTW treatment plant;
(iv) Sum up the values in paragraph (c)(4)(iii) of this section and
determine a total annual loading value (Mg/year) for all HAP entering
your POTW treatment plant for the current month;
(v) Based on the current month's information in paragraph
(c)(4)(iii) of this section along with source testing and emission
modeling, for each HAP, determine annual emissions (Mg/year) from all
wastewater units up to, but not including, secondary treatment units;
(vi) Sum up the values in paragraph (c)(4)(v) of this section and
determine the total annual emissions value for the month for all HAP
from all wastewater units up to, but not including, secondary treatment
units;
[[Page 168]]
(vii) Calculate the fraction emitted value for the month by dividing
the total annual HAP emissions value from paragraph (c)(4)(vi) of this
section by the total annual loading from paragraph (c)(4)(iv) of this
section; and
(viii) Average the fraction emitted value for the month determined
in paragraph (c)(4)(vii) of this section, with the values determined for
the previous 11 months, to calculate an annual rolling average of the
fraction HAP emitted.
Sec. 63.1589 What records must I keep?
(a) To comply with the equipment standard specified in
Sec. 63.1586(a), you must prepare and maintain the records required in
paragraphs (a)(1) through (4) of this section:
(1) A record for each treatment unit inspection required by
Sec. 63.1588(a). You must include a treatment unit identification number
(or other unique identification description as selected by you) and the
date of inspection.
(2) For each defect detected during inspections required by
Sec. 63.1588(a), you must record the location of the defect, a
description of the defect, the date of detection, the corrective action
taken to repair the defect, and the date the repair to correct the
defect is completed.
(3) In the event that repair of the defect is delayed, in accordance
with the provisions of Sec. 63.1588(a)(3), you must also record the
reason for the delay and the date you expect to complete the repair.
(4) If you own or operate a control device used to meet the
requirements for Sec. 63.1586, you must comply with the recordkeeping
requirements of Sec. 63.696(a), (b), (g), and (h).
(b) To comply with the performance standard specified in
Sec. 63.1586(b), you must prepare and maintain the records required in
paragraphs (b)(1) through (3) of this section:
(1) A record of the methods and data used to determine your POTW's
annual HAP emissions as determined in Sec. 63.1588(c)(2);
(2) A record of the methods and data used to determine that your
POTW meets the fraction emitted standard of 0.014 or less, as determined
in Sec. 63.1588(c)(3); and
(3) A record of the methods and data that demonstrates that your
POTW is in continuous compliance with the requirements of
Sec. 63.1588(c)(4).
[64 FR 57579, Oct. 26, 1999, as amended at 66 FR 16142, Mar. 23, 2001]
Sec. 63.1590 What reports must I submit?
(a)(1) If you have an existing non-industrial POTW treatment plant,
or a new or reconstructed area source non-industrial POTW treatment
plant, you are not required to submit a notification of compliance
status. If you have a new or reconstructed non-industrial POTW treatment
plant which is a major source of HAP, you must submit to the
Administrator a notification of compliance status, signed by the
responsible official who must certify its accuracy, attesting to whether
your POTW treatment plant has complied with this subpart. This
notification must be submitted initially, and each time a notification
of compliance status is required under this subpart. At a minimum, the
notification must list--
(i) The methods that were used to determine compliance;
(ii) The results of any monitoring procedures or methods that were
conducted;
(iii) The methods that will be used for determining continuing
compliance;
(iv) The type and quantity of HAP emitted by your POTW treatment
plant;
(v) A description of the air pollution control equipment (or method)
for each emission point; and
(vi) Your statement that your POTW treatment plant has complied with
this subpart.
(2) You must send this notification before the close of business on
the 60th day following the completion of the relevant compliance
demonstration activity specified in this subpart.
(b) After you have been issued a title V permit, you must comply
with all requirements for compliance status reports contained in your
title V permit, including reports required under this subpart. After you
have been issued a title V permit, and each time a notification of
compliance status is required under this subpart, you must submit the
notification of compliance status
[[Page 169]]
to the appropriate permitting authority, as described in paragraph (d)
of this section, following completion of the relevant compliance
demonstration activity specified in this subpart.
(c) You must comply with the delay of repair reporting required in
Sec. 63.1588(a)(3).
(d) If your State has not been delegated authority, you must submit
reports to your EPA Regional Office. If your State has been delegated
authority, you must submit reports to your delegated State authority,
and you must send a copy of each report submitted to the State to your
EPA Regional Office. Your EPA Regional Office, at its discretion, may
waive this requirement for any reports.
(e) You may apply to the Administrator for a waiver of recordkeeping
and reporting requirements by complying with the requirements of
Sec. 63.10(f) of subpart A of this part.
(f) If you own or operate a control device used to meet the
requirements of Sec. 63.1586(a), you must submit the reports required by
Sec. 63.697(b) of subpart DD of this part, including a notification of
performance tests; a performance test report; a startup, shutdown, and
malfunction report; and a summary report.
(g) To comply with the performance standard specified in
Sec. 63.1586(b), you must submit, for approval by the Administrator, an
initial report explaining your compliance approach 90 days prior to
beginning operation of your new or reconstructed POTW. You must also
submit a startup, shutdown, and malfunction report.
[64 FR 57579, Oct. 26, 1999, as amended at 66 FR 16142, Mar. 23, 2001;
67 FR 64746, Oct. 21, 2002]
General Requirements
Sec. 63.1591 What are my notification requirements?
(a) If you have an industrial POTW treatment plant or a new or
reconstructed non-industrial POTW which is a major source of HAP, and
your State has not been delegated authority, you must submit
notifications to the appropriate EPA Regional Office. If your State has
been delegated authority you must submit notifications to your State and
a copy of each notification to the appropriate EPA Regional Office. The
Regional Office may waive this requirement for any notifications at its
discretion.
(b) You must notify the Administrator in writing no later than 120
calendar days after the effective date of this subpart (or within 120
calendar days after your POTW treatment plant becomes subject to the
relevant standard), and you must provide the following information:
(1) Your name and address;
(2) The address (i.e., physical location) of your POTW treatment
plant;
(3) An identification of these standards as the basis of the
notification and your POTW treatment plant's compliance date; and
(4) A brief description of the nature, size, design, and method of
operation of your POTW treatment plant, including its operating design
capacity and an identification of each point of emission for each HAP,
or if a definitive identification is not yet possible, a preliminary
identification of each point of emission for each HAP.
(c) You must notify the Administrator if your data show that you are
no longer in continuous compliance.
[64 FR 57579, Oct. 26, 1999, as amended at 67 FR 64746, Oct. 21, 2002]
Sec. 63.1592 Which General Provisions apply to my POTW treatment plant?
(a) Table 1 to this subpart lists the General Provisions (40 CFR
part 63, subpart A) which do and do not apply to POTW treatment plants.
(b) Unless a permit is otherwise required by law, the owner or
operator of an industrial POTW which is not a major source is exempt
from the permitting requirements established by 40 CFR part 70.
[67 FR 64746, Oct. 21, 2002]
Sec. 63.1594 Who enforces this subpart?
If the Administrator has delegated authority to your State, then the
State enforces this subpart. If the Administrator has not delegated
authority to your State, then the EPA Regional Office enforces this
subpart.
Effective Date Note: At 68 FR 37360, June 23, 2003, Sec. 63.1594 was
revised effective August
[[Page 170]]
22, 2003. For the convenience of the user, the revised text is set forth
as follows:
Sec. 63.1594 Who enforces this subpart?
(a) This subpart can be implemented and enforced by the U.S. EPA, or
a delegated authority such as the applicable State, local, or Tribal
agency. If the U.S. EPA Administrator has delegated authority to a
State, local, or Tribal agency, then that agency, in addition to the
U.S. EPA, has the authority to implement and enforce this subpart.
Contact the applicable U.S. EPA Regional Office to find out if
implementation and enforcement of this subpart is delegated to a State,
local, or Tribal agency.
(b) In delegating implementation and enforcement authority of this
subpart to a State, local, or Tribal agency under subpart E of this
part, the authorities contained in paragraph (c) of this section are
retained by the Administrator of U.S. EPA and cannot be transferred to
the State, local, or Tribal agency.
(c) The authorities that cannot be delegated to State, local, or
Tribal agencies are as specified in paragraphs (c)(1) through (4) of
this section.
(1) Approval of alternatives to the requirements in Secs. 63.1580,
63.1583 through 63.1584, and 63.1586 through 63.1587.
(2) Approval of major alternatives to test methods under
Sec. 63.7(e)(2)(ii) and (f), as defined in Sec. 63.90, and as required
in this subpart.
(3) Approval of major alternatives to monitoring under Sec. 63.8(f),
as defined in Sec. 63.90, and as required in this subpart.
(4) Approval of major alternatives to recordkeeping and reporting
under Sec. 63.10(f), as defined in Sec. 63.90, and as required in this
subpart.
Sec. 63.1595 List of definitions.
Affected source means the group of all equipment that comprise the
POTW treatment plant.
Area source means any stationary source of HAP that is not a major
source.
Cover means a device that prevents or reduces air pollutant
emissions to the atmosphere by forming a continuous barrier over the
waste material managed in a treatment unit. A cover may have openings
(such as access hatches, sampling ports, gauge wells) that are necessary
for operation, inspection, maintenance, and repair of the treatment unit
on which the cover is used. A cover may be a separate piece of equipment
which can be detached and removed from the treatment unit, or a cover
may be formed by structural features permanently integrated into the
design of the treatment unit. The cover and its closure devices must be
made of suitable materials that will minimize exposure of the waste
material to the atmosphere, to the extent practical, and will maintain
the integrity of the cover and its closure devices throughout its
intended service life.
Fraction emitted means the fraction of the mass of HAP entering the
POTW wastewater treatment plant which is emitted prior to secondary
treatment. The value is calculated using the following steps:
(1) Determine mass emissions from all equipment up to, but not
including, secondary treatment for each HAP listed in Table 1 to subpart
DD of this part;
(2) Sum the HAP emissions ([Sigma]E);
(3) Sum the HAP mass loadings ([Sigma]L) in the influent to the POTW
wastewater treatment plant; and
(4) Calculate the fraction emitted (fe monthly) using
fe monthly = [Sigma]E/[Sigma]L.
HAP means hazardous air pollutant(s).
Industrial POTW means a POTW that accepts a waste stream regulated
by an industrial NESHAP and provides treatment and controls as an agent
for the industrial discharger. The industrial discharger complies with
its NESHAP by using the treatment and controls located at the POTW. For
example, an industry discharges its benzene-containing waste stream to
the POTW for treatment to comply with 40 CFR part 61, Subpart FF--
National Emission Standard for Benzene Waste Operations. This definition
does not include POTW treating waste streams not specifically regulated
under another NESHAP.
Industrial user means a nondomestic source introducing any pollutant
or combination of pollutants into a POTW. Industrial users can be
commercial or industrial facilities whose wastes enter local sewers.
Non-industrial POTW means a POTW that does not meet the definition
of an industrial POTW as defined above.
Publicly owned treatment works (POTW) means a treatment works, as
that term is defined by section 112(e)(5) of the Clean Air Act, which is
owned by a municipality (as defined by section
[[Page 171]]
502(4) of the Clean Water Act), a State, an intermunicipal or interstate
agency, or any department, agency, or instrumentality of the Federal
Government. This definition includes any intercepting sewers, outfall
sewers, sewage collection systems, pumping, power, and other equipment.
The wastewater treated by these facilities is generated by industrial,
commercial, and domestic sources. As used in this regulation, the term
POTW refers to both any publicly owned treatment works which is owned by
a State, municipality, or intermunicipal or interstate agency and
therefore eligible to receive grant assistance under the Subchapter II
of the Clean Water Act, and any federally owned treatment works as that
term is described in section 3023 of the Solid Waste Disposal Act.
POTW treatment plant means that portion of the POTW which is
designed to provide treatment (including recycling and reclamation) of
municipal sewage and industrial waste.
Reconstruction means the replacement of components of an affected or
a previously unaffected stationary source such that:
(1) The fixed capital cost of the new components exceeds 50 percent
of the fixed capital cost that would be required to construct a
comparable new source; and
(2) It is technologically and economically feasible for the
reconstructed source to meet the relevant standard(s) established by the
Administrator (or a State) pursuant to section 112 of the Act. Upon
reconstruction, an affected source, or a stationary source that becomes
an affected source, is subject to relevant standards for new sources,
including compliance dates, irrespective of any change in emissions of
HAP from that source.
Secondary treatment means treatment processes, typically biological,
designed to reduce the concentrations of dissolved and colloidal organic
matter in wastewater.
Waste and wastewater means a material, or spent or used water or
waste, generated from residential, industrial, commercial, mining, or
agricultural operations or from community activities that contain
dissolved or suspended matter, and that is discarded, discharged, or is
being accumulated, stored, or physically, chemically, thermally, or
biologically treated in a publicly owned treatment works.
[64 FR 57579, Oct. 26, 1999 as amended at 66 FR 16142, Mar. 23, 2001]
Table 1 to Subpart VVV of Part 63--Applicability of 40 CFR Part 63
General Provisions to Subpart VVV
----------------------------------------------------------------------------------------------------------------
General provisions reference Applicable to subpart VVV Explanation
----------------------------------------------------------------------------------------------------------------
Sec. 63.1................................. ................................... APPLICABILITY.
Sec. 63.1(a)(1)........................... Yes................................ Terms defined in the Clean Air
Act.
Sec. 63.1(a)(2)........................... Yes................................ General applicability
explanation.
Sec. 63.1(a)(3)........................... Yes................................ Cannot diminish a stricter
NESHAP.
Sec. 63.1(a)(4)........................... Yes................................ Not repetitive. Doesn't apply
to section 112(r).
Sec. 63.1(a)(5)........................... Yes................................ Section reserved.
Sec. 63.1(a)(6)-(8)....................... Yes................................ Contacts and authorities.
Sec. 63.1(a)(9)........................... Yes................................ Section reserved.
Sec. 63.1(a)(10).......................... Yes................................ Time period definition.
Sec. 63.1(a)(11).......................... Yes................................ Postmark explanation.
Sec. 63.1(a)(12)-(14)..................... Yes................................ Time period changes.
Regulation conflict. Force
and effect of subpart A.
Sec. 63.1(b)(1)........................... Yes................................ Initial applicability
determination of subpart A.
Sec. 63.1(b)(2)........................... Yes................................ Operating permits by States.
Sec. 63.1(b)(3)........................... No................................. Subpart VVV specifies
recordkeeping of records of
applicability determination.
Sec. 63.1(c)(1)........................... Yes................................ Requires compliance with both
subpart A and subpart VVV.
Sec. 63.1(c)(2)(i)........................ No................................. State options regarding title
V permit. Unless required by
the State, area sources
subject to subpart VVV are
exempted from permitting
requirements.
Sec. 63.1(c)(2)(ii)-(iii)................. No................................. State options regarding title
V permit.
Sec. 63.1(c)(3)........................... Yes................................ Section reserved.
Sec. 63.1(c)(4)........................... Yes................................ Extension of compliance.
[[Page 172]]
Sec. 63.1(c)(5)........................... No................................. Subpart VVV addresses area
sources becoming major due to
increase in emissions.
Sec. 63.1(d).............................. Yes................................ Section reserved.
Sec. 63.1(e).............................. Yes................................ Title V permit before a
relevant standard is
established.
Sec. 63.2................................. Yes................................ DEFINITIONS.
Sec. 63.3................................. Yes................................ UNITS AND ABBREVIATIONS.
Sec. 63.4................................. ................................... PROHIBITED ACTIVITIES AND
CIRCUMVENTION.
Sec. 63.4(a)(1)-(3)....................... Yes................................ Prohibits operation in
violation of subpart A.
Sec. 63.4(a)(4)........................... Yes................................ Section reserved.
Sec. 63.4(a)(5)........................... Yes................................ Compliance dates.
Sec. 63.4(b).............................. Yes................................ Circumvention.
Sec. 63.4(c).............................. Yes................................ Severability.
Sec. 63.5................................. ................................... CONSTRUCTION AND
RECONSTRUCTION.
Sec. 63.5(a)(1)........................... Yes................................ Construction and
reconstruction.
Sec. 63.5(a)(2)........................... Yes................................ New source--effective dates.
Sec. 63.5(b)(1)........................... Yes................................ New sources subject to
relevant standards.
Sec. 63.5(b)(2)........................... Yes................................ Section reserved.
Sec. 63.5(b)(3)........................... Yes................................ No new major sources without
Administrator approval.
Sec. 63.5(b)(4)........................... Yes................................ New major source notification.
Sec. 63.5(b)(5)........................... Yes................................ New major sources must comply.
Sec. 63.5(b)(6)........................... Yes................................ New equipment added considered
part of major source.
Sec. 63.5(c).............................. Yes................................ Section reserved.
Sec. 63.5(d)(1)........................... Yes................................ Implementation of section
112(I)(2)--application of
approval of new source
construction.
Sec. 63.5(d)(2)........................... Yes................................ Application for approval of
construction for new sources
listing and describing
planned air pollution control
system.
Sec. 63.5(d)(3)........................... Yes................................ Application for
reconstruction.
Sec. 63.5(d)(4)........................... Yes................................ Administrator may request
additional information.
Sec. 63.5(e).............................. Yes................................ Approval of reconstruction.
Sec. 63.5(f)(1)........................... Yes................................ Approval based on State
review.
Sec. 63.5(f)(2)........................... Yes................................ Application deadline.
Sec. 63.6................................. ................................... COMPLIANCE WITH STANDARDS AND
MAINTENANCE REQUIREMENTS.
Sec. 63.6(a).............................. Yes................................ Applicability of compliance
with standards and
maintenance requirements.
Sec. 63.6(b).............................. Yes................................ Compliance dates for new and
reconstructed sources.
Sec. 63.6(c).............................. Yes................................ Compliance dates for existing
sources apply to existing
industrial POTW treatment
plants.
Sec. 63.6(d).............................. Yes................................ Section reserved.
Sec. 63.6(e).............................. Yes................................ Operation and maintenance
requirements apply to new
sources.
Sec. 63.6(f).............................. Yes................................ Compliance with non-opacity
emission standards applies to
new sources.
Sec. 63.6(g).............................. Yes................................ Use of alternative non-opacity
emission standards applies to
new sources.
Sec. 63.6(h).............................. No................................. POTW treatment plants do not
typically have visible
emissions.
Sec. 63.6(i).............................. Yes................................ Extension of compliance with
emission standards applies to
new sources.
Sec. 63.6(j).............................. Yes................................ Presidential exemption from
compliance with emission
standards.
Sec. 63.7................................. ................................... PERFORMANCE TESTING
REQUIREMENTS.
Sec. 63.7(a).............................. Yes................................ Performance testing is
required for new sources.
Sec. 63.7(b).............................. Yes................................ New sources must notify the
Administrator of intention to
conduct performance testing.
Sec. 63.7(c).............................. Yes................................ New sources must comply with
quality assurance program
requirements.
Sec. 63.7(d).............................. Yes................................ New sources must provide
performance testing
facilities at the request of
the Administrator.
Sec. 63.7(e).............................. Yes................................ Requirements for conducting
performance tests apply to
new sources.
Sec. 63.7(f).............................. Yes................................ New sources may use an
alternative test method.
Sec. 63.7(g).............................. Yes................................ Requirements for data
analysis, recordkeeping, and
reporting associated with
performance testing apply to
new sources.
Sec. 63.7(h).............................. Yes................................ New sources may request a
waiver of performance tests.
Sec. 63.8................................. ................................... MONITORING REQUIREMENTS.
Sec. 63.8(a).............................. Yes................................ Applicability of monitoring
requirements.
Sec. 63.8(b).............................. Yes................................ Monitoring shall be conducted
by new sources.
Sec. 63.8(c).............................. Yes................................ New sources shall operate and
maintain continuous
monitoring systems (CMS).
Sec. 63.8(d).............................. Yes................................ New sources must develop and
implement a CMS quality
control program.
[[Page 173]]
Sec. 63.8(e).............................. Yes................................ New sources may be required to
conduct a performance
evaluation of CMS.
Sec. 63.8(f).............................. Yes................................ New sources may use an
alternative monitoring
method.
Sec. 63.8(g).............................. Yes................................ Requirements for reduction of
monitoring data.
Sec. 63.9................................. ................................... NOTIFICATION REQUIREMENTS.
Sec. 63.9(a).............................. Yes................................ Applicability of notification
requirements.
Sec. 63.9(b).............................. Yes................................ Applicability of notification
requirements. Existing major
non-industrial POTW treatment
plants, and existing and new
or reconstructed area non-
industrial POTW treatment
plants are not subject to the
notification requirements.
Sec. 63.9(c).............................. Yes................................ Request for extension of
compliance with subpart VVV.
Sec. 63.9(d).............................. Yes................................ Notification that source is
subject to special compliance
requirements as specified in
Sec. 63.6(b)(3) and (4).
Sec. 63.9(e).............................. Yes................................ Notification of performance
test.
Sec. 63.9(f).............................. No................................. POTW treatment plants do not
typically have visible
emissions.
Sec. 63.9(g).............................. Yes................................ Additional notification
requirements for sources with
continuous emission
monitoring systems.
Sec. 63.9(h).............................. Yes................................ Notification of compliance
status when the source
becomes subject to subpart
VVV.
Sec. 63.9(i).............................. Yes................................ Adjustments to time periods or
postmark deadlines or
submittal and review of
required communications.
Sec. 63.9(j).............................. Yes................................ Change of information already
provided to the
Administrator.
Sec. 63.10................................ ................................... RECORDKEEPING AND REPORTING
REQUIREMENTS.
Sec. 63.10(a)............................. Yes................................ Applicability of notification
and reporting requirements.
Sec. 63.10(b)(1)-(2)...................... Yes................................ General recordkeeping
requirements.
Sec. 63.10(b)(3).......................... No................................. Recording requirement for
applicability determination.
Sec. 63.10(c)............................. Yes................................ Additional recordkeeping
requirements for sources with
continuous monitoring
systems.
Sec. 63.10(d)............................. Yes................................ General reporting
requirements.
Sec. 63.10(e)............................. Yes................................ Additional reporting
requirements for sources with
continuous monitoring
systems.
Sec. 63.10(f)............................. Yes................................ Waiver of recordkeeping and
reporting requirements.
Sec. 63.11................................ ................................... FLARES AS A CONTROL DEVICE.
Sec. 63.11(a) and (b)..................... Yes................................ If a new source uses flares to
comply with the requirements
of subpart VVV, the
requirements of Sec. 63.11
apply.
Sec. 63.12................................ Yes................................ STATE AUTHORITY AND
DESIGNATION.
Sec. 63.13................................ Yes................................ ADDRESSES OF STATE AIR
POLLUTION CONTROL AGENCIES
AND EPA REGIONAL OFFICES.
Sec. 63.14................................ Yes................................ INCORPORATION BY REFERENCE.
Sec. 63.15................................ Yes................................ AVAILABILITY OF INFORMATION
AND CONFIDENTIALITY.
----------------------------------------------------------------------------------------------------------------
[64 FR 57579, Oct. 26, 1999 as amended at 66 FR 16142, Mar. 23, 2001; 67
FR 64746, Oct. 21, 2002]
Subpart WWW [Reserved]
Subpart XXX--National Emission Standards for Hazardous Air Pollutants
for Ferroalloys Production: Ferromanganese and Silicomanganese
Source: 64 FR 27458, May 20, 1999, unless otherwise noted.
Secs. 63.1620-63.1649 [Reserved]
Sec. 63.1650 Applicability and compliance dates.
(a) This subpart applies to all new and existing ferromanganese and
silicomanganese production facilities that manufacture ferromanganese or
silicomanganese and are major sources or are co-located at major sources
of hazardous air pollutant emissions.
(b) The following sources at a ferromanganese and silicomanganese
production facility are subject to this subpart:
(1) Open submerged arc furnaces with a furnace power input of 22 MW
or less when producing ferromanganese.
[[Page 174]]
(2) Open submerged arc furnaces with a furnace power input greater
than 22 MW when producing ferromanganese.
(3) Open submerged arc furnaces with a furnace power input greater
than 25 MW when producing silicomanganese.
(4) Open submerged arc furnaces with a furnace power input of 25 MW
or less when producing silicomanganese.
(5) Semi-sealed submerged arc furnaces when producing
ferromanganese.
(6) Metal oxygen refining (MOR) process.
(7) Crushing and screening operations.
(8) Fugitive dust sources.
(c) A new affected source is one for which construction or
reconstruction commenced after August 4, 1998.
(d) The following table specifies which provisions of subpart A of
this part apply to owners and operators of ferromanganese and
silicomanganese production facilities subject to this subpart:
General Provisions Applicability to Subpart XXX
------------------------------------------------------------------------
Applies to
Reference, Subpart A General Subpart XXX, Comment
Provisions 63.1620-63.1679
------------------------------------------------------------------------
63.1-63.5..................... Yes..............
63.6(a)-(g), (i)-(j).......... Yes..............
63.6(h)(1)-(h)(6), (h)(8)- Yes..............
(h)(9).
63.7(h)(7).................... No............... Sec. 63.6(h)(7), use
of continuous
opacity monitoring
system, not
applicable.
63.7.......................... Yes..............
63.8.......................... Yes..............
63.9.......................... Yes.............. Notification of
performance test
results changed to a
30-day notification
period.
63.10......................... Yes.............. Allow changes in
dates by which
periodic reports are
submitted by mutual
agreement between
the owner or
operator and the
State to occur any
time after the
source's compliance
date.
63.11......................... No............... Flares will not be
used to comply with
the emission limits.
63.12-63.15................... Yes..............
------------------------------------------------------------------------
(e) Compliance dates. (1) Each owner or operator of an existing
affected source must comply with the requirements of this subpart no
later than November 21, 2001.
(2) Each owner or operator of a new or reconstructed affected source
that commences construction or reconstruction after August 4, 1998, must
comply with the requirements of this subpart by May 20, 1999 or upon
startup of operations, whichever is later.
[64 FR 27458, May 20, 1999, as amended at 66 FR 16012, Mar. 22, 2001]
Sec. 63.1651 Definitions.
Terms in this subpart are defined in the Clean Air Act (Act), in
subpart A of this part, or in this section as follows:
Bag leak detection system means a system that is capable of
continuously monitoring particulate matter (dust) loadings in the
exhaust of a baghouse in order to detect bag leaks and other upset
conditions. A bag leak detection system includes, but is not limited to,
an instrument that operates on triboelectric, light scattering, light
transmittance, or other effect to continuously monitor relative
particulate matter loadings.
Capture system means the equipment (including hoods, ducts, fans,
dampers, etc.) used to capture or transport particulate matter generated
by an affected submerged arc furnace.
Casting means the period of time from when molten ferroalloy falls
from the furnace tapping runner into the ladle until pouring into molds
is completed. This includes the following operations: ladle filling,
pouring alloy from one ladle to another, slag separation, slag removal,
and ladle transfer by crane, truck, or other conveyance.
Crushing and screening equipment means the crushers, grinders,
mills, screens and conveying systems used to crush, size, and prepare
for packing manganese-containing materials, including raw materials,
intermediate products, and final products.
[[Page 175]]
Fugitive dust source means a stationary source from which manganese-
bearing particles are discharged to the atmosphere due to wind or
mechanical inducement such as vehicle traffic. Fugitive dust sources
include plant roadways, yard areas, and outdoor material storage and
transfer operations.
Furnace power input means the resistive electrical power consumption
of a submerged arc furnace, expressed as megawatts (MW).
Malfunction means any sudden, infrequent, and not reasonably
preventable failure of air pollution control equipment, process
equipment, or a process to operate in a normal or usual manner. Failures
caused in part by poor maintenance or careless operation are not
malfunctions.
Metal oxygen refining (MOR) process means the reduction of the
carbon content of ferromanganese through the use of oxygen.
Open submerged arc furnace means an electric submerged arc furnace
that is equipped with a canopy hood above the furnace to collect primary
emissions.
Operating time means the period of time in hours that the affected
source is in operation beginning at a startup and ending at the next
shutdown.
Plant roadway means any area at a ferromanganese and silicomanganese
production facility that is subject to plant mobile equipment, such as
fork lifts, front end loaders, or trucks, carrying manganese-bearing
materials. Excluded from this definition are employee and visitor
parking areas, provided they are not subject to traffic by plant mobile
equipment.
Primary emissions means gases and emissions collected by hoods and
ductwork located above an open furnace or under the cover of a semi-
closed or sealed furnace.
Sealed submerged arc furnace means an electric submerged arc furnace
equipped with a total enclosure or cover from which primary emissions
are evacuated directly.
Semi-closed submerged arc furnace means an electric submerged arc
furnace equipped with a partially sealed cover over the furnace. This
cover is equipped with openings to allow penetration of the electrodes
into the furnace. Mix is introduced into the furnace around the
electrode holes forming a partial seal between the electrodes and the
cover. Furnace emissions generated under the cover are ducted to an
emission control device. Emissions that escape the cover are collected
and vented through stacks directly to the atmosphere.
Shop means the building which houses one or more submerged arc
furnaces.
Shutdown means the cessation of operation of an affected source for
any purpose.
Startup means the setting in operation of an affected source for any
purpose.
Submerged arc furnace means any furnace wherein electrical energy is
converted to heat energy by transmission of current between electrodes
partially submerged in the furnace charge. The furnace may be of an
open, semi-sealed, or sealed design.
Tapping emissions means a source of air pollutant emissions that
occur during the process of removing the molten product from the
furnace.
Tapping period means the time from when a tap hole is opened until
the time a tap hole is closed.
Sec. 63.1652 Emission standards.
(a) New and reconstructed submerged arc furnaces. No owner or
operator shall cause to be discharged into the atmosphere from any new
or reconstructed submerged arc furnace exhaust gases (including primary
and tapping) containing particulate matter in excess of one of the
following:
(1) 0.23 kilograms per hour per megawatt (kg/hr/MW) (0.51 pounds per
hour per megawatt [lb/hr/MW]), or
(2) 35 milligrams per dry standard cubic meter (mg/dscm) (0.015
grains per dry standard cubic foot [gr/dscf]).
(b) Existing open submerged arc furnaces. No owner or operator shall
cause to be discharged into the atmosphere from any existing open
submerged arc furnace exhaust gases (including primary and tapping)
containing particulate matter in excess of one of the following:
[[Page 176]]
(1) 9.8 kilograms per hour (kg/hr) (21.7 pounds per hour (lb/hr))
when producing ferromanganese in an open furnace operating at a furnace
power input of 22 MW or less; or
(2) 13.5 kg/hr (29.8 lb/hr) when producing ferromanganese in an open
furnace operating at a furnace power input greater than 22 MW; or
(3) 16.3 kg/hr (35.9 lb/hr) when producing silicomanganese in an
open furnace operating at a furnace power input greater than 25 MW; or
(4) 12.3 kg/hr (27.2 lb/hr) when producing silicomanganese in an
open furnace operating at a furnace power input of 25 MW or less.
(c) Existing semi-sealed submerged arc furnaces. No owner or
operator shall cause to be discharged into the atmosphere from any
existing semi-sealed submerged arc furnace exhaust gases (including
primary, tapping, and vent stacks) containing particulate matter in
excess of 11.2 kg/hr (24.7 lb/hr) when producing ferromanganese.
(d) MOR process. No owner or operator shall cause to be discharged
into the atmosphere from any new, reconstructed, or existing MOR process
exhaust gases containing particulate matter in excess of 69 mg/dscm
(0.03 gr/dscf).
(e) Crushing and screening equipment. (1) New and reconstructed
equipment. No owner or operator shall cause to be discharged into the
atmosphere from any new or reconstructed piece of equipment associated
with crushing and screening exhaust gases containing particulate matter
in excess of 50 mg/dscm (0.022 gr/dscf).
(2) Existing equipment. No owner or operator shall cause to be
discharged into the atmosphere from any existing piece of equipment
associated with crushing and screening exhaust gases containing
particulate matter in excess of 69 (mg/dscm) (0.03 gr/dscf).
[64 FR 27458, May 20, 1999, as amended at 66 FR 16013, Mar. 22, 2001]
Sec. 63.1653 Opacity standards.
No owner or operator shall cause emissions exiting from a shop due
solely to operations of any affected submerged arc furnace, to exceed 20
percent opacity for more than one 6-minute period during any performance
test, with the following exceptions:
(a) Visible particulate emissions from a shop due solely to
operation of a semi-closed submerged arc furnace, may exceed 20 percent
opacity, measured as a 6-minute average, one time during any performance
test, so long as the emissions never exceed 60 percent opacity, measured
as a 6-minute average.
(b) Blowing taps, poling and oxygen lancing of the tap hole;
burndowns associated with electrode measurements; and maintenance
activities associated with submerged arc furnaces and casting operations
are exempt from the opacity standards specified in this section.
Sec. 63.1654 Operational and work practice standards.
(a) Fugitive dust sources. (1) Each owner or operator of an affected
ferromanganese and silicomanganese production facility must prepare, and
at all times operate according to, a fugitive dust control plan that
describes in detail the measures that will be put in place to control
fugitive dust emissions from the individual fugitive dust sources at the
facility.
(2) The owner or operator must submit a copy of the fugitive dust
control plan to the designated permitting authority on or before the
applicable compliance date for the affected source as specified in
Sec. 63.1650(e). The requirement for the owner or operator to operate
the facility according to a written fugitive dust control plan must be
incorporated in the operating permit for the facility that is issued by
the designated permitting authority under part 70 of this chapter.
(3) The owner or operator may use existing manuals that describe the
measures in place to control fugitive dust sources required as part of a
State implementation plan or other federally enforceable requirement for
particulate matter to satisfy the requirements of paragraph (a)(1) of
this section.
(b) Baghouses equipped with bag leak detection systems. The owner or
operator of a new or reconstructed submerged arc furnace must install
and continuously operate a bag leak detection system if the furnace's
primary and/or
[[Page 177]]
tapping emissions are ducted to a negative pressure baghouse or to a
positive pressure baghouse equipped with a stack. The owner or operator
must maintain and operate each baghouse such that the following
conditions are met:
(1) The alarm on the system does not sound for more than 5 percent
of the total operating time in a 6-month reporting period.
(2) A record is made of the date and time of each alarm and
procedures to determine the cause of the alarm are initiated within 1
hour of the alarm according to the plan for corrective action required
under Sec. 63.1657(a)(7).
Sec. 63.1655 Maintenance requirements.
(a) The owner or operator of an affected source must comply with the
requirements of Sec. 63.6(e) of subpart A.
(b)(1) The owner or operator must develop and implement a written
maintenance plan for each air pollution control device associated with
submerged arc furnaces, metal oxygen refining processes, and crushing
and screening operations subject to the provisions of this part. The
owner or operator must keep the maintenance plan on record and available
for the Administrator's inspection for the life of the air pollution
control device or until the affected source is no longer subject to the
provisions of this part.
(2) To satisfy the requirement to develop maintenance plans, the
owner or operator may use the affected source's standard operating
procedures (SOP) manual or other plan, provided the alternative plan
meets the requirements of this paragraph and is made available for
inspection when requested by the Administrator.
(c) The procedures specified in the maintenance plan must include a
preventive maintenance schedule that is consistent with good air
pollution control practices for minimizing emissions and, for baghouses,
ensure that the requirements specified in Sec. 63.1657(a) are met.
(d) The owner or operator must perform monthly inspections of the
equipment that is important to the performance of the furnace capture
system. This inspection must include an examination of the physical
condition of the equipment, suitable for detecting holes in ductwork or
hoods, flow constrictions in ductwork due to dents or accumulated dust,
and operational status of flow rate controllers (pressure sensors,
dampers, damper switches, etc.). Any deficiencies must be recorded and
proper maintenance and repairs performed.
Sec. 63.1656 Performance testing, test methods, and compliance demonstrations.
(a) Performance testing. (1) All performance tests must be conducted
according to the requirements in Sec. 63.7 of subpart A.
(2) Each performance test must consist of three separate and
complete runs using the applicable test methods.
(3) Each run must be conducted under conditions that are
representative of normal process operations.
(4) Performance tests conducted on air pollution control devices
serving submerged arc furnaces must be conducted such that at least one
tapping period, or at least 20 minutes of a tapping period, whichever is
less, is included in at least two of the three runs. The sampling time
for each run must be at least as long as three times the average tapping
period of the tested furnace, but no less than 60 minutes.
(5) The sample volume for each run must be at least 0.9 dscm (30
dscf).
(b) Test methods. The following test methods in Appendix A of part
60 of this chapter must be used to determine compliance with the
emission standards.
(1) Method 1 to select the sampling port location and the number of
traverse points.
(2) Method 2 to determine the volumetric flow rate of the stack gas.
(3) Method 3 to determine the dry molecular weight of the stack gas.
(4) Method 4 to determine the moisture content of the stack gas.
(5) Method 5 to determine the particulate matter concentration of
the stack gas for negative pressure baghouses and positive pressure
baghouses with stacks.
(6) Method 5D to determine particulate matter concentration and
volumetric flow rate of the stack gas for positive pressure baghouses
without stacks.
[[Page 178]]
(7) Method 9 to determine opacity.
(8) The owner or operator may use equivalent alternative measurement
methods approved by the Administrator following the procedures described
in Sec. 63.7(f) of subpart A.
(c) Compliance demonstration with the emission standards. (1) The
owner or operator must conduct an initial performance test for air
pollution control devices or vent stacks subject to Sec. 63.1652(a)
through (e) to demonstrate compliance with the applicable emission
standards.
(2) The owner or operator must conduct annual performance tests for
the air pollution control devices and vent stacks associated with the
submerged arc furnaces, with the exception of any air pollution control
devices that serve tapping emissions combined with non-furnace
emissions, such as the MOR process or equipment associated with crushing
and screening. Also excluded are air pollution control devices that
serve dedicated non-furnace emissions, such as the MOR process or
equipment associated with crushing and screening. The results of these
annual tests will be used to demonstrate compliance with the emission
standards in Sec. 63.1652(a) through (e), as applicable.
(3) Following development, and approval, if required, of the site-
specific test plan, the owner or operator must conduct a performance
test for each air pollution control device or vent stack to measure
particulate matter and determine compliance with the applicable
standard.
(i) An owner or operator of sources subject to the particulate
matter concentration standards in Sec. 63.1652(a)(2), (d), or (e), must
determine compliance as follows:
(A) Determine the particulate matter concentration using Method 5 or
5D, as applicable.
(B) Compliance is demonstrated if the average concentration for the
three runs comprising the performance test does not exceed the standard.
(ii) An owner or operator of sources subject to the particulate mass
rate standards in Sec. 63.1652(b) or (c) must determine compliance as
follows:
(A) Determine the particulate matter concentration and volumetric
flow rate using Method 5 or 5D, as applicable.
(B) Compute the mass rate (EM) of particulate matter for
each run using the following equation:
[GRAPHIC] [TIFF OMITTED] TR20MY99.000
Where:
EM = mass rate of particulate matter, kg/hr (lb/hr).
N = total number of exhaust streams at which emissions are quantified.
Csi = concentration of particulate matter from exhaust stream
``i'', mg/dscm (gr/dscf).
Qsdi = volumetric flow rate of effluent gas from exhaust
stream ``i'', dscm/hr (dscf/hr)
K = conversion factor, 1 x 106 mg/kg (7,000 gr/lb).
(C) Compliance is demonstrated if the average of the mass rates for
the three runs comprising the performance test does not exceed the
standard.
(iii) An owner or operator of sources subject to the particulate
matter process-weighted rate standard in Sec. 63.1652(a)(1) must
determine compliance as follows:
(A) Determine particulate matter concentration and volumetric flow
rate using Method 5 or 5D, as applicable.
(B) Compute the process-weighted mass rate (EP) of
particulate matter for each run using the following equation:
[GRAPHIC] [TIFF OMITTED] TR20MY99.001
Where:
EP = process-weighted mass rate of particulate matter, kg/hr/
MW (lb/hr/MW).
N = total number of exhaust streams at which emissions are quantified.
Csi = concentration of particulate matter from exhaust stream
``i'', mg/dscm (gr/dscf)
Qsdi = volumetric flow rate of effluent gas from exhaust
stream ``i'', dscm/hr (dscf/hr)
P = Average furnace power input, MW
K = conversion factor, 1 x 106 mg/kg (7,000 gr/lb).
(C) Compliance is demonstrated if the average process-weighted mass
rate for the three runs comprising the performance test does not exceed
the standard.
(4) If a venturi scrubber is used to comply with the emission
standards,
[[Page 179]]
the owner or operator must establish as a site-specific operating
parameter the lowest average pressure drop on any individual complying
run in the three runs constituting any compliant test. The pressure drop
must be monitored at least every 5 minutes during the test and hourly
averages recorded.
(i) [Reserved]
(ii) The owner or operator may augment the data obtained under
paragraph (a)(4) of this section by conducting multiple performance
tests to establish a range of compliant operating parameter values. The
lowest value of this range would be selected as the operating parameter
monitoring value. The use of historic compliance data may be used to
establish the compliant operating parameter value if the previous values
were recorded during performance tests using the same test methods
specified in this subpart and established as required in paragraph
(a)(4) of this section.
(d) Compliance demonstration with opacity standards. (1)(i) The
owner or operator subject to Sec. 63.1653 must conduct initial opacity
observations of the shop building to demonstrate compliance with the
applicable opacity standards according to Sec. 63.6(h)(5), which
addresses the conduct of opacity or visible emission observations.
(ii) In conducting the opacity observations of the shop building,
the observer must limit his or her field of view to the area of the shop
building roof monitor that corresponds to the placement of the affected
submerged arc furnaces.
(iii) The owner or operator must conduct the opacity observations
according to EPA Method 9 of 40 CFR part 60, appendix A, for a minimum
of 60 minutes.
(2)(i) When demonstrating initial compliance with the shop building
opacity standard, as required by paragraph (d)(1) of this section, the
owner or operator must simultaneously establish parameter values for one
of the following: the control system fan motor amperes and all capture
system damper positions, the total volumetric flow rate to the air
pollution control device and all capture system damper positions, or
volumetric flow rate through each separately ducted hood that comprises
the capture system.
(ii) The owner or operator may petition the Administrator to
reestablish these parameters whenever he or she can demonstrate to the
Administrator's satisfaction that the submerged arc furnace operating
conditions upon which the parameters were previously established are no
longer applicable. The values of these parameters determined during the
most recent demonstration of compliance must be maintained at the
appropriate level for each applicable period.
(3) The owner or operator must demonstrate continuing compliance
with the opacity standards by following the monitoring requirements
specified in Sec. 63.1657(c) and the reporting and recordkeeping
requirements specified in Secs. 63.1659(b)(4) and 63.1660(b).
(e) Compliance demonstration with the operational and work practice
standards. (1) Fugitive dust sources. Failure to have a fugitive dust
control plan or failure to report deviations from the plan and take
necessary corrective action would be a violation of the general duty to
ensure that fugitive dust sources are operated and maintained in a
manner consistent with good air pollution control practices for
minimizing emissions per Sec. 63.6(e)(1)(i) of subpart A.
(2) Baghouses equipped with bag leak detection systems. The owner or
operator demonstrates compliance with the bag leak detection system
requirements by submitting reports as required by Sec. 63.1659(b)(5)
showing that the alarm on the system does not sound for more than 5
percent of the total operating time in a 6-month period. Calculate the
percentage of total operating time the alarm on the bag leak detection
system sounds as follows:
(i) Do not include alarms that occur due solely to a malfunction of
the bag leak detection system in the calculation.
(ii) Do not include alarms that occur during startup, shutdown, and
malfunction in the calculation if the condition is described in the
startup, shutdown, and malfunction plan and the owner or operator
follows all the procedures in the plan defined for this condition.
[[Page 180]]
(iii) Count 1 hour of alarm time for each alarm where the owner or
operator initiates procedures to determine the cause within 1 hour of
the alarm.
(iv) Count the actual time it takes the owner or operator to
initiate procedures to determine the cause of the alarm for each alarm
where the owner or operator does not initiate procedures to determine
the cause within 1 hour of the alarm.
(v) Calculate the percentage of time the alarm on the bag leak
detection system sounds as the ratio of the sum of alarm times to the
total operating time multiplied by 100.
Sec. 63.1657 Monitoring requirements.
(a) Baghouses. (1) For the baghouses serving the submerged arc
furnaces, the metal oxygen refining process, and crushing and screening
operations, the owner or operator must observe on a daily basis for the
presence of any visible emissions.
(2) In addition to the daily visible emissions observation, the
owner or operator must conduct the following activities:
(i) Daily monitoring of pressure drop across each baghouse cell, or
across the baghouse if it is not possible to monitor each cell
individually, to ensure the pressure drop is within the normal operating
range identified in the baghouse maintenance plan.
(ii) Weekly confirmation that dust is being removed from hoppers
through visual inspection, or equivalent means of ensuring the proper
functioning of removal mechanisms.
(iii) Daily check of compressed air supply for pulse-jet baghouses.
(iv) An appropriate methodology for monitoring cleaning cycles to
ensure proper operation.
(v) Monthly check of bag cleaning mechanisms for proper functioning
through visual inspection or equivalent means.
(vi) Quarterly visual check of bag tension on reverse air and
shaker-type baghouses to ensure that the bags are not kinked (kneed or
bent) or laying on their sides. Such checks are not required for shaker-
type baghouses using self-tensioning (spring loaded) devices.
(vii) Quarterly confirmation of the physical integrity of the
baghouse structure through visual inspection of the baghouse interior
for air leaks.
(viii) Semiannual inspection of fans for wear, material buildup, and
corrosion through visual inspection, vibration detectors, or equivalent
means.
(3) In addition to meeting the requirements of paragraphs (a)(1) and
(a)(2) of this section, the owner or operator of a new or reconstructed
submerged arc furnace must install and continuously operate a bag leak
detection system if the furnace primary and/or tapping emissions are
ducted to a negative pressure baghouse or to a positive pressure
baghouse equipped with a stack. The bag leak detection system must meet
the following requirements:
(i) The bag leak detection system must be certified by the
manufacturer to be capable of detecting particulate matter emissions at
concentrations of 10 milligrams per actual cubic meter (0.0044 grains
per actual cubic foot) or less.
(ii) The bag leak detection system sensor must provide output of
relative particulate matter loadings, and the owner or operator must
continuously record the output from the bag leak detection system.
(iii) The bag leak detection system must be equipped with an alarm
system that will sound when an increase in relative particulate loadings
is detected over a preset level. The alarm must be located where it can
be heard by the appropriate plant personnel.
(iv) Each bag leak detection system that works based on the
triboelectric effect must be installed, calibrated, operated, and
maintained consistent with the U.S. Environmental Protection Agency
guidance document ``Fabric Filter Bag Leak Detection Guidance'' (EPA-
454/R-98-015). Other bag leak detection systems must be installed,
calibrated, and maintained consistent with the manufacturer's written
specifications and recommendations.
(v) The initial adjustment of the system must, at a minimum, consist
of establishing the baseline output by adjusting the sensitivity (range)
and the averaging period of the device, and establishing the alarm set
points and the alarm delay time.
[[Page 181]]
(vi) Following initial adjustment, the owner or operator must not
adjust the sensitivity or range, averaging period, alarm set points, or
alarm delay time, except as detailed in the maintenance plan required
under Sec. 63.1655(b). In no event must the sensitivity be increased by
more than 100 percent or decreased more than 50 percent over a 365-day
period unless a responsible official certifies the baghouse has been
inspected and found to be in good operating condition.
(vii) Where multiple detectors are required, the system's
instrumentation and alarm may be shared among detectors.
(4) As part of the maintenance plan required by Sec. 63.1655(b), the
owner or operator must develop and implement corrective action
procedures to be followed in the case of a bag leak detection system
alarm (for baghouses equipped with such a system), the observation of
visible emissions from the baghouse, or the indication through the
periodic baghouse system inspections that the system is not operating
properly. The owner or operator must initiate corrective action as soon
as practicable after the occurrence of the observation or event
indicating a problem.
(5) The corrective action plan must include procedures used to
determine the cause of an alarm or other indications of problems as well
as actions to minimize emissions. These actions may include the
following:
(i) Inspecting the baghouse for air leaks, torn or broken bags or
filter media, or any other condition that may cause an increase in
emissions.
(ii) Sealing off defective bags or filter media.
(iii) Replacing defective bags or filter media, or otherwise
repairing the control device.
(iv) Sealing off a defective baghouse compartment.
(v) Cleaning the bag leak detection system probe, or otherwise
repairing the bag leak detection system.
(vi) Shutting down the process producing the particulate matter
emissions.
(6) Failure to monitor or failure to take corrective action under
the requirements of paragraph (a) of this section would be a violation
of the general duty to operate in a manner consistent with good air
pollution control practices that minimizes emissions per
Sec. 63.6(e)(1)(i) of subpart A.
(b) Venturi scrubbers. (1) The owner or operator must monitor the
pressure drop across the venturi at least every 5 minutes and record the
average hourly pressure drop. Measurement of an average hourly pressure
drop less than the pressure drop operating parameter limit established
during a successful compliance demonstration would be a violation of the
applicable emission standard, unless the excursion in the pressure drop
is due to a malfunction.
(2) As part of the maintenance plan required by Sec. 63.1655(b), the
owner or operator must develop and implement corrective action
procedures to be followed in the case of a violation of the pressure
drop requirement. The owner or operator must initiate corrective action
as soon as practicable after the excursion.
(3) Failure to monitor or failure to take corrective action under
the requirements of paragraph (b) of this section is a violation of the
general duty to operate in a manner consistent with good air pollution
control practices that minimizes emissions per Sec. 63.6(e)(1)(i).
(c) Shop opacity. The owner or operator subject to the opacity
standards in Sec. 63.1653 must comply with one of the monitoring options
in paragraphs (c)(1), (c)(2) or (c)(3) of this section. The selected
option must be consistent with that selected during the initial
performance test described in Sec. 63.1656(d)(2). Alternatively, the
owner or operator may use the provisions of Sec. 63.8(f) to request
approval to use an alternative monitoring method.
(1) The owner or operator must check and record the control system
fan motor amperes and capture system damper positions once per shift.
(2) The owner or operator must install, calibrate, and maintain a
monitoring device that continuously records the volumetric flow rate
through each separately ducted hood.
(3) The owner or operator must install, calibrate, and maintain a
monitoring device that continuously records the volumetric flow rate at
the inlet of
[[Page 182]]
the air pollution control device and must check and record the capture
system damper positions once per shift.
(4) The flow rate monitoring devices must meet the following
requirements:
(i) Be installed in an appropriate location in the exhaust duct such
that reproducible flow rate monitoring will result.
(ii) Have an accuracy [plusmn]10 percent over its normal operating
range and be calibrated according to the manufacturer's instructions.
(5) The Administrator may require the owner or operator to
demonstrate the accuracy of the monitoring device(s) relative to Methods
1 and 2 of appendix A of part 60 of this chapter.
(6) Failure to maintain the appropriate capture system parameters
(fan motor amperes, flow rate, and/or damper positions) establishes the
need to initiate corrective action as soon as practicable after the
monitoring excursion in order to minimize excess emissions.
(7) Failure to monitor or failure to take corrective action under
the requirements of paragraph (c) of this section is a violation of the
general duty to operate in a manner consistent with good air pollution
control practices that minimizes emissions per Sec. 63.6(e)(1)(i).
Sec. 63.1658 Notification requirements.
(a) As required by Sec. 63.9(b) of subpart A, unless otherwise
specified in this subpart, the owner or operator must submit the
following written notifications to the Administrator:
(1) The owner or operator of an area source that subsequently
becomes subject to the requirements of the standard must provide
notification to the applicable permitting authority as required by
Sec. 63.9(b)(1).
(2) As required by Sec. 63.9(b)(2), the owner or operator of an
affected source that has an initial startup before the effective date of
the standard must notify the Administrator that the source is subject to
the requirements of the standard. The notification must be submitted no
later than 120 calendar days after May 20, 1999 (or within 120 calendar
days after the source becomes subject to this standard) and must contain
the information specified in Sec. 63.9(b)(2)(i) through (b)(2)(v).
(3) As required by Sec. 63.9(b)(3), the owner or operator of a new
or reconstructed affected source, or a source that has been
reconstructed such that it is an affected source, that has an initial
startup after the effective date and for which an application for
approval of construction or reconstruction is not required under
Sec. 63.5(d), must notify the Administrator in writing that the source
is subject to the standards no later than 120 days after initial
startup. The notification must contain the information specified in
Sec. 63.9(b)(2)(i) through (b)(2)(v), delivered or postmarked with the
notification required in Sec. 63.9(b)(5).
(4) As required by Sec. 63.9(b)(4), the owner or operator of a new
or reconstructed major affected source that has an initial startup after
the effective date of this standard and for which an application for
approval of construction or reconstruction is required under
Sec. 63.5(d) must provide the information specified in
Sec. 63.9(b)(4)(i) through (b)(4)(v).
(5) As required by Sec. 63.9(b)(5), the owner or operator who, after
the effective date of this standard, intends to construct a new affected
source or reconstruct an affected source subject to this standard, or
reconstruct a source such that it becomes an affected source subject to
this standard, must notify the Administrator, in writing, of the
intended construction or reconstruction.
(b) Request for extension of compliance. As required by
Sec. 63.9(c), if the owner or operator of an affected source cannot
comply with this standard by the applicable compliance date for that
source, or if the owner or operator has installed BACT or technology to
meet LAER consistent with Sec. 63.6(i)(5), he or she may submit to the
Administrator (or the State with an approved permit program) a request
for an extension of compliance as specified in Sec. 63.6(i)(4) through
(i)(6).
(c) Notification that source is subject to special compliance
requirements. As required by Sec. 63.9(d), an owner or operator of a new
source that is subject to special compliance requirements as specified
in Sec. 63.6(b)(3) and (b)(4) must notify
[[Page 183]]
the Administrator of his or her compliance obligations no later than the
notification dates established in Sec. 63.9(b) for new sources that are
not subject to the special provisions.
(d) Notification of performance test. As required by Sec. 63.9(e),
the owner or operator of an affected source must notify the
Administrator in writing of his or her intention to conduct a
performance test at least 30 calendar days before the performance test
is scheduled to begin to allow the Administrator to review and approve
the site-specific test plan required under Sec. 63.7(c) and to have an
observer present during the test.
(e) Notification of opacity and visible emission observations. As
required by Sec. 63.9(f), the owner or operator of an affected source
must notify the Administrator in writing of the anticipated date for
conducting the opacity or visible emission observations specified in
Sec. 63.6(h)(5). The notification must be submitted with the
notification of the performance test date, as specified in paragraph (d)
of this section, or if visibility or other conditions prevent the
opacity or visible emission observations from being conducted
concurrently with the initial performance test required under Sec. 63.7,
the owner or operator must deliver or postmark the notification not less
than 30 days before the opacity or visible emission observations are
scheduled to take place.
(f) Notification of compliance status. The owner or operator of an
affected source must submit a notification of compliance status as
required by Sec. 63.9(h). The notification must be sent before the close
of business on the 60th day following completion of the relevant
compliance demonstration.
Sec. 63.1659 Reporting requirements.
(a) General reporting requirements. The owner or operator of a
ferromanganese and silicomanganese production facility must comply with
all of the reporting requirements under Sec. 63.10 of subpart A, unless
otherwise specified in this subpart.
(1) Frequency of reports. As provided by Sec. 63.10(a)(5), if the
owner or operator is required to submit periodic reports to a State on
an established time line, he or she may change the dates by which
periodic reports submitted under this part may be submitted (without
changing the frequency of reporting) to be consistent with the State's
schedule by mutual agreement between the owner or operator and the
State. This provision may be applied at any point after the source's
compliance date.
(2) Reporting results of performance tests. As required by
Sec. 63.10(d)(2), the owner or operator of an affected source must
report the results of the initial performance test as part of the
notification of compliance status required in Sec. 63.1658(f).
(3) [Reserved]
(4) Periodic startup, shutdown, and malfunction reports. (i) As
required by Sec. 63.10(d)(5)(i), if actions taken by an owner or
operator during a startup, shutdown, or malfunction of an affected
source (including actions taken to correct a malfunction) are consistent
with the procedures specified in the startup, shutdown, and malfunction
plan, the owner or operator must state such information in a semiannual
report. The report, to be certified by the owner or operator or other
responsible official, must be submitted semiannually and delivered or
postmarked by the 30th day following the end of each calendar half; and
(ii) Any time an action taken by an owner or operator during a
startup, shutdown, or malfunction (including actions taken to correct a
malfunction) is not consistent with the procedures in the startup,
shutdown, and malfunction plan, the owner or operator must comply with
all requirements of Sec. 63.10(d)(5)(ii).
(b) Specific reporting requirements. In addition to the information
required under Sec. 63.10, reports required under paragraph (a) of this
section must include the information specified in paragraphs (b)(1)
through (b)(5) of this section. As allowed by Sec. 63.10(a)(3), if any
State requires a report that contains all of the information required in
a report listed in this section, an owner or operator may send the
Administrator a copy of the report sent to the State to satisfy the
requirements of this section for that report.
(1) Air pollution control devices. The owner or operator must submit
reports that summarize the records maintained as part of the practices
described in the
[[Page 184]]
maintenance plan for air pollution control devices required under
Sec. 63.1655(b), including an explanation of the periods when the
procedures were not followed and the corrective actions taken.
(2) Venturi scrubbers. In addition to the information required to be
submitted in paragraph (b)(1) of this section, the owner or operator
must submit reports that identify the periods when the average hourly
pressure drop of venturi scrubbers used to control particulate emissions
dropped below the levels established in Sec. 63.1656(c)(4), and an
explanation of the corrective actions taken.
(3) Fugitive dust. The owner or operator must submit reports that
explain the periods when the procedures outlined in the fugitive dust
control plan pursuant to Sec. 63.1654(a) were not followed and the
corrective actions taken.
(4) Capture system. The owner or operator must submit reports that
summarize the monitoring parameter excursions measured pursuant to
Sec. 63.1657(c) and the corrective actions taken.
(5) Bag leak detection system. The owner or operator must submit
reports including the following information:
(i) Records of all alarms.
(ii) Description of the actions taken following each bag leak
detection system alarm.
(iii) Calculation of the percent of time the alarm on the bag leak
detection system sounded during the reporting period.
(6) Frequency of reports. (i) The owner or operator must submit
reports pursuant to Sec. 63.10(e)(3) that are associated with excess
emissions events such as the excursion of the scrubber pressure drop
limit per paragraph (b)(2) of this section. These reports are to be
submitted on a quarterly basis, unless the owner or operator can satisfy
the requirements in Sec. 63.10(e)(3) to reduce the frequency to a
semiannual basis.
(ii) All other reports specified in paragraphs (b)(1) through (b)(5)
of this section must be submitted semiannually.
Sec. 63.1660 Recordkeeping requirements.
(a) General recordkeeping requirements. (1) The owner or operator of
a ferromanganese and silicomanganese production facility must comply
with all of the recordkeeping requirements under Sec. 63.10.
(2) As required by Sec. 63.10(b)(2), the owner or operator must
maintain records for 5 years from the date of each record of:
(i) The occurrence and duration of each startup, shutdown, or
malfunction of operation (i.e., process equipment and control devices);
(ii) The occurrence and duration of each malfunction of the source
or air pollution control equipment;
(iii) All maintenance performed on the air pollution control
equipment;
(iv) Actions taken during periods of startup, shutdown, and
malfunction (including corrective actions to restore malfunctioning
process and air pollution control equipment to its normal or usual
manner of operation) when such actions are different from the procedures
specified in the startup, shutdown, and malfunction plan;
(v) All information necessary to demonstrate conformance with the
startup, shutdown, and malfunction plan when all actions taken during
periods of startup, shutdown, and malfunction (including corrective
actions) are consistent with the procedures specified in such plan. This
information can be recorded in a checklist or similar form (see
Sec. 63.10(b)(2)(v));
(vi) All required measurements needed to demonstrate compliance with
the standard and to support data that the source is required to report,
including, but not limited to, performance test measurements (including
initial and any subsequent performance tests) and measurements as may be
necessary to determine the conditions of the initial test or subsequent
tests;
(vii) All results of initial or subsequent performance tests;
(viii) If the owner or operator has been granted a waiver from
recordkeeping or reporting requirements under Sec. 63.10(f), any
information demonstrating whether a source is meeting the requirements
for a waiver of recordkeeping or reporting requirements;
(ix) If the owner or operator has been granted a waiver from the
initial performance test under Sec. 63.7(h), a copy of the full request
and the Administrator's approval or disapproval;
[[Page 185]]
(x) All documentation supporting initial notifications and
notifications of compliance status required by Sec. 63.9; and
(xi) As required by Sec. 63.10(b)(3), records of any applicability
determination, including supporting analyses.
(b) Specific recordkeeping requirements. (1) In addition to the
general records required by paragraph (a) of this section, the owner or
operator must maintain records for 5 years from the date of each record
of:
(i) Records of pressure drop across the venturi if a venturi
scrubber is used.
(ii) Records of manufacturer certification that monitoring devices
are accurate to within 5 percent (unless otherwise specified in this
subpart) and of calibrations performed at the manufacturer's recommended
frequency, or at a frequency consistent with good engineering practice,
or as experience dictates.
(iii) Records of bag leak detection system output.
(iv) An identification of the date and time of all bag leak
detection system alarms, the time that procedures to determine the cause
of the alarm were initiated, the cause of the alarm, an explanation of
the actions taken, and the date and time the alarm was corrected.
(v) Copy of the written maintenance plan for each air pollution
control device.
(vi) Copy of the fugitive dust control plan.
(vii) Records of each maintenance inspection and repair,
replacement, or other corrective action.
(2) All records for the most recent 2 years of operation must be
maintained on site. Records for the previous 3 years may be maintained
off site.
Sec. 63.1661 Delegation of authorities.
In delegating implementation and enforcement authority to a State
under subpart E of this part, the Administrator retains no authorities.
Effective Date Note: At 68 FR 37360, June 23, 2003, Sec. 63.1661 was
revised effective August 22, 2003. For the convenience of the user, the
revised text is set forth as follows:
Sec. 63.1661 Implementation and enforcement.
(a) This subpart can be implemented and enforced by the U.S. EPA, or
a delegated authority such as the applicable State, local, or Tribal
agency. If the U.S. EPA Administrator has delegated authority to a
State, local, or Tribal agency, then that agency, in addition to the
U.S. EPA, has the authority to implement and enforce this subpart.
Contact the applicable U.S. EPA Regional Office to find out if this
subpart is delegated to a State, local, or Tribal agency.
(b) In delegating implementation and enforcement authority of this
subpart to a State, local, or Tribal agency under subpart E of this
part, the authorities contained in paragraph (c) of this section are
retained by the Administrator of U.S. EPA and cannot be transferred to
the State, local, or Tribal agency.
(c) The authorities that cannot be delegated to State, local, or
Tribal agencies are as specified in paragraphs (c)(1) through (4) of
this section.
(1) Approval of alternatives to requirements in Secs. 63.1650 and
63.1652 through 63.1654.
(2) Approval of major alternatives to test methods under
Sec. 63.7(e)(2)(ii) and (f), as defined in Sec. 63.90, and as required
in this subpart.
(3) Approval of major alternatives to monitoring under Sec. 63.8(f),
as defined in Sec. 63.90, and as required in this subpart.
(4) Approval of major alternatives to recordkeeping and reporting
under Sec. 63.10(f), as defined in Sec. 63.90, and as required in this
subpart.
Secs. 63.1662-63.1679 [Reserved]
Subpart AAAA--National Emission Standards for Hazardous Air Pollutants:
Municipal Solid Waste Landfills
Source: 68 FR 2238, Jan. 16, 2003, unless otherwise noted.
What This Subpart Covers
Sec. 63.1930 What is the purpose of this subpart?
This subpart establishes national emission standards for hazardous
air pollutants for existing and new municipal solid waste (MSW)
landfills. This subpart requires all landfills described in Sec. 63.1935
to meet the requirements of 40 CFR part 60, subpart Cc or WWW and
requires timely control of bioreactors. This subpart also requires such
landfills to meet the startup, shutdown, and malfunction (SSM)
requirements of the general provisions of this part and provides that
compliance with the
[[Page 186]]
operating conditions shall be demonstrated by parameter monitoring
results that are within the specified ranges. It also includes
additional reporting requirements.
Sec. 63.1935 Am I subject to this subpart?
You are subject to this subpart if you meet the criteria in
paragraph (a) or (b) of this section.
(a) You are subject to this subpart if you own or operate a MSW
landfill that has accepted waste since November 8, 1987 or has
additional capacity for waste deposition and meets any one of the three
criteria in paragraphs (a)(1) through (3) of this section:
(1) Your MSW landfill is a major source as defined in 40 CFR 63.2 of
subpart A.
(2) Your MSW landfill is collocated with a major source as defined
in 40 CFR 63.2 of subpart A.
(3) Your MSW landfill is an area source landfill that has a design
capacity equal to or greater than 2.5 million megagrams (Mg) and 2.5
million cubic meters (m3) and has estimated uncontrolled
emissions equal to or greater than 50 megagrams per year (Mg/yr) NMOC as
calculated according to Sec. 60.754(a) of the MSW landfills new source
performance standards in 40 CFR part 60, subpart WWW, the Federal plan,
or an EPA approved and effective State or tribal plan that applies to
your landfill.
(b) You are subject to this subpart if you own or operate a MSW
landfill that has accepted waste since November 8, 1987 or has
additional capacity for waste deposition, that includes a bioreactor, as
defined in Sec. 63.1990, and that meets any one of the criteria in
paragraphs (b)(1) through (3) of this section:
(1) Your MSW landfill is a major source as defined in 40 CFR 63.2 of
subpart A.
(2) Your MSW landfill is collocated with a major source as defined
in 40 CFR 63.2 of subpart A.
(3) Your MSW landfill is an area source landfill that has a design
capacity equal to our greater than 2.5 million Mg and 2.5 million m\3\
and that is not permanently closed as of January 16, 2003.
Sec. 63.1940 What is the affected source of this subpart?
(a) An affected source of this subpart is a MSW landfill, as defined
in Sec. 63.1990, that meets the criteria in Sec. 63.1935(a) or (b). The
affected source includes the entire disposal facility in a contiguous
geographic space where household waste is placed in or on land,
including any portion of the MSW landfill operated as a bioreactor.
(b) A new affected source of this subpart is an affected source that
commenced construction or reconstruction after November 7, 2000. An
affected source is reconstructed if it meets the definition of
reconstruction in 40 CFR 63.2 of subpart A.
(c) An affected source of this subpart is existing if it is not new.
Sec. 63.1945 When do I have to comply with this subpart?
(a) If your landfill is a new affected source, you must comply with
this subpart by January 16, 2003 or at the time you begin operating,
whichever is last.
(b) If your landfill is an existing affected source, you must comply
with this subpart by January 16, 2004.
(c) If your landfill is a new affected source and is a major source
or is collocated with a major source, you must comply with the
requirements in Secs. 63.1955(b) and 63.1960 through 63.1980 by the date
your landfill is required to install a collection and control system by
40 CFR 60.752(b)(2) of subpart WWW.
(d) If your landfill is an existing affected source and is a major
source or is collocated with a major source, you must comply with the
requirements in Secs. 63.1955(b) and 63.1960 through 63.1980 by the date
your landfill is required to install a collection and control system by
40 CFR 60.752(b)(2) of subpart WWW, the Federal plan, or EPA approved
and effective State or tribal plan that applies to your landfill or by
January 13, 2004, whichever occurs later.
(e) If your landfill is a new affected source and is an area source
meeting the criteria in Sec. 63.1935(a)(3), you must comply with the
requirements of Secs. 63.1955(b) and 63.1960 through 63.1980 by the date
your landfill is required to install a collection and control system by
40 CFR 60.752(b)(2) of subpart WWW.
[[Page 187]]
(f) If your landfill is an existing affected source and is an area
source meeting the criteria in Sec. 63.1935(a)(3), you must comply with
the requirements in Secs. 63.1955(b) and 63.1960 through 63.1980 by the
date your landfill is required to install a collection and control
system by 40 CFR 60.752(b)(2) of subpart WWW, the Federal plan, or EPA
approved and effective State or tribal plan that applies to your
landfill or by January 16, 2004, whichever occurs later.
Sec. 63.1947 When do I have to comply with this subpart if I own or operate a bioreactor?
You must comply with this subpart by the dates specified in
Sec. 63.1945(a) or (b) of this subpart. If you own or operate a
bioreactor located at a landfill that is not permanently closed as of
January 16, 2003 and has a design capacity equal to or greater than 2.5
million Mg and 2.5 million m\3\, then you must install and operate a
collection and control system that meets the criteria in 40 CFR
60.752(b)(2)(v) of part 60, subpart WWW, the Federal plan, or EPA
approved and effective State plan according to the schedule specified in
paragraph (a), (b), or (c) of this section.
(a) If your bioreactor is at a new affected source, then you must
meet the requirements in paragraphs (a)(1) and (2) of this section:
(1) Install the gas collection and control system for the bioreactor
before initiating liquids addition.
(2) Begin operating the gas collection and control system within 180
days after initiating liquids addition or within 180 days after
achieving a moisture content of 40 percent by weight, whichever is
later. If you choose to begin gas collection and control system
operation 180 days after achieving a 40 percent moisture content instead
of 180 days after liquids addition, use the procedures in
Sec. 63.1980(g) and (h) to determine when the bioreactor moisture
content reaches 40 percent.
(b) If your bioreactor is at an existing affected source, then you
must install and begin operating the gas collection and control system
for the bioreactor by January 17, 2006 or by the date your bioreactor is
required to install a gas collection and control system under 40 CFR
part 60, subpart WWW, the Federal plan, or EPA approved and effective
State plan or tribal plan that applies to your landfill, whichever is
earlier.
(c) If your bioreactor is at an existing affected source and you do
not initiate liquids addition to your bioreactor until later than
January 17, 2006, then you must meet the requirements in paragraphs
(c)(1) and (2) of this section:
(1) Install the gas collection and control system for the bioreactor
before initiating liquids addition.
(2) Begin operating the gas collection and control system within 180
days after initiating liquids addition or within 180 days after
achieving a moisture content of 40 percent by weight, whichever is
later. If you choose to begin gas collection and control system
operation 180 days after achieving a 40 percent moisture content instead
of 180 days after liquids addition, use the procedures in
Sec. 63.1980(g) and (h) to determine when the bioreactor moisture
content reaches 40 percent.
Sec. 63.1950 When am I no longer required to comply with this subpart?
You are no longer required to comply with the requirements of this
subpart when you are no longer required to apply controls as specified
in 40 CFR 60.752(b)(2)(v) of subpart WWW, or the Federal plan or EPA
approved and effective State plan or tribal plan that implements 40 CFR
part 60, subpart Cc, whichever applies to your landfill.
Sec. 63.1952 When am I no longer required to comply with the requirements of this subpart if I own or operate a bioreactor?
If you own or operate a landfill that includes a bioreactor, you are
no longer required to comply with the requirements of this subpart for
the bioreactor provided you meet the conditions of either paragraphs (a)
or (b).
(a) Your affected source meets the control system removal criteria
in 40 CFR 60.752(b)(2)(v) of part 60, subpart WWW or the bioreactor
meets the criteria for a nonproductive area of the landfill in 40 CFR
60.759(a)(3)(ii) of part 60, subpart WWW.
(b) The bioreactor portion of the landfill is a closed landfill as
defined in
[[Page 188]]
40 CFR 60.751, subpart WWW, you have permanently ceased adding liquids
to the bioreactor, and you have not added liquids to the bioreactor for
at least 1 year. A closure report for the bioreactor must be submitted
to the Administrator as provided in 40 CFR 60.757(d) of subpart WWW.
(c) Compliance with the bioreactor control removal provisions in
this section constitutes compliance with 40 CFR part 60, subpart WWW or
the Federal plan, whichever applies to your bioreactor.
Standards
Sec. 63.1955 What requirements must I meet?
(a) You must fulfill one of the requirements in paragraph (a)(1) or
(2) of this section, whichever is applicable:
(1) Comply with the requirements of 40 CFR part 60, subpart WWW.
(2) Comply with the requirements of the Federal plan or EPA approved
and effective State plan or tribal plan that implements 40 CFR part 60,
subpart Cc.
(b) If you are required by 40 CFR 60.752(b)(2) of subpart WWW, the
Federal plan, or an EPA approved and effective State or tribal plan to
install a collection and control system, you must comply with the
requirements in Secs. 63.1960 through 63.1985 and with the general
provisions of this part specified in table 1 of this subpart.
(c) For approval of collection and control systems that include any
alternatives to the operational standards, test methods, procedures,
compliance measures, monitoring, recordkeeping or reporting provisions,
you must follow the procedures in 40 CFR 60.752(b)(2). If alternatives
have already been approved under 40 CFR part 60 subpart WWW or the
Federal plan, or EPA approved and effective State or tribal plan, these
alternatives can be used to comply with this subpart, except that all
affected sources must comply with the SSM requirements in Subpart A of
this part as specified in Table 1 of this subpart and all affected
sources must submit compliance reports every 6 months as specified in
Sec. 63.1980(a) and (b), including information on all deviations that
occurred during the 6-month reporting period. Deviations for continuous
emission monitors or numerical continuous parameter monitors must be
determined using a 3 hour monitoring block average.
(d) If you own or operate a bioreactor that is located at a MSW
landfill that is not permanently closed and has a design capacity equal
to or greater than 2.5 million Mg and 2.5 million m\3\, then you must
meet the requirements of paragraph (a) and the additional requirements
in paragraphs (d)(1) and (2) of this section.
(1) You must comply with the general provisions specified in Table 1
of this subpart and Secs. 63.1960 through 63.1985 starting on the date
you are required to install the gas collection and control system.
(2) You must extend the collection and control system into each new
cell or area of the bioreactor prior to initiating liquids addition in
that area, instead of the schedule in 40 CFR 60.752(b)(2)(ii)(A)(2).
General and Continuing Compliance Requirements
Sec. 63.1960 How is compliance determined?
Compliance is determined in the same way it is determined for 40 CFR
part 60, subpart WWW, including performance testing, monitoring of the
collection system, continuous parameter monitoring, and other credible
evidence. In addition, continuous parameter monitoring data, collected
under 40 CFR 60.756(b)(1), (c)(1), and (d) of subpart WWW, are used to
demonstrate compliance with the operating conditions for control
systems. If a deviation occurs, you have failed to meet the control
device operating conditions described in this subpart and have deviated
from the requirements of this subpart. Finally, you must develop and
implement a written SSM plan according to the provisions in 40 CFR
63.6(e)(3). A copy of the SSM plan must be maintained on site. Failure
to write, implement, or maintain a copy of the SSM plan is a deviation
from the requirements of this subpart.
[[Page 189]]
Sec. 63.1965 What is a deviation?
A deviation is defined in Sec. 63.1990. For the purposes of the
landfill monitoring and SSM plan requirements, deviations include the
items in paragraphs (a) through (c) of this section.
(a) A deviation occurs when the control device operating parameter
boundaries described in 40 CFR 60.758(c)(1) of subpart WWW are exceeded.
(b) A deviation occurs when 1 hour or more of the hours during the
3-hour block averaging period does not constitute a valid hour of data.
A valid hour of data must have measured values for at least three 15-
minute monitoring periods within the hour.
(c) A deviation occurs when a SSM plan is not developed,
implemented, or maintained on site.
Sec. 63.1975 How do I calculate the 3-hour block average used to demonstrate compliance?
Averages are calculated in the same way as they are calculated in 40
CFR part 60, subpart WWW, except that the data collected during the
events listed in paragraphs (a), (b), (c), and (d) of this section are
not to be included in any average computed under this subpart:
(a) Monitoring system breakdowns, repairs, calibration checks, and
zero (low-level) and high-level adjustments.
(b) Startups.
(c) Shutdowns.
(d) Malfunctions.
Notifications, Records, and Reports
Sec. 63.1980 What records and reports must I keep and submit?
(a) Keep records and reports as specified in 40 CFR part 60, subpart
WWW, or in the Federal plan, EPA approved State plan or tribal plan that
implements 40 CFR part 60, subpart Cc, whichever applies to your
landfill, with one exception: You must submit the annual report
described in 40 CFR 60.757(f) every 6 months.
(b) You must also keep records and reports as specified in the
general provisions of 40 CFR part 60 and this part as shown in Table 1
of this subpart. Applicable records in the general provisions include
items such as SSM plans and the SSM plan reports.
(c) For bioreactors at new affected sources you must submit the
initial semiannual compliance report and performance test results
described in 40 CFR 60.757(f) within 180 days after the date you are
required to begin operating the gas collection and control system by
Sec. 63.1947(a)(2) of this subpart.
(d) For bioreactors at existing affected sources, you must submit
the initial semiannual compliance report and performance test results
described in 40 CFR 60.757(f) within 180 days after the compliance date
specified in Sec. 63.1947(b) of this subpart, unless you have previously
submitted a compliance report for the bioreactor required by 40 CFR part
60, subpart WWW, the Federal plan, or an EPA approved and effective
State plan or tribal plan.
(e) For bioreactors that are located at existing affected sources,
but do not initiate liquids addition until later than the compliance
date in Sec. 63.1947(b) of this subpart, you must submit the initial
semiannual compliance report and performance tests results described in
40 CFR 60.757(f) within 180 days after the date you are required to
begin operating the gas collection and control system by Sec. 63.1947(c)
of this subpart.
(f) If you must submit a semiannual compliance report for a
bioreactor as well as a semiannual compliance report for a conventional
portion of the same landfill, you may delay submittal of a subsequent
semiannual compliance report for the bioreactor according to paragraphs
(f)(1) through (3) of this section so that the reports may be submitted
on the same schedule.
(1) After submittal of your initial semiannual compliance report and
performance test results for the bioreactor, you may delay submittal of
the subsequent semiannual compliance report for the bioreactor until the
date the initial or subsequent semiannual compliance report is due for
the conventional portion of your landfill.
(2) You may delay submittal of your subsequent semiannual compliance
report by no more than 12 months after the due date for submitting the
initial semiannual compliance report and performance test results
described in 40 CFR 60.757(f) for the bioreactor. The report shall cover
the time period since the previous semiannual report for the
[[Page 190]]
bioreactor, which would be a period of at least 6 months and no more
than 12 months.
(3) After the delayed semiannual report, all subsequent semiannual
reports for the bioreactor must be submitted every 6 months on the same
date the semiannual report for the conventional portion of the landfill
is due.
(g) If you add any liquids other than leachate in a controlled
fashion to the waste mass and do not comply with the bioreactor
requirements in Secs. 63.1947, 63.1955(c) and 63.1980(c) through (f) of
this subpart, you must keep a record of calculations showing that the
percent moisture by weight expected in the waste mass to which liquid is
added is less than 40 percent. The calculation must consider the waste
mass, moisture content of the incoming waste, mass of water added to the
waste including leachate recirculation and other liquids addition and
precipitation, and the mass of water removed through leachate or other
water losses. Moisture level sampling or mass balances calculations can
be used. You must document the calculations and the basis of any
assumptions. Keep the record of the calculations until you cease liquids
addition.
(h) If you calculate moisture content to establish the date your
bioreactor is required to begin operating the collection and control
system under Sec. 63.1947(a)(2) or (c)(2), keep a record of the
calculations including the information specified in paragraph (g) of
this section for 5 years. Within 90 days after the bioreactor achieves
40 percent moisture content, report the results of the calculation, the
date the bioreactor achieved 40 percent moisture content by weight, and
the date you plan to begin collection and control system operation.
Other Requirements and Information
Sec. 63.1985 Who enforces this subpart?
(a) This subpart can be implemented and enforced by the U.S. EPA, or
a delegated authority such as the applicable State, local, or tribal
agency. If the EPA Administrator has delegated authority to a State,
local, or tribal agency, then that agency as well as the U.S. EPA has
the authority to implement and enforce this subpart. Contact the
applicable EPA Regional Office to find out if this subpart is delegated
to a State, local, or tribal agency.
(b) In delegating implementation and enforcement authority of this
subpart to a State, local, or tribal agency under subpart E of this
part, the authorities contained in paragraph (c) of this section are
retained by the EPA Administrator and are not transferred to the State,
local, or tribal agency.
(c) The authorities that will not be delegated to State, local, or
tribal agencies are as follows. Approval of alternatives to the
standards in Sec. 63.1955. Where these standards reference another
subpart, the cited provisions will be delegated according to the
delegation provisions of the referenced subpart.
Sec. 63.1990 What definitions apply to this subpart?
Terms used in this subpart are defined in the Clean Air Act, 40 CFR
part 60, subparts A, Cc, and WWW; 40 CFR part 62, subpart GGG, and
subpart A of this part, and this section that follows:
Bioreactor means a MSW landfill or portion of a MSW landfill where
any liquid other than leachate (leachate includes landfill gas
condensate) is added in a controlled fashion into the waste mass (often
in combination with recirculating leachate) to reach a minimum average
moisture content of at least 40 percent by weight to accelerate or
enhance the anaerobic (without oxygen) biodegradation of the waste.
Deviation means any instance in which an affected source subject to
this subpart, or an owner or operator of such a source:
(1) Fails to meet any requirement or obligation established by this
subpart, including, but not limited to, any emissions limitation
(including any operating limit) or work practice standard;
(2) Fails to meet any term or condition that is adopted to implement
an applicable requirement in this subpart and that is included in the
operating permit for any affected source required to obtain such a
permit; or
(3) Fails to meet any emission limitation, (including any operating
limit), or work practice standard in this subpart during SSM, regardless
of whether
[[Page 191]]
or not such failure is permitted by this subpart.
Emissions limitation means any emission limit, opacity limit,
operating limit, or visible emissions limit.
EPA approved State plan means a State plan that EPA has approved
based on the requirements in 40 CFR part 60, subpart B to implement and
enforce 40 CFR part 60, subpart Cc. An approved State plan becomes
effective on the date specified in the notice published in the Federal
Register announcing EPA's approval.
Federal plan means the EPA plan to implement 40 CFR part 60, subpart
Cc for existing MSW landfills located in States and Indian country where
State plans or tribal plans are not currently in effect. On the
effective date of an EPA approved State or tribal plan, the Federal plan
no longer applies. The Federal plan is found at 40 CFR part 62, subpart
GGG.
Municipal solid waste landfill or MSW landfill means an entire
disposal facility in a contiguous geographical space where household
waste is placed in or on land. A municipal solid waste landfill may also
receive other types of RCRA Subtitle D wastes (see Sec. 257.2 of this
chapter) such as commercial solid waste, nonhazardous sludge,
conditionally exempt small quantity generator waste, and industrial
solid waste. Portions of a municipal solid waste landfill may be
separated by access roads. A municipal solid waste landfill may be
publicly or privately owned. A municipal solid waste landfill may be a
new municipal solid waste landfill, an existing municipal solid waste
landfill, or a lateral expansion.
Tribal plan means a plan submitted by a tribal authority pursuant to
40 CFR parts 9, 35, 49, 50, and 81 to implement and enforce 40 CFR part
60, subpart Cc.
Work practice standard means any design, equipment, work practice,
or operational standard, or combination thereof, that is promulgated
pursuant to section 112(h) of the Clean Air Act.
As stated in Secs. 63.1955 and 63.1980, you must meet each
requirement in the following table that applies to you.
Table 1 of Subpart AAAA of Part 63--Applicability of NESHAP General
Provisions to Subpart AAAA
------------------------------------------------------------------------
Part 63 Citation Description Explanation
------------------------------------------------------------------------
63.1(a)..................... Applicability: Affected sources are
general already subject to
applicability of the provisions of
NESHAP in this part. paragraphs (a)(10)-
(12) through the
same provisions
under 40 CFR, part
60 subpart A.
63.1(b)..................... Applicability
determination for
stationary sources.
63.1(e)..................... Title V permitting..
63.2........................ Definitions.........
63.4........................ Prohibited Affected sources are
activities and already subject to
circumvention. the provisions of
paragraph (b)
through the same
provisions under 40
CFR, part 60
subpart A.
63.5(b)..................... Requirements for
existing, newly
constructed, and
reconstructed
sources.
63.6(e)..................... Operation and
maintenance
requirements,
startup, shutdown
and malfunction
plan provisions.
63.6(f)..................... Compliance with Affected sources are
nonopacity emission already subject to
standards. the provisions of
paragraphs (f)(1)
and (2)(i) through
the same provisions
under 40 CFR, part
60 subpart A.
63.10(b)(2)(i)-(b)(2)(v).... General
recordkeeping
requirements.
63.10(d)(5)................. If actions taken
during a startup,
shutdown and
malfunction plan
are consistent with
the procedures in
the startup,
shutdown and
malfunction plan,
this information
shall be included
in a semi-annual
startup, shutdown
and malfunction
plan report. Any
time an action
taken during a
startup, shutdown
and malfunction
plan is not
consistent with the
startup, shutdown
and malfunction
plan, the source
shall report
actions taken
within 2 working
days after
commencing such
actions, followed
by a letter 7 days
after the event.
[[Page 192]]
63.12(a).................... These provisions do
not preclude the
State from adopting
and enforcing any
standard,
limitation, etc.,
requiring permits,
or requiring
emissions
reductions in
excess of those
specified.
63.15....................... Availability of
information and
confidentiality.
------------------------------------------------------------------------
Subpart CCCC--National Emission Standards for Hazardous Air Pollutants:
Manufacturing of Nutritional Yeast
Source: 66 FR 27884, May 21, 2001, unless otherwise noted.
What This Subpart Covers
Sec. 63.2130 What is the purpose of this subpart?
This subpart establishes national emission limitations for hazardous
air pollutants emitted from manufacturers of nutritional yeast. This
subpart also establishes requirements to demonstrate initial and
continuous compliance with the emission limitations.
Sec. 63.2131 Am I subject to this subpart?
(a) You are subject to this subpart if you own or operate a
nutritional yeast manufacturing facility that is, is located at, or is
part of a major source of hazardous air pollutants (HAP) emissions.
(1) A manufacturer of nutritional yeast is a facility that makes
yeast for the purpose of becoming an ingredient in dough for bread or
any other yeast-raised baked product, or for becoming a nutritional food
additive intended for consumption by humans. A manufacturer of
nutritional yeast does not include production of yeast intended for
consumption by animals, such as an additive for livestock feed.
(2) A major source of HAP emissions is any stationary source or
group of stationary sources located within a contiguous area and under
common control that emits or has the potential to emit, considering
controls, any single HAP at a rate of 9.07 megagrams (10 tons) or more
per year or any combination of HAP at a rate of 22.68 megagrams (25
tons) or more per year.
(b) [Reserved]
Sec. 63.2132 What parts of my plant does this subpart cover?
(a) This subpart applies to each new, reconstructed, or existing
``affected source'' that produces Saccharomyces cerevisiae at a
nutritional yeast manufacturing facility.
(b) The affected source is the collection of equipment used in the
manufacture of the nutritional yeast species Saccharomyces cerevisiae.
This collection of equipment includes, but is not limited to,
fermentation vessels (fermenters). The collection of equipment used in
the manufacture of the nutritional yeast species Candida utilis (torula
yeast) is not part of the affected source.
(c) The emission limitations in this subpart apply to fermenters in
the affected source that meet all of the criteria listed in paragraphs
(c)(1) through (2) of this section.
(1) The fermenters are ``fed-batch'' as defined in Sec. 63.2192.
(2) The fermenters are used to support one of the last three
fermentation stages in a production run, which may be referred to as
``stock, first generation, and trade,'' ``seed, semi-seed, and
commercial,'' or ``CB4, CB5, and CB6'' stages.
(d) The emission limitations in this subpart do not apply to flask,
pure-culture, yeasting-tank, or any other set-batch fermentation, and
they do not apply to any operations after the last dewatering operation,
such as filtration.
(e) The emission limitations in this subpart do not apply to the
affected source during the production of specialty yeast (defined in
Sec. 63.2192).
(f) An affected source is a ``new affected source'' if you commenced
construction of the affected source after October 19, 1998, and you met
the applicability criteria in Sec. 63.2131 at the time you commenced
construction.
[[Page 193]]
(g) An affected source is ``reconstructed'' if you meet the criteria
as defined in Sec. 63.2.
(h) An affected source is ``existing'' if it is not new or
reconstructed.
Sec. 63.2133 When do I have to comply with this subpart?
(a) If you have a new or reconstructed affected source, you must
comply with paragraphs (a)(1) through (2) of this section.
(1) If you start up your affected source before May 21, 2001, then
you must comply with the emission limitations in this subpart no later
than May 21, 2001.
(2) If you start up your affected source after May 21, 2001, then
you must comply with the emission limitations in this subpart upon
startup of your affected source.
(b) If you have an existing affected source, you must comply with
the emission limitations for existing sources no later than May 21,
2004.
(c) If you have an area source that increases its emissions, or its
potential to emit, so that it becomes a major source of HAP, paragraphs
(c)(1) through (2) of this section apply.
(1) Any portion of the existing facility that is a new affected
source or a new reconstructed source must be in compliance with this
subpart upon startup.
(2) All other parts of the source must be in compliance with this
subpart by not later than 3 years after it becomes a major source.
(d) You must meet the notification requirements in Sec. 63.2180
according to the schedule in Sec. 63.2180 and in subpart A of this part.
Emission Limitations
Sec. 63.2140 What emission limitations must I meet?
You must meet all of the emission limitations in Table 1 to this
subpart.
General Compliance Requirements
Sec. 63.2150 What are my general requirements for complying with this subpart?
(a) You must be in compliance with the emission limitations in Table
1 to this subpart at all times, except during periods of malfunction.
(b) You must always operate and maintain your affected source,
including monitoring equipment, according to the provisions in
Sec. 63.6(e)(1)(i). If the date upon which you must demonstrate initial
compliance as specified in Sec. 63.2160 falls after the compliance date
specified for your affected source in Sec. 63.2133, then you must
maintain a log detailing the operation and maintenance of the continuous
monitoring systems and the process and emissions control equipment
during the period between those dates.
(c) You must develop and implement a written malfunction plan. It
will be as specified in Sec. 63.6(e)(3), except that the requirements
for startup, shutdown, and maintenance plans, records and reports apply
only to malfunctions. Under this subpart, a period of malfunction is
expressed in whole batches and not in portions of batches.
Testing and Initial Compliance Requirements
Sec. 63.2160 By what date must I conduct an initial compliance demonstration?
(a) For each emission limitation in Table 1 to this subpart for
which compliance is demonstrated by monitoring fermenter exhaust, you
must demonstrate initial compliance for the period ending on the last
day of the month that is 12 calendar months (or 11 calendar months, if
the compliance date for your source is the first day of the month) after
the compliance date that is specified for your source in Sec. 63.2133.
(For example, if the compliance date is October 15, 2003, the first 12-
month period for which you must demonstrate compliance would be October
15, 2003 through October 31, 2004.)
(b) For each emission limitation in Table 1 to this subpart for
which initial compliance is demonstrated by monitoring brew ethanol
concentration and calculating volatile organic compound (VOC)
concentration in the fermenter exhaust according to the procedures in
Sec. 63.2161, you must demonstrate initial compliance within 180
calendar days before the compliance date that is specified for your
source in Sec. 63.2133.
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Sec. 63.2161 What performance tests and other procedures must I use if I monitor brew ethanol?
(a) You must conduct each performance test in Table 2 to this
subpart that applies to you.
(b) Each performance test must be conducted according to the
requirements in Sec. 63.7(e)(1) and under the specific conditions that
this subpart specifies in Table 2 to this subpart and in paragraphs
(b)(1) through (4) of this section.
(1) Conduct each performance test simultaneously with brew ethanol
monitoring to establish a brew-to-exhaust correlation equation as
specified in paragraph (f) of this section.
(2) For each fermentation stage, conduct one run of the EPA Test
Method 25A of 40 CFR part 60, appendix A, over the entire length of a
batch. The three fermentation stages do not have to be from the same
production run.
(3) Do the test at a point in the exhaust-gas stream before you
inject any dilution air, which is any air not needed to control
fermentation.
(4) Record the results of the test for each fermentation stage.
(c) You may not conduct performance tests during periods of startup,
shutdown, or malfunction, as specified in Sec. 63.7(e)(1).
(d) You must collect data to correlate the brew ethanol
concentration measured by the continuous emission monitoring system
(CEMS) to the VOC concentration in the fermenter exhaust according to
paragraphs (d)(1) through (3) of this section.
(1) You must collect a separate set of brew ethanol concentration
data for each fed-batch fermentation stage while manufacturing the
product that comprises the largest percentage (by mass) of average
annual production.
(2) Measure brew ethanol as specified in Sec. 63.2164 simultaneously
with conducting a performance test for VOC in fermenter exhaust as
specified in paragraph (b) of this section. You must measure brew
ethanol at least once during each successive 30-minute period over the
entire period of the performance test for VOC in fermenter exhaust.
(3) Keep a record of the brew ethanol concentration data for each
fermentation stage over the period of EPA Test Method 25A of 40 CFR part
60, appendix A, performance test when the VOC concentration in the
fermenter exhaust does not exceed the applicable emission limitation in
Table 1 to this subpart.
(e) For each set of data that you collected under paragraph (d) of
this section, perform a linear regression of brew ethanol concentration
(percent) on VOC fermenter exhaust concentration (parts per million by
volume (ppmv) measured as propane). The correlation between the brew
ethanol concentration as measured by the CEMS and the VOC fermenter
exhaust concentration as measured by EPA Test Method 25A of 40 CFR part
60, appendix A, must be linear with a correlation coefficient of at
least 0.90.
(f) Calculate the VOC concentration in the fermenter exhaust using
the brew ethanol concentration data collected under paragraph (d) of
this section and according to Equation 1 of this section.
BAVOC = BAE * CF + y (Eq. 1)
Where:
BAVOC = batch-average concentration of VOC in fermenter exhaust (ppmv
measured as propane), calculated for compliance demonstration
BAE = batch-average concentration of brew ethanol in fermenter liquid
(percent), measured by CEMS
CF = constant established at performance test and representing the slope
of the regression line
y = constant established at performance test and representing the y-
intercept of the regression line
Sec. 63.2162 When must I conduct subsequent performance tests?
(a) For each emission limitation in Table 1 to this subpart for
which compliance is demonstrated by monitoring brew ethanol
concentration and calculating VOC concentration in the fermenter exhaust
according to the procedures in Sec. 63.2161, you must conduct an EPA
Test Method 25A of 40 CFR part 60, appendix A, performance test and
establish a brew-to-exhaust correlation according to the procedures in
Table 2 to this subpart and in Sec. 63.2161, at least once every year.
(b) The first subsequent performance test must be conducted no later
than
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365 calendar days after the initial performance test conducted according
to Sec. 63.2160. Each subsequent performance test must be conducted no
later than 365 calendar days after the previous performance test. You
must conduct a performance test for each 365 calendar day period for the
lifetime of the affected source.
Sec. 63.2163 If I monitor fermenter exhaust, what are my monitoring installation, operation, and maintenance requirements?
(a) Each CEMS must be installed, operated, and maintained according
to the applicable Performance Specification (PS) of 40 CFR part 60,
appendix B.
(b) You must conduct a performance evaluation of each CEMS according
to the requirements in Sec. 63.8, according to the applicable
Performance Specification of 40 CFR part 60, appendix B, and according
to paragraphs (b)(1) through (4) of this section.
(1) If your CEMS monitor generates a single combined response value
for VOC (examples of such detection principles are flame ionization,
photoionization, and non-dispersive infrared absorption), but it is not
a flame ionization analyzer, you must use PS 8 to show that your CEMS is
operating properly.
(i) Use EPA Test Method 25A of 40 CFR part 60, appendix A, to do the
relative-accuracy test PS 8 requires.
(ii) Calibrate the reference method with propane.
(iii) Collect a 1-hour sample for each reference-method test.
(2) If you continuously monitor VOC emissions using a flame
ionization analyzer, then you must conduct the calibration drift test PS
8 requires, but you are not required to conduct the relative-accuracy
test PS 8 requires.
(3) If you continuously monitor VOC emissions using gas
chromatography, you must use PS 9 of CFR part 60, appendix B, to show
that your CEMS is operating properly.
(4) You must complete the performance evaluation and submit the
performance evaluation report before the compliance date that is
specified for your source in Sec. 63.2133.
(c) Calibrate the CEMS with propane.
(d) Set the CEMS span at not greater than 5 times the relevant
emission limit, with 1.5 to 2.5 times the relevant emission limit being
the range considered by us to be generally optimum.
(e) You must monitor VOC concentration in fermenter exhaust at any
point prior to dilution of the exhaust stream.
(f) Each CEMS must complete a minimum of one cycle of operation
(sampling, analyzing, and data recording) for each successive 30-minute
period within each batch monitoring period. Except as specified in
paragraph (g) of this section, you must have a minimum of two cycles of
operation in a 1-hour period to have a valid hour of data.
(g) The CEMS data must be reduced to arithmetic batch averages
computed from two or more data points over each 1-hour period, except
during periods when calibration, quality assurance, or maintenance
activities pursuant to provisions of this part are being performed.
During these periods, a valid hour of data shall consist of at least one
data point representing a 30-minute period.
(h) You must have valid CEMS data from at least 75 percent of the
full hours over the entire batch monitoring period.
(i) For each CEMS, record the results of each inspection,
calibration, and validation check.
(j) You must check the zero (low-level) and high-level calibration
drifts for each CEMS in accordance with the applicable PS of 40 CFR part
60, appendix B. The zero (low-level) and high-level calibration drifts
shall be adjusted, at a minimum, whenever the zero (low-level) drift
exceeds 2 times the limits of the applicable PS. The calibration drift
checks must be performed at least once daily except that they may be
performed less frequently under the conditions of paragraphs (j)(1)
through (3) of this section.
(1) If a 24-hour calibration drift check for your CEMS is performed
immediately prior to, or at the start of, a batch monitoring period of a
duration exceeding 24 hours, you are not required to perform 24-hour-
interval calibration drift checks during that batch monitoring period.
(2) If the 24-hour calibration drift exceeds 2.5 percent of the span
value (or
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more than 10 percent of the calibration gas value if your CEMS is a gas
chromatograph (GC)) in fewer than 5 percent of the checks over a 1-month
period, and the 24-hour calibration drift never exceeds 7.5 percent of
the span value, then the frequency of calibration drift checks may be
reduced to at least weekly (once every 7 days).
(3) If, during two consecutive weekly checks, the weekly calibration
drift exceeds 5 percent of the span value (or more than 20 percent of
the calibration gas value, if your CEMS is a GC), then a frequency of at
least 24-hour interval calibration checks must be resumed until the 24-
hour calibration checks meet the test of paragraph (j)(2) of this
section.
(k) If your CEMS is out of control, you must take corrective action
according to paragraphs (k)(1) through (3) of this section.
(1) Your CEMS is out of control if the zero (low-level) or high-
level calibration drift exceeds 2 times the limits of the applicable PS.
(2) When the CEMS is out of control, take the necessary corrective
action and repeat all necessary tests that indicate that the system is
out of control. You must take corrective action and conduct retesting
until the performance requirements are below the applicable limits.
(3) During the batch monitoring periods in which the CEMS is out of
control, recorded data shall not be used in data averages and
calculations, or to meet any data availability requirement established
under this subpart. The beginning of the out-of-control period is the
beginning of the first batch monitoring period that follows the most
recent calibration drift check during which the system was within
allowable performance limits. The end of the out-of-control period is
the end of the last batch monitoring period before you have completed
corrective action and successfully demonstrated that the system is
within the allowable limits. If your successful demonstration that the
system is within the allowable limits occurs during a batch monitoring
period, then the out-of-control period ends at the end of that batch
monitoring period. If the CEMS is out of control for any part of a
particular batch monitoring period, it is out of control for the whole
batch monitoring period.
Sec. 63.2164 If I monitor brew ethanol, what are my monitoring installation, operation, and maintenance requirements?
(a) Each CEMS must be installed, operated, and maintained according
to manufacturer's specifications and the plan for malfunctions that you
must develop and use according to Sec. 63.6(e).
(b) Each CEMS must complete a minimum of one cycle of operation
(sampling, analyzing, and data recording) for each successive 30-minute
period within each batch monitoring period. Except as specified in
paragraph (c) of this section, you must have a minimum of two cycles of
operation in a 1-hour period to have a valid hour of data.
(c) The CEMS data must be reduced to arithmetic batch averages
computed from two or more data points over each 1-hour period, except
during periods when calibration, quality assurance, or maintenance
activities pursuant to provisions of this part are being performed.
During these periods, a valid hour of data shall consist of at least one
data point representing a 30-minute period.
(d) You must have valid CEMS data from at least 75 percent of the
full hours over the entire batch monitoring period.
(e) Set the CEMS span to correspond to not greater than 5 times the
relevant emission limit, with 1.5 to 2.5 times the relevant emission
limit being the range considered by us to be generally optimum. Use the
brew-to-exhaust correlation equation established under Sec. 63.2161(f)
to determine the span value for your CEMS that corresponds to the
relevant emission limit.
(f) For each CEMS, record the results of each inspection,
calibration, and validation check.
(g) The GC that you use to calibrate your CEMS must meet the
requirements of paragraphs (g)(1) through (3) of this section.
(1) Calibrate the GC at least daily, by analyzing standard solutions
of ethanol in water (0.05 percent, 0.15 percent, and 0.3 percent).
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(2) For use in calibrating the GC, prepare the standard solutions of
ethanol using the procedures listed in paragraphs (g)(2)(i) through (vi)
of this section.
(i) Starting with 100 percent ethanol, dry the ethanol by adding a
small amount of anhydrous magnesium sulfate (granular) to 15-20
milliliters (ml) of ethanol.
(ii) Place approximately 50 ml of water into a 100-ml volumetric
flask and place the flask on a balance. Tare the balance. Weigh 2.3670
grams of the dry (anhydrous) ethanol into the volumetric flask.
(iii) Add the 100-ml volumetric flask contents to a 1000-ml
volumetric flask. Rinse the 100-ml volumetric flask with water into the
1000-ml flask. Bring the volume to 1000 ml with water.
(iv) Place an aliquot into a sample bottle labeled ``0.3% Ethanol.''
(v) Fill a 50-ml volumetric flask from the contents of the 1000-ml
flask. Add the contents of the 50-ml volumetric flask to a 100-ml
volumetric flask and rinse the 50-ml flask into the 100-ml flask with
water. Bring the volume to 100 ml with water. Place the contents into a
sample bottle labeled ``0.15% Ethanol.''
(vi) With a 10-ml volumetric pipette, add two 10.0-ml volumes of
water to a sample bottle labeled ``0.05% Ethanol.'' With a 10.0-ml
volumetric pipette, pipette 10.0 ml of the 0.15 percent ethanol solution
into the sample bottle labeled ``0.05% Ethanol.''
(3) For use in calibrating the GC, dispense samples of the standard
solutions of ethanol in water in aliquots to appropriately labeled and
dated glass sample bottles fitted with caps having a Teflon[reg] seal.
Refrigerated samples may be kept unopened for 1 month. Prepare new
calibration standards of ethanol in water at least monthly.
(h) Calibrate the CEMS according to paragraphs (h)(1) through (3) of
this section.
(1) To calibrate the CEMS, inject a brew sample into a calibrated GC
and compare the simultaneous ethanol value given by the CEMS to that
given by the GC. Use either the Porapak[reg] Q, 80-100 mesh, 6[min] x
\1/8\[min], stainless steel packed column or the DB Wax, 0.53 mm x 30 m
capillary column.
(2) If a CEMS ethanol value differs by 20 percent or more from the
corresponding GC ethanol value, determine the brew ethanol values
throughout the rest of the batch monitoring period by injecting brew
samples into the GC not less frequently than every 30 minutes. From the
time at which the difference of 20 percent or more is detected until the
batch monitoring period ends, the GC data will serve as the CEMS data.
(3) Perform a calibration of the CEMS at least four times per batch.
Sec. 63.2165 How do I demonstrate initial compliance with the emission limitations if I monitor fermenter exhaust?
(a) You must demonstrate initial compliance with each emission
limitation that applies to you according to Table 3 to this subpart.
(b) You must submit the Notification of Compliance Status containing
the results of the initial compliance demonstration according to the
requirements in Sec. 63.2180(e).
Sec. 63.2166 How do I demonstrate initial compliance with the emission limitations if I monitor brew ethanol?
(a) You must demonstrate initial compliance with each emission
limitation that applies to you according to Table 3 to this subpart.
(b) You must establish the brew-to-exhaust correlation for each
fermentation stage according to Sec. 63.2161(e).
(c) You must submit the Notification of Compliance Status containing
the results of the initial compliance demonstration according to the
requirements in Sec. 63.2180(e).
Continuous Compliance Requirements
Sec. 63.2170 How do I monitor and collect data to demonstrate continuous compliance?
(a) You must monitor and collect data according to this section.
(b) Except for monitor malfunctions, associated repairs, and
required quality assurance or control activities (including, as
applicable, calibration checks and required zero and span adjustments),
you must monitor continuously during each batch monitoring period.
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(c) You may not use data recorded during monitoring malfunctions,
associated repairs, and required quality assurance or quality control
activities in data averages and calculations used to report emission or
operating levels, or to fulfill a minimum data availability requirement.
You must use all the data collected during all other periods in
assessing the operation of the control system.
Sec. 63.2171 How do I demonstrate continuous compliance with the emission limitations?
(a) You must demonstrate continuous compliance with each emission
limitation in Table 1 to this subpart that applies to you according to
methods specified in Table 4 to this subpart.
(b) You must calculate the percentage of within-concentration
batches (defined in Sec. 63.2192) for each 12-month period according to
paragraphs (b)(1) through (4) of this section.
(1) Determine the percentage of batches over a 12-month calculation
period that were in compliance with the applicable maximum
concentration. The total number of batches in the calculation period is
the sum of the numbers of batches of each fermentation stage for which
emission limits apply. To calculate the 12-month percentage, do not
include batches in production during periods of malfunction. In counting
the number of batches in the 12-month calculation period, include those
batches for which the batch monitoring period ended on or after 12 a.m.
on the first day of the period and exclude those batches for which the
batch monitoring period did not end on or before 11:59 p.m. on the last
day of the period.
(2) You must determine the 12-month percentage at the end of each
calendar month.
(3) The first 12-month calculation period begins on the compliance
date that is specified for your source in Sec. 63.2133 and ends on the
last day of the month that includes the date 365 days after your
compliance date, unless the compliance date for your source is the first
day of the month, in which case the first 12-month calculation period
ends on the last day of the month that is 11 calendar months after the
compliance date. (For example, if the compliance date for your source is
October 15, 2003, the first 12-month calculation period would begin on
October 15, 2003, and end on October 31, 2004. If the compliance date
for your source is October 1, 2003, the first 12-month calculation
period would begin on October 1, 2003, and end on September 30, 2004.)
(4) The second 12-month calculation period and each subsequent 12-
month calculation period begin on the first day of the month following
the first full month of the previous 12-month averaging period and end
on the last day of the month 11 calendar months later. (For example, if
the compliance date for your source is October 15, 2003, the second
calculation period would begin on December 1, 2003 and end on November
30, 2004.)
(c) You must report each instance (that is, each 12-month
calculation period) in which you did not meet each emission requirement
in Table 4 to this subpart that applies to you. (Failure of a single
batch to meet a concentration limit does not in and of itself constitute
a failure to meet the emission limitation.) Each instance in which you
failed to meet each applicable emission limitation is reported as part
of the requirements in Sec. 63.2181.
(d) During periods of malfunction, you must operate in accordance
with the malfunction plan.
Notification, Reports, and Records
Sec. 63.2180 What notifications must I submit and when?
(a) You must submit all of the notifications in Secs. 63.7(b) and
(c), 63.8(e), (f)(4) and (6), and 63.9(b) through (h) that apply to you
by the dates specified.
(b) If you start up your affected source before May 21, 2001, you
are not subject to the initial notification requirements of
Sec. 63.9(b)(2).
(c) If you are required to conduct a performance test as specified
in Table 2 to this subpart, you must submit a notification of intent to
conduct a performance test at least 60 calendar days before the
performance test is scheduled to begin as required in Sec. 63.7(b)(1).
(d) If you are required to conduct a performance evaluation as
specified in
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Sec. 63.2163(b), you must submit a notification of the date of the
performance evaluation at least 60 days prior to the date the
performance evaluation is scheduled to begin as required in
Sec. 63.8(e)(2).
(e) If you are required to conduct a performance test or other
initial compliance demonstration as specified in Table 2 or 3 to this
subpart, you must submit a Notification of Compliance Status according
to Sec. 63.9(h)(2)(ii) and according to paragraphs (e)(1) through (2) of
this section.
(1) For each initial compliance demonstration required in Table 3 to
this subpart that does not include a performance test, you must submit
the Notification of Compliance Status no later than July 31 or January
31, whichever date follows the end of the first 12 calendar months after
the compliance date that is specified for your source in Sec. 63.2133.
If your initial compliance demonstration does not include a performance
test, the first compliance report, described in Sec. 63.2181(b)(1),
serves as the Notice of Compliance Status.
(2) For each initial compliance demonstration required in Table 2 or
3 to this subpart that includes a performance test conducted according
to the requirements in Table 2, you must submit the Notification of
Compliance Status, including the performance test results, before the
close of business on the 60th calendar day following the completion of
the performance test according to Sec. 63.10(d)(2).
Sec. 63.2181 What reports must I submit and when?
(a) You must submit each report in Table 5 to this subpart that
applies to you.
(b) Unless the Administrator has approved a different schedule for
submission of reports under Sec. 63.10(a), you must submit each report
by the date in Table 5 to this subpart and according to paragraphs
(b)(1) through (5) of this section.
(1) The first compliance report must cover the period beginning on
the compliance date that is specified for your affected source in
Sec. 63.2133 and ending on either June 30 or December 31 (use whichever
date is the first date following the end of the first 12 calendar months
after the compliance date that is specified for your source in
Sec. 63.2133). The first compliance report must include the percentage
of within-concentration batches, as described in Sec. 63.2171(b), for
the first 12-month calculation period described in Sec. 63.2171(b)(3).
It must also include a percentage for each subsequent 12-month
calculation period, as described in Sec. 63.2171(b)(4), ending on a
calendar month that falls within the first compliance period. (For
example, if the compliance date for your source is October 15, 2003, the
first compliance report would cover the period from October 15, 2003 to
December 31, 2004. It would contain percentages for the 12-month periods
ending October 31, 2004; November 30, 2004; and December 31, 2004.)
(2) The first compliance report must be postmarked or delivered no
later than July 31 or January 31, whichever date follows the end of the
first 12 calendar months after the compliance date that is specified for
your affected source in Sec. 63.2133.
(3) Each subsequent compliance report must cover the semiannual
reporting period from January 1 through June 30 or the semiannual
reporting period from July 1 through December 31. Each subsequent
compliance report must include the percentage of within-concentration
batches for each 12-month calculation period ending on a calendar month
that falls within the reporting period. (For example, if the compliance
date for your source is October 15, 2003, the second compliance report
would cover the period from January 1, 2005 through June 30, 2005. It
would contain percentages for the 12-month periods ending January 31,
2005; February 28, 2005; March 31, 2005; April 30, 2005; May 31, 2005;
and June 30, 2005.)
(4) Each subsequent compliance report must be postmarked or
delivered no later than July 31 or January 31, whichever date is the
first date following the end of the semiannual reporting period.
(5) For each affected source that is subject to permitting
regulations pursuant to 40 CFR part 70 or part 71, and if the permitting
authority has established dates for submitting semiannual
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reports pursuant to 40 CFR 70.6(a)(3)(a)(iii)(A) or 40 CFR
71.6(a)(3)(a)(iii)(A), you may submit the first and subsequent
compliance reports according to the dates the permitting authority has
established instead of according to the dates in paragraphs (b)(1)
through (4) of this section.
(c) The compliance report must contain the information listed in
paragraphs (c)(1) through (5) of this section.
(1) Company name and address.
(2) Statement by a responsible official with that official's name,
title, and signature, certifying the accuracy of the content of the
report.
(3) Date of report and beginning and ending dates of the reporting
period.
(4) Percentage of batches that are within-concentration batches for
each 12-month period ending on a calendar month that falls within the
reporting period.
(5) If you had a malfunction during the reporting period and you
took actions consistent with your malfunction plan, the compliance
report must include the information in Sec. 63.10(d)(5)(i) for each
malfunction.
Sec. 63.2182 What records must I keep?
(a) You must keep the records listed in paragraphs (a)(1) through
(4) of this section. These include:
(1) A copy of each notification and report that you submitted to
comply with this subpart, including all documentation supporting any
Notification of Compliance Status and compliance report that you
submitted, according to the requirements in Sec. 63.10(b)(2)(xiv).
(2) The records in Sec. 63.6(e)(3)(iii) through (v) related to
malfunction;
(3) Records of performance tests and performance evaluations as
required in Sec. 63.10(b)(2)(viii); and
(4) Records of results of brew-to-exhaust correlation tests
specified in Sec. 63.2161.
(b) For each CEMS, you must keep the records listed in paragraphs
(b)(1) through (9) of this section. These include:
(1) Records described in Sec. 63.10 (b)(2)(vi);
(2) All required measurements needed to demonstrate compliance with
a relevant standard (including, but not limited to, 30-minute averages
of CEMS data, raw performance testing measurements, and raw performance
evaluation measurements, that support data that the source is required
to report);
(3) Records described in Sec. 63.10 (b)(2)(viii) through (xi). The
CEMS system must allow the amount of excess zero (low-level) and high-
level calibration drift measured at the interval checks to be quantified
and recorded;
(4) All required CEMS measurements (including monitoring data
recorded during unavoidable CEMS breakdowns and out-of-control periods);
(5) Identification of each batch during which the CEMS was
inoperative, except for zero (low-level) and high-level checks;
(6) Identification of each batch during which the CEMS was out of
control, as defined in Sec. 63.2163(k);
(7) Previous (i.e., superseded) versions of the performance
evaluation plan as required in Sec. 63.8(d)(3);
(8) Request for alternatives to relative accuracy test for CEMS as
required in Sec. 63.8(f)(6)(i); and
(9) Records of each batch for which the batch-average VOC
concentration exceeded the applicable maximum VOC concentration in Table
1 to this subpart and whether the batch was in production during a
period of malfunction or during another period.
(c) You must keep the records required in Table 4 to this subpart to
show continuous compliance with each emission limitation that applies to
you.
(d) You must also keep the records listed in paragraphs (d)(1)
through (3) of this section for each batch in your affected source.
(1) Unique batch identification number.
(2) Fermentation stage for which you are using the fermenter.
(3) Unique CEMS equipment identification number.
Sec. 63.2183 In what form and how long must I keep my records?
(a) Your records must be in a form suitable and readily available
for expeditious review, according to Sec. 63.10(b)(1).
(b) As specified in Sec. 63.10(b)(1), you must keep each record for
5 years following the date of each occurrence,
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measurement, maintenance, corrective action, report, or record.
(c) You must keep each record on site for at least 2 years after the
date of each occurrence, measurement, maintenance, corrective action,
report, or record, according to Sec. 63.10(b)(1). You can keep the
records offsite for the remaining 3 years.
Other Requirements and Information
Sec. 63.2190 What parts of the General Provisions apply to me?
Table 6 to this subpart shows which parts of the General Provisions
in Secs. 63.1 through 63.13 apply to you.
Sec. 63.2191 Who implements and enforces this subpart?
(a) This subpart can be implemented and enforced by us, the U.S.
EPA, or a delegated authority such as your State, local, or tribal
agency. If the U.S. EPA Administrator has delegated authority to your
State, local, or tribal agency, then that agency has the authority to
implement and enforce this subpart. You should contact your U.S. EPA
Regional Office to find out if this subpart is delegated to your State,
local, or tribal agency.
(b) In delegating implementation and enforcement authority of this
subpart to a State, local, or tribal agency under 40 CFR part 63,
subpart E, the authorities contained in paragraph (c) of this section
are retained by the Administrator of the U.S. EPA and are not
transferred to the State, local, or tribal agency.
(c) The authorities that will not be delegated to State, local, or
tribal agencies are as listed in paragraphs (c)(1) through (4) of this
section.
(1) Approval of alternatives to the non-opacity emission limitations
in Sec. 63.2140 under Sec. 63.6(g).
(2) Approval of major alternatives to test methods under
Sec. 63.7(e)(2)(ii) and (f) and as defined in Sec. 63.90.
(3) Approval of major alternatives to monitoring under Sec. 63.8(f)
and as defined in Sec. 63.90.
(4) Approval of major alternatives to recordkeeping and reporting
under Sec. 63.10(f) and as defined in Sec. 63.90.
Sec. 63.2192 What definitions apply to this subpart?
Terms used in this subpart are defined in the Clean Air Act, in 40
CFR 63.2, the General Provisions of this part, and in this section as
follows:
Batch means a single fermentation cycle in a single fermentation
vessel (fermenter).
Batch monitoring period means the period that begins at the later of
either the start of aeration or the addition of yeast to the fermenter;
the period ends at the earlier of either the end of aeration or the
point at which the yeast has begun being emptied from the fermenter.
Brew means the mixture of yeast and additives in the fermenter.
Brew ethanol means the ethanol in fermenter liquid.
Brew ethanol monitor means the monitoring system that you use to
measure brew ethanol to demonstrate compliance with this subpart. The
monitoring system includes a resistance element used as an ethanol
sensor, with the measured resistance proportional to the concentration
of ethanol in the brew.
Brew-to-exhaust correlation means the correlation between the
concentration of ethanol in the brew and the concentration of VOC in the
fermenter exhaust. This correlation is specific to each fed-batch
fermentation stage and is established while manufacturing the product
that comprises the largest percentage (by mass) of average annual
production.
Emission limitation means any emission limit or operating limit.
Fed-batch means the yeast is fed carbohydrates and additives during
fermentation in the vessel. In contrast, carbohydrates and additives are
added to ``set-batch'' fermenters only at the start of the batch.
1-hour period means any 60-minute period commencing on the minute at
which the batch monitoring period begins.
Product means the yeast resulting from the final stage in a
production run. Products are distinguished by yeast species, strain, and
variety.
Responsible official means responsible official as defined in 40 CFR
70.2.
[[Page 202]]
Specialty yeast includes but is not limited to yeast produced for
use in wine, champagne, whiskey, and beer.
Within-concentration batch means a batch for which the average VOC
concentration is not higher than the maximum concentration that is
allowed as part of the applicable emission limitation.
Tables
Table 1 to Subpart CCCC--Emission Limitations
As stated in Sec. 63.2140, you must comply with the emission
limitations in the following table:
------------------------------------------------------------------------
For each fed-batch fermenter producing
yeast in the following fermentation You must meet the following
stage . . . emission limitation . . .
------------------------------------------------------------------------
Last stage (Trade); or Second-to-last a. For at least 98 percent of
stage (First Generation); or Third-to- all batches (sum of batches
last stage (Stock). from last, second-to-last, and
third-to-last stages) in each
12-month calculation period
described in Sec. 63.2171(b),
the VOC concentration in the
fermenter exhaust does not
exceed the applicable maximum
concentration (100 ppmv for
last stage, 200 ppmv for
second-to-last stage, or 300
ppmv for third-to-last stage),
measured as propane, and
averaged over the duration of
a batch.
b. The emission limitation does
not apply during the
production of specialty yeast.
------------------------------------------------------------------------
Table 2 to Subpart CCCC--Requirements for Performance Tests
As stated in Sec. 63.2161, if you demonstrate compliance by monitoring
brew ethanol, you must comply with the requirements for performance
tests in the following table:
[Brew Ethanol Monitoring Only]
------------------------------------------------------------------------
For each fed-batch fermenter
for which compliance is
determined by monitoring
brew ethanol concentration
and calculating VOC According to the
concentration in the Using . . . following
fermenter exhaust according requirements . . .
to the procedures in Sec.
63.2161, you must . . .
------------------------------------------------------------------------
1. Measure VOC as propane... Method 25A*, or an You must measure the
alternative VOC concentration
validated by EPA in the fermenter
Method in the 301* exhaust at any
and approved by the point prior to
Administrator. dilution of the
exhaust stream.
2. Select the sampling Method 1* ....................
port's location and the
number of traverse points.
3. Measure volumetric flow Method 2* ....................
rate..
4. Perform gas analysis to Method 3* ....................
determine the dry molecular
weight of the stack gas.
5. Determine moisture Method 4* ....................
content of the stack gas.
------------------------------------------------------------------------
*EPA Test Methods found in appendix A of 40 CFR part 60.
As stated in Sec. 63.2165 (if you monitor fermenter exhaust) and
Sec. 63.2166 (if you monitor brew ethanol), you must comply with the
requirements to demonstrate initial compliance with the applicable
emission limitations in the following table:
Table 3 to Subpart CCCC--Initial Compliance With Emission Limitations
------------------------------------------------------------------------
For the following You have
For . . . emission limitation demonstrated initial
. . . compliance if . . .
------------------------------------------------------------------------
1. Each fed-batch fermenter The VOC a. You reduce the
producing yeast in a concentration in CEMS data batch
fermentation stage (last the fermenter averages according
Trade), second-to-last exhaust, averaged to Sec.
(First Generation), or over the duration 63.2163(g).
third-to-last (Stock)) for of the batch, does b. The average VOC
which compliance is not exceed the concentration in
determined by monitoring applicable maximum the fermenter
VOC concentration in the concentration (100 exhaust for at
fermenter exhaust. ppmv for last least 98 percent of
stage, 200 ppmv for the batches (sum of
second-to-last batches from last,
stage, or 300 ppmv second-to-last, and
for third-to-last third-to-last
stage), measured as stages) during the
propane.. initial compliance
period described in
Sec. 63.2160(a)
does not exceed the
applicable maximum
concentration.
[[Page 203]]
2. Each fed-batch fermenter The VOC a. The VOC fermenter
producing yeast in a concentration in exhaust
fermentation stage (last the fermenter concentration over
(Trade), second-to-last exhaust, averaged the period of the
(First Generation), or over the duration Method 25A*
third-to-last (Stock)) for of the batch, does performance test
which compliance is not exceed the does not exceed the
determined by monitoring applicable maximum applicable maximum
brew ethanol concentration concentration (100 concentration.
and calculating VOC ppmv for last b. You have a record
concentration in the stage, 2000 ppmv of the brew-to-
fermenter exhaust according for second-to-last exhaust correlation
to the procedures in Sec. stage, or 300 ppmv during the Method
63.2161. for third-to-last 25A* performance
stage), measured as test during which
propane. the VOC fermenter
exhaust
concentration did
not exceed the
applicable maximum
concentration.
------------------------------------------------------------------------
* EPA Test Method in appendix A of 40 CFR part 60.
As stated in Sec. 63.2171, you must comply with the requirements to
demonstrate continuous compliance with the applicable emission
limitations in the following table:
Table 4 to Subpart CCCC--Continuous Compliance With Emission Limitations
------------------------------------------------------------------------
For the following You must demonstrate
For . . . emission limitation continuous
. . . compliance by . . .
------------------------------------------------------------------------
1. Each fed-batch fermenter For at least 98 a. Collecting the
producing yeast in a percent of all monitoring data
fermentation stage (last batches (sum of according to Sec.
(Trade), second-to-last batches from last, 63.2163(f).
(First Generation), or second-to-last, and b. Reducing the data
third-to-last (Stock)) for third-to-last according to Sec.
which compliance is stages) in each 12- 63.2163(g).
determined by monitoring month calculation c. For at least 98
VOC concentration in the period described in percent of the
fermenter exhaust. Sec. 63.2171(b), batches (sum of
the VOC batches from last,
concentration in second-to-last, and
the fermenter third-to-last
exhaust, averaged stages) for each 12-
over the duration month period ending
of the batch, does within a semiannual
not exceed the reporting period
applicable maximum described in Sec.
concentration (100 63.2181(b)(3), the
ppmv for last batch average VOC
stage, 200 ppmv for concentration in
second-to-last the fermenter
stage, or 300 ppmv exhaust does not
for third-to-last exceed the
stage), measured as applicable maximum
propane. concentration.
2. Each fed-batch fermenter .For at least 98 a. Collecting the
producing yeast in a percent of all monitoring data
fermentation stage (last batches (sum of according to Sec.
(Trade), second-to-last batches from last, 63.2164(b).
(First Generation), or second-to-last, and b. Reducing the data
third-to-last (Stock)) for third-to-last according to Sec.
which compliance is stages) in each 12- 63.2164(c).
determined by monitoring month calculation c. For at least 98
brew ethanol concentration period described in percent of the
and calculating VOC Sec. 63.2171(b), batches (sum of
concentration in the the VOC batches from last,
fermenter exhaust according concentration in second-to-last, and
to the procedures in Sec. the fermenter third-to-last
63.2161. exhaust, averaged stages) for each 12-
over the duration month period ending
of the batch, does within a semiannual
not exceed the reporting period
applicable maximum described in Sec.
concentration (100 63.2181(b)(3), the
ppmvc for last batch average VOC
stage, 200 ppmv for concentration in
second-to-last the fermenter
stage, or 300 ppmv exhaust does not
for third-to-last exceed the
stage), measured as applicable maximum
propane. concentration.
------------------------------------------------------------------------
As stated in Sec. 63.2181, you must submit a compliance report that
contains the information in Sec. 63.2181(c) as well as the information
in the following table; you must also submit malfunction reports
according to the requirements in the following table:
Table 5 to Subpart CCCC--Requirements for Reports
------------------------------------------------------------------------
The report must You must submit the
You must submit a(n) contain . . . report . . .
------------------------------------------------------------------------
1. Compliance report........ a. Your calculated Semiannually
percentage of according to the
within- requirements in
concentration Sec. 63.2181(b).
batches, as
described in Sec.
63.2171(b), for 12-
month calculation
periods ending on
each calendar month
that falls within
the reporting
period.
[[Page 204]]
b. If you had a Semiannually
malfunction during according to the
the reporting requirements in
period and you took Sec. 63.2181(b).
actions consistent
with your
malfunction plan,
the compliance
report must include
the information in
Sec. 63.10(d)(5)(i
).
2. Immediate malfunction a. Actions taken for By fax or telephone
report if you had a the event. within 2 working
malfunction during the days after starting
reporting period that is actions
not consistent with your inconsistent with
malfunction plan. the plan.
b. The information By letter within 7
in Sec. working days after
63.10(d)(5)(ii). the end of the
event unless you
have made
alternative
arrangements with
the permitting
authority (Sec.
63.10(d)(5)(ii)).
------------------------------------------------------------------------
As stated in Sec. 63.2190, you must comply with the applicable
General Provisions requirements according to the following table:
Table 6 to Subpart CCCC--Applicability of General Provisions to Subpart
CCCC
------------------------------------------------------------------------
Applicable to
Citation Subject subpart CCCC?
------------------------------------------------------------------------
Sec. 63.1.................. Applicability....... Yes.
Sec. 63.2.................. Definitions......... Yes.
Sec. 63.3.................. Units and Yes.
Abbreviations.
Sec. 63.4.................. Prohibited Yes.
Activities and
Circumvention.
Sec. 63.5.................. Construction and Yes.
Reconstruction.
Sec. 63.6.................. Compliance With 1. For Sec. 63.6(e)
Standards and and (f),
Maintenance requirements for
Requirements. startup, shutdown,
and malfunctions
apply only to
malfunctions.
2. Sec. 63.6(h)
does not apply.
3. Otherwise, all
apply.
Sec. 63.7.................. Performance Testing 1. Sec. 63.7(a)(1)-
Requirements. (2) and (e)(3) do
not apply, instead
specified in this
subpart.
2. Otherwise, all
apply.
Sec. 63.8.................. Monitoring 1. Sec. 63.8(a)(2)
Requirements. is modified by Sec.
63.2163.
2. Sec. 63.8(a)(4)
does not apply.
3. For Sec.
63.8(c)(1),
requirements for
startup, shutdown,
and malfunctions
apply only to
malfunctions, and
no report pursuant
to Sec.
63.10(d)(5)(i) is
required.
4. For Sec.
63.8(d),
requirements for
startup, shutdown,
and malfunctions
apply only to
malfunctions.
5. Sec.
63.8(c)(4)(i),
(c)(5), (e)(5)(ii),
and (g)(5), do not
apply.
6. Sec.
63.8(c)(4)(ii),
(c)(6)-(8), (e)(4),
and (g)(1)-(4) do
not apply, instead
specified in this
subpart.
7. Otherwise, all
apply.
Sec. 63.9.................. Notification 1. Sec. 63.9(b)(2)
Requirements. does not apply
because rule omits
requirements for
initial
notification for
sources that start
up prior to May 21,
2001
2. Sec. 63.9(f)
does not apply.
3. Otherwise, all
apply.
Sec. 63.10................. Recordkeeping and 1. For Sec.
Reporting 63.10(b)(2)(i)-(v),
Requirements. (c)(9)-(15), and
(d)(5),
requirements for
startup, shutdown,
and malfunctions
apply only to
malfunctions.
2. Sec.
63.10(b)(2)(vii)
and (c)(1)-(6) do
not apply, instead
specified in this
subpart.
3. Sec. 63.10(c)(7)-
(8), (d)(3),
(e)(2)(ii)-(4),
(e)(3)-(4) do not
apply.
4. Otherwise, all
apply.
Sec. 63.11................. Flares.............. No.
Sec. 63.12................. Delegation.......... Yes.
Sec. 63.13................. Addresses........... Yes.
Sec. 63.14................. Incorporation by Yes.
Reference.
Sec. 63.15................. Availability of Yes.
Information.
------------------------------------------------------------------------
[[Page 205]]
Subpart GGGG--National Emission Standards for Hazardous Air Pollutants:
Solvent Extraction for Vegetable Oil Production
Source: 66 FR 19011, Apr. 12, 2001, unless otherwise noted.
What This Subpart Covers
Sec. 63.2830 What is the purpose of this subpart?
This subpart establishes national emission standards for hazardous
air pollutants (NESHAP) for emissions during vegetable oil production.
This subpart limits hazardous air pollutant (HAP) emissions from
specified vegetable oil production processes. This subpart also
establishes requirements to demonstrate initial and continuous
compliance with the emission standards.
Sec. 63.2831 Where can I find definitions of key words used in this subpart?
You can find definitions of key words used in this subpart in
Sec. 63.2872.
Sec. 63.2832 Am I subject to this subpart?
(a) You are an affected source subject to this subpart if you meet
all of the criteria listed in paragraphs (a)(1) and (2) of this section:
(1) You own or operate a vegetable oil production process that is a
major source of HAP emissions or is collocated within a plant site with
other sources that are individually or collectively a major source of
HAP emissions.
(i) A vegetable oil production process is defined in Sec. 63.2872.
In general, it is the collection of continuous process equipment and
activities that produce crude vegetable oil and meal products by
removing oil from oilseeds listed in Table 1 to Sec. 63.2840 through
direct contact with an organic solvent, such as a hexane isomer blend.
(ii) A major source of HAP emissions is a plant site that emits or
has the potential to emit any single HAP at a rate of 10 tons (9.07
megagrams) or more per year or any combination of HAP at a rate of 25
tons (22.68 megagrams) or more per year.
(2) Your vegetable oil production process processes any combination
of eight types of oilseeds listed in paragraphs (a)(2)(i) through (viii)
of this section:
(i) Corn germ;
(ii) Cottonseed;
(iii) Flax;
(iv) Peanut;
(v) Rapeseed (for example, canola);
(vi) Safflower;
(vii) Soybean; and
(viii) Sunflower.
(b) You are not subject to this subpart if your vegetable oil
production process meets any of the criteria listed in paragraphs (b)(1)
through (4) of this section:
(1) It uses only mechanical extraction techniques that use no
organic solvent to remove oil from a listed oilseed.
(2) It uses only batch solvent extraction and batch desolventizing
equipment.
(3) It processes only agricultural products that are not listed
oilseeds as defined in Sec. 63.2872.
(4) It functions only as a research and development facility and is
not a major source.
(c) As listed in Sec. 63.1(c)(5) of the General Provisions, if your
HAP emissions increase such that you become a major source, then you are
subject to all of the requirements of this subpart.
Sec. 63.2833 Is my source categorized as existing or new?
(a) This subpart applies to each existing and new affected source.
You must categorize your vegetable oil production process as either an
existing or a new source in accordance with the criteria in Table 1 of
this section, as follows:
Table 1 to Sec. 63.2833--Categorizing Your Source as Existing or New
------------------------------------------------------------------------
Then your affected
If your affected source... And if... source...
------------------------------------------------------------------------
(1) was constructed or began reconstruction has is an existing
construction before May 26, not occurred. source.
2000.
[[Page 206]]
(2) began reconstruction, as (i) reconstruction remains an
defined in Sec. 63.2, on or was part of a existing source.
after May 26, 2000. scheduled plan to
comply with the
existing source
requirements of
this subpart; and.
(ii)
reconstruction
was completed no
later than 3
years after the
effective date of
this subpart.
(3) began a significant the modification remains an
modification, as defined in does not existing source.
Sec. 63.2872, at any time on constitute
an existing source. reconstruction.
(4) began a significant the modification remains a new
modification, as defined in does not source.
Sec. 63.2872, at any time on a constitute
new source. reconstruction.
(5) began reconstruction on or reconstruction was is a new source
after May 26, 2000. completed later
than 3 years
after the
effective date of
this subpart.
(6) began construction on or .................. is a new source.
after May 26, 2000.
------------------------------------------------------------------------
(b) Reconstruction of a source. Any affected source is reconstructed
if components are replaced so that the criteria in the definition of
reconstruction in Sec. 63.2 are satisfied. In general, a vegetable oil
production process is reconstructed if the fixed capital cost of the new
components exceeds 50 percent of the fixed capital cost for constructing
a new vegetable oil production process, and it is technically and
economically feasible for the reconstructed source to meet the relevant
new source requirements of this subpart. The effect of reconstruction on
the categorization of your existing and new affected source is described
in paragraphs (b)(1) and (2) of this section:
(1) After reconstruction of an existing source, the affected source
is recategorized as a new source and becomes subject to the new source
requirements of this subpart.
(2) After reconstruction of a new source, the affected source
remains categorized as a new source and remains subject to the new
source requirements of this subpart.
(c) Significant modification of a source. A significant modification
to an affected source is a term specific to this subpart and is defined
in Sec. 63.2872.
(1) In general, a significant modification to your source consists
of adding new equipment or the modification of existing equipment within
the affected source that significantly affects solvent losses from the
affected source. Examples include adding or replacing extractors,
desolventizer-toasters (conventional and specialty), and meal dryer-
coolers. All other significant modifications must meet the criteria
listed in paragraphs (c)(1)(i) and (ii) of this section:
(i) The fixed capital cost of the modification represents a
significant percentage of the fixed capital cost of building a
comparable new vegetable oil production process.
(ii) It does not constitute reconstruction as defined in Sec. 63.2.
(2) A significant modification has no effect on the categorization
of your source as existing and new. An existing source remains
categorized as an existing source and subject to the existing source
requirements of this subpart. A new source remains categorized as a new
source and subject to the new source requirements of this subpart.
(d) Changes in the type of oilseed processed by your affected source
does not affect the categorization of your source as new or existing.
Recategorizing an affected source from existing to new occurs only when
you add or modify process equipment within the source which meets the
definition of reconstruction.
Sec. 63.2834 When do I have to comply with the standards in this subpart?
You must comply with this subpart in accordance with one of the
schedules in Table 1 of this section, as follows:
[[Page 207]]
Table 1 of Sec. 63.2834--Compliance Dates for Existing and New Sources
------------------------------------------------------------------------
Then your
If your affected source is And if... compliance date
categorized as... is...
------------------------------------------------------------------------
(a) an existing source.......... .................. 3 years after the
effective date of
this subpart.
(b) a new source................ you startup your the effective date
affected source of this subpart.
before the
effective date of
this subpart.
(c) a new source................ you startup your your startup date.
affected source
on or after the
effective date of
this subpart.
------------------------------------------------------------------------
Standards
Sec. 63.2840 What emission requirements must I meet?
(a)(1) The emission requirements limit the number of gallons of HAP
lost per ton of listed oilseeds processed. For each operating month, you
must calculate a compliance ratio which compares your actual HAP loss to
your allowable HAP loss for the previous 12 operating months as shown in
Equation 1 of this section. An operating month, as defined in
Sec. 63.2872, is any calendar month in which a source processes a listed
oilseed, excluding any entire calendar month in which the source
operated under an initial startup period subject to Sec. 63.2850(c)(2)
or (d)(2) or a malfunction period subject to Sec. 63.2850(e)(2).
Equation 1 of this section follows:
[GRAPHIC] [TIFF OMITTED] TR12AP01.001
(2) Equation 1 of this section can also be expressed as a function
of total solvent loss as shown in Equation 2 of this section. Equation 2
of this section follows:
[GRAPHIC] [TIFF OMITTED] TR12AP01.002
Where:
f = The weighted average volume fraction of HAP in solvent received
during the previous 12 operating months, as determined in Sec. 63.2854,
dimensionless.
0.64 = The average volume fraction of HAP in solvent in the baseline
performance data, dimensionless.
Actual Solvent Loss = Gallons of actual solvent loss during previous 12
operating months, as determined in Sec. 63.2853.
Oilseed = Tons of each oilseed type ``i'' processed during the previous
12 operating months, as shown in Sec. 63.2855.
SLF = The corresponding solvent loss factor (gal/ton) for oilseed ``i''
listed in Table 1 of this section, as follows:
[[Page 208]]
Table 1 of Sec. 63.2840--Oilseed Solvent Loss Factors for Determining
Allowable HAP Loss
------------------------------------------------------------------------
Oilseed solvent loss
factor (gal/ton)
Type of oilseed process A source that... ---------------------
Existing New
sources sources
------------------------------------------------------------------------
(i) Corn Germ, Wet Milling..... processes corn 0.4 0.3
germ that has
been separated
from other corn
components using
a ``wet''
process of
centrifuging a
slurry steeped
in a dilute
sulfurous acid
solution.
(ii) Corn Germ, Dry Milling.... processes corn 0.7 0.7
germ that has
been separated
from the other
corn components
using a ``dry''
process of
mechanical
chafing and air
sifting.
(iii) Cottonseed, Large........ processes 120,000 0.5 0.4
tons or more of
a combination of
cottonseed and
other listed
oilseeds during
all normal
operating
periods in a 12
operating month
period.
(iv) Cottonseed, Small......... processes less 0.7 0.4
than 120,000
tons of a
combination of
cottonseed and
other listed
oilseeds during
all normal
operating
periods in a 12
operating month
period.
(v) Flax....................... processes flax... 0.6 0.6
(vi) Peanuts................... processes peanuts 1.2 0.7
(vii) Rapeseed................. processes 0.7 0.3
rapeseed.
(viii) Safflower............... processes 0.7 0.7
safflower.
(ix) Soybean, Conventional..... uses a 0.2 0.2
conventional
style
desolventizer to
produce crude
soybean oil
products and
soybean animal
feed products.
(x) Soybean, Specialty......... uses a special 1.7 1.5
style
desolventizer to
produce soybean
meal products
for human and
animal
consumption.
(xi) Soybean, Combination Plant processes 0.25 0.25
with Low Specialty Production. soybeans in both
specialty and
conventional
desolventizers
and the quantity
of soybeans
processed in
specialty
desolventizers
during normal
operating
periods is less
than 3.3 percent
of total
soybeans
processed during
all normal
operating
periods in a 12
operating month
period. The
corresponding
solvent loss
factor is an
overall value
and applies to
the total
quantity of
soybeans
processed..
(xii) Sunflower................ processes 0.4 0.3
sunflower.
------------------------------------------------------------------------
(b) When your source has processed listed oilseed for 12 operating
months, calculate the compliance ratio by the end of each calendar month
following an operating month using Equation 2 of this section. When
calculating your compliance ratio, consider the conditions and
exclusions in paragraphs (b)(1) through (6) of this section:
(1) If your source processes any quantity of listed oilseeds in a
calendar month and the source is not operating under an initial startup
period or malfunction period subject to Sec. 63.2850, then you must
categorize the month as an operating month, as defined in Sec. 63.2872.
(2) The 12-month compliance ratio may include operating months
occurring prior to a source shutdown and operating months that follow
after the source resumes operation.
(3) If your source shuts down and processes no listed oilseed for an
entire calendar month, then you must categorize the month as a
nonoperating month, as defined in Sec. 63.2872. Exclude any nonoperating
months from the compliance ratio determination.
(4) If your source is subject to an initial startup period as
defined in Sec. 63.2872, exclude from the compliance ratio determination
any solvent and oilseed information recorded for the initial startup
period.
(5) If your source is subject to a malfunction period as defined in
Sec. 63.2872, exclude from the compliance ratio determination any
solvent and oilseed information recorded for the malfunction period.
(6) For sources processing cottonseed or specialty soybean, the
solvent loss
[[Page 209]]
factor you use to determine the compliance ratio may change each
operating month depending on the tons of oilseed processed during all
normal operating periods in a 12 operating month period.
(c) If the compliance ratio is less than or equal to 1.00, your
source was in compliance with the HAP emission requirements for the
previous operating month.
(d) To determine the compliance ratio in Equation 2 of this section,
you must select the appropriate oilseed solvent loss factor from Table 1
of this section. First, determine whether your source is new or existing
using Table 1 of Sec. 63.2833. Then, under the appropriate existing or
new source column, select the oilseed solvent loss factor that
corresponds to each type oilseed or process operation for each operating
month.
Compliance Requirements
Sec. 63.2850 How do I comply with the hazardous air pollutant emission standards?
(a) General requirements. The requirements in paragraphs (a)(1)(i)
through (iv) of this section apply to all affected sources:
(1) Submit the necessary notifications in accordance with
Sec. 63.2860, which include:
(i) Initial notifications for existing sources.
(ii) Initial notifications for new and reconstructed sources.
(iii) Initial notifications for significant modifications to
existing or new sources.
(iv) Notification of compliance status.
(2) Develop and implement a plan for demonstrating compliance in
accordance with Sec. 63.2851.
(3) Develop a written startup, shutdown and malfunction (SSM) plan
in accordance with the provisions in Sec. 63.2852.
(4) Maintain all the necessary records you have used to demonstrate
compliance with this subpart in accordance with Sec. 63.2862.
(5) Submit the reports in paragraphs (a)(5)(i) through (iii) of this
section:
(i) Annual compliance certifications in accordance with
Sec. 63.2861(a).
(ii) Periodic SSM reports in accordance with Sec. 63.2861(c).
(iii) Immediate SSM reports in accordance with Sec. 63.2861(d).
(6) Submit all notifications and reports and maintain all records
required by the General Provisions for performance testing if you add a
control device that destroys solvent.
(b) Existing sources under normal operation. You must meet all of
the requirements listed in paragraph (a) of this section and Table 1 of
this section for sources under normal operation, and the schedules for
demonstrating compliance for existing sources under normal operation in
Table 2 of this section.
(c) New sources. Your new source, including a source that is
categorized as new due to reconstruction, must meet the requirements
associated with one of two compliance options. Within 15 days of the
startup date, you must choose to comply with one of the options listed
in paragraph (c)(1) or (2) of this section:
(1) Normal operation. Upon startup of your new source, you must meet
all of the requirements listed in Sec. 63.2850(a) and Table 1 of this
section for sources under normal operation, and the schedules for
demonstrating compliance for new sources under normal operation in Table
2 of this section.
(2) Initial startup period. For up to 6 calendar months after the
startup date of your new source, you must meet all of the requirements
listed in paragraph (a) of this section and Table 1 of this section for
sources operating under an initial startup period, and the schedules for
demonstrating compliance for new sources operating under an initial
startup period in Table 2 of this section. After a maximum of 6 calendar
months, your new source must then meet all of the requirements listed in
Table 1 of this section for sources under normal operation.
(d) Existing or new sources that have been significantly modified.
Your existing or new source that has been significantly modified must
meet the requirements associated with one of two compliance options.
Within 15 days of the modified source startup date, you must
[[Page 210]]
choose to comply with one of the options listed in paragraph (d)(1) or
(2) of this section:
(1) Normal operation. Upon startup of your significantly modified
existing or new source, you must meet all of the requirements listed in
paragraph (a) of this section and Table 1 of this section for sources
under normal operation, and the schedules for demonstrating compliance
for an existing or new source that has been significantly modified in
Table 2 of this section.
(2) Initial startup period. For up to 3 calendar months after the
startup date of your significantly modified existing or new source, you
must meet all of the requirements listed in paragraph (a) of this
section and Table 1 of this section for sources operating under an
initial startup period, and the schedules for demonstrating compliance
for a significantly modified existing or new source operating under an
initial startup period in Table 2 of this section. After a maximum of 3
calendar months, your new or existing source must meet all of the
requirements listed in Table 1 of this section for sources under normal
operation.
(e) Existing or new sources experiencing a malfunction. A
malfunction is defined in Sec. 63.2. In general, it means any sudden,
infrequent, and not reasonably preventable failure of air pollution
control equipment or process equipment to function in a usual manner. If
your existing or new source experiences an unscheduled shutdown as a
result of a malfunction, continues to operate during a malfunction
(including the period reasonably necessary to correct the malfunction),
or starts up after a shutdown resulting from a malfunction, then you
must meet the requirements associated with one of two compliance
options. Routine or scheduled process startups and shutdowns resulting
from, but not limited to, market demands, maintenance activities, and
switching types of oilseed processed, are not startups or shutdowns
resulting from a malfunction and, therefore, do not qualify for this
provision. Within 15 days of the beginning date of the malfunction, you
must choose to comply with one of the options listed in paragraphs
(e)(1) through (2) of this section:
(1) Normal operation. Your source must meet all of the requirements
listed in paragraph (a) of this section and one of the options listed in
paragraphs (e)(1)(i) through (iii) of this section:
(i) Existing source normal operation requirements in paragraph (b)
of this section.
(ii) New source normal operation requirements in paragraph (c)(1) of
this section.
(iii) Normal operation requirements for sources that have been
significantly modified in paragraph (d)(1) of this section.
(2) Malfunction period. Throughout the malfunction period, you must
meet all of the requirements listed in paragraph (a) of this section and
Table 1 of this section for sources operating during a malfunction
period. At the end of the malfunction period, your source must then meet
all of the requirements listed in Table 1 of this section for sources
under normal operation. Table 1 of this section follows:
Table 1 of Sec. 63.2850--Requirements for Compliance with HAP Emission Standards
----------------------------------------------------------------------------------------------------------------
For initial startup
For periods of normal periods subject to Sec. For malfunction periods
Are you required to . . . operation? 63.2850(c)(2) or (d)(2)? subject to Sec.
63.2850(e)(2)?
----------------------------------------------------------------------------------------------------------------
(a) Operate and maintain your No, your source is Yes, throughout the Yes, throughout the entire
source in accordance with your not subject to the entire initial startup malfunction period.
SSM plan as described in Sec. SSM plan, but rather period.
63.2852?. the HAP emission
limits of this
standard.
(b) Determine and record the Yes, as described in Yes, as described in Sec. Yes, as described in Sec.
extraction solvent loss in Sec. 63.2853. 63.2862(e). 63.2862(e).
gallons from your source?.
(c) Record the volume fraction of Yes.................. Yes...................... Yes.
HAP present at greater than 1
percent by volume and gallons of
extraction solvent in shipment
received?.
[[Page 211]]
(d) Determine and record the tons Yes, as described in No....................... No.
of each oilseed type processed by Sec. 63.2855.
your source?.
(e) Determine the weighted average Yes.................. No. Except for solvent No, the HAP volume
volume fraction of HAP in received by a new or fraction in any solvent
extraction solvent received as reconstructed source received during a
described in Sec. 63.2854 by the commencing operation malfunction period is
end of the following calendar under an initial startup included in the weighted
month?. period, the HAP volume average HAP determination
fraction in any solvent for the next operating
received during an month.
initial startup period
is included in the
weighted average HAP
determination for the
next operating month.
(f) Determine and record the Yes,................. No, these requirements No, these requirements are
actual solvent loss, weighted are not applicable not applicable because
average volume fraction HAP, because your source is your source is not
oilseed processed and compliance not required to required to determine the
ratio for each 12 operating month determine the compliance compliance ratio with
period as described in Sec. ratio with data recorded data recorded for a
63.2840 by the end of the for an initial startup malfunction period.
following calendar month?. period.
(g) Submit a Notification of Yes, as described in No. However, you may be No. However, you may be
Compliance Status or Annual Secs. 63.2860(d) required to submit an required to submit an
Compliance Certification as and 63.2861(a). annual compliance annual compliance
appropriate?. certification for certification for
previous operating previous operating
months, if the deadline months, if the deadline
for the annual for the annual compliance
compliance certification certification happens to
happens to occur during occur during the
the initial startup malfunction period.
period.
(h) Submit a Deviation Yes.................. No, these requirements No, these requirements are
Notification Report by the end of are not applicable not applicable because
the calendar month following the because your source is your source is not
month in which you determined not required to required to determine the
that the compliance ratio exceeds determine the compliance compliance ratio with
1.00 as described in Sec. ratio with data recorded data recorded for a
63.2861(b)?. for an initial startup malfunction period.
period.
(i) Submit a Periodic SSM Report No, a SSM activity is Yes...................... Yes.
as described in Sec. 63.2861(c)?. not categorized as
normal operation.
(j) Submit an Immediate SSM Report No, a SSM activity is Yes, only if your source Yes, only if your source
as described in Sec. 63.2861(d)?. not categorized as does not follow the SSM does not follow the SSM
normal operation. plan. plan.
----------------------------------------------------------------------------------------------------------------
Table 2 of Sec. 63.2850--Schedules for Demonstrating Compliance Under Various Source Operating Modes
----------------------------------------------------------------------------------------------------------------
You must determine
your first Base your first
and is operating then your compliance ratio compliance ratio
If your source is . . . under. . . recordkeeping by the end of the on information
schedule. . . calendar month recorded. . .
following. . .
----------------------------------------------------------------------------------------------------------------
(a) Existing.................... Normal operation.. Begins on the The first 12 During the first
compliance date. operating months 12 operating
after the months after the
compliance date. compliance date.
(b) New......................... (1) Normal Begins on the The first 12 During the first
operation. startup date of operating months 12 operating
your new source. after the startup months after the
date of the new startup date of
source. the new source.
[[Page 212]]
(2) An initial Begins on the The first 12 During the first
startup period. startup date of operating months 12 operating
your new source. after termination months after the
of the initial initial startup
startup period, period, which can
which can last last for up to 6
for up to 6 months.
months.
(c) Existing or new that has (1) Normal Resumes on the The first During the
been significantly modified. operation. startup date of operating month previous 11
the modified after the startup operating months
source. date of the prior to the
modified source. significant
modification and
the first
operating month
following the
initial startup
date of the
source.
(2) An initial Resumes on the The first During the 11
startup period. startup date of operating month operating months
the modified after termination before the
source. of the initial significant
startup period, modification and
which can last up the first
to 3 months. operating month
after the initial
startup period.
----------------------------------------------------------------------------------------------------------------
Sec. 63.2851 What is a plan for demonstrating compliance?
(a) You must develop and implement a written plan for demonstrating
compliance that provides the detailed procedures you will follow to
monitor and record data necessary for demonstrating compliance with this
subpart. Procedures followed for quantifying solvent loss from the
source and amount of oilseed processed vary from source to source
because of site-specific factors such as equipment design
characteristics and operating conditions. Typical procedures include one
or more accurate measurement methods such as weigh scales, volumetric
displacement, and material mass balances. Because the industry does not
have a uniform set of procedures, you must develop and implement your
own site-specific plan for demonstrating compliance before the
compliance date for your source. You must also incorporate the plan for
demonstrating compliance by reference in the source's title V permit and
keep the plan on-site and readily available as long as the source is
operational. If you make any changes to the plan for demonstrating
compliance, then you must keep all previous versions of the plan and
make them readily available for inspection for at least 5 years after
each revision. The plan for demonstrating compliance must include the
items in paragraphs (a)(1) through (7) of this section:
(1) The name and address of the owner or operator.
(2) The physical address of the vegetable oil production process.
(3) A detailed description of all methods of measurement your source
will use to determine your solvent losses, HAP content of solvent, and
the tons of each type of oilseed processed.
(4) When each measurement will be made.
(5) Examples of each calculation you will use to determine your
compliance status. Include examples of how you will convert data
measured with one parameter to other terms for use in compliance
determination.
(6) Example logs of how data will be recorded.
(7) A plan to ensure that the data continue to meet compliance
demonstration needs.
(b) The responsible agency of these NESHAP may require you to revise
your plan for demonstrating compliance. The responsible agency may
require reasonable revisions if the procedures lack detail, are
inconsistent or do not accurately determine solvent
[[Page 213]]
loss, HAP content of the solvent, or the tons of oilseed processed.
Sec. 63.2852 What is a startup, shutdown, and malfunction plan?
You must develop a written SSM plan in accordance with
Sec. 63.6(e)(3) and implement the plan, when applicable. You must
complete the SSM plan before the compliance date for your source. You
must also keep the SSM plan on-site and readily available as long as the
source is operational.The SSM plan provides detailed procedures for
operating and maintaining your source to minimize emissions during a
qualifying SSM event for which the source chooses the Sec. 63.2850(e)(2)
malfunction period, or the Sec. 63.2850(c)(2) or (d)(2) initial startup
period. The SSM plan must specify a program of corrective action for
malfunctioning process and air pollution control equipment and reflect
the best practices now in use by the industry to minimize emissions.
Some or all of the procedures may come from plans you developed for
other purposes such as a Standard Operating Procedure manual or an
Occupational Safety and Health Administration Process Safety Management
plan. To qualify as a SSM plan, other such plans must meet all the
applicable requirements of these NESHAP.
[66 FR 19011, Apr. 12, 2001, as amended at 67 FR 16321, Apr. 5, 2002]
Sec. 63.2853 How do I determine the actual solvent loss?
By the end of each calendar month following an operating month, you
must determine the total solvent loss in gallons for the previous
operating month. The total solvent loss for an operating month includes
all solvent losses that occur during normal operating periods within the
operating month. If you have determined solvent losses for 12 or more
operating months, then you must also determine the 12 operating months
rolling sum of actual solvent loss in gallons by summing the monthly
actual solvent loss for the previous 12 operating months. The 12
operating months rolling sum of solvent loss is the ``actual solvent
loss,'' which is used to calculate your compliance ratio as described in
Sec. 63.2840.
(a) To determine the actual solvent loss from your source, follow
the procedures in your plan for demonstrating compliance to determine
the items in paragraphs (a)(1) through (7) of this section:
(1) The dates that define each operating status period during a
calendar month. The dates that define each operating status period
include the beginning date of each calendar month and the date of any
change in the source operating status. If the source maintains the same
operating status during an entire calendar month, these dates are the
beginning and ending dates of the calendar month. If, prior to the
effective date of this rule, your source determines the solvent loss on
an accounting month, as defined in Sec. 63.2872, rather than a calendar
month basis, and you have 12 complete accounting months of approximately
equal duration in a calendar year, you may substitute the accounting
month time interval for the calendar month time interval. If you choose
to use an accounting month rather than a calendar month, you must
document this measurement frequency selection in your plan for
demonstrating compliance, and you must remain on this schedule unless
you request and receive written approval from the agency responsible for
these NESHAP.
(2) Source operating status. You must categorize the operating
status of your source for each recorded time interval in accordance with
criteria in Table 1 of this section, as follows:
Table 1 of Sec. 63.2853--Categorizing Your Source Operating Status
------------------------------------------------------------------------
If during a recorded time interval . . then your source operating
. status is . . .
------------------------------------------------------------------------
(i) Your source processes any amount of A normal operating period.
listed oilseed and source is not
operating under an initial startup
operating period or a malfunction
period subject to Sec. 63.2850(c)(2),
(d)(2), or (e)(2).
(ii) Your source processes no A nonoperating period.
agricultural product and your source
is not operating under an initial
startup period or malfunction period
subject to Sec. 63.2850(c)(2),
(d)(2), or (e)(2).
[[Page 214]]
(iii) You choose to operate your source An initial startup period.
under an initial startup period
subject to Sec. 63.2850(c)(2) or
(d)(2).
(iv) You choose to operate your source A malfunction period.
under a malfunction period subject to
Sec. 63.2850(e)(2).
(v) Your source processes agricultural An exempt period.
products not defined as listed oilseed.
------------------------------------------------------------------------
(3) Measuring the beginning and ending solvent inventory. You are
required to measure and record the solvent inventory on the beginning
and ending dates of each normal operating period that occurs during an
operating month. An operating month is any calendar month with at least
one normal operating period. You must consistently follow the procedures
described in your plan for demonstrating compliance, as specified in
Sec. 63.2851, to determine the extraction solvent inventory, and
maintain readily available records of the actual solvent loss inventory,
as described in Sec. 63.2862(c)(1). In general, you must measure and
record the solvent inventory only when the source is actively processing
any type of agricultural product. When the source is not active, some or
all of the solvent working capacity is transferred to solvent storage
tanks which can artificially inflate the solvent inventory.
(4) Gallons of extraction solvent received. Record the total gallons
of extraction solvent received in each shipment. For most processes, the
gallons of solvent received represents purchases of delivered solvent
added to the solvent storage inventory. However, if your process refines
additional vegetable oil from off-site sources, recovers solvent from
the off-site oil, and adds it to the on-site solvent inventory, then you
must determine the quantity of recovered solvent and include it in the
gallons of extraction solvent received.
(5) Solvent inventory adjustments. In some situations, solvent
losses determined directly from the measured solvent inventory and
quantity of solvent received is not an accurate estimate of the ``actual
solvent loss'' for use in determining compliance ratios. In such cases,
you may adjust the total solvent loss for each normal operating period
as long as you provide a reasonable justification for the adjustment.
Situations that may require adjustments of the total solvent loss
include, but are not limited to, situations in paragraphs (a)(5)(i) and
(ii) of this section:
(i) Solvent destroyed in a control device. You may use a control
device to reduce solvent emissions to meet the emission standard. The
use of a control device does not alter the emission limit for the
source. If you use a control device that reduces solvent emissions
through destruction of the solvent instead of recovery, then determine
the gallons of solvent that enter the control device and are destroyed
there during each normal operating period. All solvent destroyed in a
control device during a normal operating period can be subtracted from
the total solvent loss. Examples of destructive emission control devices
include catalytic incinerators, boilers, or flares. Identify and
describe, in your plan for demonstrating compliance, each type of
reasonable and sound measurement method that you use to quantify the
gallons of solvent entering and exiting the control device and to
determine the destruction efficiency of the control device. You may use
design evaluations to document the gallons of solvent destroyed or
removed by the control device instead of performance testing under
Sec. 63.7. The design evaluations must be based on the procedures and
options described in Sec. 63.985(b)(1)(i)(A) through (C) or Sec. 63.11,
as appropriate. All data, assumptions, and procedures used in such
evaluations must be documented and available for inspection. If you use
performance testing to determine solvent flow rate to the control device
or destruction efficiency of the device, follow the procedures as
outlined in Sec. 63.997(e)(1) and (2). Instead of periodic performance
testing to demonstrate continued good operation of the control device,
you
[[Page 215]]
may develop a monitoring plan, following the procedures outlined in
Sec. 63.988(c) and using operational parametric measurement devices such
as fan parameters, percent measurements of lower explosive limits, and
combustion temperature.
(ii) Changes in solvent working capacity. In records you keep on-
site, document any process modifications resulting in changes to the
solvent working capacity in your vegetable oil production process.
Solvent working capacity is defined in Sec. 63.2872. In general, solvent
working capacity is the volume of solvent normally retained in solvent
recovery equipment such as the extractor, desolventizer-toaster, solvent
storage, working tanks, mineral oil absorber, condensers, and oil/
solvent distillation system. If the change occurs during a normal
operating period, you must determine the difference in working solvent
volume and make a one-time documented adjustment to the solvent
inventory.
(b) Use Equation 1 of this section to determine the actual solvent
loss occurring from your affected source for all normal operating
periods recorded within a calendar month. Equation 1 of this section
follows:
[GRAPHIC] [TIFF OMITTED] TR12AP01.003
Where:
SOLVB = Gallons of solvent in the inventory at the beginning
of normal operating period ``i'' as determined in paragraph (a)(3) of
this section.
SOLVE = Gallons of solvent in the inventory at the end of
normal operating period ``i'' as determined in paragraph (a)(3) of this
section.
SOLVR = Gallons of solvent received between the beginning and
ending inventory dates of normal operating period ``i'' as determined in
paragraph (a)(4) of this section.
SOLVA = Gallons of solvent added or removed from the
extraction solvent inventory during normal operating period ``i'' as
determined in paragraph (a)(5) of this section.
n = Number of normal operating periods in a calendar month.
(c) The actual solvent loss is the total solvent losses during
normal operating periods for the previous 12 operating months. You
determine your actual solvent loss by summing the monthly actual solvent
losses for the previous 12 operating months. You must record the actual
solvent loss by the end of each calendar month following an operating
month. Use the actual solvent loss in Equation 2 of Sec. 63.2840 to
determine the compliance ratio. Actual solvent loss does not include
losses that occur during operating status periods listed in paragraphs
(c)(1) through (4) of this section. If any one of these four operating
status periods span an entire month, then the month is treated as
nonoperating and there is no compliance ratio determination.
(1) Nonoperating periods as described in paragraph (a)(2)(ii) of
this section.
(2) Initial startup periods as described in Sec. 63.2850(c)(2) or
(d)(2).
(3) Malfunction periods as described in Sec. 63.2850(e)(2).
(4) Exempt operation periods as described in paragraph (a)(2)(v) of
this section.
Sec. 63.2854 How do I determine the weighted average volume fraction of HAP in the actual solvent loss?
(a) This section describes the information and procedures you must
use to determine the weighted average volume fraction of HAP in
extraction solvent received for use in your vegetable oil production
process. By the end of each calendar month following an operating month,
determine the weighted average volume fraction of HAP in extraction
solvent received since the end of the previous operating month. If you
have determined the monthly weighted average volume fraction of HAP in
solvent received for 12 or more operating
[[Page 216]]
months, then also determine an overall weighted average volume fraction
of HAP in solvent received for the previous 12 operating months. Use the
volume fraction of HAP determined as a 12 operating months weighted
average in Equation 2 of Sec. 63.2840 to determine the compliance ratio.
(b) To determine the volume fraction of HAP in the extraction
solvent determined as a 12 operating months weighted average, you must
comply with paragraphs (b)(1) through (3) of this section:
(1) Record the volume fraction of each HAP comprising more than 1
percent by volume of the solvent in each delivery of solvent, including
solvent recovered from off-site oil. To determine the HAP content of the
material in each delivery of solvent, the reference method is EPA Method
311 of appendix A of this part. You may use EPA Method 311, an approved
alternative method, or any other reasonable means for determining the
HAP content. Other reasonable means of determining HAP content include,
but are not limited to, a material safety data sheet or a manufacturer's
certificate of analysis. A certificate of analysis is a legal and
binding document provided by a solvent manufacturer. The purpose of a
certificate of analysis is to list the test methods and analytical
results that determine chemical properties of the solvent and the volume
percentage of all HAP components present in the solvent at quantities
greater than 1 percent by volume. You are not required to test the
materials that you use, but the Administrator may require a test using
EPA Method 311 (or an approved alternative method) to confirm the
reported HAP content. However, if the results of an analysis by EPA
Method 311 are different from the HAP content determined by another
means, the EPA Method 311 results will govern compliance determinations.
(2) Determine the weighted average volume fraction of HAP in the
extraction solvent each operating month. The weighted average volume
fraction of HAP for an operating month includes all solvent received
since the end of the last operating month, regardless of the operating
status at the time of the delivery. Determine the monthly weighted
average volume fraction of HAP by summing the products of the HAP volume
fraction of each delivery and the volume of each delivery and dividing
the sum by the total volume of all deliveries as expressed in Equation 1
of this section. Record the result by the end of each calendar month
following an operating month. Equation 1 of this section follows:
[GRAPHIC] [TIFF OMITTED] TR12AP01.004
Where:
Receivedi = Gallons of extraction solvent received in
delivery ``i.''
Contenti = The volume fraction of HAP in extraction solvent
delivery ``i.''
Total Received = Total gallons of extraction solvent received since the
end of the previous operating month.
n = Number of extraction solvent deliveries since the end of the
previous operating month.
(3) Determine the volume fraction of HAP in your extraction solvent
as a 12 operating months weighted average. When your source has
processed oilseed for 12 operating months, sum the products of the
monthly weighted average HAP volume fraction and corresponding volume of
solvent received, and divide the sum by the total volume of solvent
received for the 12 operating months, as expressed by Equation 2 of this
section. Record the result by the end of each calendar month following
[[Page 217]]
an operating month and use it in Equation 2 of Sec. 63.2840 to determine
the compliance ratio. Equation 2 of this section follows:
[GRAPHIC] [TIFF OMITTED] TR12AP01.005
Where:
Receivedi = Gallons of extraction solvent received in
operating month ``i'' as determined in accordance with
Sec. 63.2853(a)(4).
Contenti = Average volume fraction of HAP in extraction
solvent received in operating month ``i'' as determined in accordance
with paragraph (b)(1) of this section.
Total Received = Total gallons of extraction solvent received during the
previous 12 operating months.
Sec. 63.2855 How do I determine the quantity of oilseed processed?
All oilseed measurements must be determined on an as received basis,
as defined in Sec. 63.2872. The as received basis refers to the oilseed
chemical and physical characteristics as initially received by the
source and prior to any oilseed handling and processing. By the end of
each calendar month following an operating month, you must determine the
tons as received of each listed oilseed processed for the operating
month. The total oilseed processed for an operating month includes the
total of each oilseed processed during all normal operating periods that
occur within the operating month. If you have determined the tons of
oilseed processed for 12 or more operating months, then you must also
determine the 12 operating months rolling sum of each type oilseed
processed by summing the tons of each type of oilseed processed for the
previous 12 operating months. The 12 operating months rolling sum of
each type of oilseed processed is used to calculate the compliance ratio
as described in Sec. 63.2840.
(a) To determine the tons as received of each type of oilseed
processed at your source, follow the procedures in your plan for
demonstrating compliance to determine the items in paragraphs (a)(1)
through (5) of this section:
(1) The dates that define each operating status period. The dates
that define each operating status period include the beginning date of
each calendar month and the date of any change in the source operating
status. If, prior to the effective date of this rule, your source
determines the oilseed inventory on an accounting month rather than a
calendar month basis, and you have 12 complete accounting months of
approximately equal duration in a calendar year, you may substitute the
accounting month time interval for the calendar month time interval. If
you choose to use an accounting month rather than a calendar month, you
must document this measurement frequency selection in your plan for
demonstrating compliance, and you must remain on this schedule unless
you request and receive written approval from the agency responsible for
these NESHAP. The dates on each oilseed inventory log must be consistent
with the dates recorded for the solvent inventory.
(2) Source operating status. You must categorize the source
operation for each recorded time interval. The source operating status
for each time interval recorded on the oilseed inventory for each type
of oilseed must be consistent with the operating status recorded on the
solvent inventory logs as described in Sec. 63.2853(a)(2).
(3) Measuring the beginning and ending inventory for each oilseed.
You are required to measure and record the oilseed inventory on the
beginning and ending dates of each normal operating period that occurs
during an operating month. An operating month is any calendar month with
at least one normal
[[Page 218]]
operating period. You must consistently follow the procedures described
in your plan for demonstrating compliance, as specified in Sec. 63.2851,
to determine the oilseed inventory on an as received basis and maintain
readily available records of the oilseed inventory as described by
Sec. 63.2862(c)(3).
(4) Tons of each oilseed received. Record the type of oilseed and
tons of each shipment of oilseed received and added to your on-site
storage.
(5) Oilseed inventory adjustments. In some situations, determining
the quantity of oilseed processed directly from the measured oilseed
inventory and quantity of oilseed received is not an accurate estimate
of the tons of oilseed processed for use in determining compliance
ratios. For example, spoiled and molded oilseed removed from storage but
not processed by your source will result in an overestimate of the
quantity of oilseed processed. In such cases, you must adjust the
oilseed inventory and provide a justification for the adjustment.
Situations that may require oilseed inventory adjustments include, but
are not limited to, the situations listed in paragraphs (a)(5)(i)
through (v) of this section:
(i) Oilseed that mold or otherwise become unsuitable for processing.
(ii) Oilseed you sell before it enters the processing operation.
(iii) Oilseed destroyed by an event such as a process malfunction,
fire, or natural disaster.
(iv) Oilseed processed through operations prior to solvent
extraction such as screening, dehulling, cracking, drying, and
conditioning; but that are not routed to the solvent extractor for
further processing.
(v) Periodic physical measurements of inventory. For example, some
sources periodically empty oilseed storage silos to physically measure
the current oilseed inventory. This periodic measurement procedure
typically results in a small inventory correction. The correction
factor, usually less than 1 percent, may be used to make an adjustment
to the source's oilseed inventory that was estimated previously with
indirect measurement techniques. To make this adjustment, your plan for
demonstrating compliance must provide for such an adjustment.
(b) Use Equation 1 of this section to determine the quantity of each
oilseed type processed at your affected source during normal operating
periods recorded within a calendar month. Equation 1 of this section
follows:
[GRAPHIC] [TIFF OMITTED] TR12AP01.000
Where:
SEEDB = Tons of oilseed in the inventory at the beginning of
normal operating period ``i'' as determined in accordance with paragraph
(a)(3) of this section.
SEEDE = Tons of oilseed in the inventory at the end of normal
operating period ``i'' as determined in accordance with paragraph (a)(3)
of this section.
SEEDR = Tons of oilseed received during normal operating
period ``i'' as determined in accordance with paragraph (a)(4) of this
section.
SEEDA = Tons of oilseed added or removed from the oilseed
inventory during normal operating period ``i'' as determined in
accordance with paragraph (a)(5) of this section.
n = Number of normal operating periods in the calendar month during
which this type oilseed was processed.
(c) The quantity of each oilseed processed is the total tons of each
type of listed oilseed processed during normal operating periods in the
previous 12 operating months. You determine the tons of each oilseed
processed by summing the monthly quantity of each oilseed processed for
the previous 12 operating months. You must record the 12 operating
months quantity of each type of oilseed processed by the end of
[[Page 219]]
each calendar month following an operating month. Use the 12 operating
months quantity of each type of oilseed processed to determine the
compliance ratio as described in Sec. 63.2840. The quantity of oilseed
processed does not include oilseed processed during the operating status
periods in paragraphs (c)(1) through (4) of this section:
(1) Nonoperating periods as described in Sec. 63.2853 (a)(2)(ii).
(2) Initial startup periods as described in Sec. 63.2850(c)(2) or
(d)(2).
(3) Malfunction periods as described in Sec. 63.2850(e)(2).
(4) Exempt operation periods as described in Sec. 63.2853 (a)(2)(v).
(5) If any one of these four operating status periods span an entire
calendar month, then the calendar month is treated as a nonoperating
month and there is no compliance ratio determination.
Notifications, Reports, and Records
Sec. 63.2860 What notifications must I submit and when?
You must submit the one-time notifications listed in paragraphs (a)
through (d) of this section to the responsible agency:
(a) Initial notification for existing sources. For an existing
source, submit an initial notification to the agency responsible for
these NESHAP no later than 120 days after the effective date of this
subpart. In the notification, include the items in paragraphs (a)(1)
through (5) of this section:
(1) The name and address of the owner or operator.
(2) The physical address of the vegetable oil production process.
(3) Identification of the relevant standard, such as the vegetable
oil production NESHAP, and compliance date.
(4) A brief description of the source including the types of listed
oilseeds processed, nominal operating capacity, and type of
desolventizer(s) used.
(5) A statement designating the source as a major source of HAP or a
demonstration that the source meets the definition of an area source. An
area source is a source that is not a major source and is not collocated
within a plant site with other sources that are individually or
collectively a major source.
(b) Initial notifications for new and reconstructed sources. New or
reconstructed sources must submit a series of notifications before,
during, and after source construction per the schedule listed in
Sec. 63.9. The information requirements for the notifications are the
same as those listed in the General Provisions with the exceptions
listed in paragraphs (b)(1) and (2) of this section:
(1) The application for approval of construction does not require
the specific HAP emission data required in Sec. 63.5(d)(1)(ii)(H) and
(iii), (d)(2) and (d)(3)(ii). The application for approval of
construction would include, instead, a brief description of the source
including the types of listed oilseeds processed, nominal operating
capacity, and type of desolventizer(s) used.
(2) The notification of actual startup date must also include
whether you have elected to operate under an initial startup period
subject to Sec. 63.2850(c)(2) and provide an estimate and justification
for the anticipated duration of the initial startup period.
(c) Significant modification notifications. Any existing or new
source that plans to undergo a significant modification as defined in
Sec. 63.2872 must submit two reports as described in paragraphs (c)(1)
and (2) of this section:
(1) Initial notification. You must submit an initial notification to
the agency responsible for these NESHAP 30 days prior to initial startup
of the significantly modified source. The initial notification must
demonstrate that the proposed changes qualify as a significant
modification. The initial notification must include the items in
paragraphs (c)(1)(i) and (ii) of this section:
(i) The expected startup date of the modified source.
(ii) A description of the significant modification including a list
of the equipment that will be replaced or modified. If the significant
modification involves changes other than adding or replacing extractors,
desolventizer-toasters (conventional and specialty), and meal dryer-
coolers, then you must also include the fixed capital cost of the new
components, expressed as a percentage of the fixed capital cost to build
a comparable new
[[Page 220]]
vegetable oil production process; supporting documentation for the cost
estimate; and documentation that the proposed changes will significantly
affect solvent losses.
(2) Notification of actual startup. You must submit a notification
of actual startup date within 15 days after initial startup of the
modified source. The notification must include the items in paragraphs
(c)(2)(i) through (iv) of this section:
(i) The initial startup date of the modified source.
(ii) An indication whether you have elected to operate under an
initial startup period subject to Sec. 63.2850(d)(2).
(iii) The anticipated duration of any initial startup period.
(iv) A justification for the anticipated duration of any initial
startup period.
(d) Notification of compliance status. As an existing, new, or
reconstructed source, you must submit a notification of compliance
status report to the responsible agency no later than 60 days after
determining your initial 12 operating months compliance ratio. If you
are an existing source, you generally must submit this notification no
later than 50 calendar months after the effective date of these NESHAP
(36 calendar months for compliance, 12 operating months to record data,
and 2 calendar months to complete the report). If you are a new or
reconstructed source, the notification of compliance status is generally
due no later than 20 calendar months after initial startup (6 calendar
months for the initial startup period, 12 operating months to record
data, and 2 calendar months to complete the report). The notification of
compliance status must contain the items in paragraphs (d)(1) through
(6) of this section:
(1) The name and address of the owner or operator.
(2) The physical address of the vegetable oil production process.
(3) Each listed oilseed type processed during the previous 12
operating months.
(4) Each HAP identified under Sec. 63.2854(a) as being present in
concentrations greater than 1 percent by volume in each delivery of
solvent received during the 12 operating months period used for the
initial compliance determination.
(5) A statement designating the source as a major source of HAP or a
demonstration that the source qualifies as an area source. An area
source is a source that is not a major source and is not collocated
within a plant site with other sources that are individually or
collectively a major source.
(6) A compliance certification indicating whether the source
complied with all of the requirements of this subpart throughout the 12
operating months used for the initial source compliance determination.
This certification must include a certification of the items in
paragraphs (d)(6)(i) through (iii) of this section:
(i) The plan for demonstrating compliance (as described in
Sec. 63.2851) and SSM plan (as described in Sec. 63.2852) are complete
and available on-site for inspection.
(ii) You are following the procedures described in the plan for
demonstrating compliance.
(iii) The compliance ratio is less than or equal to 1.00.
Sec. 63.2861 What reports must I submit and when?
After the initial notifications, you must submit the reports in
paragraphs (a) through (d) of this section to the agency responsible for
these NESHAP at the appropriate time intervals:
(a) Annual compliance certifications. The first annual compliance
certification is due 12 calendar months after you submit the
notification of compliance status. Each subsequent annual compliance
certification is due 12 calendar months after the previous annual
compliance certification. The annual compliance certification provides
the compliance status for each operating month during the 12 calendar
months period ending 60 days prior to the date on which the report is
due. Include the information in paragraphs (a)(1) through (6) of this
section in the annual certification:
(1) The name and address of the owner or operator.
(2) The physical address of the vegetable oil production process.
[[Page 221]]
(3) Each listed oilseed type processed during the 12 calendar months
period covered by the report.
(4) Each HAP identified under Sec. 63.2854(a) as being present in
concentrations greater than 1 percent by volume in each delivery of
solvent received during the 12 calendar months period covered by the
report.
(5) A statement designating the source as a major source of HAP or a
demonstration that the source qualifies as an area source. An area
source is a source that is not a major source and is not collocated
within a plant site with other sources that are individually or
collectively a major source.
(6) A compliance certification to indicate whether the source was in
compliance for each compliance determination made during the 12 calendar
months period covered by the report. For each such compliance
determination, you must include a certification of the items in
paragraphs (a)(6)(i) through (ii) of this section:
(i) You are following the procedures described in the plan for
demonstrating compliance.
(ii) The compliance ratio is less than or equal to 1.00.
(b) Deviation notification report. Submit a deviation report for
each compliance determination you make in which the compliance ratio
exceeds 1.00 as determined under Sec. 63.2840(c). Submit the deviation
report by the end of the month following the calendar month in which you
determined the deviation. The deviation notification report must include
the items in paragraphs (b)(1) through (4) of this section:
(1) The name and address of the owner or operator.
(2) The physical address of the vegetable oil production process.
(3) Each listed oilseed type processed during the 12 operating
months period for which you determined the deviation.
(4) The compliance ratio comprising the deviation. You may reduce
the frequency of submittal of the deviation notification report if the
agency responsible for these NESHAP does not object as provided in
Sec. 63.10(e)(3)(iii).
(c) Periodic startup, shutdown, and malfunction report. If you
choose to operate your source under an initial startup period subject to
Sec. 63.2850(c)(2) or (d)(2) or a malfunction period subject to
Sec. 63.2850(e)(2), you must submit a periodic SSM report by the end of
the calendar month following each month in which the initial startup
period or malfunction period occurred. The periodic SSM report must
include the items in paragraphs (c)(1) through (3) of this section:
(1) The name, title, and signature of a source's responsible
official who is certifying that the report accurately states that all
actions taken during the initial startup or malfunction period were
consistent with the SSM plan.
(2) A description of events occurring during the time period, the
date and duration of the events, and reason the time interval qualifies
as an initial startup period or malfunction period.
(3) An estimate of the solvent loss during the initial startup or
malfunction period with supporting documentation.
(d) Immediate SSM reports. If you handle a SSM during an initial
startup period subject to Sec. 63.2850(c)(2) or (d)(2) or a malfunction
period subject to Sec. 63.2850(e)(2) differently from procedures in the
SSM plan and the relevant emission requirements in Sec. 63.2840 are
exceeded, then you must submit an immediate SSM report. Immediate SSM
reports consist of a telephone call or facsimile transmission to the
responsible agency within 2 working days after starting actions
inconsistent with the SSM plan, followed by a letter within 7 working
days after the end of the event. The letter must include the items in
paragraphs (d)(1) through (3) of this section:
(1) The name, title, and signature of a source's responsible
official who is certifying the accuracy of the report, an explanation of
the event, and the reasons for not following the SSM plan.
(2) A description and date of the SSM event, its duration, and
reason it qualifies as a SSM.
(3) An estimate of the solvent loss for the duration of the SSM
event with supporting documentation.
[66 FR 19011, Apr. 12, 2001, as amended at 67 FR 16321, Apr. 5, 2002]
[[Page 222]]
Sec. 63.2862 What records must I keep?
(a) You must satisfy the recordkeeping requirements of this section
by the compliance date for your source specified in Table 1 of
Sec. 63.2834.
(b) Prepare a plan for demonstrating compliance (as described in
Sec. 63.2851) and a SSM plan (as described in Sec. 63.2852). In these
two plans, describe the procedures you will follow in obtaining and
recording data, and determining compliance under normal operations or a
SSM subject to the Sec. 63.2850(c)(2) or (d)(2) initial startup period
or the Sec. 63.2850(e)(2) malfunction period. Complete both plans before
the compliance date for your source and keep them on-site and readily
available as long as the source is operational.
(c) If your source processes any listed oilseed, record the items in
paragraphs (c)(1) through (5) of this section:
(1) For the solvent inventory, record the information in paragraphs
(c)(1)(i) through (vii) of this section in accordance with your plan for
demonstrating compliance:
(i) Dates that define each operating status period during a calendar
month.
(ii) The operating status of your source such as normal operation,
nonoperating, initial startup period, malfunction period, or exempt
operation for each recorded time interval.
(iii) Record the gallons of extraction solvent in the inventory on
the beginning and ending dates of each normal operating period.
(iv) The gallons of all extraction solvent received, purchased, and
recovered during each calendar month.
(v) All extraction solvent inventory adjustments, additions or
subtractions. You must document the reason for the adjustment and
justify the quantity of the adjustment.
(vi) The total solvent loss for each calendar month, regardless of
the source operating status.
(vii) The actual solvent loss in gallons for each operating month.
(2) For the weighted average volume fraction of HAP in the
extraction solvent, you must record the items in paragraphs (c)(2)(i)
through (iii) of this section:
(i) The gallons of extraction solvent received in each delivery.
(ii) The volume fraction of each HAP exceeding 1 percent by volume
in each delivery of extraction solvent.
(iii) The weighted average volume fraction of HAP in extraction
solvent received since the end of the last operating month as determined
in accordance with Sec. 63.2854(b)(2).
(3) For each type of listed oilseed processed, record the items in
paragraphs (c)(3)(i) through (vi) of this section, in accordance with
your plan for demonstrating compliance:
(i) The dates that define each operating status period. These dates
must be the same as the dates entered for the extraction solvent
inventory.
(ii) The operating status of your source such as normal operation,
nonoperating, initial startup period, malfunction period, or exempt
operation for each recorded time interval. On the log for each type of
listed oilseed that is not being processed during a normal operating
period, you must record which type of listed oilseed is being processed
in addition to the source operating status.
(iii) The oilseed inventory for the type of listed oilseed being
processed on the beginning and ending dates of each normal operating
period.
(iv) The tons of each type of listed oilseed received at the
affected source each normal operating period.
(v) All listed oilseed inventory adjustments, additions or
subtractions for normal operating periods. You must document the reason
for the adjustment and justify the quantity of the adjustment.
(vi) The tons of each type of listed oilseed processed during each
operating month.
(d) After your source has processed listed oilseed for 12 operating
months, and you are not operating during an initial startup period as
described in Sec. 63.2850(c)(2) or (d)(2), or a malfunction period as
described in Sec. 63.2850(e)(2), record the items in paragraphs (d)(1)
through (5) of this section by the end of the calendar month following
each operating month:
(1) The 12 operating months rolling sum of the actual solvent loss
in gallons as described in Sec. 63.2853(c).
(2) The weighted average volume fraction of HAP in extraction
solvent
[[Page 223]]
received for the previous 12 operating months as described in
Sec. 63.2854(b)(3).
(3) The 12 operating months rolling sum of each type of listed
oilseed processed at the affected source in tons as described in
Sec. 63.2855(c).
(4) A determination of the compliance ratio. Using the values from
Secs. 63.2853, 63.2854, 63.2855, and Table 1 of Sec. 63.2840, calculate
the compliance ratio using Equation 2 of Sec. 63.2840.
(5) A statement of whether the source is in compliance with all of
the requirements of this subpart. This includes a determination of
whether you have met all of the applicable requirements in Sec. 63.2850.
(e) For each SSM event subject to an initial startup period as
described in Sec. 63.2850(c)(2) or (d)(2), or a malfunction period as
described in Sec. 63.2850(e)(2), record the items in paragraphs (e)(1)
through (3) of this section by the end of the calendar month following
each month in which the initial startup period or malfunction period
occurred:
(1) A description and date of the SSM event, its duration, and
reason it qualifies as an initial startup or malfunction.
(2) An estimate of the solvent loss in gallons for the duration of
the initial startup or malfunction period with supporting documentation.
(3) A checklist or other mechanism to indicate whether the SSM plan
was followed during the initial startup or malfunction period.
Sec. 63.2863 In what form and how long must I keep my records?
(a) Your records must be in a form suitable and readily available
for review in accordance with Sec. 63.10(b)(1).
(b) As specified in Sec. 63.10(b)(1), you must keep each record for
5 years following the date of each occurrence, measurement, maintenance,
corrective action, report, or record.
(c) You must keep each record on-site for at least 2 years after the
date of each occurrence, measurement, maintenance, corrective action,
report, or record, in accordance with Sec. 3.10(b)(1). You can keep the
records off-site for the remaining 3 years.
Other Requirements and Information
Sec. 63.2870 What parts of the General Provisions apply to me?
Table 1 of this section shows which parts of the General Provisions
in Secs. 63.1 through 63.15 apply to you. Table 1 of Sec. 63.2870
follows:
Table 1 of Sec. 63.2870--Applicability of 40 CFR Part 63, Subpart A, to 40 CFR, Part 63, Subpart GGGG
----------------------------------------------------------------------------------------------------------------
Subject of Brief description Applies to
General provisions citation citation of requirement subpart Explanation
----------------------------------------------------------------------------------------------------------------
Sec. 63.1..................... Applicability..... Initial Yes.............. ....................
applicability
determination;
applicability
after standard
established;
permit
requirements;
extensions;
notifications.
Sec. 63.2..................... Definitions....... Definitions for Yes.............. Except as
part 63 standards. specifically
provided in this
subpart.
Sec. 63.3..................... Units and Units and Yes..............
abbreviations. abbreviations for
part 63 standards.
Sec. 63.4..................... Prohibited Prohibited Yes.............. ....................
activities and activities;
circumvention. compliance date;
circumvention;
severability.
Sec. 63.5..................... Construction/ Applicability; Yes.............. Except for
reconstruction. applications; subsections of Sec.
approvals. 63.5 as listed
below.
Sec. 63.5(c).................. [Reserved]........ .................. ................. ....................
Sec. 63.5(d)(1)(ii)(H)........ Application for Type and quantity No............... All sources emit
approval. of HAP, operating HAP. Subpart GGGG
parameters. does not require
control from
specific emission
points.
Sec. 63.5(d)(1)(ii)(I)........ [Reserved]........ .................. ................. ....................
[[Page 224]]
Sec. 63.5(d)(1)(iii), (d)(2), .................. Application for No............... The requirements of
(d)(3)(ii). approval. the application for
approval for new,
reconstructed and
significantly
modified sources
are described in
Sec. 63.2860(b)
and (c) of subpart
GGGG. General
provision
requirements for
identification of
HAP emission points
or estimates of
actual emissions
are not required.
Descriptions of
control and
methods, and the
estimated and
actual control
efficiency of such
do not apply.
Requirements for
describing control
equipment and the
estimated and
actual control
efficiency of such
equipment apply
only to control
equipment to which
the subpart GGGG
requirements for
quantifying.
Sec. 63.6..................... Applicability of Applicability..... Yes.............. Except for
General subsections of Sec.
Provisions. 63.6 as listed
below.
Sec. 63.6(b)(1)-(3)........... Compliance dates, .................. No............... Section 63.2834 of
new and subpart GGGG
reconstructed specifies the
sources. compliance dates
for new and
reconstructed
sources.
Sec. 63.6(b)(6)............... [Reserved]........ .................. ................. ....................
Sec. 63.6(c)(3)-(4)........... [Reserved]........ .................. ................. ....................
Sec. 63.6(d).................. [Reserved]........ .................. ................. ....................
Sec. 63.6(e)(1) through Operation and .................. Yes.............. Implement your SSM
(e)(3)(ii) and Sec. maintanance plan, as specified
63.6(e)(3)(v) through (vii). requirements. in Sec. 63.2852.
Sec. 63.6(e)(3)(v)(iii)....... Operation and .................. No............... Implement your plan,
maintenance as specified in
requirements. Sec. 63.2852.
Sec. 63.6(e)(3)(iv)........... Operation and .................. No............... Report SSM and in
maintenance accordance with
requirements. Sec. 63.2861(c)
and (d).
Sec. 63.6(e)(3)(viii)......... Operation and .................. Yes.............. Except, report each
maintenance revision to your
requirements. SSM plan in
accordance with
Sec. 63.2861(c)
rather than Sec.
63.10(d)(5) as
required under Sec.
63.6(e)(3) (viii).
Sec. 63.6(f)-(g).............. Compliance with Comply with No............... Subpart GGGG does
nonopacity emission not have nonopacity
emission standards at all requirements.
standards except times except
during SSM. during SSM.
Sec. 63.6(h).................. Opacity/Visible .................. No............... Subpart GGGG has no
emission (VE) opacity or VE
standards. standards.
Sec. 63.6(i).................. Compliance Procedures and Yes.............. ....................
extension. criteria for
responsible
agency to grant
compliance
extension.
Sec. 63.6(j).................. Presidential President may Yes.............. ....................
compliance exempt source
exemption. category from
requirement to
comply with
subpart.
Sec. 63.7..................... Performance Schedule, Yes.............. Subpart GGGG
testing conditions, requires
requirements. notifications and performance testing
procedures. only if the source
applies additional
control that
destroys solvent.
Section
63.2850(a)(6)
requires sources to
follow the
performance testing
guidelines of the
General Provisions
if a control is
added.
Sec. 63.8..................... Monitoring .................. No............... Subpart GGGG does
requirements. not require
monitoring other
than as specified
therein.
Sec. 63.9..................... Notification Applicability and Yes.............. Except for
requirements. state delegation. subsections of Sec.
63.9 as listed
below.
[[Page 225]]
Sec. 63.9(b)(2)............... Notification Initial No............... Section 63.2860(a)
requirements. notification of subpart GGGG
requirements for specifies the
existing sources. requirements of the
initial
notification for
existing sources.
Sec. 63.9(b)(3)-(5)........... Notification Notification Yes.............. Except the
requirements. requirement for information
certain new/ requirements differ
reconstructed as described in
sources. Sec. 63.2860(b) of
subpart GGGG.
Sec. 63.9(e).................. Notification of Notify responsible Yes.............. Applies only if
performance test. agency 60 days performance testing
ahead. is performed.
Sec. 63.9(f).................. Notification of VE/ Notify responsible No............... Subpart GGGG has no
opacity agency 30 days opacity or VE
observations. ahead. standards.
Sec. 63.9(g).................. Additional Notification of No............... Subpart GGGG has no
notifications performance CMS requirements.
when using a evaluation;
continuous Notification
monitoring system using COMS data;
(CMS). notification that
exceeded
criterion for
relative accuracy.
Sec. 63.9(h).................. Notification of Contents.......... No............... Section 63.2860(d)
compliance status. of subpart GGGG
specifies
requirements for
the notification of
compliance status.
Sec. 63.10.................... Recordkeeping/ Schedule for Yes.............. Except for
reporting. reporting, record subsections of Sec.
storage. 63.10 as listed
below.
Sec. 63.10(b)(2)(i)........... Recordkeeping..... Record SSM event.. Yes.............. Applicable to
periods when
sources must
implement their SSM
plan as specified
in subpart GGGG.
Sec. 63.10(b)(2)(ii)-(iii).... Recordkeeping..... Malfunction of air No............... Applies only if air
pollution pollution control
equipment. equipment has been
added to the
process and is
necessary for the
source to meet the
emission limit.
Sec. 63.10(b)(2)(vi).......... Recordkeeping..... CMS recordkeeping. No............... Subpart GGGG has no
CMS requirements.
Sec. 63.10(b)(2)(viii)-(ix)... Recordkeeping..... Conditions of Yes.............. Applies only if
performance test. performance tests
are performed.
Subpart GGGG does
not have any CMS
opacity or VE
observation
requirements.
Sec. 63.10(b)(2)(x)-(xii)..... Recordkeeping..... CMS, performance No............... Subpart GGGG does
testing, and not require CMS.
opacity and VE
observations
recordkeeping.
Sec. 63.10(c)................. Recordkeeping..... Additional CMS No............... Subpart GGGG does
recordkeeping. not require CMS.
Sec. 63.10(d)(2).............. Reporting......... Reporting Yes.............. Applies only if
performance test performance testing
results. is performed.
Sec. 63.10(d)(3).............. Reporting......... Reporting opacity No............... Subpart GGGG has no
or VE opacity or VE
observations. standards.
Sec. 63.10(d)(4).............. Reporting......... Progress reports.. Yes.............. Applies only if a
condition of
compliance
extension exists.
Sec. 63.10(d)(5).............. Reporting......... SSM reporting..... No............... Section 63.2861(c)
and (d) specify SSM
reporting
requirements.
Sec. 63.10(e)................. Reporting......... Additional CMS No............... Subpart GGGG does
reports. not require CMS.
Sec. 63.11.................... Control device Requirements for Yes.............. Applies only if your
requirements. flares. source uses a flare
to control solvent
emissions. Subpart
GGGG does not
require flares.
Sec. 63.12.................... State authority State authority to Yes.............. ....................
and delegations. enforce standards.
Sec. 63.13.................... State/regional Addresses where Yes.............. ....................
addresses. reports,
notifications,
and requests are
sent.
Sec. 63.14.................... Incorporation by Test methods Yes.............. ....................
reference. incorporated by
reference.
[[Page 226]]
Sec. 63.15.................... Availability of Public and Yes.............. ....................
information and confidential
confidentiality. information.
----------------------------------------------------------------------------------------------------------------
[66 FR 19011, Apr. 12, 2001, as amended at 67 FR 16321, Apr. 5, 2002]
Sec. 63.2871 Who implements and enforces this subpart?
(a) This subpart can be implemented by us, the U.S. EPA, or a
delegated authority such as your State, local, or tribal agency. If the
U.S. EPA Administrator has delegated authority to your State, local, or
tribal agency, then that agency, as well as the U.S. EPA, has the
authority to implement and enforce this subpart. You should contact your
U.S. EPA Regional Office to find out if this subpart is delegated to
your State, local, or tribal agency.
(b) In delegating implementation and enforcement authority of this
subpart to a State, local, or tribal agency under section 40 CFR part
63, subpart E, the authorities contained in paragraph (c) of this
section are retained by the Administrator of the U.S. EPA and are not
transferred to the State, local, or tribal agency.
(c) The authorities that will not be delegated to State, local, or
tribal agencies are as follows:
(1) Approval of alternative nonopacity emissions standards under
Sec. 63.6(g).
(2) Approval of alternative opacity standards under Sec. 63.6(h)(9).
(3) Approval of major alternatives to test methods under
Sec. 63.7(e)(2)(ii) and (f) and as defined in Sec. 63.90.
(4) Approval of major alternatives to monitoring under Sec. 63.8(f)
and as defined in Sec. 63.90.
(5) Approval of major alternatives to recordkeeping and reporting
under Sec. 63.10(f) and as defined in Sec. 63.90.
Sec. 63.2872 What definitions apply to this subpart?
Terms used in this subpart are defined in the sources listed:
(a) The Clean Air Act, section 112(a).
(b) In 40 CFR 63.2, the NESHAP General Provisions.
(c) In this section as follows:
Accounting month means a time interval defined by a business firm
during which corporate economic and financial factors are determined on
a consistent and regular basis. An accounting month will consist of
approximately 4 to 5 calendar weeks and each accounting month will be of
approximate equal duration. An accounting month may not correspond
exactly to a calendar month, but 12 accounting months will correspond
exactly to a calendar year.
Actual solvent loss means the gallons of solvent lost from a source
during 12 operating months as determined in accordance with
Sec. 63.2853.
Agricultural product means any commercially grown plant or plant
product.
Allowable HAP loss means the gallons of HAP that would have been
lost from a source if the source was operating at the solvent loss
factor for each listed oilseed type. The allowable HAP loss in gallons
is determined by multiplying the tons of each oilseed type processed
during the previous 12 operating months, as determined in accordance
with Sec. 63.2855, by the corresponding oilseed solvent loss factor
(gal/ton) listed in Table 1 of Sec. 63.2840, and by the dimensionless
constant 0.64, and summing the result for all oilseed types processed.
Area source means any source that does not meet the major source
definition.
As received is the basis upon which all oilseed measurements must be
determined and refers to the oilseed chemical and physical
characteristics as initially received by the source and prior to any
oilseed handling and processing.
Batch operation means any process that operates in a manner where
the
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addition of raw material and withdrawal of product do not occur
simultaneously. Typically, raw material is added to a process,
operational steps occur, and a product is removed from the process. More
raw material is then added to the process and the cycle repeats.
Calendar month means 1 month as specified in a calendar.
Compliance date means the date on which monthly compliance
recordkeeping begins. For existing sources, recordkeeping typically
begins 3 years after the effective date of the subpart. For new and
reconstructed sources, recordkeeping typically begins upon initial
startup, except as noted in Sec. 63.2834.
Compliance ratio means a ratio of the actual HAP loss in gallons
from the previous 12 operating months to an allowable HAP loss in
gallons, which is determined by using oilseed solvent loss factors in
Table 1 of Sec. 63.2840, the weighted average volume fraction of HAP in
solvent received for the previous 12 operating months, and the tons of
each type of listed oilseed processed in the previous 12 operating
months. Months during which no listed oilseed is processed, or months
during which the Sec. 63.2850(c)(2) or (d)(2) initial startup period or
the Sec. 63.2850(e)(2) malfunction period applies, are excluded from
this calculation. Equation 2 of Sec. 63.2840 is used to calculate this
value. If the value is less than or equal to 1.00, the source is in
compliance. If the value is greater than 1.00, the source is deviating
from compliance.
Continuous operation means any process that adds raw material and
withdraws product simultaneously. Mass, temperature, concentration and
other properties typically approach steady-state conditions.
Conventional desolventizer means a desolventizer toaster that
operates with indirect and direct-contact steam to remove solvent from
the extracted meal. Oilseeds processed in a conventional desolventizer
produce crude vegetable oil and crude meal products, such as animal
feed.
Corn germ dry milling means a source that processes corn germ that
has been separated from the other corn components using a ``dry''
process of mechanical chafing and air sifting.
Corn germ wet milling means a source that processes corn germ that
has been separated from other corn components using a ``wet'' process of
centrifuging a slurry steeped in a dilute sulfurous acid solution.
Exempt period means a period of time during which a source processes
agricultural products not defined as listed oilseed.
Extraction solvent means an organic chemical medium used to remove
oil from an oilseed. Typically, the extraction solvent is a commercial
grade of hexane isomers which have an approximate HAP content of 64
percent by volume.
Hazardous air pollutant (HAP) means any substance or mixture of
substances listed as a hazardous air pollutant under section 112(b) of
the Clean Air Act, as of April 12, 2001.
Initial startup date means the first calendar day that a new,
reconstructed or significantly modified source processes any listed
oilseed.
Initial startup period means a period of time from the initial
startup date of a new, reconstructed or significantly modified source,
for which you choose to operate the source under an initial startup
period subject to Sec. 63.2850(c)(2) or (d)(2). During an initial
startup period, a source is in compliance with the standards by
following the operating and maintenance procedures listed for minimizing
HAP emissions in the source's SSM plan rather than being subject to a
HAP emission limit. The initial startup period following initial startup
of a new or reconstructed source may not exceed 6 calendar months. The
initial startup period following a significant modification may not
exceed 3 calendar months. Solvent and oilseed inventory information
recorded during the initial startup period is excluded from use in any
compliance ratio determinations.
Large cottonseed plant means a vegetable oil production process that
processes 120,000 tons or more of cottonseed and other listed oilseed
during all normal operating periods in a 12 operating months period used
to determine compliance.
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Malfunction period means a period of time between the beginning and
end of a process malfunction and the time reasonably necessary for a
source to correct the malfunction for which you choose to operate the
source under a malfunction period subject to Sec. 63.2850(e)(2). This
period may include the duration of an unscheduled process shutdown,
continued operation during a malfunction, or the subsequent process
startup after a shutdown resulting from a malfunction. During a
malfunction period, a source complies with the standards by following
the operating and maintenance procedures described for minimizing HAP
emissions in the source's SSM plan rather than being subject to a HAP
emission limit. Therefore, solvent and oilseed inventory information
recorded during a malfunction period is excluded from use in any
compliance ratio determinations.
Mechanical extraction means removing vegetable oil from oilseeds
using only mechanical devices such as presses or screws that physically
force the oil from the oilseed. Mechanical extraction techniques use no
organic solvents to remove oil from an oilseed.
Nonoperating period means any period of time in which a source
processes no agricultural product. This operating status does not apply
during any period in which the source operates under an initial startup
period as described in Sec. 63.2850(c)(2) or (d)(2), or a malfunction
period, as described in Sec. 63.2850(e)(2).
Normal operating period means any period of time in which a source
processes a listed oilseed that is not categorized as an initial startup
period as described in Sec. 63.2850(c)(2) or (d)(2), or a malfunction
period, as described in Sec. 63.2850(e)(2). At the beginning and ending
dates of a normal operating period, solvent and oilseed inventory
information is recorded and included in the compliance ratio
determination.
Oilseed or listed oilseed means the following agricultural products:
corn germ, cottonseed, flax, peanut, rapeseed (for example, canola),
safflower, soybean, and sunflower.
Oilseed solvent loss factor means a ratio expressed as gallons of
solvent loss per ton of oilseed processed. The solvent loss factors are
presented in Table 1 of Sec. 63.2840 and are used to determine the
allowable HAP loss.
Operating month means any calendar or accounting month in which a
source processes any quantity of listed oilseed, excluding any entire
calendar or accounting month in which the source operated under an
initial startup period as described in Sec. 63.2850(c)(2) or (d)(2), or
a malfunction period as described in Sec. 63.2850(e)(2). An operating
month may include time intervals characterized by several types of
operating status. However, an operating month must have at least one
normal operating period.
Significant modification means the addition of new equipment or the
modification of existing equipment that:
(1) Significantly affects solvent losses from your vegetable oil
production process;
(2) The fixed capital cost of the new components represents a
significant percentage of the fixed capital cost of building a
comparable new vegetable oil production process;
(3) The fixed capital cost of the new equipment does not constitute
reconstruction as defined in Sec. 63.2; and
(4) Examples of significant modifications include replacement of or
major changes to solvent recovery equipment such as extractors,
desolventizer-toasters/dryer-coolers, flash desolventizers, and
distillation equipment associated with the mineral oil system, and
equipment affecting desolventizing efficiency and steady-state operation
of your vegetable oil production process such as flaking mills, oilseed
heating and conditioning equipment, and cracking mills.
Small cottonseed plant means a vegetable oil production process that
processes less than 120,000 tons of cottonseed and other listed oilseed
during all normal operating periods in a 12 operating months period used
to determine compliance.
Solvent extraction means removing vegetable oil from listed oilseed
using an organic solvent in a direct-contact system.
Solvent working capacity means the volume of extraction solvent
normally retained in solvent recovery equipment. Examples include
components such as the solvent extractor,
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desolventizer-toaster, solvent storage and working tanks, mineral oil
absorption system, condensers, and oil/solvent distillation system.
Specialty desolventizer means a desolventizer that removes excess
solvent from soybean meal using vacuum conditions, energy from
superheated solvent vapors, or reduced operating conditions (e.g.,
temperature) as compared to the typical operation of a conventional
desolventizer. Soybeans processed in a specialty desolventizer result in
high-protein vegetable meal products for human and animal consumption,
such as calf milk replacement products and meat extender products.
Vegetable oil production process means the equipment comprising a
continuous process for producing crude vegetable oil and meal products,
including specialty soybean products, in which oil is removed from
listed oilseeds through direct contact with an organic solvent. Process
equipment typically includes the following components: oilseed
preparation operations (including conditioning, drying, dehulling, and
cracking), solvent extractors, desolventizer-toasters, meal dryers, meal
coolers, meal conveyor systems, oil distillation units, solvent
evaporators and condensers, solvent recovery system (also referred to as
a mineral oil absorption system), vessels storing solvent-laden
materials, and crude meal packaging and storage vessels. A vegetable oil
production process does not include vegetable oil refining operations
(including operations such as bleaching, hydrogenation, and deodorizing)
and operations that engage in additional chemical treatment of crude
soybean meals produced in specialty desolventizer units (including
operations such as soybean isolate production).
Subpart HHHH--National Emission Standards for Hazardous Air Pollutants
for Wet-Formed Fiberglass Mat Production
Source: 67 FR 17835, Apr. 11, 2002, unless otherwise noted.
What This Subpart Covers
Sec. 63.2980 What is the purpose of this subpart?
This subpart establishes national emission standards for hazardous
air pollutants (NESHAP) for emissions from facilities that produce wet-
formed fiberglass mat. This subpart also establishes requirements to
demonstrate initial and continuous compliance with the emission
limitations.
Sec. 63.2981 Does this subpart apply to me?
You must comply with this subpart if you meet the criteria in
paragraphs (a) and (b) of this section:
(a) You own or operate a drying and curing oven at a wet-formed
fiberglass mat production facility.
(b) Your drying and curing oven or the facility at which your drying
and curing oven is located is a major source of hazardous air pollutants
(HAP). A major source is any stationary source or group of stationary
sources located within a contiguous area and under common control that
emits or can potentially emit, considering controls, in the aggregate,
9.07 megagrams (10 tons) or more per year of a single HAP or 22.68
megagrams (25 tons) or more per year of any combination of HAP.
Sec. 63.2982 What parts of my plant does this subpart cover?
(a) This subpart applies to each new, reconstructed, or existing
affected source. The affected source (the portion of your plant covered
by this subpart) is each wet-formed fiberglass mat drying and curing
oven.
(b) An affected source is a new affected source if you commenced
construction of the affected source after May 26, 2000, and you meet the
applicability criteria in Sec. 63.2981 at start-up.
(c) An affected source is reconstructed if you meet the criteria as
defined in Sec. 63.2.
(d) An affected source is existing if it is not new or
reconstructed.
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Emission Limitations
Sec. 63.2983 What emission limits must I meet?
(a) You must limit the formaldehyde emissions from each drying and
curing oven by either:
(1) Limiting emissions of formaldehyde to 0.03 kilograms or less per
megagram (0.05 pounds per ton) of fiberglass mat produced; or
(2) Reducing uncontrolled formaldehyde emissions by 96 percent or
more.
(b) [Reserved]
Sec. 63.2984 What operating limits must I meet?
(a) You must maintain operating parameters within established limits
or ranges specified in your operation, maintenance, and monitoring (OMM)
plan described in Sec. 63.2987. If there is a deviation of any of the
specified parameters from the limit or range specified in the OMM plan,
you must address the deviation according to paragraph (b) of this
section. You must comply with the operating limits specified in
paragraphs (a)(1) through (4) of this section:
(1) You must operate the thermal oxidizer so that the average
operating temperature in any 3-hour block period does not fall below the
temperature established during your performance test and specified in
your OMM plan.
(2) You must not use a resin with a free-formaldehyde content
greater than that of the resin used during your performance test and
specified in your OMM plan.
(3) You must operate the wet-formed fiberglass mat production
process so that the average urea formaldehyde resin solids application
rate in any 3-hour block period does not exceed the average application
rate achieved during your performance test and specified in your OMM
plan.
(4) If you use an add-on control device other than a thermal
oxidizer or wish to monitor an alternative parameter and comply with a
different operating limit, you must obtain approval for the alternative
monitoring under Sec. 63.8(f). You must include the approved alternative
monitoring and operating limits in the OMM plan specified in
Sec. 63.2987.
(b) When during a period of normal operations you detect that an
operating parameter deviates from the limit or range established in
paragraph (a) of this section, you must initiate corrective actions
within 1 hour according to the provisions of your OMM plan. During
periods of start up, shut down, or malfunction you must follow your
start up, shut down and malfunction plan (SSMP). The corrective action
actions must be completed in an expeditious manner as specified in the
OMM plan or SSMP.
(c) You must maintain and inspect control devices according to the
procedures specified in the OMM plan.
(d) You must include the operating limits specified in paragraphs
(a)(1) through (4) of this section and their allowable ranges or levels
in your OMM plan. Your 40 CFR part 70 operating permit for the drying
and curing oven must contain a requirement that you develop and operate
according to an OMM plan at all times.
(e) If you use a thermal oxidizer or other control device to achieve
the emission limits in Sec. 63.2983, you must capture and convey the
formaldehyde emissions from each drying and curing oven according to the
procedures in chapters 3 and 5 of ``Industrial Ventilation: A Manual of
Recommended Practice'' (23rd Edition). This publication is incorporated
by reference in Sec. 63.3003.
Sec. 63.2985 When do I have to comply with these standards?
(a) Existing drying and curing ovens must be in compliance with this
subpart no later than April 11, 2005.
(b) New or reconstructed drying and curing ovens must be in
compliance with this subpart at startup or by April 11, 2002, whichever
is later.
(c) If your facility is an area source that increases its emissions
or its potential to emit such that it becomes a major source of
hazardous air pollutants, the following apply:
(1) Any portion of the existing facility that is a new affected
source or a new reconstructed affected source must be in compliance upon
startup.
(2) All other parts of the source must be in compliance with this
subpart 1 year after becoming a major source or by April 11, 2005,
whichever is later.
[[Page 231]]
Sec. 63.2986 How do I comply with the standards?
(a) You must install, maintain, and operate a thermal oxidizer or
other control device or implement a process modification that reduces
formaldehyde emissions from each drying and curing oven to the emission
limits specified in Sec. 63.2983.
(b) You must comply with the operating limits specified in
Sec. 63.2984. The operating limits prescribe the requirements for
demonstrating continuous compliance based on the OMM plan. You must
begin complying with the operating limits on the date by which you must
complete the initial performance test.
(c) You must conduct a performance test according to Secs. 63.2991,
63.2992, and 63.2993 to demonstrate compliance for each drying and
curing oven subject to the emission limits in Sec. 63.2983, and to
establish or modify the operating limits or ranges for process or
control device parameters that will be monitored to demonstrate
continuous compliance.
(d) You must install, calibrate, maintain, and operate devices that
monitor the parameters specified in your OMM plan at the frequency
specified in the plan. All continuous parameter monitoring systems must
be installed and operating no later than the applicable compliance date
specified in Sec. 63.2985.
(e) You must prepare and follow a written OMM plan as specified in
Sec. 63.2987.
(f) You must comply with the monitoring, recordkeeping,
notification, and reporting requirements of this subpart as required by
Secs. 63.2996 through 63.3000.
(g) You must comply with the requirements in paragraphs (g)(1)
through (3) of this section.
(1) You must be in compliance with the emission limits in
Sec. 63.2983 and the operating limits in Sec. 63.2984 at all times,
except during periods of startup, shutdown, or malfunction.
(2) You must always operate and maintain your affected source,
including air pollution control and monitoring equipment, according to
the provisions in Sec. 63.6(e)(1).
(3) You must develop and implement a written SSMP according to the
provisions in Sec. 63.6(e)(3). The SSMP must address the startup,
shutdown, and corrective actions taken for malfunctioning process and
air pollution control equipment.
Operation, Maintenance, and Monitoring Plan
Sec. 63.2987 What must my operation, maintenance, and monitoring (OMM) plan include?
(a) You must prescribe the monitoring that will be performed to
ensure compliance with these emission limitations. Minimum monitoring
requirements are listed in table 1 of this subpart. Your plan must
specify the items listed in paragraphs (a)(1) through (3) of this
section:
(1) Each process and control device to be monitored, the type of
monitoring device that will be used, and the operating parameters that
will be monitored.
(2) A monitoring schedule that specifies the frequency that the
parameter values will be determined and recorded.
(3) The operating limits or ranges for each parameter that represent
continuous compliance with the emission limits in Sec. 63.2983.
Operating limits and ranges must be based on values of the monitored
parameters recorded during performance tests.
(b) You must establish routine and long-term maintenance and
inspection schedules for each control device. You must incorporate in
the schedules the control device manufacturer's recommendations for
maintenance and inspections or equivalent procedures. If you use a
thermal oxidizer, the maintenance schedule must include procedures for
annual or more frequent inspection of the thermal oxidizer to ensure
that the structural and design integrity of the combustion chamber is
maintained. At a minimum, you must meet the requirements of paragraphs
(b)(1) through (10) of this section:
(1) Inspect all burners, pilot assemblies, and pilot sensing devices
for proper operation. Clean pilot sensor if necessary.
(2) Ensure proper adjustment of combustion air and adjust if
necessary.
(3) Inspect, when possible, all internal structures (such as
baffles) to ensure structural integrity per the design specifications.
[[Page 232]]
(4) Inspect dampers, fans, and blowers for proper operation.
(5) Inspect motors for proper operation.
(6) Inspect, when possible, combustion chamber refractory lining.
Clean and repair or replace lining if necessary.
(7) Inspect the thermal oxidizer shell for proper sealing,
corrosion, and hot spots.
(8) For the burn cycle that follows the inspection, document that
the thermal oxidizer is operating properly and make any necessary
adjustments.
(9) Generally observe whether the equipment is maintained in good
operating condition.
(10) Complete all necessary repairs as soon as practicable.
(c) You must establish procedures for responding to operating
parameter deviations. At a minimum, the procedures must include the
information in paragraphs (c)(1) through (3) of this section.
(1) Procedures for determining the cause of the operating parameter
deviation.
(2) Actions for correcting the deviation and returning the operating
parameters to the allowable ranges or limits.
(3) Procedures for recording the date and time that the deviation
began and ended, and the times corrective actions were initiated and
completed.
(d) Your plan must specify the recordkeeping procedures to document
compliance with the emissions and operating limits. Table 1 of this
subpart establishes the minimum recordkeeping requirements.
Sec. 63.2988 [Reserved]
Sec. 63.2989 How do I change my OMM plan?
Changes to the operating limits or ranges in your OMM plan require a
new performance test.
(a) In order to revise the ranges or levels established for your
operating limits in Sec. 63.2984, you must meet the requirements in
paragraphs (a)(1) and (2) of this section:
(1) Submit a notification of performance test to the Administrator
as specified in Sec. 63.7(b) to revise your operating ranges or limits.
(2) After completing the performance test to demonstrate that
compliance with the emissions limits can be achieved at the revised
levels of the operating limits, you must submit the performance test
results and the revised operating limits as part of the notification of
compliance status required under Sec. 63.9(h).
(b) If you are revising the inspection and maintenance procedures in
your plan that are specified in Sec. 63.2987(b), you do not need to
conduct a new performance test.
(c) If you plan to operate your process or control device under
alternative operating conditions and do not wish to revise your OMM plan
when you change operating conditions, you can perform a separate
compliance test to establish operating limits for each condition. You
can then include the operating limits for each condition in your OMM
plan. After completing the performance tests, you must record the date
and time when you change operations from one condition to another, the
condition under which you are operating, and the operating limits that
apply under that condition. If you can perform a single performance test
that establishes the most stringent operating limits that cover all
alternative operating conditions, then you do not need to comply with
the provisions of this paragraph.
Sec. 63.2990 Can I conduct short-term experimental production runs that cause parameters to deviate from operating limits?
With the approval of the Administrator, you may conduct short-term
experimental production runs during which your operating parameters
deviate from the operating limits. Experimental runs may include, but
are not limited to, runs using resin with a higher free-formaldehyde
content than specified in the OMM plan, or using experimental pollution
prevention techniques. To conduct a short-term experimental production
run, you must complete the requirements in paragraphs (a) and (b) of
this section.
(a) Prepare an application to the Administrator for approval to
conduct the experimental production runs. Your application must include
the items listed
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in paragraphs (a)(1) through (6) of this section.
(1) The purpose of the experimental production run.
(2) Identification of the affected line.
(3) An explanation of how the operating parameters will deviate from
the previously approved ranges and limits.
(4) The duration of the experimental production run.
(5) The date and time of the experimental production run.
(6) A description of any emission testing to be performed during the
experimental production run.
(b) Submit the application to the Administrator for approval at
least 30 days before you conduct the experimental production run.
(c) If you conduct such experimental production runs without first
receiving approval from the Administrator, then you must conduct a
performance test under those same experimental production run conditions
to show that you were in compliance with the formaldehyde emission
limits in Sec. 63.2983.
Testing and Initial Compliance Requirements
Sec. 63.2991 When must I conduct performance tests?
You must conduct a performance test for each drying and curing oven
subject to this subpart according to the provisions in paragraphs (a)
through (c) of this section:
(a) Initially. You must conduct an initial performance test no later
than 180 days after the applicable compliance date specified in
Sec. 63.2985. The initial performance test is used to demonstrate
initial compliance and establish operating parameter limits and ranges
to be used to demonstrate continuous compliance with the emission
standards.
(b) Every 5 years. You must conduct a performance test every 5 years
as part of renewing your 40 CFR part 70 operating permit.
(c) To change your OMM plan. You must conduct a performance test
according to the requirements specified in Sec. 63.2992 to change the
limit or range for any operating limit specified in your OMM plan
established during a previous compliance test.
Sec. 63.2992 How do I conduct a performance test?
(a) You must verify the performance of monitoring equipment as
specified in Sec. 63.2994 before performing the test.
(b) You must conduct the performance test according to the
procedures in Sec. 63.7.
(c) You must conduct the performance test under the conditions
specified in paragraphs (c)(1) and (2) of this section.
(1) The resin must have the highest specified free-formaldehyde
content that will be used.
(2) You must operate at the maximum feasible urea-formaldehyde resin
solids application rate (pounds urea-formaldehyde resin solids applied
per hour) that will be used.
(d) During the performance test, you must monitor and record the
operating parameters that you will use to demonstrate continuous
compliance after the test. These parameters are listed in table 1 of
this subpart.
(e) You may not conduct performance tests during periods of startup,
shutdown, or malfunction as specified in Sec. 63.7(e)(1).
(f) You must conduct three separate test runs for each performance
test as specified in Sec. 63.7(e)(3), and each test run must last at
least 1 hour.
Sec. 63.2993 What test methods must I use in conducting performance tests?
(a) Use EPA Method 1 (40 CFR part 60, appendix A) for selecting the
sampling port location and the number of sampling ports.
(b) Use EPA Method 2 (40 CFR part 60, appendix A) for measuring the
volumetric flow rate.
(c) Use EPA Method 316 or 318 (40 CFR part 63, appendix A) for
measuring the concentration of formaldehyde.
(d) Use the method contained in appendix A of this subpart or the
resin purchase specification and the vendor specification sheet for each
resin lot for determining the free-formaldehyde content in the urea-
formaldehyde resin.
(e) Use the method in appendix B of this subpart for determining
product loss-on-ignition.
[[Page 234]]
Sec. 63.2994 How do I verify the performance of monitoring equipment?
(a) Before conducting the performance test, you must take the steps
listed in paragraphs (a)(1) and (2) of this section:
(1) Install and calibrate all process equipment, control devices,
and monitoring equipment.
(2) Conduct a performance evaluation of the continuous monitoring
system (CMS) according to Sec. 63.8(e) which specifies the general
requirements and requirements for notifications, the site-specific
performance evaluation plan, conduct of the performance evaluation, and
reporting of performance evaluation results.
(b) If you use a thermal oxidizer, the temperature monitoring device
must meet the performance and equipment specifications listed in
paragraphs (b)(1) through (3) of this section:
(1) The temperature monitoring device must be installed either at
the exit of the combustion zone of each thermal oxidizer, or at the
location specified by the manufacturer. The temperature monitoring
device must also be installed in a location before any heat recovery or
heat exchange equipment, and it must remain in the same location for
both the performance test and the continuous monitoring of temperature.
(2) The recorder response range must include zero and 1.5 times the
average temperature required in Sec. 63.2984(a)(1).
(3) The measurement method or reference method for calibration must
be a National Institute of Standards and Technology calibrated reference
thermocouple-potentiometer system or an alternate reference subject to
the approval of the Administrator.
Sec. 63.2995 What equations must I use to determine compliance?
(a) Percent reduction for formaldehyde. To determine compliance with
the percent reduction formaldehyde emission standard, use equation 1 of
this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.021
Where:
Ef = Formaldehyde control efficiency, percent.
Mi = Mass flow rate of formaldehyde entering the control
device, kilograms (pounds) per hour.
Mo = Mass flow rate of formaldehyde exiting the control
device, kilograms (pounds) per hour.
(b) Formaldehyde mass emissions rate. To determine compliance with
the kilogram per megagram (pound per ton) formaldehyde emission
standard, use equation 2 of this section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.022
Where:
E = Formaldehyde mass emissions rate, kilograms (pounds) of formaldehyde
per megagram (ton) of fiberglass mat produced.
M = Formaldehyde mass emissions rate, kilograms (pounds) per hour.
P = The wet-formed fiberglass mat production rate during the emissions
sampling period, including any material trimmed from the final product,
megagrams (tons) per hour.
(c) Urea-formaldehyde (UF) resin solids application rate. To
determine the UF resin solids application rate, use equation 3 of this
section as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.023
Where:
UF solids/hour = UF resin solids application rate (pounds per hour).
LOI = loss on ignition (weight faction), or pound of organic binder per
pound of mat.
[[Page 235]]
UFL = UF-to-latex ratio in the binder (mass fraction of UF resin solids
in total combined resin solids for UF and latex), or pound of UF solids
per pound of total resin solids (UF and latex).
MW = weight of the final mat per square (pounds per roofing square).
SQ = roofing squares produced per hour.
Monitoring Requirements
Sec. 63.2996 What must I monitor?
You must monitor the parameters listed in table 1 of this subpart
and any other parameters specified in your OMM plan. The parameters must
be monitored, at a minimum, at the corresponding frequencies listed in
table 1 of this subpart.
Sec. 63.2997 What are the requirements for monitoring devices?
(a) If formaldehyde emissions are controlled using a thermal
oxidizer, you must meet the requirements in paragraphs (a)(1) and (2) of
this section:
(1) Install, calibrate, maintain, and operate a device to monitor
and record continuously the thermal oxidizer temperature at the exit of
the combustion zone before any substantial heat exchange occurs or at
the location consistent with the manufacturer's recommendations.
(2) Continuously monitor the thermal oxidizer temperature and
determine and record the average temperature in 15-minute and 3-hour
block averages. You may determine the average temperature more
frequently than every 15 minutes and every 3 hours, but not less
frequently.
(b) If formaldehyde emissions are controlled by process
modifications or a control device other than a thermal oxidizer, you
must install, calibrate, maintain, and operate devices to monitor the
parameters established in your OMM plan at the frequency established in
the plan.
Notifications, Reports, and Records
Sec. 63.2998 What records must I maintain?
You must maintain records according to the procedures of Sec. 63.10.
You must maintain the records listed in paragraphs (a) through (g) of
this section.
(a) All records required by Sec. 63.10. Table 2 of this subpart
presents the applicable requirements of the general provisions.
(b) The OMM plan.
(c) Records of values of monitored parameters listed in table 1 of
this subpart to show continuous compliance with each operating limit
specified in table 1 of this subpart.
(d) Records of maintenance and inspections performed on the control
devices.
(e) If an operating parameter deviation occurs, you must record:
(1) The date, time, and duration of the operating parameter
deviation;
(2) A brief description of the cause of the operating parameter
deviation;
(3) The dates and times at which corrective actions were initiated
and completed;
(4) A brief description of the corrective actions taken to return
the parameter to the limit or to within the range specified in the OMM
plan; and
(5) A record of whether the deviation occurred during a period of
startup, shutdown, or malfunction.
(f) Keep all records specified in Sec. 63.6(e)(3)(iii) through (v)
related to startup, shutdown, and malfunction.
(g) If you operate your process or control device under alternative
operating condition and have established operating limits for each
condition as specified in Sec. 63.2989(c), then you must keep records of
the date and time you changed operations from one condition to another,
the condition under which you are operating, and the applicable
operating limits for that condition.
Sec. 63.2999 In what form and for how long must I maintain records?
(a) You must maintain each record required by this subpart for 5
years. You must maintain the most recent 2 years of records at the
facility. The remaining 3 years of records may be retained offsite.
(b) Your records must be readily available and in a form so they can
be easily inspected and reviewed. You can
[[Page 236]]
keep the records on paper or an alternative media, such as microfilm,
computer, computer disks, magnetic tape, or on microfiche.
Sec. 63.3000 What notifications and reports must I submit?
(a) You must submit all notifications and reports required by the
applicable general provisions and this section. Table 2 of this subpart
presents the applicable requirements of the general provisions.
(b) Notification of compliance status. You must submit the
notification of compliance status, including the performance test
results, the operating limits or ranges as determined during the
performance test, and other information specified in Sec. 63.9(h),
before the close of business on the 60th calendar day after you complete
the performance test according to Sec. 63.10(d)(2).
(c) Semiannual compliance reports. You must submit semiannual
compliance reports according to the requirements of paragraphs (c)(1)
through (5) of this section.
(1) Dates for submitting reports. Unless the Administrator has
agreed to a different schedule for submitting reports under
Sec. 63.10(a), you must deliver or postmark each semiannual compliance
report no later than 30 days following the end of each semiannual
reporting period. The first semiannual reporting period begins on the
compliance date for your affected source and ends on June 30 or December
31, whichever date immediately follows your compliance date. Each
subsequent semiannual reporting period for which you must submit a
semiannual compliance report begins on July 1 or January 1 and ends 6
calendar months later. As required by Sec. 63.10(e)(3), you must begin
submitting quarterly compliance reports if you deviate from the emission
limits in Sec. 63.2983 or the operating limits in Sec. 63.2984.
(2) Inclusion with title V report. For each affected source that is
subject to permitting regulations pursuant to 40 CFR part 70 or 71, and
for which the permitting authority has established dates for submitting
semiannual reports pursuant to 40 CFR 70.6(a)(3)(iii)(A) or 71.6
(a)(3)(iii)(A), you may submit the first and subsequent compliance
reports according to the dates the permitting authority has established
instead of according to the dates in paragraph (c)(1) of this section.
(3) Contents of reports. The semiannual compliance report must
contain the information in paragraphs (c)(3)(i) through (vi) of this
section:
(i) Company name and address.
(ii) Statement by a responsible official with that official's name,
title, and signature, certifying the truth, accuracy, and completeness
of the content of the report.
(iii) Date of report and beginning and ending dates of the reporting
period.
(iv) A summary of the total duration of continuous parameter
monitoring system downtime during the semiannual reporting period and
the total duration of continuous parameter monitoring system downtime as
a percent of the total source operating time during that semiannual
reporting period.
(v) The date of the latest continuous parameter monitoring system
certification or audit.
(vi) A description of any changes in the wet-formed fiberglass mat
manufacturing process, continuous parameter monitoring system, or add-on
control device since the last semiannual reporting period.
(4) No deviations. If there were no deviations from the emission
limit in Sec. 63.2983 or the operating limits in Sec. 63.2984, the
semiannual compliance report must include a statement to that effect. If
there were no periods during which the continuous parameter monitoring
systems were out-of-control as specified in Sec. 63.8(c)(7), the
semiannual compliance report must include a statement to that effect.
(5) Deviations. If there was a deviation from the emission limit in
Sec. 63.2983 or an operating limit in Sec. 63.2984, the semiannual
compliance report must contain the information in paragraphs (c)(5)(i)
through (ix) of this section:
(i) The date and time that each malfunction started and stopped.
(ii) The date and time that each continuous parameter monitoring
system was inoperative, except for zero (low-level) and high-level
checks.
[[Page 237]]
(iii) The date, time, and duration that each continuous parameter
monitoring system was out-of-control, including the information in
Sec. 63.8(c)(8).
(iv) The date and time that each deviation started and stopped, and
whether each deviation occurred during a period of startup, shutdown, or
malfunction or during another period.
(v) The date and time that corrective actions were taken, a
description of the cause of the deviation, and a description of the
corrective actions taken.
(vi) A summary of the total duration of each deviation during the
semiannual reporting period and the total duration as a percent of the
total source operating time during that semiannual reporting period.
(vii) A breakdown of the total duration of the deviations during the
semiannual reporting period into those that were due to startup,
shutdown, control equipment problems, process problems, other known
causes, and other unknown causes.
(viii) A brief description of the process units.
(ix) A brief description of the continuous parameter monitoring
system.
(d) Performance test reports. You must submit reports of performance
test results for add-on control devices no later than 60 days after
completing the tests as specified in Sec. 63.10(d)(2). You must include
in the performance test reports the values measured during the
performance test for the parameters listed in table 1 of this subpart
and the operating limits or ranges to be included in your OMM plan. For
the thermal oxidizer temperature, you must include 15-minute averages
and the average for the three 1-hour test runs.
(e) Startup, shutdown, malfunction reports. If you have a startup,
shutdown, or malfunction during the semiannual reporting period, you
must submit the reports specified Sec. ;63.10(d)(5).
Other Requirements and Information
Sec. 63.3001 What sections of the general provisions apply to me?
You must comply with the requirements of the general provisions of
40 CFR part 63, subpart A, as specified in table 2 of this subpart.
Sec. 63.3002 Who implements and enforces this subpart?
(a) This subpart can be implemented and enforced by the U.S. EPA or
a delegated authority, such as your State, local, or tribal agency. If
the Administrator has delegated authority to your State, local, or
tribal agency, then that agency is the primary enforcement authority. If
the Administrator has not delegated authority to your State, only EPA
enforces this subpart. You should contact your U.S. EPA Regional Office
to find out if implementation and enforcement of this subpart is
delegated to your State, local, or tribal agency.
(b) In delegating implementation and enforcement authority of this
subpart to a State, local, or tribal agency under section 40 CFR part
63, subpart E, the authorities contained in paragraphs (b)(1) through
(4) of this section are retained by the Administrator of U.S. EPA and
are not transferred to the State, local, or tribal agency.
(1) The authority under Sec. 63.6(g) to approve alternatives to the
emission limits in Sec. 63.2983 and operating limits in Sec. 63.2984 is
not delegated.
(2) The authority under Sec. 63.7(e)(2)(ii) and (f) to approve of
major alternatives (as defined in Sec. 63.90) to the test methods in
Sec. 63.2993 is not delegated.
(3) The authority under Sec. 63.8(f) to approve major alternatives
(as defined in Sec. 63.90) to the monitoring requirements in
Secs. 63.2996 and 63.2997 is not delegated.
(4) The authority under Sec. 63.10(f) to approve major alternatives
(as defined in Sec. 63.90) to recordkeeping, notification, and reporting
requirements in Secs. 63.2998 through 63.3000 is not delegated.
Sec. 63.3003 Incorporation by reference.
(a) The following material is incorporated by reference and referred
to at Sec. 63.2984: chapters 3 and 5 of ``Industrial Ventilation: A
Manual of Recommended Practice,'' American Conference of Governmental
Industrial Hygienists, (23rd edition, 1998). The incorporation by
reference of this material is approved by the Director of the Office of
the Federal Register as of the date of publication of the final rule
according to 5 U.S.C. 552(a) and 1 CFR part 51. This material is
incorporated as it exists on the date of approval and
[[Page 238]]
notice of any change in the material will be published in the Federal
Register.
(b) The materials referenced in this section are incorporated by
reference and are available for inspection at the Office of the Federal
Register, 800 North Capitol Street NW, Suite 700, 7th Floor, Washington,
DC; and at the Air and Radiation Docket and Information Center, U.S.
EPA, 401 M Street SW, Washington, DC. The material is also available for
purchase from the following address: Customer Service Department,
American Conference of Governmental Industrial Hygienists (ACGIH), 1330
Kemper Meadow Drive, Cincinnati, OH 45240, telephone number (513) 742-
2020.
Sec. 63.3004 What definitions apply to this subpart?
Terms used in this subpart are defined the Clean Air Act, in
Sec. 63.2, and in this section as follows:
Administrator means the Administrator of the United States
Environmental Protection Agency or his or her authorized representative
(e.g., a State that has been delegated the authority to implement the
provisions of this part).
Binder application vacuum exhaust means the exhaust from the vacuum
system used to remove excess resin solution from the wet-formed
fiberglass mat before it enters the drying and curing oven.
Deviation means any instance in which an affected source subject to
this subpart, or an owner or operator of such a source:
(1) Fails to meet any requirement or obligation established by this
subpart, including but not limited to any emission limit, or operating
limit, or work practice standard;
(2) Fails to meet any term or condition that is adopted to implement
an applicable requirement in this subpart and that is included in the
operating permit for any affected source required to obtain such a
permit; or
(3) Fails to meet any emission limit, or operating limit, or work
practice standard in this subpart during startup, shutdown, or
malfunction, regardless of whether or not such failure is permitted by
this subpart.
Drying and curing oven means the process section that evaporates
excess moisture from a fiberglass mat and cures the resin that binds the
fibers.
Emission limitation means an emission limit, operating limit, or
work practice standard.
Fiberglass mat production rate means the weight of finished
fiberglass mat produced per hour of production including any trim
removed after the binder is applied and before final packaging.
Loss-on-ignition means the percentage decrease in weight of
fiberglass mat measured before and after it has been ignited to burn off
the applied binder. The loss-on-ignition is used to monitor the weight
percent of binder in fiberglass mat.
Nonwoven wet-formed fiberglass mat manufacturing means the
production of a fiberglass mat by bonding glass fibers to each other
using a resin solution. Nonwoven wet-formed fiberglass mat manufacturing
is also referred to as wet-formed fiberglass mat manufacturing.
Roofing square means the amount of finished product needed to cover
an area 10 feet by 10 feet (100 square feet) of finished roof.
Thermal oxidizer means an air pollution control device that uses
controlled flame combustion inside a combustion chamber to convert
combustible materials to noncombustible gases.
Urea-formaldehyde content in binder formulation means the mass-based
percent of urea-formaldehyde resin in the total binder mix as it is
applied to the glass fibers to form the mat.
Secs. 63.3005-63.3079 [Reserved]
[[Page 239]]
Table 1 to Subpart HHHH--Minimum Requirements for Monitoring and
Recordkeeping
[As stated in Sec. 63.2998(c), you must comply with the minimum
requirements for monitoring and recordkeeping in the following table]
------------------------------------------------------------------------
You must monitor these And record for the
parameters: At this frequency: monitored perameter:
------------------------------------------------------------------------
1. Thermal oxidizer Continuously........ 15-minute and 3-hour
temperature \a\. block averages.
2. Other process or control As specified in your As specified in your
device parameters specified OMM plan. OMM plan.
in your OMM \b\ plan.
3. Urea-formaldehyde resin On each operating The average lb/hr
solids application rate. day, calculate the value for each
average lb/hr product
application rate manufactured during
for each product the day.
manufactured during
that day.
4. Resin free-formaldehyde For each lot of The value for each
content. resin purchased. lot used during the
operating day.
5. Loss-on-ignition \c\..... Measured at least The value for each
once per day, for product
each product manufactured during
manufactured during the operating day.
that day.
6. UF-to-latex ratio in the For each batch of The value for each
binder \c\. binder prepared the batch of binder
operating day. prepared during the
operating day.
7. Weight of the final mat Each product The value for each
product per square (lb/ manufactured during product
roofing square)\c\. the operating day. manufactured during
the operating day.
8. Average nonwoven wet- For each product The average value
formed fiberglass mat manufactured during for each product
production rate (roofing the operating day. manufactured during
squares per the hour) \c\. operating day.
------------------------------------------------------------------------
\a\ Required if a thermal oxidizer is used to control formaldehyde
emissions.
\b\ Required if process modifications or a control device other than a
thermal oxidizer is used to control emissions.
\c\ These parameters must be monitored and values recorded, but no
operating limits apply.
Table 2 to Subpart HHHH--Applicability of General Provisions (40 CFR
Part 63, Subpart A) to Subpart HHHH
[As stated in Sec. 63.3001, you must comply with the applicable General Provisions requirements according to
the following table]
----------------------------------------------------------------------------------------------------------------
Citation Requirement Applies to subpart HHHH Explanation
----------------------------------------------------------------------------------------------------------------
Sec. 63.1(a)(1)-(4)................. General Applicability.. Yes....................
Sec. 63.1(a)(5)..................... ....................... No..................... [Reserved].
Sec. 63.1(a)(6)-(8)................. ....................... Yes....................
Sec. 63.1(a)(9)..................... ....................... No..................... [Reserved].
Sec. 63.1(a)(10)-(14)............... ....................... Yes....................
Sec. 63.1(b)........................ Initial Applicability Yes....................
Determination.
Sec. 63.1(c)(1)..................... Applicability After Yes....................
Standard Established.
Sec. 63.1(c)(2)..................... ....................... Yes.................... Some plants may be area
sources.
Sec. 63.1(c)(3)..................... ....................... No..................... [Reserved].
Sec. 63.1(c)(4)-(5)................. ....................... Yes....................
Sec. 63.1(d)........................ ....................... No..................... [Reserved].
Sec. 63.1(e)........................ Applicability of Permit Yes....................
Program.
Sec. 63.2........................... Definitions............ Yes.................... Additional definitions
in Sec. 63.3004.
Sec. 63.3........................... Units and Abbreviations Yes....................
Sec. 63.4(a)(1)-(3)................. Prohibited Activities.. Yes....................
Sec. 63.4(a)(4)..................... ....................... No..................... [Reserved].
Sec. 63.4(a)(5)..................... ....................... Yes....................
Sec. 63.4(b)-(c).................... Circumvention/ Yes....................
Severability.
Sec. 63.5(a)........................ Construction/ Yes....................
Reconstruction.
Sec. 63.5(b)(1)..................... Existing/Constructed/ Yes....................
Reconstruction.
Sec. 63.5(b)(2)..................... ....................... No..................... [Reserved].
Sec. 63.5(b)(3)-(6)................. ....................... Yes....................
Sec. 63.5(c)........................ ....................... No..................... [Reserved].
Sec. 63.5(d)........................ Application for Yes....................
Approval of
Construction/
Reconstruction.
Sec. 63.5(e)........................ Approval of Yes....................
Construction/
Reconstruction.
Sec. 63.5(f)........................ Approval of Yes....................
Construction/
Reconstruction Based
on State Review.
Sec. 63.6(a)........................ Compliance with Yes....................
Standards and
Maintenance--
Applicability.
Sec. 63.6(b)(1)-(5)................. New and Reconstructed Yes....................
Sources-Dates.
Sec. 63.6(b)(6)..................... ....................... No..................... [Reserved].
Sec. 63.6(b)(7)..................... ....................... Yes....................
[[Page 240]]
Sec. 63.6(c)(1)-(2)................. Existing Sources Dates. Yes.................... Sec. 63.2985 specifies
dates.
Sec. 63.6(c)(3)-(4)................. ....................... No..................... [Reserved].
Sec. 63.6(c)(5)..................... ....................... Yes....................
Sec. 63.6(d)........................ ....................... No..................... [Reserved].
Sec. 63.6(e)........................ Operation and Yes.................... Secs. 63.2984 and
Maintenance 63.2987 specify
Requirements. additional
requirements.
Sec. 63.6(f)........................ Compliance with Yes....................
Emission Standards.
Sec. 63.6(g)........................ Alternative Standard... Yes.................... EPA retains approval
authority.
Sec. 63.6(h)........................ Compliance with Opacity/ No..................... Subpart HHHH does not
Visible Emissions specify opacity or
Standards. visible emission
standards.
Sec. 63.6(i)(1)-(14)................ Extension of Compliance Yes....................
Sec. 63.6(i)(15).................... ....................... No..................... [Reserved].
Sec. 63.6(i)(16).................... ....................... Yes....................
Sec. 63.6(j)........................ Exemption from Yes....................
Compliance.
Sec. 63.7(a)........................ Performance Test Yes....................
Requirements--
Applicability and
Dates.
Sec. 63.7(b)........................ Notification of Yes....................
Performance Test.
Sec. 63.7(c)........................ Quality Assurance Yes....................
Program/Test Plan.
Sec. 63.7(d)........................ Testing Facilities..... Yes....................
Sec. 63.7(e)........................ Conduct of Tests....... Yes.................... Sec. 63.2991-63.2994
specify additional
requirements.
Sec. 63.7(f)........................ Alternative Test Method Yes.................... EPA retains approval
authority
Sec. 63.7(g)........................ Data Analysis.......... Yes....................
Sec. 63.7(h)........................ Waiver of Tests........ Yes....................
Sec. 63.8(a)(1)-(2)................. Monitoring Requirements- Yes....................
-Applicability.
Sec. 63.8(a)(3)..................... ....................... No..................... [Reserved].
Sec. 63.8(a)(4)..................... ....................... Yes....................
Sec. 63.8(b)........................ Conduct of Monitoring.. Yes....................
Sec. 63.8(c)(1)-(3)................. Continuous Monitoring Yes....................
System (CMS) Operation
and Maintenance.
Sec. 63.8(c)(4)..................... ....................... Yes....................
Sec. 63.8(c)(5)..................... ....................... No..................... Subpart HHHH does not
specify opacity or
visible emission
standards
Sec. 63.8(c)(6)-(8)................. ....................... Yes....................
Sec. 63.8(d)........................ Quality Control........ Yes....................
Sec. 63.8(e)........................ CMS Performance Yes....................
Evaluation.
Sec. 63.8(f)(1)-(5)................. Alternative Monitoring Yes.................... EPA retains approval
Method. authority
Sec. 63.8(f)(6)..................... Alternative to Relative No..................... Subpart HHHH does not
Accuracy Test. require the use of
continuous emissions
monitoring systems
(CEMS)
Sec. 63.8(g)(1)..................... Data Reduction......... Yes....................
Sec. 63.8(g)(2)..................... Data Reduction......... No..................... Subpart HHHH does not
require the use of
CEMS or continuous
opacity monitoring
systems (COMS).
Sec. 63.8(g)(3)-(5)................. Data Reduction......... Yes....................
Sec. 63.9(a)........................ Notification Yes....................
Requirements--
Applicability.
Sec. 63.9(b)........................ Initial Notifications.. Yes....................
Sec. 63.9(c)........................ Request for Compliance Yes....................
Extension.
Sec. 63.9(d)........................ New Source Notification Yes....................
for Special Compliance
Requirements.
Sec. 63.9(e)........................ Notification of Yes....................
Performance Test.
Sec. 63.9(f)........................ Notification of Visible No..................... Subpart HHHH does not
Emissions/Opacity Test. specify opacity or
visible emission
standards.
Sec. 63.9(g)(1)..................... Additional CMS Yes....................
Notifications.
Sec. 63.9(g)(2)-(3)................. ....................... No..................... Subpart HHHH does not
require the use of
COMS or CEMS.
Sec. 63.9(h)(1)-(3)................. Notification of Yes.................... Sec. 63.3000(b)
Compliance Status. specifies additional
requirements.
Sec. 63.9(h)(4)..................... ....................... No..................... [Reserved].
[[Page 241]]
Sec. 63.9(h)(5)-(6)................. ....................... Yes....................
Sec. 63.9(i)........................ Adjustment of Deadlines Yes....................
Sec. 63.9(j)........................ Change in Previous Yes....................
Information.
Sec. 63.10(a)....................... Recordkeeping/Reporting- Yes....................
-Applicability.
Sec. 63.10(b)....................... General Recordkeeping Yes.................... Sec. 63.2998 includes
Requirements. additional
requirements.
Sec. 63.10(c)(1).................... Additional CMS Yes....................
Recordkeeping.
Sec. 63.10(c)(2)-(4)................ ....................... No..................... [Reserved].
Sec. 63.10(c)(5)-(8)................ ....................... Yes....................
Sec. 63.10(c)(9).................... ....................... No..................... [Reserved].
Sec. 63.10(c)(10)-(15).............. ....................... Yes....................
Sec. 63.10(d)(1).................... General Reporting Yes.................... Sec. 63.3000 includes
Requirements. additional
requirements.
Sec. 63.10(d)(2).................... Performance Test Yes.................... Sec. 63.3000 includes
Results. additional
requirements
Sec. 63.10(d)(3).................... Opacity or Visible No..................... Subpart HHHH does not
Emissions specify opacity or
Observations. visible emission
standards.
Sec. 63.10(d)(4)-(5)................ Progress Reports/ Yes....................
Startup, Shutdown, and
Malfunction Reports.
Sec. 63.10(e)(1).................... Additional CMS Reports-- No..................... Subpart HHHH does not
General. require CEMS.
Sec. 63.10(e)(2).................... Reporting results of Yes....................
CMS performance
evaluations.
Sec. 63.10(e)(3).................... Excess Emission/CMS Yes....................
Performance Reports.
Sec. 63.10(e)(4).................... COMS Data Reports...... No..................... Subpart HHHH does not
specify opacity or
visible emission
standards.
Sec. 63.10(f)....................... Recordkeeping/Reporting Yes.................... EPA retains approval
Waiver. authority
Sec. 63.11.......................... Control Device No..................... Facilities subject to
Requirments-- subpart HHHH do not
Applicability. use flares as control
devices.
Sec. 63.12.......................... State Authority and Yes....................
Delegations.
Sec. 63.13.......................... Addresses.............. Yes....................
Sec. 63.14.......................... Incorporation by No.....................
Reference.
Sec. 63.15.......................... Availability of Yes....................
Information/
Confidentiality.
----------------------------------------------------------------------------------------------------------------
Appendix A to Subpart HHHH--Method for Determining Free-Formaldehyde in
Urea-Formaldehyde Resins by Sodium Sulfite (Iced & Cooled)
1.0 Scope
This procedure corresponds to the Housing and Urban Development
method of determining free-formaldehyde in urea-formaldehyde resins.
This method applies to samples that decompose to yield formaldehyde
under the conditions of other free-formaldehyde methods. The primary use
is for urea-formaldehyde resins.
2.0 Part A--Testing Resins
Formaldehyde will react with sodium sulfite to form the sulfite
addition products and liberate sodium hydroxide (NaOH); however, at room
temperature, the methanol groups present will also react to liberate
NaOH. Titrate at 0 degrees Celsius ( [deg]C) to minimize the reaction of
the methanol groups.
2.1 Apparatus Required.
2.1.1 Ice crusher.
2.1.2 One 100-milliliter (mL) graduated cylinder.
2.1.3 Three 400-mL beakers.
2.1.4 One 50-mL burette.
2.1.5 Analytical balance accurate to 0.1 milligrams (mg).
2.1.6 Magnetic stirrer.
2.1.7 Magnetic stirring bars.
2.1.8 Disposable pipettes.
2.1.9 Several 5-ounce (oz.) plastic cups.
2.1.10 Ice cube trays (small cubes).
2.2 Materials Required.
2.2.1 Ice cubes (made with distilled water).
2.2.2 A solution of 1 molar (M) sodium sulfite
(Na2SO3) (63 grams (g)
Na2SO3/500 mL water (H2O) neutralized
to thymolphthalein endpoint).
2.2.3 Standardized 0.1 normal (N) hydrochloric acid (HCl).
2.2.4 Thymolphthalein indicator (1.0 g thymolphthalein/199 g
methanol).
2.2.5 Sodium chloride (NaCl) (reagent grade).
[[Page 242]]
2.2.6 Sodium hydroxide (NaOH).
2.3 Procedure.
2.3.1 Prepare sufficient quantity of crushed ice for three
determinations (two trays of cubes).
2.3.2 Put 70 cubic centimeters (cc) of 1 M
Na2SO3 solution into a 400-mL beaker. Begin
stirring and add approximately 100 g of crushed ice and 2 g of NaCl.
Maintain 0 [deg]C during test, adding ice as necessary.
2.3.3 Add 10-15 drops of thymolphthalein indicator to the chilled
solution. If the solution remains clear, add 0.1 N NaOH until the
solution turns blue; then add 0.1 N HCl back to the colorless endpoint.
If the solution turns blue upon adding the indicator, add 0.1 N HCl to
the colorless endpoint.
2.3.4 On the analytical balance, accurately weigh the amount of
resin indicated under the ``Resin Sample Size'' chart (see below) as
follows.
Resin Sample Size
------------------------------------------------------------------------
Sample
Approximate free HCHO (percent) weight
(gram(s))
------------------------------------------------------------------------
<0.5........................................................ 10
0.5-1.0..................................................... 5
1.0-3.0..................................................... 2
3.0......................................................... 1
------------------------------------------------------------------------
2.3.4.1 Pour about 1 inch of resin into a 5 oz. plastic cup.
2.3.4.2 Determine the gross weight of the cup, resin, and disposable
pipette (with the narrow tip broken off) fitted with a small rubber
bulb.
2.3.4.3 Pipette out the desired amount of resin into the stirring,
chilled solution (approximately 1.5 to 2 g per pipette-full).
2.3.4.4 Quickly reweigh the cup, resin, and pipette with the bulb.
2.3.4.5 The resultant weight loss equals the grams of resin being
tested.
2.3.5 Rapidly titrate the solution with 0.1 N HCl to the colorless
endpoint described in Step 3 (2.3.3).
2.3.6 Repeat the test in triplicate.
2.4 Calculation.
2.4.1 The percent free-formaldehyde (%HCHO) is calculated as
follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.024
2.4.2 Compute the average percent free-formaldehyde of the three
tests.
(Note: If the results of the three tests are not within a range of
[plusmn]0.5 percent or if the average of the three tests does not meet
expected limits, carry out Part B and then repeat Part A.)
3.0 Part B--Standard Check
Part B ensures that test reagents used in determining percent free-
formaldehyde in urea-formaldehyde resins are of proper concentration and
that operator technique is correct. Should any doubts arise in either of
these areas, the formaldehyde standard solution test should be carried
out.
3.1 Preparation and Standardization of a 1 Percent Formalin
Solution.
Prepare a solution containing approximately 1 percent formaldehyde
from a stock 37 percent formalin solution. Standardize the prepared
solution by titrating the hydroxyl ions resulting from the formation of
the formaldehyde bisulfite complex.
3.2 Apparatus Required.
Note: All reagents must be American Chemical Society analytical
reagent grade or better.
3.2.1 One 1-liter (L) volumetric flask (class A).
3.2.2 One 250-mL volumetric flask (class A).
3.2.3 One 250-mL beaker.
3.2.4 One 100-mL pipette (class A).
3.2.5 One 10-mL pipette (class A).
3.2.6 One 50-mL graduated cylinder (class A).
3.2.7 A pH meter, standardized using pH 7 and pH 10 buffers.
3.2.8 Magnetic stirrer.
3.2.9 Magnetic stirring bars.
3.2.10 Several 5-oz. plastic cups.
3.2.11 Disposal pipettes.
3.2.12 Ice cube trays (small cubes).
3.3 Materials Required.
3.3.1 A solution of 37 percent formalin.
3.3.2 Anhydrous Na2SO3.
3.3.3 Distilled water.
3.3.4 Standardized 0.100 N HCl.
3.3.5 Thymolphthalein indicator (1.0 g thymolphthalein/199 g
methanol).
3.4 Preparation of Solutions and Reagents.
3.4.1 Formaldehyde Standard Solution (approximately 1 percent).
Measure, using a graduated cylinder, 27.0 mL of analytical reagent 37
percent formalin solution into a 1-L volumetric flask. Fill the flask to
volume with distilled water.
[[Page 243]]
(Note: You must standardize this solution as described in section
3.5. This solution is stable for 3 months.)
3.4.2 Sodium Sulfite Solution 1.0 M (used for standardization of
Formaldehyde Standard Solution). Quantitatively transfer, using
distilled water as the transfer solvent, 31.50 g of anhydrous
Na2SO3 into a 250-mL volumetric flask. Dissolve in
approximately 100 mL of distilled water and fill to volume.
(Note: You must prepare this solution daily, but the calibration of
the Formaldehyde Standard Solution needs to be done only once.)
3.4.3 Hydrochloric Acid Standard Solution 0.100 M. This reagent
should be readily available as a primary standard that only needs to be
diluted.
3.5 Standardization.
3.5.1 Standardization of Formaldehyde Standard Solution.
3.5.1.1 Pipette 100.0 mL of 1 M sodium sulfite into a stirred 250-mL
beaker.
3.5.1.2 Using a standardized pH meter, measure and record the pH.
The pH should be around 10. It is not essential the pH be 10; however,
it is essential that the value be accurately recorded.
3.5.1.3 To the stirring Na2SO3 solution,
pipette in 10.0 mL of Formaldehyde Standard Solution. The pH should rise
sharply to about 12.
3.5.1.4 Using the pH meter as a continuous monitor, titrate the
solution back to the original exact pH using 0.100 N HCl. Record the
milliliters of HCl used as titrant. (Note: Approximately 30 to 35 mL of
HCl will be required.)
3.5.1.5 Calculate the concentration of the Formaldehyde Standard
Solution using the equation as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.025
3.6 Procedure.
3.6.1 Prepare a sufficient quantity of crushed ice for three
determinations (two trays of cubes).
3.6.2 Put 70 cc of 1 M Na2SO3 solution into a
400-mL beaker. Begin stirring and add approximately 100 g of crushed ice
and 2 g NaCl. Maintain 0 [deg]C during the test, adding ice as
necessary.
3.6.3 Add 10-15 drops of thymolphthalein indicator to the chilled
solution. If the solution remains clear, add 0.1 N NaOH until the
solution turns blue; then add 0.1 N HCl back to the colorless endpoint.
If the solution turns blue upon adding the indicator, add 0.1 N HCl to
the colorless endpoint.
3.6.4 On the analytical balance, accurately weigh a sample of
Formaldehyde Standard Solution as follows.
3.6.4.1 Pour about 0.5 inches of Formaldehyde Standard Solution into
a 5-oz. plastic cup.
3.6.4.2 Determine the gross weight of the cup, Formaldehyde Standard
Solution, and a disposable pipette fitted with a small rubber bulb.
3.6.4.3 Pipette approximately 5 g of the Formaldehyde Standard
Solution into the stirring, chilled Na2SO3
solution.
3.6.4.4 Quickly reweigh the cup, Formaldehyde Standard Solution, and
pipette with the bulb.
3.6.4.5 The resultant weight loss equals the grams of Formaldehyde
Standard Solution being tested.
3.6.5 Rapidly titrate the solution with 0.1 N HCl to the colorless
endpoint in Step 3 (3.6.3).
3.6.6 Repeat the test in triplicate.
3.7 Calculation for Formaldehyde Standard Solution.
3.7.1 The percent free-formaldehyde (% HCHO) is calculated as
follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.026
3.7.2 The range of the results of three tests should be no more than
[plusmn]5 percent of the actual Formaldehyde Standard Solution
concentration. Report results to two decimal places.
3.8 Reference.
West Coast Adhesive Manufacturers Trade Association Test 10.1.
Appendix B to Subpart HHHH--Method for the Determination of Loss-on-
Ignition
1.0 Purpose
The purpose of this test is to determine the loss-on-ignition (LOI)
of wet-formed fiberglass mat.
2.0 Equipment
2.1 Scale sensitive to 0.001 gram (g).
[[Page 244]]
2.2 Drying oven equipped with a means of constant temperature
regulation and mechanical air convection.
2.3 Furnace designed to heat to at least 625 [deg]C (1,157 [deg]F)
and controllable to [plusmn]25 [deg]C ([plusmn]45 [deg]F).
2.4 Crucible, high form, 250 milliliter (mL).
2.5 Desiccator.
2.6 Pan balance (see Note 2 in 4.9)
3.0 Sample Collection Procedure
3.1 Obtain a sample of mat in accordance with Technical Association
of the Pulp and Paper Industry (TAPPI) method 1007 ``Sample Location.''
3.2 Use a 5- to 10-g sample cut into pieces small enough to fit into
the crucible.
3.3 Place the sample in the crucible. (Note 1: To test without the
use of a crucible, see Note 2 after Section 4.8.)
3.4 Condition the sample in the furnace set at 105 [plusmn] 3 [deg]C
(221 [plusmn] 9 [deg]F) for 5 minutes [plusmn] 30 seconds.
4.0 Procedure
4.1 Condition each sample by drying for 5 minutes [plusmn] 30
seconds at 105 [plusmn] 3 [deg]C (22 [plusmn] 5 [deg]F).
4.2 Remove the test sample from the furnace and cool in the
desiccator for 30 minutes in the standard atmosphere for testing glass
textiles.
4.3 Place the empty crucible in the furnace at 625 [plusmn] 25
[deg]C (1,157 [plusmn] 45 [deg]F). After 30 minutes, remove and cool the
crucible in the standard atmosphere (TAPPI method 1008) for 30 minutes.
4.4 Identify each crucible with respect to each test sample of mat.
4.5 Weigh the empty crucible to the nearest 0.001 g. Record this
weight as the tare mass, T.
4.6 Place the test sample in the crucible and weigh to the nearest
0.001 g. Record this weight as the initial mass, A.
4.7 Place the test sample and crucible in the furnace and ignite at
625 [plusmn] 25 [deg]C (1,157 [plusmn] 45 [deg]F).
4.8 After ignition for at least 30 minutes, remove the test sample
and crucible from the furnace and cool in the desiccator for 30 minutes
in the standard atmosphere (TAPPI method 1008).
4.9 Remove each crucible, and test each sample separately from the
desiccator, and immediately weigh each sample to the nearest 0.001 g.
Record this weight as the ignited mass, B. (Note 2: When it is known
that no ash residue separates from the test sample during the weighing
and igniting processes, you may weigh the sample separately without the
crucible. When this occurs, the tare mass (T) equals zero. With
appropriate care, you can dry and weigh a single piece of mat and place
with tongs into the ignition oven on appropriate refractory supports.
When the ignition time is over, remove the sample as an intact fragile
web and weigh it directly on a pan balance.)
5.0 Calculation
5.1 Calculate the LOI for each sample as follows:
[GRAPHIC] [TIFF OMITTED] TR11AP02.027
Where:
A = initial mass of crucible and sample before ignition (g);
B = mass of crucible and glass residue after ignition (g); and
T = tare mass of crucible, (g) (see Note 2).
5.2 Report the percent LOI of the glass mat to the nearest 0.1
percent.
6.0 Precision
The repeatability of this test method for measurements on adjacent
specimens from the same sample of mat is better than 1 percent.
Subpart JJJJ--National Emission Standards for Hazardous Air Pollutants:
Paper and Other Web Coating
Source: 67 FR 72341, Dec. 4, 2002, unless otherwise noted.
What This Subpart Covers
63.3280 What is in this subpart?
This subpart describes the actions you must take to reduce emissions
of organic hazardous air pollutants (HAP) from paper and other web
coating operations. This subpart establishes emission standards for web
coating lines and specifies what you must do to comply if you own or
operate a facility with web coating lines that is a major source of HAP.
Certain requirements apply to all who are subject to this subpart;
others depend on the means you use to comply with an emission standard.
Sec. 63.3290 Does this subpart apply to me?
The provisions of this subpart apply to each new and existing
facility that is a major source of HAP, as defined in Sec. 63.2, at
which web coating lines are operated.
[[Page 245]]
Sec. 63.3300 Which of my emission sources are affected by this subpart?
The affected source subject to this subpart is the collection of all
web coating lines at your facility. This includes web coating lines
engaged in the coating of metal webs that are used in flexible
packaging, and web coating lines engaged in the coating of fabric
substrates for use in pressure sensitive tape and abrasive materials.
Web coating lines specified in paragraphs (a) through (g) of this
section are not part of the affected source of this subpart.
(a) Any web coating line that is stand-alone coating equipment under
subpart KK of this part (national emission standards for the printing
and publishing industry) which the owner or operator includes in the
affected source under subpart KK.
(b) Any web coating line that is a product and packaging rotogravure
or wide-web flexographic press under subpart KK of this part (national
emission standards for the printing and publishing industry) which is
included in the affected source under subpart KK.
(c) Web coating in lithography, screenprinting, letterpress, and
narrow-web flexographic printing processes.
(d) Any web coating line subject to subpart EE of this part
(national emission standards for magnetic tape manufacturing
operations).
(e) Any web coating line that will be subject to the national
emission standards for hazardous air pollutants (NESHAP) for surface
coating of metal coil currently under development.
(f) Any web coating line that will be subject to the NESHAP for the
printing, coating, and dyeing of fabric and other textiles currently
under development. This would include any web coating line that coats
both a paper or other web substrate and a fabric or other textile
substrate, except for a fabric substrate used for pressure sensitive
tape and abrasive materials.
(g) Any web coating line that is defined as research or laboratory
equipment in Sec. 63.3310.
Sec. 63.3310 What definitions are used in this subpart?
All terms used in this subpart that are not defined in this section
have the meaning given to them in the Clean Air Act (CAA) and in subpart
A of this part.
Always-controlled work station means a work station associated with
a dryer from which the exhaust is delivered to a control device with no
provision for the dryer exhaust to bypass the control device unless
there is an interlock to interrupt and prevent continued coating during
a bypass. Sampling lines for analyzers, relief valves needed for safety
purposes, and periodic cycling of exhaust dampers to ensure safe
operation are not considered bypass lines.
Applied means, for the purposes of this subpart, the amount of
organic HAP, coating material, or coating solids (as appropriate for the
emission standards in Sec. 63.3320(b)) used by the affected source
during the compliance period.
As-applied means the condition of a coating at the time of
application to a substrate, including any added solvent.
As-purchased means the condition of a coating as delivered to the
user.
Capture efficiency means the fraction of all organic HAP emissions
generated by a process that is delivered to a control device, expressed
as a percentage.
Capture system means a hood, enclosed room, or other means of
collecting organic HAP emissions into a closed-vent system that exhausts
to a control device.
Car-seal means a seal that is placed on a device that is used to
change the position of a valve or damper (e.g., from open to closed) in
such a way that the position of the valve or damper cannot be changed
without breaking the seal.
Coating material(s) means all inks, varnishes, adhesives, primers,
solvents, reducers, and other coating materials applied to a substrate
via a web coating line. Materials used to form a substrate are not
considered coating materials.
Control device means a device such as a solvent recovery device or
oxidizer which reduces the organic HAP in an exhaust gas by recovery or
by destruction.
[[Page 246]]
Control device efficiency means the ratio of organic HAP emissions
recovered or destroyed by a control device to the total organic HAP
emissions that are introduced into the control device, expressed as a
percentage.
Day means a 24-consecutive-hour period.
Deviation means any instance in which an affected source, subject to
this subpart, or an owner or operator of such a source:
(1) Fails to meet any requirement or obligation established by this
subpart including, but not limited to, any emission limitation
(including any operating limit) or work practice standard;
(2) Fails to meet any term or condition that is adopted to implement
an applicable requirement in this subpart and that is included in the
operating permit for any affected source required to obtain such a
permit; or
(3) Fails to meet any emission limitation (including any operating
limit) or work practice standard in this subpart during start-up,
shutdown, or malfunction, regardless of whether or not such failure is
permitted by this subpart.
Existing affected source means any affected source the construction
or reconstruction of which is commenced on or before September 13, 2000,
and has not undergone reconstruction as defined in Sec. 63.2.
Fabric means any woven, knitted, plaited, braided, felted, or non-
woven material made of filaments, fibers, or yarns including thread.
This term includes material made of fiberglass, natural fibers,
synthetic fibers, or composite materials.
Facility means all contiguous or adjoining property that is under
common ownership or control, including properties that are separated
only by a road or other public right-of-way.
Flexible packaging means any package or part of a package the shape
of which can be readily changed. Flexible packaging includes, but is not
limited to, bags, pouches, labels, liners and wraps utilizing paper,
plastic, film, aluminum foil, metalized or coated paper or film, or any
combination of these materials.
Formulation data means data on the organic HAP mass fraction,
volatile matter mass fraction, or coating solids mass fraction of a
material that is generated by the manufacturer or means other than a
test method specified in this subpart or an approved alternative method.
HAP means hazardous air pollutants.
HAP applied means the organic HAP content of all coating materials
applied to a substrate by a web coating line at an affected source.
Intermittently-controlled work station means a work station
associated with a dryer with provisions for the dryer exhaust to be
delivered to or diverted from a control device through a bypass line,
depending on the position of a valve or damper. Sampling lines for
analyzers, relief valves needed for safety purposes, and periodic
cycling of exhaust dampers to ensure safe operation are not considered
bypass lines.
Metal coil means a continuous metal strip that is at least 0.15
millimeter (0.006 inch) thick which is packaged in a roll or coil prior
to coating. After coating, it may or may not be rewound into a roll or
coil. Metal coil does not include metal webs that are coated for use in
flexible packaging.
Month means a calendar month or a pre-specified period of 28 days to
35 days to allow for flexibility in recordkeeping when data are based on
a business accounting period.
Never-controlled work station means a work station that is not
equipped with provisions by which any emissions, including those in the
exhaust from any associated dryer, may be delivered to a control device.
New affected source means any affected source the construction or
reconstruction of which is commenced after September 13, 2000.
Overall organic HAP control efficiency means the total efficiency of
a capture and control system.
Pressure sensitive tape means a flexible backing material with a
pressure-sensitive adhesive coating on one or both sides of the backing.
Examples include, but are not limited to, duct/duct insulation tape and
medical tape.
Research or laboratory equipment means any equipment for which the
primary purpose is to conduct research and development into new
processes and products where such equipment is operated under the close
supervision of
[[Page 247]]
technically trained personnel and is not engaged in the manufacture of
products for commercial sale in commerce except in a de minimis manner.
Rewind or cutting station means a unit from which substrate is
collected at the outlet of a web coating line.
Uncontrolled coating line means a coating line consisting of only
never-controlled work stations.
Unwind or feed station means a unit from which substrate is fed to a
web coating line.
Web means a continuous substrate (e.g., paper, film, foil) which is
flexible enough to be wound or unwound as rolls.
Web coating line means any number of work stations, of which one or
more applies a continuous layer of coating material across the entire
width or any portion of the width of a web substrate, and any associated
curing/drying equipment between an unwind or feed station and a rewind
or cutting station.
Work station means a unit on a web coating line where coating
material is deposited onto a web substrate.
Emission Standards and Compliance Dates
Sec. 63.3320 What emission standards must I meet?
(a) If you own or operate any affected source that is subject to the
requirements of this subpart, you must comply with these requirements on
and after the compliance dates as specified in Sec. 63.3330.
(b) You must limit organic HAP emissions to the level specified in
paragraph (b)(1), (2), (3), or (4) of this section.
(1) No more than 5 percent of the organic HAP applied for each month
(95 percent reduction) at existing affected sources, and no more than 2
percent of the organic HAP applied for each month (98 percent reduction)
at new affected sources; or
(2) No more than 4 percent of the mass of coating materials applied
for each month at existing affected sources, and no more than 1.6
percent of the mass of coating materials applied for each month at new
affected sources; or
(3) No more than 20 percent of the mass of coating solids applied
for each month at existing affected sources, and no more than 8 percent
of the coating solids applied for each month at new affected sources.
(4) If you use an oxidizer to control organic HAP emissions, operate
the oxidizer such that an outlet organic HAP concentration of no greater
than 20 parts per million by volume (ppmv) by compound on a dry basis is
achieved and the efficiency of the capture system is 100 percent.
(c) You must demonstrate compliance with this subpart by following
the procedures in Sec. 63.3370.
Sec. 63.3321 What operating limits must I meet?
(a) For any web coating line or group of web coating lines for which
you use add-on control devices, unless you use a solvent recovery system
and conduct a liquid-liquid material balance, you must meet the
operating limits specified in Table 1 to this subpart or according to
paragraph (b) of this section. These operating limits apply to emission
capture systems and control devices, and you must establish the
operating limits during the performance test according to the
requirements in Sec. 63.3360(e)(3). You must meet the operating limits
at all times after you establish them.
(b) If you use an add-on control device other than those listed in
Table 1 to this subpart or wish to monitor an alternative parameter and
comply with a different operating limit, you must apply to the
Administrator for approval of alternative monitoring under Sec. 63.8(f).
Sec. 63.3330 When must I comply?
(a) If you own or operate an existing affected source subject to the
provisions of this subpart, you must comply by the compliance date. The
compliance date for existing affected sources in this subpart is
December 5, 2005. You must complete any performance test required in
Sec. 63.3360 within the time limits specified in Sec. 63.7(a)(2).
(b) If you own or operate a new affected source subject to the
provisions of this subpart, your compliance date is immediately upon
start-up of the
[[Page 248]]
new affected source or by December 4, 2002, whichever is later. You must
complete any performance test required in Sec. 63.3360 within the time
limits specified in Sec. 63.7(a)(2).
(c) If you own or operate a reconstructed affected source subject to
the provisions of this subpart, your compliance date is immediately upon
startup of the affected source or by December 4, 2002, whichever is
later. Existing affected sources which have undergone reconstruction as
defined in Sec. 63.2 are subject to the requirements for new affected
sources. The costs associated with the purchase and installation of air
pollution control equipment are not considered in determining whether
the existing affected source has been reconstructed. Additionally, the
costs of retrofitting and replacing of equipment that is installed
specifically to comply with this subpart are not considered
reconstruction costs. You must complete any performance test required in
Sec. 63.3360 within the time limits specified in Sec. 63.7(a)(2).
General Requirements for Compliance With the Emission Standards and for
Monitoring and Performance Tests
Sec. 63.3340 What general requirements must I meet to comply with the standards?
Table 2 to this subpart specifies the provisions of subpart A of
this part that apply if you are subject to this subpart, such as
startup, shutdown, and malfunction plans (SSMP) in Sec. 63.6(e)(3) for
affected sources using a control device to comply with the emission
standards.
Sec. 63.3350 If I use a control device to comply with the emission standards, what monitoring must I do?
(a) A summary of monitoring you must do follows:
------------------------------------------------------------------------
If you operate a web coating
line, and have the following: Then you must:
------------------------------------------------------------------------
(1) Intermittently-controlled Record parameters related to possible
work stations. exhaust flow bypass of control device
and to coating use (Sec. 63.3350(c)).
(2) Solvent recovery unit.... Operate continuous emission monitoring
system and perform quarterly audits or
determine volatile matter recovered and
conduct a liquid-liquid material balance
(Sec. 63.3350(d)).
(3) Control Device........... Operate continuous parameter monitoring
system (Sec. 63.3350(e)).
(4) Capture system........... Monitor capture system operating
parameter (Sec. 63.3350(f)).
------------------------------------------------------------------------
(b) Following the date on which the initial performance test of a
control device is completed to demonstrate continuing compliance with
the standards, you must monitor and inspect each capture system and each
control device used to comply with Sec. 63.3320. You must install and
operate the monitoring equipment as specified in paragraphs (c) and (f)
of this section.
(c) Bypass and coating use monitoring. If you own or operate web
coating lines with intermittently-controlled work stations, you must
monitor bypasses of the control device and the mass of each coating
material applied at the work station during any such bypass. If using a
control device for complying with the requirements of this subpart, you
must demonstrate that any coating material applied on a never-controlled
work station or an intermittently-controlled work station operated in
bypass mode is allowed in your compliance demonstration according to
Sec. 63.3370(n) and (o). The bypass monitoring must be conducted using
at least one of the procedures in paragraphs (c)(1) through (4) of this
section for each work station and associated dryer.
(1) Flow control position indicator. Install, calibrate, maintain,
and operate according to the manufacturer's specifications a flow
control position indicator that provides a record indicating whether the
exhaust stream from the dryer was directed to the control device or was
diverted from the control device. The time and flow control position
must be recorded at least once per hour as well as every time the flow
direction is changed. A flow control position indicator must be
installed at the entrance to any bypass line that could
[[Page 249]]
divert the exhaust stream away from the control device to the
atmosphere.
(2) Car-seal or lock-and-key valve closures. Secure any bypass line
valve in the closed position with a car-seal or a lock-and-key type
configuration. A visual inspection of the seal or closure mechanism must
be performed at least once every month to ensure that the valve or
damper is maintained in the closed position, and the exhaust stream is
not diverted through the bypass line.
(3) Valve closure continuous monitoring. Ensure that any bypass line
valve or damper is in the closed position through continuous monitoring
of valve position when the emission source is in operation and is using
a control device for compliance with the requirements of this subpart.
The monitoring system must be inspected at least once every month to
verify that the monitor will indicate valve position.
(4) Automatic shutdown system. Use an automatic shutdown system in
which the web coating line is stopped when flow is diverted away from
the control device to any bypass line when the control device is in
operation. The automatic system must be inspected at least once every
month to verify that it will detect diversions of flow and would shut
down operations in the event of such a diversion.
(d) Solvent recovery unit. If you own or operate a solvent recovery
unit to comply with Sec. 63.3320, you must meet the requirements in
either paragraph (d)(1) or (2) of this section depending on how control
efficiency is determined.
(1) Continuous emission monitoring system (CEMS). If you are
demonstrating compliance with the emission standards in Sec. 63.3320
through continuous emission monitoring of a control device, you must
install, calibrate, operate, and maintain the CEMS according to
paragraphs (d)(1)(i) through (iii) of this section.
(i) Measure the total organic volatile matter mass flow rate at both
the control device inlet and the outlet such that the reduction
efficiency can be determined. Each continuous emission monitor must
comply with performance specification 6, 8, or 9 of 40 CFR part 60,
appendix B, as appropriate.
(ii) You must follow the quality assurance procedures in procedure
1, appendix F of 40 CFR part 60. In conducting the quarterly audits of
the monitors as required by procedure 1, appendix F, you must use
compounds representative of the gaseous emission stream being
controlled.
(iii) You must have valid data from at least 90 percent of the hours
during which the process is operated.
(2) Liquid-liquid material balance. If you are demonstrating
compliance with the emission standards in Sec. 63.3320 through liquid-
liquid material balance, you must install, calibrate, maintain, and
operate according to the manufacturer's specifications a device that
indicates the cumulative amount of volatile matter recovered by the
solvent recovery device on a monthly basis. The device must be certified
by the manufacturer to be accurate to within [plusmn]2.0 percent by
mass.
(e) Continuous parameter monitoring system (CPMS). If you are using
a control device to comply with the emission standards in Sec. 63.3320,
you must install, operate, and maintain each CPMS specified in
paragraphs (e)(9) and (10) and (f) of this section according to the
requirements in paragraphs (e)(1) through (8) of this section. You must
install, operate, and maintain each CPMS specified in paragraph (c) of
this section according to paragraphs (e)(5) through (7) of this section.
(1) Each CPMS must complete a minimum of one cycle of operation for
each successive 15-minute period. You must have a minimum of four
equally spaced successive cycles of CPMS operation to have a valid hour
of data.
(2) You must have valid data from at least 90 percent of the hours
during which the process operated.
(3) You must determine the hourly average of all recorded readings
according to paragraphs (e)(3)(i) and (ii) of this section.
(i) To calculate a valid hourly value, you must have at least three
of four equally spaced data values from that hour from a continuous
monitoring system (CMS) that is not out-of-control.
(ii) Provided all of the readings recorded in accordance with
paragraph
[[Page 250]]
(e)(3) of this section clearly demonstrate continuous compliance with
the standard that applies to you, then you are not required to determine
the hourly average of all recorded readings.
(4) You must determine the rolling 3-hour average of all recorded
readings for each operating period. To calculate the average for each 3-
hour averaging period, you must have at least two of three of the hourly
averages for that period using only average values that are based on
valid data (i.e., not from out-of-control periods).
(5) You must record the results of each inspection, calibration, and
validation check of the CPMS.
(6) At all times, you must maintain the monitoring system in proper
working order including, but not limited to, maintaining necessary parts
for routine repairs of the monitoring equipment.
(7) Except for monitoring malfunctions, associated repairs, or
required quality assurance or control activities (including calibration
checks or required zero and span adjustments), you must conduct all
monitoring at all times that the unit is operating. Data recorded during
monitoring malfunctions, associated repairs, out-of-control periods, or
required quality assurance or control activities shall not be used for
purposes of calculating the emissions concentrations and percent
reductions specified in Sec. 63.3370. You must use all the valid data
collected during all other periods in assessing compliance of the
control device and associated control system. A monitoring malfunction
is any sudden, infrequent, not reasonably preventable failure of the
monitoring system to provide valid data. Monitoring failures that are
caused in part by poor maintenance or careless operation are not
malfunctions.
(8) Any averaging period for which you do not have valid monitoring
data and such data are required constitutes a deviation, and you must
notify the Administrator in accordance with Sec. 63.3400(c).
(9) Oxidizer. If you are using an oxidizer to comply with the
emission standards, you must comply with paragraphs (e)(9)(i) through
(iii) of this section.
(i) Install, calibrate, maintain, and operate temperature monitoring
equipment according to the manufacturer's specifications. The
calibration of the chart recorder, data logger, or temperature indicator
must be verified every 3 months or the chart recorder, data logger, or
temperature indicator must be replaced. You must replace the equipment
whether you choose not to perform the calibration or the equipment
cannot be calibrated properly.
(ii) For an oxidizer other than a catalytic oxidizer, install,
calibrate, operate, and maintain a temperature monitoring device
equipped with a continuous recorder. The device must have an accuracy of
[plusmn]1 percent of the temperature being monitored in degrees Celsius,
or [plusmn]1 [deg]Celsius, whichever is greater. The thermocouple or
temperature sensor must be installed in the combustion chamber at a
location in the combustion zone.
(iii) For a catalytic oxidizer, install, calibrate, operate, and
maintain a temperature monitoring device equipped with a continuous
recorder. The device must be capable of monitoring temperature with an
accuracy of [plusmn]1 percent of the temperature being monitored in
degrees Celsius or [plusmn] 1 degree Celsius, whichever is greater. The
thermocouple or temperature sensor must be installed in the vent stream
at the nearest feasible point to the inlet and outlet of the catalyst
bed. Calculate the temperature rise across the catalyst.
(10) Other types of control devices. If you use a control device
other than an oxidizer or wish to monitor an alternative parameter and
comply with a different operating limit, you must apply to the
Administrator for approval of an alternative monitoring method under
Sec. 63.8(f).
(f) Capture system monitoring. If you are complying with the
emission standards in Sec. 63.3320 through the use of a capture system
and control device for one or more web coating lines, you must develop a
site-specific monitoring plan containing the information specified in
paragraphs (f)(1) and (2) of this section for these capture systems. You
must monitor the capture system in accordance with paragraph (f)(3) of
this
[[Page 251]]
section. You must make the monitoring plan available for inspection by
the permitting authority upon request.
(1) The monitoring plan must:
(i) Identify the operating parameter to be monitored to ensure that
the capture efficiency determined during the initial compliance test is
maintained; and
(ii) Explain why this parameter is appropriate for demonstrating
ongoing compliance; and
(iii) Identify the specific monitoring procedures.
(2) The monitoring plan must specify the operating parameter value
or range of values that demonstrate compliance with the emission
standards in Sec. 63.3320. The specified operating parameter value or
range of values must represent the conditions present when the capture
system is being properly operated and maintained.
(3) You must conduct all capture system monitoring in accordance
with the plan.
(4) Any deviation from the operating parameter value or range of
values which are monitored according to the plan will be considered a
deviation from the operating limit.
(5) You must review and update the capture system monitoring plan at
least annually.
Sec. 63.3360 What performance tests must I conduct?
(a) The performance test methods you must conduct are as follows:
------------------------------------------------------------------------
If you control organic HAP on any
individual web coating line or any You must:
group of web coating lines by:
------------------------------------------------------------------------
(1) Limiting organic HAP or Determine the organic HAP or
volatile matter content of volatile matter and coating solids
coatings. content of coating materials
according to procedures in Sec.
63.3360(c) and (d). If applicable,
determine the mass of volatile
matter retained in the coated web
or otherwise not emitted to the
atmosphere according to Sec.
63.3360(g).
(2) Using a capture and control Conduct a performance test for each
system. capture and control system to
determine: the destruction or
removal efficiency of each control
device other than solvent recovery
according to Sec. 63.3360(e), and
the capture efficiency of each
capture system according to Sec.
63.3360(f). If applicable,
determine the mass of volatile
matter retained in the coated web
or otherwise not emitted to the
atmosphere according to Sec.
63.3360(g).
------------------------------------------------------------------------
(b) If you are using a control device to comply with the emission
standards in Sec. 63.3320, you are not required to conduct a performance
test to demonstrate compliance if one or more of the criteria in
paragraphs (b)(1) through (3) of this section are met.
(1) The control device is equipped with continuous emission monitors
for determining inlet and outlet total organic volatile matter
concentration and capture efficiency has been determined in accordance
with the requirements of this subpart such that an overall organic HAP
control efficiency can be calculated, and the continuous emission
monitors are used to demonstrate continuous compliance in accordance
with Sec. 63.3350; or
(2) You have met the requirements of Sec. 63.7(h) (for waiver of
performance testing; or
(3) The control device is a solvent recovery system and you comply
by means of a monthly liquid-liquid material balance.
(c) Organic HAP content. If you determine compliance with the
emission standards in Sec. 63.3320 by means other than determining the
overall organic HAP control efficiency of a control device, you must
determine the organic HAP mass fraction of each coating material ``as-
purchased'' by following one of the procedures in paragraphs (c)(1)
through (3) of this section, and determine the organic HAP mass fraction
of each coating material ``as-applied'' by following the procedures in
paragraph (c)(4) of this section. If the organic HAP content values are
not determined using the procedures in paragraphs (c)(1) through (3) of
this section, the owner or operator must submit an alternative test
method for determining their values for approval by the Administrator in
accordance with Sec. 63.7(f). The recovery efficiency of the test method
must be determined for all of
[[Page 252]]
the target organic HAP and a correction factor, if necessary, must be
determined and applied.
(1) Method 311. You may test the coating material in accordance with
Method 311 of appendix A of this part. The Method 311 determination may
be performed by the manufacturer of the coating material and the results
provided to the owner or operator. The organic HAP content must be
calculated according to the criteria and procedures in paragraphs
(c)(1)(i) through (iii) of this section.
(i) Include each organic HAP determined to be present at greater
than or equal to 0.1 mass percent for Occupational Safety and Health
Administration (OSHA)-defined carcinogens as specified in 29 CFR
1910.1200(d)(4) and greater than or equal to 1.0 mass percent for other
organic HAP compounds.
(ii) Express the mass fraction of each organic HAP you include
according to paragraph (c)(1)(i) of this section as a value truncated to
four places after the decimal point (for example, 0.3791).
(iii) Calculate the total mass fraction of organic HAP in the tested
material by summing the counted individual organic HAP mass fractions
and truncating the result to three places after the decimal point (for
example, 0.763).
(2) Method 24. For coatings, determine the volatile organic content
as mass fraction of nonaqueous volatile matter and use it as a
substitute for organic HAP using Method 24 of 40 CFR part 60, appendix
A. The Method 24 determination may be performed by the manufacturer of
the coating and the results provided to you.
(3) Formulation data. You may use formulation data to determine the
organic HAP mass fraction of a coating material. Formulation data may be
provided to the owner or operator by the manufacturer of the material.
In the event of an inconsistency between Method 311 (appendix A of 40
CFR part 63) test data and a facility's formulation data, and the Method
311 test value is higher, the Method 311 data will govern. Formulation
data may be used provided that the information represents all organic
HAP present at a level equal to or greater than 0.1 percent for OSHA-
defined carcinogens as specified in 29 CFR 1910.1200(d)(4) and equal to
or greater than 1.0 percent for other organic HAP compounds in any raw
material used.
(4) As-applied organic HAP mass fraction. If the as-purchased
coating material is applied to the web without any solvent or other
material added, then the as-applied organic HAP mass fraction is equal
to the as-purchased organic HAP mass fraction. Otherwise, the as-applied
organic HAP mass fraction must be calculated using Equation 1a of
Sec. 63.3370.
(d) Volatile organic and coating solids content. If you determine
compliance with the emission standards in Sec. 63.3320 by means other
than determining the overall organic HAP control efficiency of a control
device and you choose to use the volatile organic content as a surrogate
for the organic HAP content of coatings, you must determine the as-
purchased volatile organic content and coating solids content of each
coating material applied by following the procedures in paragraph (d)(1)
or (2) of this section, and the as-applied volatile organic content and
coating solids content of each coating material by following the
procedures in paragraph (d)(3) of this section.
(1) Method 24. You may determine the volatile organic and coating
solids mass fraction of each coating applied using Method 24 (40 CFR
part 60, appendix A.) The Method 24 determination may be performed by
the manufacturer of the material and the results provided to you. If
these values cannot be determined using Method 24, you must submit an
alternative technique for determining their values for approval by the
Administrator.
(2) Formulation data. You may determine the volatile organic content
and coating solids content of a coating material based on formulation
data and may rely on volatile organic content data provided by the
manufacturer of the material. In the event of any inconsistency between
the formulation data and the results of Method 24 of 40 CFR part 60,
appendix A, and the Method 24 results are higher, the results of Method
24 will govern.
(3) As-applied volatile organic content and coating solids content.
If the as-purchased coating material is applied to the web without any
solvent or other
[[Page 253]]
material added, then the as-applied volatile organic content is equal to
the as-purchased volatile content and the as-applied coating solids
content is equal to the as-purchased coating solids content. Otherwise,
the as-applied volatile organic content must be calculated using
Equation 1b of Sec. 63.3370 and the as-applied coating solids content
must be calculated using Equation 2 of Sec. 63.3370.
(e) Control device efficiency. If you are using an add-on control
device other than solvent recovery, such as an oxidizer, to comply with
the emission standards in Sec. 63.3320, you must conduct a performance
test to establish the destruction or removal efficiency of the control
device according to the methods and procedures in paragraphs (e)(1) and
(2) of this section. During the performance test, you must establish the
operating limits required by Sec. 63.3321 according to paragraph (e)(3)
of this section.
(1) An initial performance test to establish the destruction or
removal efficiency of the control device must be conducted such that
control device inlet and outlet testing is conducted simultaneously, and
the data are reduced in accordance with the test methods and procedures
in paragraphs (e)(1)(i) through (ix) of this section. You must conduct
three test runs as specified in Sec. 63.7(e)(3), and each test run must
last at least 1 hour.
(i) Method 1 or 1A of 40 CFR part 60, appendix A, must be used for
sample and velocity traverses to determine sampling locations.
(ii) Method 2, 2A, 2C, 2D, 2F, or 2G of 40 CFR part 60, appendix A,
must be used to determine gas volumetric flow rate.
(iii) Method 3, 3A, or 3B of 40 CFR part 60, appendix A, must be
used for gas analysis to determine dry molecular weight. You may also
use as an alternative to Method 3B the manual method for measuring the
oxygen, carbon dioxide, and carbon monoxide content of exhaust gas in
ANSI/ASME PTC 19.10-1981, ``Flue and Exhaust Gas Analyses [Part 10,
Instruments and Apparatus],'' (incorporated by reference, see
Sec. 63.14).
(iv) Method 4 of 40 CFR part 60, appendix A, must be used to
determine stack gas moisture.
(v) The gas volumetric flow rate, dry molecular weight, and stack
gas moisture must be determined during each test run specified in
paragraph (f)(1)(vii) of this section.
(vi) Method 25 or 25A of 40 CFR part 60, appendix A, must be used to
determine total gaseous non-methane organic matter concentration. Use
the same test method for both the inlet and outlet measurements which
must be conducted simultaneously. You must submit notice of the intended
test method to the Administrator for approval along with notification of
the performance test required under Sec. 63.7(b). You must use Method
25A if any of the conditions described in paragraphs (e)(1)(vi)(A)
through (D) of this section apply to the control device.
(A) The control device is not an oxidizer.
(B) The control device is an oxidizer but an exhaust gas volatile
organic matter concentration of 50 ppmv or less is required to comply
with the emission standards in Sec. 63.3320; or
(C) The control device is an oxidizer but the volatile organic
matter concentration at the inlet to the control system and the required
level of control are such that they result in exhaust gas volatile
organic matter concentrations of 50 ppmv or less; or
(D) The control device is an oxidizer but because of the high
efficiency of the control device the anticipated volatile organic matter
concentration at the control device exhaust is 50 ppmv or less,
regardless of inlet concentration.
(vii) Except as provided in Sec. 63.7(e)(3), each performance test
must consist of three separate runs with each run conducted for at least
1 hour under the conditions that exist when the affected source is
operating under normal operating conditions. For the purpose of
determining volatile organic compound concentrations and mass flow
rates, the average of the results of all the runs will apply.
(viii) Volatile organic matter mass flow rates must be determined
for each run specified in paragraph (e)(1)(vii) of
[[Page 254]]
this section using Equation 1 of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.025
Where:
Mf = Total organic volatile matter mass flow rate, kilograms
(kg)/hour (h).
Qsd = Volumetric flow rate of gases entering or exiting the
control device, as determined according to Sec. 63.3360(e)(1)(ii), dry
standard cubic meters (dscm)/h.
Cc = Concentration of organic compounds as carbon, ppmv.
12.0 = Molecular weight of carbon.
0.0416 = Conversion factor for molar volume, kg-moles per cubic meter
(mol/m\3\) (@ 293 Kelvin (K) and 760 millimeters of mercury (mmHg)).
(ix) For each run, emission control device destruction or removal
efficiency must be determined using Equation 2 of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.026
Where:
E = Organic volatile matter control efficiency of the control device,
percent.
Mfi = Organic volatile matter mass flow rate at the inlet to
the control device, kg/h.
Mfo = Organic volatile matter mass flow rate at the outlet of
the control device, kg/h.
(x) The control device destruction or removal efficiency is
determined as the average of the efficiencies determined in the test
runs and calculated in Equation 2 of this section.
(2) You must record such process information as may be necessary to
determine the conditions in existence at the time of the performance
test. Operations during periods of startup, shutdown, and malfunction
will not constitute representative conditions for the purpose of a
performance test.
(3) Operating limits. If you are using one or more add-on control
device other than a solvent recovery system for which you conduct a
liquid-liquid material balance to comply with the emission standards in
Sec. 63.3320, you must establish the applicable operating limits
required by Sec. 63.3321. These operating limits apply to each add-on
emission control device, and you must establish the operating limits
during the performance test required by paragraph (e) of this section
according to the requirements in paragraphs (e)(3)(i) and (ii) of this
section.
(i) Thermal oxidizer. If your add-on control device is a thermal
oxidizer, establish the operating limits according to paragraphs
(e)(3)(i)(A) and (B) of this section.
(A) During the performance test, you must monitor and record the
combustion temperature at least once every 15 minutes during each of the
three test runs. You must monitor the temperature in the firebox of the
thermal oxidizer or immediately downstream of the firebox before any
substantial heat exchange occurs.
(B) Use the data collected during the performance test to calculate
and record the average combustion temperature maintained during the
performance test. This average combustion temperature is the minimum
operating limit for your thermal oxidizer.
(ii) Catalytic oxidizer. If your add-on control device is a
catalytic oxidizer, establish the operating limits according to
paragraphs (e)(3)(ii)(A) and (B) or paragraphs (e)(3)(ii)(C) and (D) of
this section.
(A) During the performance test, you must monitor and record the
temperature just before the catalyst bed and the temperature difference
across the catalyst bed at least once every 15 minutes during each of
the three test runs.
(B) Use the data collected during the performance test to calculate
and record the average temperature just before the catalyst bed and the
average temperature difference across the catalyst bed maintained during
the performance test. These are the minimum operating limits for your
catalytic oxidizer.
(C) As an alternative to monitoring the temperature difference
across the catalyst bed, you may monitor the temperature at the inlet to
the catalyst bed and implement a site-specific inspection and
maintenance plan for your catalytic oxidizer as specified in paragraph
(e)(3)(ii)(D) of this section.
[[Page 255]]
During the performance test, you must monitor and record the temperature
just before the catalyst bed at least once every 15 minutes during each
of the three test runs. Use the data collected during the performance
test to calculate and record the average temperature just before the
catalyst bed during the performance test. This is the minimum operating
limit for your catalytic oxidizer.
(D) You must develop and implement an inspection and maintenance
plan for your catalytic oxidizer(s) for which you elect to monitor
according to paragraph (e)(3)(ii)(C) of this section. The plan must
address, at a minimum, the elements specified in paragraphs
(e)(3)(ii)(D)(1) through (3) of this section.
(1) Annual sampling and analysis of the catalyst activity (i.e.,
conversion efficiency) following the manufacturer's or catalyst
supplier's recommended procedures,
(2) Monthly inspection of the oxidizer system including the burner
assembly and fuel supply lines for problems, and
(3) Annual internal and monthly external visual inspection of the
catalyst bed to check for channeling, abrasion, and settling. If
problems are found, you must take corrective action consistent with the
manufacturer's recommendations and conduct a new performance test to
determine destruction efficiency in accordance with this section.
(f) Capture efficiency. If you demonstrate compliance by meeting the
requirements of Sec. 63.3370(e), (f), (g), (h), (i)(2), (k), (n)(2) or
(3), or (p), you must determine capture efficiency using the procedures
in paragraph (f)(1), (2), or (3) of this section, as applicable.
(1) You may assume your capture efficiency equals 100 percent if
your capture system is a permanent total enclosure (PTE). You must
confirm that your capture system is a PTE by demonstrating that it meets
the requirements of section 6 of EPA Method 204 of 40 CFR part 51,
appendix M, and that all exhaust gases from the enclosure are delivered
to a control device.
(2) You may determine capture efficiency according to the protocols
for testing with temporary total enclosures that are specified in
Methods 204 and 204A through F of 40 CFR part 51, appendix M. You may
exclude never-controlled work stations from such capture efficiency
determinations.
(3) You may use any capture efficiency protocol and test methods
that satisfy the criteria of either the Data Quality Objective or the
Lower Confidence Limit approach as described in appendix A of subpart KK
of this part. You may exclude never-controlled work stations from such
capture efficiency determinations.
(g) Volatile matter retained in the coated web or otherwise not
emitted to the atmosphere. You may choose to take into account the mass
of volatile matter retained in the coated web after curing or drying or
otherwise not emitted to the atmosphere when determining compliance with
the emission standards in Sec. 63.3320. If you choose this option, you
must develop a testing protocol to determine the mass of volatile matter
retained in the coated web or otherwise not emitted to the atmosphere
and submit this protocol to the Administrator for approval. You must
submit this protocol with your site-specific test plan under
Sec. 63.7(f). If you intend to take into account the mass of volatile
matter retained in the coated web after curing or drying or otherwise
not emitted to the atmosphere and demonstrate compliance according to
Sec. 63.3370(c)(3), (c)(4), (c)(5), or (d), then the test protocol you
submit must determine the mass of organic HAP retained in the coated web
or otherwise not emitted to the atmosphere. Otherwise, compliance must
be shown using the volatile organic matter content as a surrogate for
the HAP content of the coatings.
(h) Control devices in series. If you use multiple control devices
in series to comply with the emission standards in Sec. 63.3320, the
performance test must include, at a minimum, the inlet to the first
control device in the series, the outlet of the last control device in
the series, and all intermediate streams (e.g., gaseous exhaust to the
atmosphere or a liquid stream from a recovery device) that are not
subsequently treated by any of the control devices in the series.
[[Page 256]]
Requirements for Showing Compliance
Sec. 63.3370 How do I demonstrate compliance with the emission standards?
(a) A summary of how you must demonstrate compliance follows:
------------------------------------------------------------------------
If you choose to demonstrate Then you must
compliance by: demonstrate that: To accomplish this:
------------------------------------------------------------------------
(1) Use of ``as-purchased'' (i) Each coating Follow the
compliant coating materials. material used at an procedures set out
existing affected in Sec.
source does not 63.3370(b).
exceed 0.04 kg
organic HAP per kg
coating material,
and each coating
material used at a
new affected source
does not exceed
0.016 kg organic
HAP per kg coating
material as-
purchased; or.
(ii) Each coating Follow the
material used at an procedures set out
existing affected in Sec.
source does not 63.3370(b).
exceed 0.2 kg
organic HAP per kg
coating solids, and
each coating
material used at a
new affected source
does not exceed
0.08 kg organic HAP
per kg coating
solids as-purchased.
(2) Use of ``as-applied'' (i) Each coating Follow the
compliant coating materials. material used at an procedures set out
existing affected in Sec.
source does not 63.3370(c)(1). Use
exceed 0.04 kg either Equation 1a
organic HAP per kg or b of Sec.
coating material, 63.3370 to
and each coating determine
material used at a compliance with
new affected source Sec. 63.3320(b)(2)
does not exceed in accordance with
0.016 kg organic Sec. 63.3370(c)(5)
HAP per kg coating (i).
material as-
applied; or.
(ii) Each coating Follow the
material used at an procedures set out
existing affected in Sec.
source does not 63.3370(c)(2). Use
exceed 0.2 kg Equations 2 and 3
organic HAP per kg of Sec. 63.3370 to
coating solids, and determine
each coating compliance with
material used at a Sec. 63.3320(b)(3)
new affected source in accordance with
does not exceed Sec. 63.3370(c)(5)
0.08 kg organic HAP (i).
per kg coating
solids as-applied;
or.
(iii) Monthly Follow the
average of all procedures set out
coating materials in Sec.
used at an existing 63.3370(c)(3). Use
affected source Equation 4 of Sec.
does not exceed 63.3370 to
0.04 kg organic HAP determine
per kg coating compliance with
material, and Sec. 63.3320(b)(2)
monthly average of in accordance with
all coating Sec. 63.3370(c)(5)
materials used at a (ii).
new affected source
does not exceed
0.016 kg organic
HAP per kg coating
material as-applied
on a monthly
average basis; or.
(iv) Monthly average Follow the
of all coating procedures set out
materials used at in Sec.
an existing 63.3370(c)(4). Use
affected source Equation 5 of Sec.
does not exceed 0.2 63.3370 to
kg organic HAP per determine
kg coating solids, compliance with
and monthly average Sec. 63.3320(b)(3)
of all coating in accordance with
materials used at a Sec. 63.3370(c)(5)
new affected source (ii).
does not exceed
0.08 kg organic HAP
per kg coating
solids as-applied
on a monthly
average basis.
(3) Tracking total monthly Total monthly Follow the
organic HAP applied. organic HAP applied procedures set out
does not exceed the in Sec.
calculated limit 63.3370(d). Show
based on emission that total monthly
limitations. HAP applied
(Equation 6 of Sec.
63.3370) is less
than the calculated
equivalent
allowable organic
HAP (Equation 13a
or b of Sec.
63.3370).
(4) Use of a capture system (i) Overall organic Follow the
and control device. HAP control procedures set out
efficiency is equal in Sec. 63.3370(e)
to 95 percent at an to determine
existing affected compliance with
source and 98 Sec. 63.3320(b)(1)
percent at a new according to Sec.
affected source on 63.3370(i) if using
a monthly basis; or a solvent recovery
oxidizer outlet device, or Sec.
organic HAP 63.3370(j) if using
concentration is no a control device
greater than 20 and CPMS, or Sec.
ppmv by compound 63.3370(k) if using
and capture an oxidizer.
efficiency is 100
percent; or
operating
parameters are
continuously
monitored; or.
[[Page 257]]
(ii) Overall organic Follow the
HAP emission rate procedures set out
does not exceed 0.2 in Sec. 63.3370(f)
kg organic HAP per to determine
kg coating solids compliance with
for an existing Sec. 63.3320(b)(3)
affected source or according to Sec.
0.08 kg organic HAP 63.3370(i) if using
per kg coating a solvent recovery
solids for a new device, or Sec.
affected source on 63.3370(k) if using
a monthly average an oxidizer.
as-applied basis;.
(iii) Overall Follow the
organic HAP procedures set out
emission rate does in Sec. 63.3370(g)
not exceed 0.04 kg to determine
organic HAP per kg compliance with
coating material Sec. 63.3320(b)(2)
for an existing according to Sec.
affected source or 63.3370(i) if using
0.016 kg organic a solvent recovery
HAP per kg coating device, or Sec.
material for a new 63.3370(k) if using
affected source on an oxidizer.
a monthly average
as-applied basis;
or.
(iv) Overall organic Follow the
HAP emission rate procedures set out
does not exceed the in Sec.
calculated limit 63.3370(h). Show
based on emission that the monthly
limitations. organic HAP
emission rate is
less than the
calculated
equivalent
allowable organic
HAP emission rate
(Equation 13a or b
of Sec. 63.3370).
Calculate the
monthly organic HAP
emission rate
according to Sec.
63.3370(i) if using
a solvent recovery
device, or Sec.
63.3370(k) if using
an oxidizer.
(5) Use of multiple capture (i) Overall organic Follow the
and/or control devices. HAP control procedures set out
efficiency is equal in Sec. 63.3370(e)
to 95 percent at an to determine
existing affected compliance with
source and 98 Sec. 63.3320(b)(1)
percent at a new according to Sec.
affected source on 63.3370(e)(1) or
a monthly basis; or. (2).
(ii) Average Follow the
equivalent organic procedures set out
HAP emission rate in Sec. 63.3370(f)
does not exceed 0.2 to determine
kg organic HAP per compliance with
kg coating solids Sec. 63.3320(b)(3)
for an existing according to Sec.
affected source or 63.3370(n).
0.08 kg organic HAP
per kg coating
solids for a new
affected source on
a monthly average
as-applied basis;
or.
(iii) Average Follow the
equivalent organic procedures set out
HAP emission rate in Sec. 63.3370(g)
does not exceed to determine
0.04 kg organic HAP compliance with
per kg coating Sec. 63.3320(b)(2)
material for an according to Sec.
existing affected 63.3370(n).
source or 0.016 kg
organic HAP per kg
coating material
for a new affected
source on a monthly
average as-applied
basis; or.
(iv) Average Follow the
equivalent organic procedures set out
HAP emission rate in Sec.
does not exceed the 63.3370(h). Show
calculated limit that the monthly
based on emission organic HAP
limitations. emission rate is
less than the
calculated
equivalent
allowable organic
HAP emission rate
(Equation 13a or b
of Sec. 63.3370)
according to Sec.
63.3370(n).
(6) Use of a combination of (i) Average Follow the
compliant coatings and equivalent organic procedures set out
control devices. HAP emission rate in Sec. 63.3370(f)
does not exceed 0.2 to determine
kg organic HAP per compliance with
kg coating solids Sec. 63.3320(b)(3)
for an existing according to Sec.
affected source or 63.3370(n).
0.08 kg organic HAP
per kg coating
solids for a new
affected source on
a monthly average
as-applied basis;
or.
(ii) Average Follow the
equivalent organic procedures set out
HAP emission rate in Sec. 63.3370(g)
does not exceed to determine
0.04 kg organic HAP compliance with
per kg coating Sec. 63.3320(b)(2)
material for an according to Sec.
existing affected 63.3370(n).
source or 0.016 kg
organic HAP per kg
coating material
for a new affected
source on a monthly
average as-applied
basis; or.
[[Page 258]]
(iii) Average Follow the
equivalent organic procedures set out
HAP emission rate in Sec.
does not exceed the 63.3370(h). Show
calculated limit that the monthly
based on emission organic HAP
limitations. emission rate is
less than the
calculated
equivalent
allowable organic
HAP emission rate
(Equation 13a or b
of Sec. 63.3370)
according to Sec.
63.3370(n).
------------------------------------------------------------------------
(b) As-purchased ``compliant'' coating materials. (1) If you comply
by using coating materials that individually meet the emission standards
in Sec. 63.3320(b)(2) or (3), you must demonstrate that each coating
material applied during the month at an existing affected source
contains no more than 0.04 mass fraction organic HAP or 0.2 kg organic
HAP per kg coating solids, and that each coating material applied during
the month at a new affected source contains no more than 0.016 mass
fraction organic HAP or 0.08 kg organic HAP per kg coating solids on an
as-purchased basis as determined in accordance with Sec. 63.3360(c).
(2) You are in compliance with emission standards in
Sec. 63.3320(b)(2) and (3) if each coating material applied at an
existing affected source is applied as-purchased and contains no more
than 0.04 kg organic HAP per kg coating material or 0.2 kg organic HAP
per kg coating solids, and each coating material applied at a new
affected source is applied as-purchased and contains no more than 0.016
kg organic HAP per kg coating material or 0.08 kg organic HAP per kg
coating solids.
(c) As-applied ``compliant'' coating materials. If you comply by
using coating materials that meet the emission standards in
Sec. 63.3320(b)(2) or (3) as-applied, you must demonstrate compliance by
following one of the procedures in paragraphs (c)(1) through (4) of this
section. Compliance is determined in accordance with paragraph (c)(5) of
this section.
(1) Each coating material as-applied meets the mass fraction of
coating material standard (Sec. 63.3320(b)(2)). You must demonstrate
that each coating material applied at an existing affected source during
the month contains no more than 0.04 kg organic HAP per kg coating
material applied, and each coating material applied at a new affected
source contains no more than 0.016 kg organic HAP per kg coating
material applied as determined in accordance with paragraphs (c)(1)(i)
and (ii) of this section. You must calculate the as-applied organic HAP
content of as-purchased coating materials which are reduced, thinned, or
diluted prior to application.
(i) Determine the organic HAP content or volatile organic content of
each coating material applied on an as-purchased basis in accordance
with Sec. 63.3360(c).
(ii) Calculate the as-applied organic HAP content of each coating
material using Equation 1a of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.027
Where:
Cahi = Monthly average, as-applied, organic HAP content of
coating material, i, expressed as a mass fraction, kg/kg.
Chi = Organic HAP content of coating material, i, as-
purchased, expressed as a mass fraction, kg/kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
q = number of different materials added to the coating material.
Chij = Organic HAP content of material, j, added to as-
purchased coating material, i, expressed as a mass fraction, kg/kg.
Mij = Mass of material, j, added to as-purchased coating
material, i, in a month, kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
[[Page 259]]
or calculate the as-applied volatile organic content of each coating
material using Equation 1b of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.028
Where:
Cavi = Monthly average, as-applied, volatile organic content
of coating material, i, expressed as a mass fraction, kg/kg.
Cvi = Volatile organic content of coating material, i,
expressed as a mass fraction, kg/kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
q = Number of different materials added to the coating material.
Cvij = Volatile organic content of material, j, added to as-
purchased coating material, i, expressed as a mass fraction, kg/kg.
Mij = Mass of material, j, added to as-purchased coating
material, i, in a month, kg.
(2) Each coating material as-applied meets the mass fraction of
coating solids standard (Sec. 63.3320(b)(3)). You must demonstrate that
each coating material applied at an existing affected source contains no
more than 0.20 kg of organic HAP per kg of coating solids applied and
each coating material applied at a new affected source contains no more
than 0.08 kg of organic HAP per kg of coating solids applied. You must
demonstrate compliance in accordance with paragraphs (c)(2)(i) and (ii)
of this section.
(i) Determine the as-applied coating solids content of each coating
material following the procedure in Sec. 63.3360(d). You must calculate
the as-applied coating solids content of coating materials which are
reduced, thinned, or diluted prior to application, using Equation 2 of
this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.029
Where:
Csi = Coating solids content of coating material, i,
expressed as a mass fraction, kg/kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
q = Number of different materials added to the coating material.
Csij = Coating solids content of material, j, added to as-
purchased coating material, i, expressed as a mass-fraction, kg/kg.
Mij = Mass of material, j, added to as-purchased coating
material, i, in a month, kg.
(ii) Calculate the as-applied organic HAP to coating solids ratio
using Equation 3 of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.030
Where:
Hsi = As-applied, organic HAP to coating solids ratio of
coating material, i.
Cahi = Monthly average, as-applied, organic HAP content of
coating material, i, expressed as a mass fraction, kg/kg.
Casi = Monthly average, as-applied, coating solids content of
coating material, i, expressed as a mass fraction, kg/kg.
(3) Monthly average organic HAP content of all coating materials as-
applied is less than the mass percent limit (Sec. 63.3320(b)(2)).
Demonstrate that the monthly average as-applied organic HAP content of
all coating materials applied at an existing affected source is less
than 0.04 kg organic HAP per kg of coating material applied, and all
coating materials applied at a new affected source are less than 0.016
kg organic
[[Page 260]]
HAP per kg of coating material applied, as determined by Equation 4 of
this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.031
Where:
HL = Monthly average, as-applied, organic HAP content of all
coating materials applied, expressed as kg organic HAP per kg of coating
material applied, kg/kg.
p = Number of different coating materials applied in a month.
Chi = Organic HAP content of coating material, i, as-
purchased, expressed as a mass fraction, kg/kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
q = Number of different materials added to the coating material.
Chij = Organic HAP content of material, j, added to as-
purchased coating material, i, expressed as a mass fraction, kg/kg.
Mij = Mass of material, j, added to as-purchased coating
material, i, in a month, kg.
Mvret = Mass of volatile matter retained in the coated web
after curing or drying, or otherwise not emitted to the atmosphere, kg.
The value of this term will be zero in all cases except where you choose
to take into account the volatile matter retained in the coated web or
otherwise not emitted to the atmosphere for the compliance demonstration
procedures in Sec. 63.3370.
(4) Monthly average organic HAP content of all coating materials as-
applied is less than the mass fraction of coating solids limit
(Sec. 63.3320(b)(3)). Demonstrate that the monthly average as-applied
organic HAP content on the basis of coating solids applied of all
coating materials applied at an existing affected source is less than
0.20 kg organic HAP per kg coating solids applied, and all coating
materials applied at a new affected source are less than 0.08 kg organic
HAP per kg coating solids applied, as determined by Equation 5 of this
section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.032
Where:
Hs = Monthly average, as-applied, organic HAP to coating
solids ratio, kg organic HAP/kg coating solids applied.
p = Number of different coating materials applied in a month.
Chi = Organic HAP content of coating material, i, as-
purchased, expressed as a mass fraction, kg/kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
q = Number of different materials added to the coating material.
[[Page 261]]
Chij = Organic HAP content of material, j, added to as-
purchased coating material, i, expressed as a mass fraction, kg/kg.
Mij = Mass of material, j, added to as-purchased coating
material, i, in a month, kg.
Mvret = Mass of volatile matter retained in the coated web
after curing or drying, or otherwise not emitted to the atmosphere, kg.
The value of this term will be zero in all cases except where you choose
to take into account the volatile matter retained in the coated web or
otherwise not emitted to the atmosphere for the compliance demonstration
procedures in Sec. 63.3370.
Csi = Coating solids content of coating material, i,
expressed as a mass fraction, kg/kg.
Csij = Coating solids content of material, j, added to as-
purchased coating material, i, expressed as a mass-fraction, kg/kg.
(5) The affected source is in compliance with emission standards in
Sec. 63.3320(b)(2) or (3) if:
(i) The organic HAP content of each coating material as-applied at
an existing affected source is no more than 0.04 kg organic HAP per kg
coating material or 0.2 kg organic HAP per kg coating solids, and the
organic HAP content of each coating material as-applied at a new
affected source contains no more than 0.016 kg organic HAP per kg
coating material or 0.08 kg organic HAP per kg coating solids; or
(ii) The monthly average organic HAP content of all as-applied
coating materials at an existing affected source are no more than 0.04
kg organic HAP per kg coating material or 0.2 kg organic HAP per kg
coating solids, and the monthly average organic HAP content of all as-
applied coating materials at a new affected source is no more than 0.016
kg organic HAP per kg coating material or 0.08 kg organic HAP per kg
coating solids.
(d) Monthly allowable organic HAP applied. Demonstrate that the
total monthly organic HAP applied as determined by Equation 6 of this
section is less than the calculated equivalent allowable organic HAP as
determined by Equation 13a or b in paragraph (l) of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.033
Where:
Hm = Total monthly organic HAP applied, kg.
p = Number of different coating materials applied in a month.
Chi = Organic HAP content of coating material, i, as-
purchased, expressed as a mass fraction, kg/kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
q = Number of different materials added to the coating material.
Chij = Organic HAP content of material, j, added to as-
purchased coating material, i, expressed as a mass fraction, kg/kg.
Mij = Mass of material, j, added to as-purchased coating
material, i, in a month, kg.
Mvret = Mass of volatile matter retained in the coated web
after curing or drying, or otherwise not emitted to the atmosphere, kg.
The value of this term will be zero in all cases except where you choose
to take into account the volatile matter retained in the coated web or
otherwise not emitted to the atmosphere for the compliance demonstration
procedures in Sec. 63.3370.
(e) Capture and control to reduce emissions to no more than
allowable limit (Sec. 63.3320(b)(1)). Operate a capture system and
control device and demonstrate an overall organic HAP control efficiency
of at least 95 percent at an existing affected source and at least 98
percent at a new affected source for each month, or operate a capture
system and oxidizer so that an outlet organic HAP concentration of no
greater than 20 ppmv by compound on a dry
[[Page 262]]
basis is achieved as long as the capture efficiency is 100 percent as
detailed in Sec. 63.3320(b)(4). Unless one of the cases described in
paragraph (e)(1), (2), or (3) of this section applies to the affected
source, you must either demonstrate compliance in accordance with the
procedure in paragraph (i) of this section when emissions from the
affected source are controlled by a solvent recovery device, or the
procedure in paragraph (k) of this section when emissions are controlled
by an oxidizer or demonstrate compliance for a web coating line by
operating each capture system and each control device and continuous
parameter monitoring according to the procedures in paragraph (j) of
this section.
(1) If the affected source has only always-controlled work stations
and operates more than one capture system or more than one control
device, you must demonstrate compliance in accordance with the
provisions of either paragraph (n) or (p) of this section.
(2) If the affected source operates one or more never-controlled
work stations or one or more intermittently-controlled work stations,
you must demonstrate compliance in accordance with the provisions of
paragraph (n) of this section.
(3) An alternative method of demonstrating compliance with
Sec. 63.3320(b)(1) is the installation of a PTE around the web coating
line that achieves 100 percent capture efficiency and ventilation of all
organic HAP emissions from the total enclosure to an oxidizer with an
outlet organic HAP concentration of no greater than 20 ppmv by compound
on a dry basis. If this method is selected, you must demonstrate
compliance by following the procedures in paragraphs (e)(3)(i) and (ii)
of this section. Compliance is determined according to paragraph
(e)(3)(iii) of this section.
(i) Demonstrate that a total enclosure is installed. An enclosure
that meets the requirements in Sec. 63.3360(f)(1) will be considered a
total enclosure.
(ii) Determine the organic HAP concentration at the outlet of your
total enclosure using the procedures in paragraph (e)(3)(ii)(A) or (B)
of this section.
(A) Determine the control device efficiency using Equation 2 of
Sec. 63.3360 and the applicable test methods and procedures specified in
Sec. 63.3360(e).
(B) Use a CEMS to determine the organic HAP emission rate according
to paragraphs (i)(2)(i) through (x) of this section.
(iii) You are in compliance if the installation of a total enclosure
is demonstrated and the organic HAP concentration at the outlet of the
incinerator is demonstrated to be no greater than 20 ppmv by compound on
a dry basis.
(f) Capture and control to achieve mass fraction of coating solids
applied limit (Sec. 63.3320(b)(3)). Operate a capture system and control
device and limit the organic HAP emission rate from an existing affected
source to no more than 0.20 kg organic HAP emitted per kg coating solids
applied, and from a new affected source to no more than 0.08 kg organic
HAP emitted per kg coating solids applied as determined on a monthly
average as-applied basis. If the affected source operates more than one
capture system, more than one control device, one or more never-
controlled work stations, or one or more intermittently-controlled work
stations, then you must demonstrate compliance in accordance with the
provisions of paragraph (n) of this section. Otherwise, you must
demonstrate compliance following the procedure in paragraph (i) of this
section when emissions from the affected source are controlled by a
solvent recovery device or the procedure in paragraph (k) of this
section when emissions are controlled by an oxidizer.
(g) Capture and control to achieve mass fraction limit
(Sec. 63.3320(b)(2)). Operate a capture system and control device and
limit the organic HAP emission rate to no more than 0.04 kg organic HAP
emitted per kg coating material applied at an existing affected source,
and no more than 0.016 kg organic HAP emitted per kg coating material
applied at a new affected source as determined on a monthly average as-
applied basis. If the affected source operates more than one capture
system, more than one control device, one or more never-controlled work
stations, or one or more intermittently-controlled work stations, then
you must demonstrate compliance in accordance
[[Page 263]]
with the provisions of paragraph (n) of this section. Otherwise, you
must demonstrate compliance following the procedure in paragraph (i) of
this section when emissions from the affected source are controlled by a
solvent recovery device or the procedure in paragraph (k) of this
section when emissions are controlled by an oxidizer.
(h) Capture and control to achieve allowable emission rate. Operate
a capture system and control device and limit the monthly organic HAP
emissions to less than the allowable emissions as calculated in
accordance with paragraph (l) of this section. If the affected source
operates more than one capture system, more than one control device, one
or more never-controlled work stations, or one or more intermittently-
controlled work stations, then you must demonstrate compliance in
accordance with the provisions of paragraph (n) of this section.
Otherwise, the owner or operator must demonstrate compliance following
the procedure in paragraph (i) of this section when emissions from the
affected source are controlled by a solvent recovery device or the
procedure in paragraph (k) of this section when emissions are controlled
by an oxidizer.
(i) Solvent recovery device compliance demonstration. If you use a
solvent recovery device to control emissions, you must show compliance
by following the procedures in either paragraph (i)(1) or (2) of this
section:
(1) Liquid-liquid material balance. Perform a monthly liquid-liquid
material balance as specified in paragraphs (i)(1)(i) through (v) of
this section and use the applicable equations in paragraphs (i)(1)(vi)
through (ix) of this section to convert the data to units of the
selected compliance option in paragraphs (e) through (h) of this
section. Compliance is determined in accordance with paragraph (i)(1)(x)
of this section.
(i) Determine the mass of each coating material applied on the web
coating line or group of web coating lines controlled by a common
solvent recovery device during the month.
(ii) If demonstrating compliance on the basis of organic HAP
emission rate based on coating solids applied, organic HAP emission rate
based on coating material applied, or emission of less than the
calculated allowable organic HAP, determine the organic HAP content of
each coating material as-applied during the month following the
procedure in Sec. 63.3360(c).
(iii) Determine the volatile organic content of each coating
material as-applied during the month following the procedure in
Sec. 63.3360(d).
(iv) If demonstrating compliance on the basis of organic HAP
emission rate based on coating solids applied or emission of less than
the calculated allowable organic HAP, determine the coating solids
content of each coating material applied during the month following the
procedure in Sec. 63.3360(d).
(v) Determine and monitor the amount of volatile organic matter
recovered for the month according to the procedures in Sec. 63.3350(d).
(vi) Recovery efficiency. Calculate the volatile organic matter
collection and recovery efficiency using Equation 7 of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.034
Where:
Rv = Organic volatile matter collection and recovery
efficiency, percent.
Mvr = Mass of volatile matter recovered in a month, kg.
Mvret = Mass of volatile matter retained in the coated web
after curing or drying, or otherwise not emitted to the atmosphere, kg.
The value of this term will be zero in all cases except where you choose
to take into account the volatile matter retained in the coated web or
otherwise not emitted to the atmosphere for the compliance demonstration
procedures in Sec. 63.3370.
p = Number of different coating materials applied in a month.
Cvi = Volatile organic content of coating material, i,
expressed as a mass fraction, kg/kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
q = Number of different materials added to the coating material.
[[Page 264]]
Cvij = Volatile organic content of material, j, added to as-
purchased coating material, i, expressed as a mass fraction, kg/kg.
Mij = Mass of material, j, added to as-purchased coating
material, i, in a month, kg.
(vii) Organic HAP emitted. Calculate the organic HAP emitted during
the month using Equation 8 of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.035
Where:
He = Total monthly organic HAP emitted, kg.
Rv = Organic volatile matter collection and recovery
efficiency, percent.
p = Number of different coating materials applied in a month.
Chi = Organic HAP content of coating material, i, as-
purchased, expressed as a mass fraction, kg/kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
q = Number of different materials added to the coating material.
Chij = Organic HAP content of material, j, added to as-
purchased coating material, i, expressed as a mass fraction, kg/kg.
Mij = Mass of material, j, added to as-purchased coating
material, i, in a month, kg.
Mvret = Mass of volatile matter retained in the coated web
after curing or drying, or otherwise not emitted to the atmosphere, kg.
The value of this term will be zero in all cases except where you choose
to take into account the volatile matter retained in the coated web or
otherwise not emitted to the atmosphere for the compliance demonstration
procedures in Sec. 63.3370.
(viii) Organic HAP emission rate based on coating solids applied.
Calculate the organic HAP emission rate based on coating solids applied
using Equation 9 of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.036
Where:
L = Mass organic HAP emitted per mass of coating solids applied, kg/kg.
He = Total monthly organic HAP emitted, kg.
p = Number of different coating materials applied in a month.
Csi = Coating solids content of coating material, i,
expressed as a mass fraction, kg/kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
q = Number of different materials added to the coating material.
Csij = Coating solids content of material, j, added to as-
purchased coating material, i, expressed as a mass-fraction, kg/kg.
Mij = Mass of material, j, added to as-purchased coating
material, i, in a month, kg.
(ix) Organic HAP emission rate based on coating materials applied.
Calculate the organic HAP emission rate based on coating material
applied using Equation 10 of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.037
Where:
S = Mass organic HAP emitted per mass of material applied, kg/kg.
He = Total monthly organic HAP emitted, kg.
p = Number of different coating materials applied in a month.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
q = Number of different materials added to the coating material.
[[Page 265]]
Mij = Mass of material, j, added to as-purchased coating
material, i, in a month, kg.
(x) You are in compliance with the emission standards in
Sec. 63.3320(b) if:
(A) The volatile organic matter collection and recovery efficiency
is 95 percent or greater at an existing affected source and 98 percent
or greater at a new affected source; or
(B) The organic HAP emission rate based on coating solids applied is
no more than 0.20 kg organic HAP per kg coating solids applied at an
existing affected source and no more than 0.08 kg organic HAP per kg
coating solids applied at a new affected source; or
(C) The organic HAP emission rate based on coating material applied
is no more than 0.04 kg organic HAP per kg coating material applied at
an existing affected source and no more than 0.016 kg organic HAP per kg
coating material applied at a new affected source; or
(D) The organic HAP emitted during the month is less than the
calculated allowable organic HAP as determined using paragraph (l) of
this section.
(2) Continuous emission monitoring of capture system and control
device performance. Demonstrate initial compliance through a performance
test on capture efficiency and continuing compliance through continuous
emission monitors and continuous monitoring of capture system operating
parameters following the procedures in paragraphs (i)(2)(i) through
(vii) of this section. Use the applicable equations specified in
paragraphs (i)(2)(viii) through (x) of this section to convert the
monitoring and other data into units of the selected compliance option
in paragraphs (e) through (h) of this section. Compliance is determined
in accordance with paragraph (i)(2)(xi) of this section.
(i) Control device efficiency. Continuously monitor the gas stream
entering and exiting the control device to determine the total organic
volatile matter mass flow rate (e.g., by determining the concentration
of the vent gas in grams per cubic meter and the volumetric flow rate in
cubic meters per second such that the total organic volatile matter mass
flow rate in grams per second can be calculated) such that the control
device efficiency of the control device can be calculated for each month
using Equation 2 of Sec. 63.3360.
(ii) Capture efficiency monitoring. Whenever a web coating line is
operated, continuously monitor the operating parameters established in
accordance with Sec. 63.3350(f) to ensure capture efficiency.
(iii) Determine the percent capture efficiency in accordance with
Sec. 63.3360(f).
(iv) Control efficiency. Calculate the overall organic HAP control
efficiency achieved for each month using Equation 11 of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.038
Where:
R = Overall organic HAP control efficiency, percent.
E = Organic volatile matter control efficiency of the control device,
percent.
CE = Organic volatile matter capture efficiency of the capture system,
percent.
(v) If demonstrating compliance on the basis of organic HAP emission
rate based on coating solids applied, organic HAP emission rate based on
coating materials applied, or emission of less than the calculated
allowable organic HAP, determine the mass of each coating material
applied on the web coating line or group of web coating lines controlled
by a common control device during the month.
(vi) If demonstrating compliance on the basis of organic HAP
emission rate based on coating solids applied, organic HAP emission rate
based on coating material applied, or emission of less than the
calculated allowable organic HAP, determine the organic HAP content of
each coating material as-applied during the month following the
procedure in Sec. 63.3360(c).
(vii) If demonstrating compliance on the basis of organic HAP
emission rate based on coating solids applied or emission of less than
the calculated allowable organic HAP, determine the coating solids
content of each coating material as-applied during the month following
the procedure in Sec. 63.3360(d).
(viii) Organic HAP emitted. Calculate the organic HAP emitted during
the
[[Page 266]]
month for each month using Equation 12 of this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.039
Where:
He = Total monthly organic HAP emitted, kg.
R = Overall organic HAP control efficiency, percent.
p = Number of different coating materials applied in a month.
Cahi = Monthly average, as-applied, organic HAP content of
coating material, i, expressed as a mass fraction, kg/kg.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
Mvret = Mass of volatile matter retained in the coated web
after curing or drying, or otherwise not emitted to the atmosphere, kg.
The value of this term will be zero in all cases except where you choose
to take into account the volatile matter retained in the coated web or
otherwise not emitted to the atmosphere for the compliance demonstration
procedures in this section.
(ix) Organic HAP emission rate based on coating solids applied.
Calculate the organic HAP emission rate based on coating solids applied
using Equation 9 of this section.
(x) Organic HAP emission rate based on coating materials applied.
Calculate the organic HAP emission rate based on coating material
applied using Equation 10 of this section.
(xi) Compare actual performance to the performance required by
compliance option. The affected source is in compliance with the
emission standards in Sec. 63.3320(b) for each month if the capture
system is operated such that the average capture system operating
parameter is greater than or less than (as appropriate) the operating
parameter value established in accordance with Sec. 63.3350(f); and
(A) The organic volatile matter collection and recovery efficiency
is 95 percent or greater at an existing affected source and 98 percent
or greater at a new affected source; or
(B) The organic HAP emission rate based on coating solids applied is
no more than 0.20 kg organic HAP per kg coating solids applied at an
existing affected source and no more than 0.08 kg organic HAP per kg
coating solids applied at a new affected source; or
(C) The organic HAP emission rate based on coating material applied
is no more than 0.04 kg organic HAP per kg coating material applied at
an existing affected source and no more than 0.016 kg organic HAP per kg
coating material applied at a new affected source; or
(D) The organic HAP emitted during the month is less than the
calculated allowable organic HAP as determined using paragraph (l) of
this section.
(j) Capture and control system compliance demonstration procedures
using a CPMS. If you use an add-on control device, you must demonstrate
initial compliance for each capture system and each control device
through performance tests and demonstrate continuing compliance through
continuous monitoring of capture system and control device operating
parameters as specified in paragraphs (j)(1) through (3) of this
section. Compliance is determined in accordance with paragraph (j)(4) of
this section.
(1) Determine the control device destruction or removal efficiency
using the applicable test methods and procedures in Sec. 63.3360(e).
(2) Determine the emission capture efficiency in accordance with
Sec. 63.3360(f).
(3) Whenever a web coating line is operated, continuously monitor
the operating parameters established according to Sec. 63.3350(e) and
(f).
(4) You are in compliance with the emission standards in
Sec. 63.3320(b) if the control device is operated such that the average
operating parameter value
[[Page 267]]
is greater than or less than (as appropriate) the operating parameter
value established in accordance with Sec. 63.3360(e) for each 3-hour
period, and the capture system operating parameter is operated at an
average value greater than or less than (as appropriate) the operating
parameter value established in accordance with Sec. 63.3350(f); and
(i) The overall organic HAP control efficiency is 95 percent or
greater at an existing affected source and 98 percent or greater at a
new affected source; or
(ii) The organic HAP emission rate based on coating solids applied
is no more than 0.20 kg organic HAP per kg coating solids applied at an
existing affected source and no more than 0.08 kg organic HAP per kg
coating solids applied at a new affected source; or
(iii) The organic HAP emission rate based on coating material
applied is no more than 0.04 kg organic HAP per kg coating material
applied at an existing affected source and no more than 0.016 kg organic
HAP per kg coating material applied at a new affected source; or
(iv) The organic HAP emitted during the month is less than the
calculated allowable organic HAP as determined using paragraph (l) of
this section.
(k) Oxidizer compliance demonstration procedures. If you use an
oxidizer to control emissions, you must show compliance by following the
procedures in paragraph (k)(1) of this section. Use the applicable
equations specified in paragraph (k)(2) of this section to convert the
monitoring and other data into units of the selected compliance option
in paragraph (e) through (h) of this section. Compliance is determined
in accordance with paragraph (k)(3) of this section.
(1) Demonstrate initial compliance through performance tests of
capture efficiency and control device efficiency and continuing
compliance through continuous monitoring of capture system and control
device operating parameters as specified in paragraphs (k)(1)(i) through
(vi) of this section:
(i) Determine the oxidizer destruction efficiency using the
procedure in Sec. 63.3360(e).
(ii) Determine the capture system capture efficiency in accordance
with Sec. 63.3360(f).
(iii) Capture and control efficiency monitoring. Whenever a web
coating line is operated, continuously monitor the operating parameters
established in accordance with Sec. 63.3350(e) and (f) to ensure capture
and control efficiency.
(iv) If demonstrating compliance on the basis of organic HAP
emission rate based on coating solids applied, organic HAP emission rate
based on coating materials applied, or emission of less than the
calculated allowable organic HAP, determine the mass of each coating
material applied on the web coating line or group of web coating lines
controlled by a common oxidizer during the month.
(v) If demonstrating compliance on the basis of organic HAP emission
rate based on coating solids applied, organic HAP emission rate based on
coating material applied, or emission of less than the calculated
allowable organic HAP, determine the organic HAP content of each coating
material as-applied during the month following the procedure in
Sec. 63.3360(c).
(vi) If demonstrating compliance on the basis of organic HAP
emission rate based on coating solids applied or emission of less than
the calculated allowable organic HAP, determine the coating solids
content of each coating material applied during the month following the
procedure in Sec. 63.3360(d).
(2) Convert the information obtained under paragraph (p)(1) of this
section into the units of the selected compliance option using the
calculation procedures specified in paragraphs (k)(2)(i) through (iv) of
this section.
(i) Control efficiency. Calculate the overall organic HAP control
efficiency achieved using Equation 11 of this section.
(ii) Organic HAP emitted. Calculate the organic HAP emitted during
the month using Equation 12 of this section.
(iii) Organic HAP emission rate based on coating solids applied.
Calculate the organic HAP emission rate based on coating solids applied
for each month using Equation 9 of this section.
(iv) Organic HAP based on coating materials applied. Calculate the
organic HAP emission rate based on coating material applied using
Equation 10 of this section.
[[Page 268]]
(3) You are in compliance with the emission standards in
Sec. 63.3320(b) if the oxidizer is operated such that the average
operating parameter value is greater than the operating parameter value
established in accordance with Sec. 63.3360(e) for each 3-hour period,
and the capture system operating parameter is operated at an average
value greater than or less than (as appropriate) the operating parameter
value established in accordance with Sec. 63.3350(f); and
(i) The overall organic HAP control efficiency is 95 percent or
greater at an existing affected source and 98 percent or greater at a
new affected source; or
(ii) The organic HAP emission rate based on coating solids applied
is no more than 0.20 kg organic HAP per kg coating solids applied at an
existing affected source and no more than 0.08 kg organic HAP per kg
coating solids applied at a new affected source; or
(iii) The organic HAP emission rate based on coating material
applied is no more than 0.04 kg organic HAP per kg coating material
applied at an existing affected source and no more than 0.016 kg organic
HAP per kg coating material applied at a new affected source; or
(iv) The organic HAP emitted during the month is less than the
calculated allowable organic HAP as determined using paragraph (l) of
this section.
(l) Monthly allowable organic HAP emissions. This paragraph provides
the procedures and calculations for determining monthly allowable
organic HAP emissions for use in demonstrating compliance in accordance
with paragraph (d), (h), (i)(1)(x)(D), (i)(2)(xi)(D), or (k)(3)(iv) of
this section. You will need to determine the amount of coating material
applied at greater than or equal to 20 mass percent coating solids and
the amount of coating material applied at less than 20 mass percent
coating solids. The allowable organic HAP limit is then calculated based
on coating material applied at greater than or equal to 20 mass percent
coating solids complying with 0.2 kg organic HAP per kg coating solids
at an existing affected source or 0.08 kg organic HAP per kg coating
solids at a new affected source, and coating material applied at less
than 20 mass percent coating solids complying with 4 mass percent
organic HAP at an existing affected source and 1.6 mass-percent organic
HAP at a new affected source as follows:
(1) Determine the as-purchased mass of each coating material applied
each month.
(2) Determine the as-purchased coating solids content of each
coating material applied each month in accordance with
Sec. 63.3360(d)(1).
(3) Determine the as-purchased mass fraction of each coating
material which was applied at 20 mass percent or greater coating solids
content on an as-applied basis.
(4) Determine the total mass of each solvent, diluent, thinner, or
reducer added to coating materials which were applied at less than 20
mass percent coating solids content on an as-applied basis each month.
(5) Calculate the monthly allowable organic HAP emissions using
Equation 13a of this section for an existing affected source:
[GRAPHIC] [TIFF OMITTED] TR04DE02.040
Where:
Ha = Monthly allowable organic HAP emissions, kg.
p = Number of different coating materials applied in a month.
Mi = mass of as-purchased coating material, i, applied in a
month, kg.
Gi = Mass fraction of each coating material, i, which was
applied at 20 mass percent or greater coating solids content, on an as-
applied basis, kg/kg.
Csi = Coating solids content of coating material, i,
expressed as a mass fraction, kg/kg.
[[Page 269]]
q = Number of different materials added to the coating material.
MLj = Mass of non-coating-solids-containing coating material,
j, added to coating-solids-containing coating materials which were
applied at less than 20 mass percent coating solids content, on an as-
applied basis, in a month, kg.
or Equation 13b of this section for a new affected source:
[GRAPHIC] [TIFF OMITTED] TR04DE02.041
Where:
Ha = Monthly allowable organic HAP emissions, kg.
p = Number of different coating materials applied in a month.
Mi = Mass of as-purchased coating material, i, applied in a
month, kg.
Gi = Mass fraction of each coating material, i, which was
applied at 20 mass percent or greater coating solids content, on an as-
applied basis, kg/kg.
Csi = Coating solids content of coating material, i,
expressed as a mass fraction, kg/kg.
q = Number of different materials added to the coating material.
MLj = Mass of non-coating-solids-containing coating material,
j, added to coating-solids-containing coating materials which were
applied at less than 20 mass percent coating solids content, on an as-
applied basis, in a month, kg.
(m) [Reserved]
(n) Combinations of capture and control. If you operate more than
one capture system, more than one control device, one or more never-
controlled work stations, or one or more intermittently-controlled work
stations, you must calculate organic HAP emissions according to the
procedures in paragraphs (n)(1) through (4) of this section, and use the
calculation procedures specified in paragraph (n)(5) of this section to
convert the monitoring and other data into units of the selected control
option in paragraphs (e) through (h) of this section. Use the procedures
specified in paragraph (n)(6) of this section to demonstrate compliance.
(1) Solvent recovery system using liquid-liquid material balance
compliance demonstration. If you choose to comply by means of a liquid-
liquid material balance for each solvent recovery system used to control
one or more web coating lines, you must determine the organic HAP
emissions for those web coating lines controlled by that solvent
recovery system either:
(i) In accordance with paragraphs (i)(1)(i) through (iii) and (v)
through (vii) of this section, if the web coating lines controlled by
that solvent recovery system have only always-controlled work stations;
or
(ii) In accordance with paragraphs (i)(1)(ii), (iii), (v), and (vi)
and (o) of this section, if the web coating lines controlled by that
solvent recovery system have one or more never-controlled or
intermittently-controlled work stations.
(2) Solvent recovery system using performance test compliance
demonstration and CEMS. To demonstrate compliance through an initial
test of capture efficiency, continuous monitoring of a capture system
operating parameter, and a CEMS on each solvent recovery system used to
control one or more web coating lines, you must:
(i) For each capture system delivering emissions to that solvent
recovery system, monitor the operating parameter established in
accordance with Sec. 63.3350(f) to ensure capture system efficiency; and
(ii) Determine the organic HAP emissions for those web coating lines
served by each capture system delivering emissions to that solvent
recovery system either:
(A) In accordance with paragraphs (i)(2)(i) through (iii), (v),
(vi), and (viii)
[[Page 270]]
of this section, if the web coating lines served by that capture and
control system have only always-controlled work stations; or
(B) In accordance with paragraphs (i)(2)(i) through (iii), (vi), and
(o) of this section, if the web coating lines served by that capture and
control system have one or more never-controlled or intermittently-
controlled work stations.
(3) Oxidizer. To demonstrate compliance through performance tests of
capture efficiency and control device efficiency, continuous monitoring
of capture system, and CPMS for control device operating parameters for
each oxidizer used to control emissions from one or more web coating
lines, you must:
(i) Monitor the operating parameter in accordance with
Sec. 63.3350(e) to ensure control device efficiency; and
(ii) For each capture system delivering emissions to that oxidizer,
monitor the operating parameter established in accordance with
Sec. 63.3350(f) to ensure capture efficiency; and
(iii) Determine the organic HAP emissions for those web coating
lines served by each capture system delivering emissions to that
oxidizer either:
(A) In accordance with paragraphs (k)(1)(i) through (vi) of this
section, if the web coating lines served by that capture and control
system have only always-controlled work stations; or
(B) In accordance with paragraphs (k)(1)(i) through (iii), (v), and
(o) of this section, if the web coating lines served by that capture and
control system have one or more never-controlled or intermittently-
controlled work stations.
(4) Uncontrolled coating lines. If you own or operate one or more
uncontrolled web coating lines, you must determine the organic HAP
applied on those web coating lines using Equation 6 of this section. The
organic HAP emitted from an uncontrolled web coating line is equal to
the organic HAP applied on that web coating line.
(5) Convert the information obtained under paragraphs (n)(1) through
(4) of this section into the units of the selected compliance option
using the calculation procedures specified in paragraphs (n)(5)(i)
through (iv) of this section.
(i) Organic HAP emitted. Calculate the organic HAP emissions for the
affected source for the month by summing all organic HAP emissions
calculated according to paragraphs (n)(1), (2)(ii), (3)(iii), and (4) of
this section.
(ii) Coating solids applied. If demonstrating compliance on the
basis of organic HAP emission rate based on coating solids applied or
emission of less than the calculated allowable organic HAP, the owner or
operator must determine the coating solids content of each coating
material applied during the month following the procedure in
Sec. 63.3360(d).
(iii) Organic HAP emission rate based on coating solids applied.
Calculate the organic HAP emission rate based on coating solids applied
for each month using Equation 9 of this section.
(iv) Organic HAP based on materials applied. Calculate the organic
HAP emission rate based on material applied using Equation 10 of this
section.
(6) Compliance. The affected source is in compliance with the
emission standards in Sec. 63.3320(b) for the month if all operating
parameters required to be monitored under paragraphs (n)(1) through (3)
of this section were maintained at the values established under
Secs. 63.3350 and 63.3360; and
(i) The total mass of organic HAP emitted by the affected source
based on coating solids applied is no more than 0.20 kg organic HAP per
kg coating solids applied at an existing affected source and no more
than 0.08 kg organic HAP per kg coating solids applied at a new affected
source; or
(ii) The total mass of organic HAP emitted by the affected source
based on material applied is no more than 0.04 kg organic HAP per kg
material applied at an existing affected source and no more than 0.016
kg organic HAP per kg material applied at a new affected source; or
(iii) The total mass of organic HAP emitted by the affected source
during the month is less than the calculated allowable organic HAP as
determined using paragraph (l) of this section; or
(iv) The total mass of organic HAP emitted by the affected source
was not more than 5 percent of the total mass
[[Page 271]]
of organic HAP applied for the month at an existing affected source and
no more than 2 percent of the total mass of organic HAP applied for the
month at a new affected source. The total mass of organic HAP applied by
the affected source in the month must be determined using Equation 6 of
this section.
(o) Intermittently-controlled and never-controlled work stations. If
you have been expressly referenced to this paragraph by paragraphs
(n)(1)(ii), (n)(2)(ii)(B), or (n)(3)(iii)(B) of this section for
calculation procedures to determine organic HAP emissions for your
intermittently-controlled and never-controlled work stations, you must:
(1) Determine the sum of the mass of all coating materials as-
applied on intermittently-controlled work stations operating in bypass
mode and the mass of all coating materials as-applied on never-
controlled work stations during the month.
(2) Determine the sum of the mass of all coating materials as-
applied on intermittently-controlled work stations operating in a
controlled mode and the mass of all coating materials applied on always-
controlled work stations during the month.
(3) Liquid-liquid material balance compliance demonstration. For
each web coating line or group of web coating lines for which you use
the provisions of paragraph (n)(1)(ii) of this section, you must
calculate the organic HAP emitted during the month using Equation 14 of
this section:
[GRAPHIC] [TIFF OMITTED] TR04DE02.042
Where:
He = Total monthly organic HAP emitted, kg.
p = Number of different coating materials applied in a month.
Mci = Sum of the mass of coating material, i, as-applied on
intermittently-controlled work stations operating in controlled mode and
the mass of coating material, i, as-applied on always-controlled work
stations, in a month, kg.
Cahi = Monthly average, as-applied, organic HAP content of
coating material, i, expressed as a mass fraction, kg/kg.
Rv = Organic volatile matter collection and recovery
efficiency, percent.
MBi = Sum of the mass of coating material, i, as-applied on
intermittently-controlled work stations operating in bypass mode and the
mass of coating material, i, as-applied on never-controlled work
stations, in a month, kg.
Cahi = Monthly average, as-applied, organic HAP content of
coating material, i, expressed as a mass fraction, kg/kg.
Mvret = Mass of volatile matter retained in the coated web
after curing or drying, or otherwise not emitted to the atmosphere, kg.
The value of this term will be zero in all cases except where you choose
to take into account the volatile matter retained in the coated web or
otherwise not emitted to the atmosphere for the compliance demonstration
procedures in this section.
(4) Performance test to determine capture efficiency and control
device efficiency. For each web coating line or group of web coating
lines for which you use the provisions of paragraph (n)(2)(ii)(B) or
(n)(3)(iii)(B) of this section, you must calculate the organic HAP
emitted during the month using Equation 15 of this section:
[[Page 272]]
[GRAPHIC] [TIFF OMITTED] TR04DE02.043
Where:
He = Total monthly organic HAP emitted, kg.
p = Number of different coating materials applied in a month.
Mci = Sum of the mass of coating material, i, as-applied on
intermittently-controlled work stations operating in controlled mode and
the mass of coating material, i, as-applied on always-controlled work
stations, in a month, kg.
Cahi = Monthly average, as-applied, organic HAP content of
coating material, i, expressed as a mass fraction, kg/kg.
R = Overall organic HAP control efficiency, percent.
MBi = Sum of the mass of coating material, i, as-applied on
intermittently-controlled work stations operating in bypass mode and the
mass of coating material, i, as-applied on never-controlled work
stations, in a month, kg.
Cahi = Monthly average, as-applied, organic HAP content of
coating material, i, expressed as a mass fraction, kg/kg.
Mvret = Mass of volatile matter retained in the coated web
after curing or drying, or otherwise not emitted to the atmosphere, kg.
The value of this term will be zero in all cases except where you choose
to take into account the volatile matter retained in the coated web or
otherwise not emitted to the atmosphere for the compliance demonstration
procedures in this section.
(p) Always-controlled work stations with more than one capture and
control system. If you operate more than one capture system or more than
one control device and only have always-controlled work stations, then
you are in compliance with the emission standards in Sec. 63.3320(b)(1)
for the month if for each web coating line or group of web coating lines
controlled by a common control device:
(1) The volatile matter collection and recovery efficiency as
determined by paragraphs (i)(1)(i), (iii), (v), and (vi) of this section
is at least 95 percent at an existing affected source and at least 98
percent at a new affected source; or
(2) The overall organic HAP control efficiency as determined by
paragraphs (i)(2)(i) through (iv) of this section for each web coating
line or group of web coating lines served by that control device and a
common capture system is at least 95 percent at an existing affected
source and at least 98 percent at a new affected source; or
(3) The overall organic HAP control efficiency as determined by
paragraphs (k)(1)(i) through (iii) and (k)(2)(i) of this section for
each web coating line or group of web coating lines served by that
control device and a common capture system is at least 95 percent at an
existing affected source and at least 98 percent at a new affected
source.
Notifications, Reports, and Records
Sec. 63.3400 What notifications and reports must I submit?
(a) Each owner or operator of an affected source subject to this
subpart must submit the reports specified in paragraphs (b) through (g)
of this section to the Administrator:
(b) You must submit an initial notification as required by
Sec. 63.9(b).
(1) Initial notification for existing affected sources must be
submitted no later than 1 year before the compliance date specified in
Sec. 63.3330(a).
(2) Initial notification for new and reconstructed affected sources
must be submitted as required by Sec. 63.9(b).
(3) For the purpose of this subpart, a title V or part 70 permit
application may be used in lieu of the initial notification required
under Sec. 63.9(b), provided the same information is contained in the
permit application as required by Sec. 63.9(b) and the State to which
the permit application has been submitted has an approved operating
permit program under part 70 of this chapter and has received delegation
of
[[Page 273]]
authority from the EPA to implement and enforce this subpart.
(4) If you are using a permit application in lieu of an initial
notification in accordance with paragraph (b)(3) of this section, the
permit application must be submitted by the same due date specified for
the initial notification.
(c) You must submit a semiannual compliance report according to
paragraphs (c)(1) and (2) of this section.
(1) Compliance report dates.
(i) The first compliance report must cover the period beginning on
the compliance date that is specified for your affected source in
Sec. 63.3330 and ending on June 30 or December 31, whichever date is the
first date following the end of the calendar half immediately following
the compliance date that is specified for your affected source in
Sec. 63.3330.
(ii) The first compliance report must be postmarked or delivered no
later than July 31 or January 31, whichever date follows the end of the
calendar half immediately following the compliance date that is
specified for your affected source in Sec. 63.3330.
(iii) Each subsequent compliance report must cover the semiannual
reporting period from January 1 through June 30 or the semiannual
reporting period from July 1 through December 31.
(iv) Each subsequent compliance report must be postmarked or
delivered no later than July 31 or January 31, whichever date is the
first date following the end of the semiannual reporting period.
(v) For each affected source that is subject to permitting
regulations pursuant to 40 CFR part 70 or 40 CFR part 71, and the
permitting authority has established dates for submitting semiannual
reports pursuant to Sec. 70.6(a)(3)(iii)(A) or Sec. 71.6(a)(3)(iii)(A),
you may submit the first and subsequent compliance reports according to
the dates the permitting authority has established instead of according
to the dates in paragraphs (c)(1)(i) through (iv) of this section.
(2) The compliance report must contain the information in paragraphs
(c)(2)(i) through (vi) of this section:
(i) Company name and address.
(ii) Statement by a responsible official with that official's name,
title, and signature certifying the accuracy of the content of the
report.
(iii) Date of report and beginning and ending dates of the reporting
period.
(iv) If there are no deviations from any emission limitations
(emission limit or operating limit) that apply to you, a statement that
there were no deviations from the emission limitations during the
reporting period, and that no CMS was inoperative, inactive,
malfunctioning, out-of-control, repaired, or adjusted.
(v) For each deviation from an emission limitation (emission limit
or operating limit) that applies to you and that occurs at an affected
source where you are not using a CEMS to comply with the emission
limitations in this subpart, the compliance report must contain the
information in paragraphs (c)(2)(i) through (iii) of this section, and:
(A) The total operating time of each affected source during the
reporting period.
(B) Information on the number, duration, and cause of deviations
(including unknown cause), if applicable, and the corrective action
taken.
(C) Information on the number, duration, and cause for CPMS downtime
incidents, if applicable, other than downtime associated with zero and
span and other calibration checks.
(vi) For each deviation from an emission limit occurring at an
affected source where you are using a CEMS to comply with the emission
limit in this subpart, you must include the information in paragraphs
(c)(2)(i) through (iii) and (vi)(A) through (J) of this section.
(A) The date and time that each malfunction started and stopped.
(B) The date and time that each CEMS and CPMS, if applicable, was
inoperative except for zero (low-level) and high-level checks.
(C) The date and time that each CEMS and CPMS, if applicable, was
out-of-control, including the information in Sec. 63.8(c)(8).
(D) The date and time that each deviation started and stopped, and
whether each deviation occurred during a period of startup, shutdown, or
malfunction or during another period.
[[Page 274]]
(E) A summary of the total duration (in hours) of each deviation
during the reporting period and the total duration of each deviation as
a percent of the total source operating time during that reporting
period.
(F) A breakdown of the total duration of the deviations during the
reporting period into those that are due to startup, shutdown, control
equipment problems, process problems, other known causes, and other
unknown causes.
(G) A summary of the total duration (in hours) of CEMS and CPMS
downtime during the reporting period and the total duration of CEMS and
CPMS downtime as a percent of the total source operating time during
that reporting period.
(H) A breakdown of the total duration of CEMS and CPMS downtime
during the reporting period into periods that are due to monitoring
equipment malfunctions, nonmonitoring equipment malfunctions, quality
assurance/quality control calibrations, other known causes, and other
unknown causes.
(I) The date of the latest CEMS and CPMS certification or audit.
(J) A description of any changes in CEMS, CPMS, or controls since
the last reporting period.
(d) You must submit a Notification of Performance Tests as specified
in Secs. 63.7 and 63.9(e) if you are complying with the emission
standard using a control device and you are required to conduct a
performance test of the control device. This notification and the site-
specific test plan required under Sec. 63.7(c)(2) must identify the
operating parameters to be monitored to ensure that the capture
efficiency of the capture system and the control efficiency of the
control device determined during the performance test are maintained.
Unless EPA objects to the parameter or requests changes, you may
consider the parameter approved.
(e) You must submit a Notification of Compliance Status as specified
in Sec. 63.9(h).
(f) You must submit performance test reports as specified in
Sec. 63.10(d)(2) if you are using a control device to comply with the
emission standard and you have not obtained a waiver from the
performance test requirement or you are not exempted from this
requirement by Sec. 63.3360(b). The performance test reports must be
submitted as part of the notification of compliance status required in
Sec. 63.3400(e).
(g) You must submit startup, shutdown, and malfunction reports as
specified in Sec. 63.10(d)(5), except that the provisions in subpart A
of this part pertaining to startups, shutdowns, and malfunctions do not
apply unless a control device is used to comply with this subpart.
(1) If actions taken by an owner or operator during a startup,
shutdown, or malfunction of an affected source (including actions taken
to correct a malfunction) are not consistent with the procedures
specified in the affected source's SSMP required by Sec. 63.6(e)(3), the
owner or operator must state such information in the report. The
startup, shutdown, or malfunction report must consist of a letter
containing the name, title, and signature of the responsible official
who is certifying its accuracy and must be submitted to the
Administrator.
(2) Separate startup, shutdown, and malfunction reports are not
required if the information is included in the report specified in
paragraph (c)(2)(vi) of this section.
Sec. 63.3410 What records must I keep?
(a) Each owner or operator of an affected source subject to this
subpart must maintain the records specified in paragraphs (a)(1) and (2)
of this section on a monthly basis in accordance with the requirements
of Sec. 63.10(b)(1):
(1) Records specified in Sec. 63.10(b)(2) of all measurements needed
to demonstrate compliance with this standard, including:
(i) Continuous emission monitor data in accordance with the
requirements of Sec. 63.3350(d);
(ii) Control device and capture system operating parameter data in
accordance with the requirements of Sec. 63.3350(c), (e), and (f);
(iii) Organic HAP content data for the purpose of demonstrating
compliance in accordance with the requirements of Sec. 63.3360(c);
(iv) Volatile matter and coating solids content data for the purpose
of
[[Page 275]]
demonstrating compliance in accordance with the requirements of
Sec. 63.3360(d);
(v) Overall control efficiency determination using capture
efficiency and control device destruction or removal efficiency test
results in accordance with the requirements of Sec. 63.3360(e) and (f);
and
(vi) Material usage, organic HAP usage, volatile matter usage, and
coating solids usage and compliance demonstrations using these data in
accordance with the requirements of Sec. 63.3370(b), (c), and (d).
(2) Records specified in Sec. 63.10(c) for each CMS operated by the
owner or operator in accordance with the requirements of
Sec. 63.3350(b).
(b) Each owner or operator of an affected source subject to this
subpart must maintain records of all liquid-liquid material balances
performed in accordance with the requirements of Sec. 63.3370. The
records must be maintained in accordance with the requirements of
Sec. 63.10(b).
Delegation of Authority
Sec. 63.3420 What authorities may be delegated to the States?
(a) In delegating implementation and enforcement authority to a
State under 40 CFR part 63, subpart E, the authorities contained in
paragraph (b) of this section must be retained by the Administrator and
not transferred to a State.
(b) Authority which will not be delegated to States:
Sec. 63.3360(c), approval of alternate test method for organic HAP
content determination; Sec. 63.3360(d), approval of alternate test
method for volatile matter determination.
Tables to Subpart JJJJ of Part 63
If you are required to comply with operating limits by Sec. 63.3321,
you must comply with the applicable operating limits in the following
table:
Table 1 to Subpart JJJJ of Part 63--Operating Limits if Using Add-On
Control Devices and Capture System
------------------------------------------------------------------------
And you must
You must meet the demonstrate
For the following device: following operating continuous
limit: compliance with
operating limits by:
------------------------------------------------------------------------
1. Thermal oxidizer......... a. The average i. Collecting the
combustion combustion
temperature in any temperature data
3-hour period must according to Sec.
not fall below the 63.3350(e)(9);
combustion ii. Reducing the
temperature limit data to 3-hour
established block averages; and
according to Sec. iii. Maintain the 3-
63.3360(e)(3)(i). hour average
combustion
temperature at or
above the
temperature limit.
2. Catalytic oxidizer....... a. The average i. Collecting the
temperature at the catalyst bed inlet
inlet to the temperature data
catalyst bed in any according to Sec.
3-hour period must 63.3350(e)(9);
not fall below the ii. Reducing the
combustion data to 3-hour
temperature limit block averages; and
established iii. Maintain the 3-
according to Sec. hour average
63.3360(e)(3)(ii). catalyst bed inlet
temperature at or
above the
temperature limit.
b. The temperature i. Collecting the
rise across the catalyst bed inlet
catalyst bed must and outlet
not fall below the temperature data
limit established according to Sec.
according to Sec. 63.3350(e)(9);
63.3360(e)(3)(ii). ii. Reducing the
data to 3-hour
block averages; and
iii. Maintain the 3-
hour average
temperature rise
across the catalyst
bed at or above the
limit.
3. Emission capture system.. Submit monitoring Conduct monitoring
plan to the according to the
Administrator that plan (Sec.
identifies 63.3350(f)(3)).
operating
parameters to be
monitored according
to Sec. 63.3350(f).
------------------------------------------------------------------------
[[Page 276]]
You must comply with the applicable General Provisions requirements
according to the following table:
Table 2 to Subpart JJJJ of Part 63--Applicability of 40 CFR Part 63
General Provisions to Subpart JJJJ
------------------------------------------------------------------------
Applicable to
General provisions reference subpart JJJJ Explanation
------------------------------------------------------------------------
Sec. 63.1(a)(1)-(4)........ Yes.
Sec. 63.1(a)(5)............ No.................. Reserved.
Sec. 63.1(a)(6)-(8)........ Yes.
Sec. 63.1(a)(9)............ No.................. Reserved.
Sec. 63.1(a)(10)-(14)...... Yes.
Sec. 63.1(b)(1)............ No.................. Subpart JJJJ
specifies
applicability.
Sec. 63.1(b)(2)-(3)........ Yes.
Sec. 63.1(c)(1)............ Yes.
Sec. 63.1(c)(2)............ No.................. Area sources are not
subject to emission
standards of
subpart JJJJ.
Sec. 63.1(c)(3)............ No.................. Reserved.
Sec. 63.1(c)(4)............ Yes.
Sec. 63.1(c)(5)............ Yes.
Sec. 63.1(d)............... No.................. Reserved.
Sec. 63.1(e)............... Yes.
Sec. 63.1(e)(4)............ No.
Sec. 63.2.................. Yes................. Additional
definitions in
subpart JJJJ.
Sec. 63.3(a)-(c)........... Yes.
Sec. 63.4(a)(1)-(3)........ Yes.
Sec. 63.4(a)(4)............ No.................. Reserved.
Sec. 63.4(a)(5)............ Yes.
Sec. 63.4(b)-(c)........... Yes.
Sec. 63.5(a)(1)-(2)........ Yes.
Sec. 63.5(b)(1)............ Yes.
Sec. 63.5(b)(2)............ No.................. Reserved.
Sec. 63.5(b)(3)-(6)........ Yes.
Sec. 63.5(c)............... No.................. Reserved.
Sec. 63.5(d)............... Yes.
Sec. 63.5(e)............... Yes.
Sec. 63.5(f)............... Yes.
Sec. 63.6(a)............... Yes................. Applies only when
capture and control
system is used to
comply with the
standard.
Sec. 63.6(b)(1)-(5)........ No..................
Sec. 63.6(b)(6)............ No.................. Reserved.
Sec. 63.6(b)(7)............ Yes.
Sec. 63.6(c)(1)-(2)........ Yes.
Sec. 63.6(c)(3)-(4)........ No.................. Reserved.
Sec. 63.6(c)(5)............ Yes.
Sec. 63.6(d)............... No.................. Reserved.
Sec. 63.6(e)............... Yes................. Provisions
pertaining to SSMP,
and CMS do not
apply unless an add-
on control system
is used to comply
with the emission
limitations.
Sec. 63.6(f)............... Yes.
Sec. 63.6(g)............... Yes.
Sec. 63.6(h)............... No.................. Subpart JJJJ does
not require
continuous opacity
monitoring systems
(COMS).
Sec. 63.6(i)(1)-(14)....... Yes.
Sec. 63.6(i)(15)........... No.................. Reserved.
Sec. 63.6(i)(16)........... Yes.
Sec. 63.6(j)............... Yes.
Sec. 63.7.................. Yes.
Sec. 63.8(a)(1)-(2)........ Yes.
Sec. 63.8(a)(3)............ No.................. Reserved.
Sec. 63.8(a)(4)............ No.
Sec. 63.8(b)............... Yes.
Sec. 63.8(c)(1)-(3)........ Yes................. Sec. 63.8(c)(1)(i)
& (ii) only apply
if you use capture
and control systems
and are required to
have a start-up,
shutdown, and
malfunction plan.
Sec. 63.8(c)(4)............ Yes.
Sec. 63.8(c)(5)............ No.................. Subpart JJJJ does
not require COMS.
Sec. 63.8(c)(6)-(c)(8)..... Yes................. Provisions for COMS
are not applicable.
Sec. 63.8(d)-(f)........... Yes................. Sec. 63.8(f)(6)
only applies if you
use CEMS.
Sec. 63.8(g)............... Yes................. Only applies if you
use CEMS.
[[Page 277]]
Sec. 63.9(a)............... Yes.
Sec. 63.9(b)(1)............ Yes.
Sec. 63.9(b)(2)............ Yes................. Except Sec.
63.3400(b)(1)
requires submittal
of initial
notification for
existing affected
sources no later
than 1 year before
compliance date.
Sec. 63.9(b)(3)-(5)........ Yes.
Sec. 63.9(c)-(e)........... Yes.
Sec. 63.9(f)............... No.................. Subpart JJJJ does
not require opacity
and visible
emissions
observations.
Sec. 63.9(g)............... Yes................. Provisions for COMS
are not applicable.
Sec. 63.9(h)(1)-(3)........ Yes.
Sec. 63.9(h)(4)............ No.................. Reserved.
Sec. 63.9(h)(5)-(6)........ Yes.
Sec. 63.9(i)............... Yes.
Sec. 63.9(j)............... Yes.
Sec. 63.10(a).............. Yes.
Sec. 63.10(b)(1)-(3)....... Yes................. Sec. 63.10(b)(2)(i)
through (v) only
apply if you use a
capture and control
system.
Sec. 63.10(c)(1)........... Yes.
Sec. 63.10(c)(2)-(4)....... No.................. Reserved.
Sec. 63.10(c)(5)-(8)....... Yes.
Sec. 63.10(c)(9)........... No.................. Reserved.
Sec. 63.10(c)(10)-(15)..... Yes.
Sec. 63.10(d)(1)-(2)....... Yes.
Sec. 63.10(d)(3)........... No.................. Subpart JJJJ does
not require opacity
and visible
emissions
observations.
Sec. 63.10(d)(4)-(5)....... Yes.
Sec. 63.10(e)(1)-(2)....... Yes................. Provisions for COMS
are not applicable.
Sec. 63.10(e)(3)-(4)....... No.
Sec. 63.10(f).............. Yes.
Sec. 63.11................. No.
Sec. 63.12................. Yes.
Sec. 63.13................. Yes.
Sec. 63.14................. Yes................. Subpart JJJJ
includes provisions
for alternative
ASME test methods
that are
incorporated by
reference.
Sec. 63.15................. Yes.
------------------------------------------------------------------------
Subpart NNNN--National Emission Standards for Hazardous Air Pollutants:
Surface Coating of Large Appliances
Source: 67 FR 48262, July 23, 2002, unless otherwise noted.
What This Subpart Covers
Sec. 63.4080 What is the purpose of this subpart?
This subpart establishes national emission standards for hazardous
air pollutants for large appliance surface coating facilities. This
subpart also establishes requirements to demonstrate initial and
continuous compliance with the emission limitations.
Sec. 63.4081 Am I subject to this subpart?
(a) You are subject to this subpart if you own or operate a facility
that applies coatings to large appliance parts or products, and is a
major source, is located at a major source, or is part of a major source
of emissions of hazardous air pollutants (HAP), except as provided in
paragraph (d) of this section. A major source of HAP emissions is any
stationary source or group of stationary sources located within a
contiguous area and under common control that emits or has the potential
to emit any single HAP at a rate of 9.07 megagrams (Mg) (10 tons) or
more per year or any combination of HAP at a rate of 22.68 Mg (25 tons)
or more per year. You are not subject to this subpart if your large
appliance surface coating facility is located at, or is part of, an area
source of HAP emissions. An area source of HAP emissions is any
stationary source or group of stationary sources located within a
contiguous area and under common control that is not a major source.
(b) The large appliance surface coating source category includes any
facility engaged in the surface coating of a
[[Page 278]]
large appliance part or product. Large appliance parts and products
include but are not limited to cooking equipment; refrigerators,
freezers, and refrigerated cabinets and cases; laundry equipment;
dishwashers, trash compactors, and water heaters; and heating,
ventilation, and air-conditioning (HVAC) units, air-conditioning (except
motor vehicle) units, air-conditioning and heating combination units,
comfort furnaces, and electric heat pumps. Specifically excluded are
heat transfer coils and large commercial and industrial chillers.
(c) The large appliance surface coating activities and equipment to
which this subpart applies are listed in paragraphs (c)(1) through (9)
of this section:
(1) Surface preparation of large appliance parts and products;
(2) Preparation of a coating for application (e.g., mixing in
thinners and other components);
(3) Application of a coating to large appliance parts and products
using, for example, spray guns or dip tanks;
(4) Application of porcelain enamel, powder coating, and asphalt
interior soundproofing coating;
(5) Flash-off, drying, or curing following the coating application
operation;
(6) Cleaning of equipment used in coating operations (e.g.,
application equipment, hangers, racks);
(7) Storage of coatings, thinners, and cleaning materials;
(8) Conveying of coatings, thinners, and cleaning materials from
storage areas to mixing areas or coating application areas, either
manually (e.g., in buckets) or by automated means (e.g., transfer
through pipes using pumps); and
(9) Handling and conveying of waste materials generated by coating
operations.
(d) This subpart does not apply to surface coating that meets any of
the criteria of paragraphs (d)(1) through (5) of this section.
(1) The surface coating of large appliance parts such as metal or
plastic handles, hinges, or fasteners that have a wider use beyond large
appliances is not subject to this subpart.
(2) The surface coating of large appliances conducted for the
purpose of repairing or maintaining large appliances used by a facility
and not for commerce is not subject to this subpart unless organic HAP
emissions from the surface coating itself are as high as the rates
specified in paragraph (a) of this section.
(3) The surface coating of heat transfer coils or large commercial
and industrial chillers.
(4) The provisions of this subpart do not apply to research or
laboratory facilities; janitorial, building, and facility maintenance
operations; hobby shops operated for noncommercial purposes or coating
applications using hand-held non-refillable aerosol containers.
(5) The provisions of this subpart do not apply to processes
involving metal plating or phosphating of a substrate.
(e) If you own or operate an affected source that is subject to this
subpart and at the same affected source you also perform surface coating
subject to any other subparts in this part, you may choose for the
affected source to comply with only one subpart. In order to choose this
alternative, the total mass of organic HAP emissions from all surface
coating operations in the affected source must be less than or equal to
the total mass of organic HAP emissions that would result if it complied
separately with all applicable subparts. You must make this comparison
for the initial compliance period and report it in the Notification of
Compliance Status as required in Sec. 63.4110(b)(10) and in the
Notification of Compliance Status required by the other subparts. If you
choose this alternative, your demonstration of compliance with the other
subpart constitutes compliance with this subpart.
Sec. 63.4082 What parts of my plant does this subpart cover?
(a) This subpart applies to each new, reconstructed, and existing
affected source.
(b) The affected source is the collection of all of the items listed
in paragraphs (b)(1) through (4) of this section that are part of the
large appliance surface coating facility:
(1) All coating operations as defined in Sec. 63.4181;
[[Page 279]]
(2) All storage containers and mixing vessels in which coatings,
thinners, and cleaning materials are stored or mixed;
(3) All manual and automated equipment and containers used for
conveying coatings, thinners, and cleaning materials; and
(4) All storage containers and all manual and automated equipment
and containers used for conveying waste materials generated by a coating
operation.
(c) An affected source is a new affected source if you commenced its
construction after July 23, 2002, and the construction is of a
completely new large appliance surface coating facility where previously
no large appliance surface coating facility had existed.
(d) An affected source is reconstructed if you meet the criteria as
defined in Sec. 63.2.
(e) An affected source is existing if it is not new or
reconstructed.
Sec. 63.4083 When do I have to comply with this subpart?
The date by which you must comply with this subpart is called the
compliance date. The compliance date for each type of affected source is
specified in paragraphs (a) through (c) of this section. The compliance
date begins the initial compliance period during which you conduct the
initial compliance demonstration described in Secs. 63.4140, 63.4150,
and 63.4160.
(a) For a new or reconstructed affected source, the compliance date
is the applicable date in paragraph (a)(1) or (2) of this section.
(1) If the initial startup of your new or reconstructed affected
source is before July 23, 2002, the compliance date is July 23, 2002.
(2) If the initial startup of your new or reconstructed affected
source occurs after July 23, 2002, the compliance date is the date of
initial startup of your affected source.
(b) For an existing affected source, the compliance date is July 25,
2005.
(c) For an area source that increases its emissions or its potential
to emit such that it becomes a major source of HAP emissions, the
compliance date is specified in paragraphs (c)(1) and (2) of this
section.
(1) For any portion of the source that becomes a new or
reconstructed affected source subject to this subpart, the compliance
date is the date of initial startup of the affected source, or the date
the area source becomes a major source, or July 23, 2002, whichever is
latest.
(2) For any portion of the source that becomes an existing affected
source subject to this subpart, the compliance date is the date 1 year
after the area source becomes a major source or July 25, 2005, whichever
is later.
(d) You must meet the notification requirements in Sec. 63.4110
according to the dates specified in that section and in subpart A of
this part. Some of the notifications must be submitted before the
compliance dates described in paragraphs (a) through (c) of this
section.
Emission Limitations
Sec. 63.4090 What emission limits must I meet?
(a) For an existing affected source, you must limit organic HAP
emissions to the atmosphere to no more than 0.13 kilogram per liter (kg/
liter) (1.1 pound per gallon (lb/gal)) of coating solids used during
each compliance period.
(b) For a new or reconstructed affected source, you must limit
organic HAP emissions to the atmosphere to no more than 0.022 kg/liter
(0.18 lb/gal) of coating solids used during each compliance period.
Sec. 63.4091 What are my options for meeting the emission limits?
You must include all coatings, thinners, and cleaning materials used
in the affected source when determining whether the organic HAP emission
rate is equal to or less than the applicable emission limit in
Sec. 63.4090. To make this determination, you must use at least one of
the three compliance options listed in paragraphs (a) through (c) of
this section. You may apply any of the compliance options to an
individual coating operation or to multiple coating operations as a
group or to the entire affected source. You may use
[[Page 280]]
different compliance options for different coating operations or at
different times on the same coating operation. However, you may not use
different compliance options at the same time on the same coating
operation. If you switch between compliance options for any coating
operation or group of coating operations, you must document this switch
as required by Sec. 63.4130(c), and you must report it in the next
semiannual compliance report required in Sec. 63.4120.
(a) Compliant material option. Demonstrate that the organic HAP
content of each coating used in the coating operation(s) is less than or
equal to the applicable emission limit in Sec. 63.4090, and that each
thinner and each cleaning material used contains no organic HAP. You
must meet all the requirements of Secs. 63.4140, 63.4141, and 63.4142 to
demonstrate compliance with the emission limit using this option.
(b) Emission rate without add-on controls option. Demonstrate that,
based on data on the coatings, thinners, and cleaning materials used in
the coating operation(s), the organic HAP emission rate for the coating
operation(s) is less than or equal to the applicable emission limit in
Sec. 63.4090. You must meet all the requirements of Secs. 63.4150,
63.4151, and 63.4152 to demonstrate compliance with the emission limit
using this option.
(c) Emission rate with add-on controls option. Demonstrate that,
based on data on the coatings, thinners, and cleaning materials used in
the coating operation(s) and the emission reductions achieved by
emission capture and add-on controls, the organic HAP emission rate for
the coating operation(s) is less than or equal to the applicable
emission limit in Sec. 63.4090. If you use this compliance option, you
must also demonstrate that all emission capture systems and add-on
control devices for the coating operation(s) meet the operating limits
required in Sec. 63.4092, except for solvent recovery systems for which
you conduct liquid-liquid material balances according to
Sec. 63.4161(h), and that you meet the work practice standards required
in Sec. 63.4093. You must meet all the requirements of Secs. 63.4160
through 63.4168 to demonstrate compliance with the emission limits,
operating limits, and work practice standards using this option.
Sec. 63.4092 What operating limits must I meet?
(a) For any coating operation(s) on which you use the compliant
material option or the emission rate without add-on controls option, you
are not required to meet any operating limits.
(b) For any controlled coating operation(s) on which you use the
emission rate with add-on controls option, except those for which you
use a solvent recovery system and conduct a liquid-liquid material
balance according to Sec. 63.4161(h), you must meet the operating limits
specified in Table 1 to this subpart. These operating limits apply to
the emission capture and control systems on the coating operation(s) for
which you use this option, and you must establish the operating limits
during the performance test according to the requirements in
Sec. 63.4167. You must meet the operating limits at all times after you
establish them.
(c) If you use an add-on control device other than those listed in
Table 1 to this subpart or wish to monitor an alternative parameter and
comply with a different operating limit, you must apply to the U.S.
Environmental Protection Agency (EPA) Administrator for approval of
alternative monitoring under Sec. 63.8(f).
Sec. 63.4093 What work practice standards must I meet?
(a) For any coating operation(s) on which you use the compliant
material option or the emission rate without add-on controls option, you
are not required to meet any work practice standards.
(b) If you use the emission rate with add-on controls option, you
must develop and implement a work practice plan to minimize organic HAP
emissions from the storage, mixing, and conveying of coatings, thinners,
and cleaning materials used in, and waste materials generated by, the
coating operation(s) for which you use this option; or you must meet an
alternative standard as provided in paragraph (c) of this section. The
plan must specify practices and procedures to ensure
[[Page 281]]
that, at a minimum, the elements specified in paragraphs (b)(1) through
(5) of this section are implemented.
(1) All organic-HAP-containing coatings, thinners, cleaning
materials, and waste materials must be stored in closed containers.
(2) Spills of organic-HAP-containing coatings, thinners, cleaning
materials, and waste materials must be minimized.
(3) Organic-HAP-containing coatings, thinners, cleaning materials,
and waste materials must be conveyed from one location to another in
closed containers or pipes.
(4) Mixing vessels which contain organic-HAP-containing coatings and
other materials must be closed except when adding to, removing, or
mixing the contents.
(5) Emissions of organic HAP must be minimized during cleaning of
storage, mixing, and conveying equipment.
(c) As provided in Sec. 63.6(g), we, the EPA, may choose to grant
you permission to use an alternative to the work practice standards in
this section.
General Compliance Requirements
Sec. 63.4100 What are my general requirements for complying with this subpart?
(a) You must be in compliance with the emission limitations in this
subpart as specified in paragraphs (a)(1) and (2) of this section.
(1) Any coating operation(s) for which you use the compliant
material option or the emission rate without add-on controls option, as
specified in Sec. 63.4091(a) and (b), must be in compliance with the
applicable emission limit in Sec. 63.4090 at all times.
(2) Any coating operation(s) for which you use the emission rate
with add-on controls option, as specified in Sec. 63.4091(c), must be in
compliance with the applicable emission limit in Sec. 63.4090 and work
practice standards in Sec. 63.4093 at all times. Each controlled coating
operation must be in compliance with the operating limits for emission
capture systems and add-on control devices required by Sec. 63.4092 at
all times, except for solvent recovery systems for which you conduct
liquid-liquid material balances according to Sec. 63.4161(h).
(b) You must always operate and maintain your affected source,
including all air pollution control and monitoring equipment you use for
purposes of complying with this subpart, according to the provisions in
Sec. 63.6(e)(1)(i).
(c) If your affected source uses an emission capture system and add-
on control device, you must maintain a log detailing the operation and
maintenance of the emission capture system, add-on control device, and
continuous parameter monitors during the period between the compliance
date specified for your affected source in Sec. 63.4083 and the date
when the initial emission capture system and add-on control device
performance tests have been completed as specified in Sec. 63.4160. This
requirement does not apply to a solvent recovery system for which you
conduct a liquid-liquid material balance according to Sec. 63.4161(h) in
lieu of conducting performance tests.
(d) If your affected source uses an emission capture system and add-
on control device, you must develop and implement a written startup,
shutdown, and malfunction plan according to the provisions in
Sec. 63.6(e)(3). The plan must address the startup, shutdown, and
corrective actions in the event of a malfunction of the emission capture
system or the add-on control device. The plan must also address any
coating operation equipment that may cause increased emissions or that
would affect capture efficiency if the process equipment malfunctions,
such as conveyors that move parts among enclosures.
Sec. 63.4101 What parts of the General Provisions apply to me?
Table 2 to this subpart shows which parts of the General Provisions
in Secs. 63.1 through 63.15 apply to you.
Notifications, Reports, and Records
Sec. 63.4110 What notifications must I submit?
(a) You must submit the notifications in Secs. 63.7(b) and (c),
63.8(f)(4), and 63.9(b) through (e) and (h) that apply to you by the
dates specified in those sections, except as provided in paragraphs
(a)(1) and (2) of this section.
[[Page 282]]
(1) You must submit the Initial Notification required by
Sec. 63.9(b) for an existing affected source no later than July 23,
2003. For a new or reconstructed affected source, you must submit the
Initial Notification no later than 120 days after initial startup or
November 20, 2002, whichever is later.
(2) You must submit the Notification of Compliance Status required
by Sec. 63.9(h) no later than 30 calendar days following the end of the
initial compliance period described in Sec. 63.4140, Sec. 63.4150, or
Sec. 63.4160 that applies to your affected source.
(b) The Notification of Compliance Status must contain the
information specified in paragraphs (b)(1) through (10) of this section
and the applicable information specified in Sec. 63.9(h).
(1) Company name and address.
(2) Statement by a responsible official with that official's name,
title, and signature certifying the truth, accuracy, and completeness of
the content of the report.
(3) Date of the report and beginning and ending dates of the
reporting period. The reporting period is the initial compliance period
described in Sec. 63.4140, Sec. 63.4150, or Sec. 63.4160 that applies to
your affected source.
(4) Identification of the compliance option or options specified in
Sec. 63.4091 that you used on each coating operation in the affected
source during the initial compliance period.
(5) Statement of whether or not the affected source achieved the
emission limitations for the initial compliance period.
(6) If you had a deviation, include the information in paragraphs
(b)(6)(i) and (ii) of this section.
(i) A description of and statement of the cause of the deviation.
(ii) If you failed to meet the applicable emission limit in
Sec. 63.4090, include all the calculations you used to determine the kg
organic HAP emitted per liter of coating solids used. You do not need to
submit information provided by the materials suppliers or manufacturers
or test reports.
(7) For each of the data items listed in paragraphs (b)(7)(i)
through (iv) of this section that is required by the compliance
option(s) you used to demonstrate compliance with the emission limit,
include an example of how you determined the value, including
calculations and supporting data. Supporting data can include a copy of
the information provided by the supplier or manufacturer of the example
coating or material or a summary of the results of testing conducted
according to Sec. 63.4141(a), (b), or (c). You do not need to submit
copies of any test reports.
(i) Mass fraction of organic HAP for one coating, for one thinner,
and for one cleaning material.
(ii) Volume fraction of coating solids for one coating.
(iii) Density for one coating, one thinner, and one cleaning
material, except that if you use the compliant material option, only the
example coating density is required.
(iv) The amount of waste materials and the mass of organic HAP
contained in the waste materials for which you are claiming an allowance
in Equation 1 of Sec. 63.4151.
(8) The determination of kg organic HAP emitted per liter of coating
solids used for the compliance option(s) you use, as specified in
paragraphs (b)(8)(i) through (iii) of this section.
(i) For the compliant material option, provide an example
determination of the organic HAP content for one coating, according to
Sec. 63.4141(d).
(ii) For the emission rate without add-on controls option, provide
the calculation of the total mass of organic HAP emissions; the
calculation of the total volume of coating solids used; and the
calculation of the organic HAP emission rate, using Equations 1, 1A
through 1C, 2, and 3, respectively, of Sec. 63.4151.
(iii) For the emission rate with add-on controls option, provide the
calculation of the total mass of organic HAP emissions for the coatings,
thinners, and cleaning materials used, using Equations 1 and 1A through
1C of Sec. 63.4151; the calculation of the total volume of coating
solids used, using Equation 2 of Sec. 63.4151; the calculation of the
mass of organic HAP emission reduction by emission capture systems and
add-on control devices, using Equations 1, 1A through 1C, 2, 3, and 3A
through 3C of Sec. 63.4161, as applicable; and the calculation of the
organic HAP
[[Page 283]]
emission rate, using Equation 4 of Sec. 63.4161.
(9) For the emission rate with add-on controls option, you must
include the information specified in paragraphs (b)(9)(i) through (v) of
this section, except that the requirements in paragraphs (b)(9)(i)
through (iii) of this section do not apply to solvent recovery systems
for which you conduct liquid-liquid material balances according to
Sec. 63.4161(h).
(i) For each emission capture system, a summary of the data and
copies of the calculations supporting the determination that the
emission capture system is a permanent total enclosure (PTE) or a
measurement of the emission capture system efficiency. Include a
description of the protocol followed for measuring capture efficiency,
summaries of any capture efficiency tests conducted, and any
calculations supporting the capture efficiency determination. If you use
the data quality objective (DQO) or lower confidence limit (LCL)
approach, you must also include the statistical calculations to show you
meet the DQO or LCL criteria in appendix A to subpart KK of this part.
You do not need to submit complete test reports.
(ii) A summary of the results of each add-on control device
performance test. You do not need to submit complete test reports.
(iii) A list of each emission capture system's and add-on control
device's operating limits and a summary of the data used to calculate
those limits.
(iv) A statement of whether or not you developed and implemented the
work practice plan required by Sec. 63.4093.
(v) A statement of whether or not you developed and implemented the
startup, shutdown, and malfunction plan required by Sec. 63.4100(d).
(10) If you have chosen for your affected source to comply with the
requirements of another subpart in lieu of the requirements of this
subpart, as allowed in Sec. 63.4081(d), your Notification of Compliance
Status must include a statement certifying your intent, as well as
documentation and supporting materials showing that, during the initial
compliance period, your affected source's total organic HAP emissions
were equal to or less than the organic HAP emissions that would have
resulted from complying separately with each applicable subpart.
Sec. 63.4120 What reports must I submit?
You must submit semiannual compliance reports for each affected
source according to the requirements of this section. The semiannual
compliance reporting requirements of this section may be satisfied by
reports required under other parts of the Clean Air Act (CAA), as
specified in paragraph (a)(5) of this section.
(a) Unless the Administrator has approved a different schedule for
submission of reports under Sec. 63.10(a), you must prepare and submit
each semiannual compliance report according to the dates specified in
paragraphs (a)(1) through (4) of this section.
(1) The first semiannual compliance report must cover the first
semiannual reporting period which begins the day after the end of the
initial compliance period described in Sec. 63.4140, Sec. 63.4150, or
Sec. 63.4160 that applies to your affected source and ends on June 30 or
December 31, whichever date is the first date following the end of the
initial compliance period.
(2) Each subsequent semiannual compliance report must cover the
subsequent semiannual reporting period from January 1 through June 30 or
the semiannual reporting period from July 1 through December 31.
(3) Each semiannual compliance report must be postmarked or
delivered no later than July 31 or January 31, whichever date is the
first date following the end of the semiannual reporting period.
(4) For each affected source that is subject to permitting
regulations pursuant to 40 CFR part 70 or 40 CFR part 71, and if the
permitting authority has established dates for submitting semiannual
reports pursuant to 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR
71.6(a)(3)(iii)(A), you may submit the first and subsequent semiannual
compliance reports according to the dates the permitting authority has
established instead of the date specified in paragraph (a)(3) of this
section.
[[Page 284]]
(5) Each affected source that has obtained a title V operating
permit pursuant to 40 CFR part 70 or 40 CFR part 71 must report all
deviations as defined in this subpart in the semiannual monitoring
report required by 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR
71.6(a)(3)(iii)(A). If an affected source submits a semiannual
compliance report pursuant to this section along with, or as part of,
the semiannual monitoring report required by 40 CFR 70.6(a)(3)(iii)(A)
or 40 CFR 71.6(a)(3)(iii)(A), and the semiannual compliance report
includes all required information concerning deviations from any
emission limitation in this subpart, its submission shall be deemed to
satisfy any obligation to report the same deviations in the semiannual
monitoring report. However, submission of a semiannual compliance report
shall not otherwise affect any obligation the affected source may have
to report deviations from permit requirements to the permitting
authority.
(b) The semiannual compliance report must contain the information
specified in paragraphs (b)(1) through (4) of this section and the
information specified in paragraphs (c) through (j) of this section that
is applicable to your affected source.
(1) Company name and address.
(2) Statement by a responsible official with that official's name,
title, and signature certifying the truth, accuracy, and completeness of
the content of the report.
(3) Date of report and beginning and ending dates of the reporting
period. The reporting period is the 6-month period ending on June 30 or
December 31.
(4) Identification of the compliance option or options specified in
Sec. 63.4091 that you used on each coating operation during the
reporting period. If you switched between compliance options during the
reporting period, you must report the beginning and ending dates you
used each option.
(c) If there were no deviations from the emission limitations in
Secs. 63.4090, 63.4092, and 63.4093 that apply to you, the semiannual
compliance report must include a statement that there were no deviations
from the emission limitations during the reporting period.
(d) If you use the compliant material option and there was a
deviation from the applicable emission limit in Sec. 63.4090, the
semiannual compliance report must contain the information in paragraphs
(d)(1) through (4) of this section.
(1) Identification of each coating used that deviated from the
emission limit, each thinner and cleaning material used that contained
organic HAP, and the dates and time periods each was used.
(2) The determination of the organic HAP content, according to
Sec. 63.4141(d), for each coating identified in paragraph (d)(1) of this
section. You do not need to submit background data supporting this
calculation, for example, information provided by coating suppliers or
manufacturers or test reports.
(3) The determination of mass fraction of organic HAP for each
thinner and cleaning material identified in paragraph (d)(1) of this
section. You do not need to submit background data supporting this
calculation, for example, information provided by material suppliers or
manufacturers or test reports.
(4) A statement of the cause of each deviation.
(e) If you use the emission rate without add-on controls option and
there was a deviation from the applicable emission limit in
Sec. 63.4090, the semiannual compliance report must contain the
information in paragraphs (e)(1) through (3) of this section.
(1) The beginning and ending dates of each compliance period during
which the organic HAP emission rate exceeded the emission limit.
(2) The calculations used to determine the organic HAP emission rate
for the compliance period in which the deviation occurred. You must
provide the calculations for Equations 1, 1A through 1C, 2, and 3 in
Sec. 63.4151; and, if applicable, the calculation used to determine the
organic HAP in waste materials according to Sec. 63.4151(e)(4). You do
not need to submit background data supporting these calculations, for
example, information provided by materials suppliers or manufacturers or
test reports.
(3) A statement of the cause of each deviation.
[[Page 285]]
(f) If you use the emission rate with add-on controls option and
there were no periods during which the continuous parameter monitoring
systems (CPMS) were out-of-control as specified in Sec. 63.8(c)(7), the
semiannual compliance report must include a statement that there were no
periods during which the CPMS were out-of-control during the reporting
period.
(g) If you use the emission rate with add-on controls option and
there was a deviation from an emission limitation (including any periods
when emissions bypassed the add-on control device and were diverted to
the atmosphere), the semiannual compliance report must contain the
information in paragraphs (g)(1) through (14) of this section. This
includes periods of startup, shutdown, and malfunction during which
deviations occurred.
(1) The beginning and ending dates of each compliance period during
which the organic HAP emission rate exceeded the applicable emission
limit in Sec. 63.4090.
(2) The calculations used to determine the organic HAP emission rate
for each compliance period in which a deviation occurred. You must
provide the calculation of the total mass of organic HAP emissions for
the coatings, thinners, and cleaning materials used during the
compliance period, using Equations 1, 1A through 1C, and 2 of
Sec. 63.4151 and, if applicable, the calculation used to determine the
mass of organic HAP in waste materials according to Sec. 63.4151(e)(4);
the calculation of the total volume of coating solids used during the
compliance period, using Equation 2 of Sec. 63.4151; the calculation of
the mass of organic HAP emission reduction during the compliance period
by emission capture systems and add-on control devices, using Equations
1, 1A through 1C, 2, 3, and 3A through 3C of Sec. 63.4161; and the
calculation of the organic HAP emission rate, using Equation 4 of
Sec. 63.4161. You do not need to submit the background data supporting
these calculations, for example, information provided by materials
suppliers or manufacturers or test reports.
(3) The date and time that each malfunction started and stopped.
(4) A brief description of the CPMS.
(5) The date of the latest CPMS certification or audit.
(6) The date and time that each CPMS was inoperative, except for
zero (low-level) and high-level checks.
(7) The date, time, and duration that each CPMS was out-of-control,
including the information in Sec. 63.8(c)(8).
(8) The date and time period of each deviation from an operating
limit in Table 1 to this subpart; date and time period of any bypass of
the add-on control device; and whether each deviation occurred during a
period of startup, shutdown, or malfunction or during another period.
(9) A summary of the total duration of each deviation from an
operating limit in Table 1 to this subpart and bypass of the add-on
control device during the semiannual reporting period and the total
duration as a percent of the total source operating time during that
semiannual reporting period.
(10) A breakdown of the total duration of the deviations from the
operating limits in Table 1 to this subpart and bypasses of the add-on
control device during the semiannual reporting period into those that
were due to startup, shutdown, control equipment problems, process
problems, other known causes, and other unknown causes.
(11) A summary of the total duration of CPMS downtime during the
semiannual reporting period and the total duration of CPMS downtime as a
percent of the total source operating time during that semiannual
reporting period.
(12) A description of any changes in the CPMS, coating operation,
emission capture system, or add-on control device since the last
semiannual reporting period.
(13) For each deviation from the work practice standards, a
description of the deviation, the date and time period of the deviation,
and the actions you took to correct the deviation.
(14) A statement of the cause of each deviation.
(h) If you use the emission rate with add-on controls option, you
must submit reports of performance test results for emission capture
systems and add-on control devices no later than 60 days
[[Page 286]]
after completing the tests as specified in Sec. 63.10(d)(2).
(i) [Reserved]
(j) If you use the emission rate with add-on controls option and you
have a startup, shutdown, or malfunction during the semiannual reporting
period, you must submit the reports specified in paragraphs (j)(1) and
(2) of this section.
(1) If your actions were consistent with your startup, shutdown, and
malfunction plan (SSMP), you must include the information specified in
Sec. 63.10(d)(5) in the semiannual compliance report required by
paragraph (a) of this section.
(2) If your actions were not consistent with your SSMP, you must
submit an immediate startup, shutdown, and malfunction report as
described in paragraphs (j)(2)(i) and (ii) of this section.
(i) You must describe the actions taken during the event in a report
delivered by facsimile (fax), telephone, or other means to the
Administrator within 2 working days after starting actions that are
inconsistent with the plan.
(ii) You must submit a letter to the Administrator within 7 working
days after the end of the event, unless you have made alternative
arrangements with the Administrator as specified in
Sec. 63.10(d)(5)(ii). The letter must contain the information specified
in Sec. 63.10(d)(5)(ii).
Sec. 63.4130 What records must I keep?
You must collect and keep records of the data and information
specified in this section. Failure to collect and keep these records is
a deviation from the applicable standard.
(a) A copy of each notification and report that you submitted to
comply with this subpart and the documentation supporting each
notification and report.
(b) A current copy of information provided by materials suppliers or
manufacturers such as manufacturer's formulation data or test data used
to determine the mass fraction of organic HAP and density for each
coating, thinner, and cleaning material and the volume fraction of
coating solids for each coating. If you conducted testing to determine
mass fraction of organic HAP, density, or volume fraction of coating
solids, you must keep a copy of the complete test report. If you use
information provided to you by the manufacturer or supplier of the
material that was based on testing, you must keep the summary sheet of
results provided to you by the manufacturer or supplier. You are not
required to obtain the test report or other supporting documentation
from the manufacturer or supplier.
(c) For each compliance period, a record of the time periods
(beginning and ending dates and times) and the coating operations at
which each compliance option was used and a record of all determinations
of kg organic HAP per liter of coating solids for the compliance
option(s) you used, as specified in paragraphs (c)(1) through (3) of
this section.
(1) For the compliant material option, a record of the determination
of the organic HAP content for each coating, according to
Sec. 63.4141(d).
(2) For the emission rate without add-on controls option, a record
of the calculation of the total mass of organic HAP emissions for the
coatings, thinners, and cleaning materials used each month, using
Equations 1 and 1A through 1C of Sec. 63.4151 and, if applicable, the
calculations used to determine the mass of organic HAP in waste
materials according to Sec. 63.4151(e)(4); the calculation of the total
volume of coating solids used each month, using Equation 2 of
Sec. 63.4151; and the calculation of the organic HAP emission rate,
using Equation 3 of Sec. 63.4151.
(3) For the emission rate with add-on controls option, a record of
the calculation of the total mass of organic HAP emissions for the
coatings, thinners, and cleaning materials used each month, using
Equations 1 and 1A through 1C of Sec. 63.4151 and, if applicable, the
calculation used to determine mass of organic HAP in waste materials
according to Sec. 63.4151(e)(4); the calculation of the total volume of
coating solids used each month, using Equation 2 of Sec. 63.4151; the
calculation of the mass of organic HAP emission reduction by emission
capture systems and add-on control devices, using Equations 1, 1A
through 1C, 2, 3, and 3A
[[Page 287]]
through 3C of Sec. 63.4161, as applicable; and the calculation of the
organic HAP emission rate, using Equation 4 of Sec. 63.4161.
(d) A record of the name and volume of each coating, thinner, and
cleaning material used during each compliance period.
(e) A record of the mass fraction of organic HAP for each coating,
thinner, and cleaning material used during each compliance period.
(f) A record of the volume fraction of coating solids for each
coating used during each compliance period except for zero-HAP coatings
for which volume solids determination is not required as allowed in
Sec. 63.4141(a).
(g) A record of the density for each coating used during each
compliance period except for zero-HAP coatings for which volume solids
determination is not required as allowed in Sec. 63.4141(a) and, if you
use either the emission rate without add-on controls or the emission
rate with add-on controls compliance option, a record of the density for
each thinner and cleaning material used during each compliance period.
(h) If you use an allowance in Equation 1 of Sec. 63.4151 for
organic HAP contained in waste materials sent to or designated for
shipment to a treatment, storage, and disposal facility (TSDF) according
to Sec. 63.4151(e)(4), you must keep records of the information
specified in paragraphs (h)(1) through (3) of this section.
(1) The name and address of each TSDF to which you sent waste
materials for which you use an allowance in Equation 1 of Sec. 63.4151,
a statement of which subparts under 40 CFR parts 262, 264, 265, and 266
apply to the facility, and the date of each shipment.
(2) Identification of the coating operations producing waste
materials included in each shipment and the month or months in which you
used the allowance for these materials in Equation 1 of Sec. 63.4151.
(3) The methodology used in accordance with Sec. 63.4151(e)(4) to
determine the total amount of waste materials sent to or the amount
collected, stored, and designated for transport to a TSDF each month;
and the methodology to determine the mass of organic HAP contained in
these waste materials. This must include the sources for all data used
in the determination, methods used to generate the data, frequency of
testing or monitoring, and supporting calculations and documentation,
including the waste manifest for each shipment.
(i) [Reserved]
(j) You must keep records of the date, time, and duration of each
deviation.
(k) If you use the emission rate with add-on controls option, you
must keep the records specified in paragraphs (k)(1) through (8) of this
section.
(1) For each deviation, a record of whether the deviation occurred
during a period of startup, shutdown, or malfunction.
(2) The records in Sec. 63.6(e)(3)(iii) through (v) related to
startup, shutdown, and malfunction.
(3) The records required to show continuous compliance with each
operating limit specified in Table 1 to this subpart that applies to
you.
(4) For each capture system that is a PTE, the data and
documentation you used to support a determination that the capture
system meets the criteria in Method 204 of appendix M to 40 CFR part 51
for a PTE and has a capture efficiency of 100 percent, as specified in
Sec. 63.4165(a).
(5) For each capture system that is not a PTE, the data and
documentation you used to determine capture efficiency according to the
requirements specified in Secs. 63.4164 and 63.4165(b) through (e)
including the records specified in paragraphs (k)(5)(i) through (iii) of
this section that apply to you.
(i) Records for a liquid-to-uncaptured-gas protocol using a
temporary total enclosure or building enclosure. Records of the mass of
total volatile hydrocarbon (TVH) as measured by Method 204A or F of
appendix M to 40 CFR part 51 for each material used in the coating
operation, and the total TVH for all materials used during each capture
efficiency test run, including a copy of the test report. Records of the
mass of TVH emissions not captured by the capture system that exited the
temporary total enclosure or building enclosure during each capture
efficiency test run, as measured by Method 204D or E of appendix M to 40
CFR part 51, including a copy of the test report.
[[Page 288]]
Records documenting that the enclosure used for the capture efficiency
test met the criteria in Method 204 of appendix M to 40 CFR part 51 for
either a temporary total enclosure or a building enclosure.
(ii) Records for a gas-to-gas protocol using a temporary total
enclosure or a building enclosure. Records of the mass of TVH emissions
captured by the emission capture system as measured by Method 204B or C
of appendix M to 40 CFR part 51 at the inlet to the add-on control
device, including a copy of the test report. Records of the mass of TVH
emissions not captured by the capture system that exited the temporary
total enclosure or building enclosure during each capture efficiency
test run, as measured by Method 204D or E of appendix M to 40 CFR part
51, including a copy of the test report. Records documenting that the
enclosure used for the capture efficiency test met the criteria in
Method 204 of appendix M to 40 CFR part 51 for either a temporary total
enclosure or a building enclosure.
(iii) Records for an alternative protocol. Records needed to
document a capture efficiency determination using an alternative method
or protocol as specified in Sec. 63.4165(e), if applicable.
(6) The records specified in paragraphs (k)(6)(i) and (ii) of this
section for each add-on control device organic HAP destruction or
removal efficiency determination as specified in Sec. 63.4166.
(i) Records of each add-on control device performance test conducted
according to Secs. 63.4164 and 63.4166.
(ii) Records of the coating operation conditions during the add-on
control device performance test showing that the performance test was
conducted under representative operating conditions.
(8) Records of the data and calculations you used to establish the
emission capture and add-on control device operating limits as specified
in Sec. 63.4167 and to document compliance with the operating limits as
specified in Table 1 of this subpart.
(9) A record of the work practice plan required by Sec. 63.4093, and
documentation that you are implementing the plan on a continuous basis.
Sec. 63.4131 In what form and for how long must I keep my records?
(a) Your records must be in a form suitable and readily available
for expeditious review, according to Sec. 63.10(b)(1). Where
appropriate, the records may be maintained as electronic spreadsheets or
as a data base.
(b) As specified in Sec. 63.10(b)(1), you must keep each record for
5 years following the date of each occurrence, measurement, maintenance,
corrective action, report, or record.
(c) You must keep each record on site for at least 2 years after the
date of each occurrence, measurement, maintenance, corrective action,
report, or record, according to Sec. 63.10(b)(1). You may keep the
records off site for the remaining 3 years.
Compliance Requirements for the Compliant Material Option
Sec. 63.4140 By what date must I conduct the initial compliance demonstration?
You must complete the initial compliance demonstration for the
initial compliance period according to the requirements in Sec. 63.4141.
The initial compliance period begins on the applicable compliance date
specified in Sec. 63.4083 and ends on the last day of the first full
month after the compliance date. If the compliance date occurs on any
day other than the first day of a month, then the initial compliance
period extends through the end of that month plus the next month. The
initial compliance demonstration includes the determination according to
Sec. 63.4141 and supporting documentation showing that, during the
initial compliance period, you used no coating with an organic HAP
content that exceeded the applicable emission limit in Sec. 63.4090, and
that you used no thinners or cleaning materials that contained organic
HAP.
Sec. 63.4141 How do I demonstrate initial compliance with the emission limitations?
You may use the compliant material option for any individual coating
operation, for any group of coating operations in the affected source,
or for all the coating operations in the affected
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source. You must use either the emission rate without add-on controls
option or the emission rate with add-on controls option for any coating
operation(s) in the affected source for which you do not use this
option. To demonstrate initial compliance using the compliant material
option, the coating operation or group of coating operations must use no
coating with an organic HAP content that exceeds the applicable emission
limit in Sec. 63.4090 and must use no thinner or cleaning material that
contains organic HAP, as determined according to this section during the
initial compliance period. Any coating operation(s) for which you use
the compliant material option is not required to meet the operating
limits or work practice standards required in Secs. 63.4092 and 63.4093,
respectively. To demonstrate initial compliance with the emission
limitations using the compliant material option, you must meet all the
requirements of this section for the coating operation(s) using this
option. Use the procedures in this section on each coating, thinner, and
cleaning material in the condition it is in when it is received from its
manufacturer or supplier and prior to any alteration. You do not need to
redetermine the HAP content of coatings, thinners, or cleaning materials
that have been reclaimed onsite and reused in the coating operation(s)
for which you use the compliant material option, provided these
materials in their condition as received were demonstrated to comply
with the compliant material option. If the mass fraction of organic HAP
of a coating equals zero, determined according to paragraph (a) of this
section, and you use the compliant material option, you are not required
to comply with paragraphs (b) and (c) of this section for that coating.
(a) Determine the mass fraction of organic HAP for each material
used. You must determine the mass fraction of organic HAP for each
coating, thinner, and cleaning material used during the compliance
period by using one of the options in paragraphs (a)(1) through (5) of
this section.
(1) Method 311 (appendix A to 40 CFR part 63). You may use Method
311 for determining the mass fraction of organic HAP. Use the procedures
specified in paragraphs (a)(1)(i) and (ii) of this section when
performing a Method 311 test.
(i) Count each organic HAP that is measured to be present at 0.1
percent by mass or more for Occupational Safety and Health
Administration (OSHA)-defined carcinogens as specified in 29 CFR
1910.1200(d)(4) and at 1.0 percent by mass or more for other organic HAP
compounds. For example, if toluene (not an OSHA carcinogen) is measured
to be 0.5 percent of the material by mass, you do not have to count it.
Express the mass fraction of each organic HAP you count as a value
truncated to four places after the decimal point (for example, 0.3791).
(ii) Calculate the total mass fraction of organic HAP in the test
material by adding up the individual organic HAP mass fractions and
truncating the result to three places after the decimal point (for
example, 0.763).
(2) Method 24 (appendix A to 40 CFR part 60). For coatings, you may
use Method 24 to determine the mass fraction of nonaqueous volatile
matter and use that value as a substitute for mass fraction of organic
HAP.
(3) Alternative method. You may use an alternative test method for
determining the mass fraction of organic HAP once the Administrator has
approved it. You must follow the procedure in Sec. 63.7(f) to submit an
alternative test method for approval.
(4) Information from the supplier or manufacturer of the material.
You may rely on information other than that generated by the test
methods specified in paragraphs (a)(1) through (3) of this section, such
as manufacturer's formulation data if they represent each organic HAP
that is present at 0.1 percent by mass or more for OSHA-defined
carcinogens as specified in 29 CFR 1910.1200(d)(4) and at 1.0 percent by
mass or more for other organic HAP compounds. For example, if toluene
(not an OSHA carcinogen) is 0.5 percent of the material by mass, you do
not have to count it. If there is a disagreement between such
information and results of a test conducted according to paragraphs
(a)(1) through (3) of this section, then the test method results will
take precedence.
[[Page 290]]
(5) Solvent blends. Solvent blends may be listed as single
components for some materials in data provided by manufacturers or
suppliers. Solvent blends may contain organic HAP which must be counted
toward the total organic HAP mass fraction of the materials. When test
data and manufacturer's data for solvent blends are not available, you
may use the default values for mass fraction of organic HAP in these
solvent blends listed in Table 3 or 4 of this subpart. If you use the
tables, you must use the values in Table 3 for all solvent blends that
match Table 3 entries, and you may only use Table 4 if the solvent
blends in the materials you use do not match any of the solvent blends
in Table 3, and you only know whether the blend is aliphatic or
aromatic. However, if the results of a Method 311 test indicate higher
values than those listed on Table 3 or 4 of this subpart, the Method 311
results will take precedence.
(b) Determine the volume fraction of coating solids for each
coating. You must determine the volume fraction of coating solids
(liters of coating solids per liter of coating) for each coating used
during the compliance period by a test, by information provided by the
supplier or the manufacturer of the material, or by calculation as
specified in paragraphs (b)(1) through (3) of this section.
(1) ASTM Method D2697-86 (Reapproved 1998) or D6093-97. You may use
ASTM Method D2697-86 (Reapproved 1998), ``Standard Test Method for
Volume Nonvolatile Matter in Clear or Pigmented Coatings,'' or D6093-97,
``Standard Test Method for Percent Volume Nonvolatile Matter in Clear or
Pigmented Coatings Using a Helium Gas Pycnometer'' (incorporated by
reference, see Sec. 63.14) to determine the volume fraction of coating
solids for each coating. Divide the nonvolatile volume percent obtained
with the methods by 100 to calculate volume fraction of coating solids.
(2) Information from the supplier or manufacturer of the material.
You may obtain the volume fraction of coating solids for each coating
from the supplier or manufacturer.
(3) Calculation of volume fraction of coating solids. If the volume
fraction of coating solids cannot be determined using the options in
paragraphs (b)(1) and (2) of this section, you must determine it using
Equation 1 of this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.018
Where:
Vs = volume fraction of coating solids, liters coating solids
per liter coating.
mvolatiles = total volatile matter content of the coating,
including HAP, volatile organic compounds (VOC), water, and exempt
compounds, determined according to Method 24 in appendix A of 40 CFR
part 60, grams volatile matter per liter coating.
Davg = average density of volatile matter in the coating,
grams volatile matter per liter volatile matter, determined from test
results using ASTM Method D1475-98, ``Standard Test Method for Density
of Liquid Coatings, Inks, and Related Products'' (incorporated by
reference, see Sec. 63.14) information from the supplier or manufacturer
of the material, or reference sources providing density or specific
gravity data for pure materials. If there is disagreement between ASTM
Method D1475-98 test results and other information sources, the test
results will take precedence.
(c) Determine the density of each coating. Determine the density of
each coating used during the compliance period from test results using
ASTM Method D1475-98, ``Standard Test Method for Density of Liquid
Coatings, Inks, and Related Products'' (incorporated by reference, see
Sec. 63.14), information from the supplier or manufacturer of the
material, or reference sources providing density or specific gravity
data for pure materials. If there is disagreement between ASTM Method
D1475-98 test results and other information sources, the test results
will take precedence.
(d) Determine the organic HAP content of each coating. Determine the
organic HAP content, kg organic HAP per liter coating solids, of each
coating used during the compliance period, using Equation 2 of this
section, except
[[Page 291]]
that if the mass fraction of organic HAP equals zero, then the organic
HAP content also equals zero and you are not required to use Equation 2
to calculate the organic HAP content:
[GRAPHIC] [TIFF OMITTED] TR23JY02.019
Where:
Hc = organic HAP content of the coating, kg organic HAP per
liter coating solids.
Dc = density of coating, kg coating per liter coating,
determined according to paragraph (c) of this section.
Wc = mass fraction of organic HAP in the coating, kg organic
HAP per kg coating, determined according to paragraph (a) of this
section.
Vs = volume fraction of coating solids, liters coating solids
per liter coating, determined according to paragraph (b) of this
section.
(e) The organic HAP content for each coating used during the initial
compliance period must be less than or equal to the applicable emission
limit in Sec. 63.4090; and each thinner and cleaning material used
during the initial compliance period must contain no organic HAP,
determined according to paragraph (a) of this section. You must keep all
records required by Secs. 63.4130 and 63.4131. As part of the
Notification of Compliance Status required in Sec. 63.4110, you must
identify the coating operation(s) for which you used the compliant
material option and submit a statement that the coating operation(s) was
(were) in compliance with the emission limitations during the initial
compliance period because you used no coatings for which the organic HAP
content exceeds the applicable emission limit in Sec. 63.4090, and you
used no thinners or cleaning materials that contain organic HAP,
determined according to paragraph (a) of this section.
Sec. 63.4142 How do I demonstrate continuous compliance with the emission limitations?
(a) For each compliance period, to demonstrate continuous
compliance, you must use no coating for which the organic HAP content,
determined according to Sec. 63.4141(d), exceeds the applicable emission
limit in Sec. 63.4090, and use no thinner or cleaning material that
contains organic HAP, determined according to Sec. 63.4141(a). Each
month following the initial compliance period described in Sec. 63.4140
is a compliance period.
(b) If you choose to comply with the emission limitations by using
the compliant material option, the use of any coating, thinner, or
cleaning material that does not meet the criteria specified in paragraph
(a) of this section is a deviation from the emission limitations that
must be reported as specified in Secs. 63.4110(b)(6) and 63.4120(d).
(c) As part of each semiannual compliance report required by
Sec. 63.4120, you must submit a statement that you were in compliance
with the emission limitations during the reporting period because you
used no thinners or cleaning materials that contained organic HAP, and
you used no coatings for which the organic HAP content exceeded the
applicable emission limit in Sec. 63.4090.
(d) You must maintain records as specified in Secs. 63.4130 and
63.4131.
Compliance Requirements for the Emission Rate Without Add-On Controls
Option
Sec. 63.4150 By what date must I conduct the initial compliance demonstration?
You must complete the initial compliance demonstration for the
initial compliance period according to the requirements of Sec. 63.4151.
The initial compliance period begins on the applicable compliance date
specified in Sec. 63.4083 and ends on the last day of the first full
month after the compliance date. If the compliance date occurs on any
day other than the first day of a month, then the initial compliance
period extends through the end of that month plus the next month. The
initial compliance demonstration includes the calculations according to
Sec. 63.4151 and supporting documentation showing that the organic HAP
emission rate for the initial compliance period was equal to or less
than the applicable emission limit in Sec. 63.4090.
[[Page 292]]
Sec. 63.4151 How do I demonstrate initial compliance with the emission limitations?
You may use the emission rate without add-on controls option for any
individual coating operation, for any group of coating operations in the
affected source, or for all of the coating operations in the affected
source. You must use either the compliant material option or the
emission rate with add-on controls option for any coating operation(s)
in the affected source for which you do not use this option. To
demonstrate initial compliance using the emission rate without add-on
controls option, the coating operation(s) must meet the applicable
emission limit in Sec. 63.4090 but not the operating limits or work
practice standards in Secs. 63.4092 and 63.4093, respectively, during
the initial compliance period. You must meet all of the requirements of
this section to demonstrate initial compliance with the applicable
emission limit in Sec. 63.4090 for the coating operation(s). When
calculating the organic HAP emission rate according to this section, do
not include any coatings, thinners, or cleaning materials used on
coating operations for which you use the compliant material option or
the emission rate with add-on controls option. You do not need to
redetermine the mass of organic HAP in coatings, thinners, or cleaning
materials that have been reclaimed onsite and reused in the coating
operation(s) for which you use the emission rate without add-on controls
option.
(a) Determine the mass fraction of organic HAP for each material.
Determine the mass fraction of organic HAP for each coating, thinner,
and cleaning material used during the compliance period according to the
requirements in Sec. 63.4141(a).
(b) Determine the volume fraction of coating solids for each
coating. Determine the volume fraction of coating solids for each
coating used during the compliance period according to the requirements
in Sec. 63.4141(b).
(c) Determine the density of each material. Determine the density of
each coating, thinner, and cleaning material used during the compliance
period according to the requirements in Sec. 63.4141(c).
(d) Determine the volume of each material used during the compliance
period. Determine the volume (liters) of each coating, thinner, and
cleaning material used during the compliance period by measurement or
usage records.
(e) Calculate the mass of organic HAP emissions during the
compliance period. The mass of organic HAP emissions is the combined
mass of organic HAP contained in all coatings, thinners, and cleaning
materials used during the compliance period minus the organic HAP in
certain waste materials. Calculate it using Equation 1 of this section.
[GRAPHIC] [TIFF OMITTED] TR23JY02.000
Where:
He = total mass of organic HAP emissions during the
compliance period, kg.
A = total mass of organic HAP in the coatings used during the compliance
period, kg, as calculated in Equation 1A of this section.
B = total mass of organic HAP in the thinners used during the compliance
period, kg, as calculated in Equation 1B of this section.
C = total mass of organic HAP in the cleaning materials used during the
compliance period, kg, as calculated in Equation 1C of this section.
Rw = total mass of organic HAP in waste materials sent or
designated for shipment to a hazardous waste TSDF for treatment or
disposal during the compliance period, kg, determined according to
paragraph (e)(4) of this section. (You may assign a value of zero to
Rw if you do not wish to use this allowance.)
(1) Calculate the kg organic HAP in the coatings used during the
compliance period, using Equation 1A of this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.001
Where:
A = total mass of organic HAP in the coatings used during the compliance
period, kg.
[[Page 293]]
Volc,i = total volume of coating, i, used during the
compliance period, liters.
Dc,i = density of coating, i, kg coating per liter coating.
Wc,i = mass fraction of organic HAP in coating, i, kg organic
HAP per kg coating.
m = number of different coatings used during the compliance period.
(2) Calculate the kg of organic HAP in the thinners used during the
compliance period, using Equation 1B of this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.002
Where:
B = total mass or organic HAP in the thinners used during the compliance
period, kg.
Volt,j = total volume of thinner, j, used during the
compliance period, liters.
Dt,j = density of thinner, j, kg thinner per liter thinner.
Wt,j = mass fraction of organic HAP in thinner, j, kg organic
HAP per kg thinner.
n = number of different thinners used during the compliance period.
(3) Calculate the kg organic HAP in the cleaning materials used
during the compliance period, using Equation 1C of this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.003
Where:
C = total mass of organic HAP in the cleaning materials used during the
compliance period, kg.
Vols,k = total volume of cleaning material, k, used during
the compliance period, liters.
Ds,k = density of cleaning material, k, kg cleaning material
per liter cleaning material.
Ws,k = mass fraction of organic HAP in cleaning material, k,
kg organic HAP per kg material.
p = number of different cleaning materials used during the compliance
period.
(4) Determine the mass of organic HAP contained in waste materials
sent to a TSDF. If you choose to account for the mass of organic HAP
contained in waste materials sent or designated for shipment to a
hazardous waste TSDF in the calculation of the mass of organic HAP
emissions (Equation 1 of this section), then you must determine it
according to paragraphs (e)(4)(i) through (v) of this section.
(i) You may include in the determination of organic HAP in waste
materials only the waste materials that are generated by coating
operations for which you use Equation 1 of this section and that will be
treated or disposed of by a facility that is regulated as a TSDF under
40 CFR part 262, 264, 265, or 266. The TSDF may be either off-site or
on-site. You may not include in the determination the organic HAP
contained in wastewater.
(ii) You must determine either the amount of waste materials sent to
a TSDF during the compliance period or the amount collected and stored
during the compliance period and designated for future transport to a
TSDF. Do not include in your determination any waste materials sent to a
TSDF during a compliance period if you have already included them in the
amount collected and stored during that compliance period or a previous
compliance period.
(iii) Determine the total mass of organic HAP contained in the waste
materials specified in paragraph (e)(4)(ii) of this section.
(iv) You must document your methodology to determine the amount of
waste materials and the total mass of organic HAP they contain, as
required in Sec. 63.4130(h).
(v) To the extent that waste manifests include this information,
they may be used as part of the documentation of the amount of waste
materials and mass of organic HAP contained in them.
(f) Calculate the total volume of coating solids used during the
compliance period. Determine the total volume of coating solids used,
liters, which is the combined volume of coating solids for all of the
coatings used during the compliance period, using Equation 2 of this
section.
[[Page 294]]
[GRAPHIC] [TIFF OMITTED] TR23JY02.004
Where:
Vst = total volume of coating solids used during the
compliance period, liters.
Volc,i = total volume of coating, i, used during the
compliance period, liters.
Vs,i = volume fraction of coating solids for coating, i,
liters solids per liter coating, determined according to
Sec. 63.4141(b).
m = number of coatings used during the compliance period.
(g) Calculate the organic HAP emission rate, kg organic HAP per
liter coating solids used, using Equation 3 of this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.005
Where:
Havg = organic HAP emission rate for the compliance period,
kg organic HAP per liter coating solids.
He = total mass organic HAP emissions from all materials used
during the compliance period, kg, as calculated by Equation 1 of
this section.
Vst = total volume coating solids used during the compliance
period, liters, as calculated by Equation 2 of this section.
(h) The organic HAP emission rate for the initial compliance period
must be less than or equal to the applicable emission limit in
Sec. 63.4090. You must keep all records as required by Secs. 63.4130 and
63.4131. As part of the Notification of Compliance Status required by
Sec. 63.4110, you must identify the coating operation(s) for which you
used the emission rate without add-on controls option and submit a
statement that the coating operation(s) was (were) in compliance with
the emission limitations during the initial compliance period because
the organic HAP emission rate was less than or equal to the applicable
emission limit in Sec. 63.4090.
Sec. 63.4152 How do I demonstrate continuous compliance with the emission limitations?
(a) To demonstrate continuous compliance, the organic HAP emission
rate for each compliance period, determined according to Sec. 63.4151(a)
through (g), must be less than or equal to the applicable emission limit
in Sec. 63.4090. Each month following the initial compliance period
described in Sec. 63.4150 is a compliance period.
(b) If the organic HAP emission rate for any compliance period
exceeded the applicable emission limit in Sec. 63.4090, this is a
deviation from the emission limitations for that compliance period and
must be reported as specified in Secs. 63.4110(b)(6) and 63.4120(e).
(c) As part of each semiannual compliance report required by
Sec. 63.4120, you must submit a statement that you were in compliance
with the emission limitations during the reporting period because the
organic HAP emission rate for each compliance period was less than or
equal to the applicable emission limit in Sec. 63.4090.
(d) You must maintain records as specified in Secs. 63.4130 and
63.4131.
Compliance Requirements for the Emission Rate With Add-On Controls
Option
Sec. 63.4160 By what date must I conduct performance tests and other initial compliance demonstrations?
(a) Existing affected sources. For an existing affected source, you
must meet the requirements of paragraphs (a)(1) through (3) of this
section.
(1) All emission capture systems, add-on control devices, and CPMS
you use to demonstrate compliance must be installed and operating no
later than the applicable compliance date specified in Sec. 63.4183.
Except for solvent recovery systems for which you conduct liquid-liquid
material balances according to Sec. 63.4161(h), you must conduct a
performance test of each capture system and add-on control device
according to the procedures in Secs. 63.4164, 63.4165, and 63.4166, and
establish the operating limits required by Sec. 63.4092 no
[[Page 295]]
later than the compliance date specified in Sec. 63.4083. For a solvent
recovery system for which you conduct liquid-liquid material balances
according to Sec. 63.4161(h), you must initiate the first material
balance no later than the compliance date specified in Sec. 63.4083.
(2) You must develop and begin implementing the work practice plan
required by Sec. 63.4093 no later than the compliance date specified in
Sec. 63.4083.
(3) You must complete the compliance demonstration for the initial
compliance period according to the requirements of Sec. 63.4161. The
initial compliance period begins on the applicable compliance date
specified in Sec. 63.4083 and ends on the last day of the first full
month after the compliance date. If the compliance date occurs on any
day other than the first day of a month, then the initial compliance
period extends through the end of that month plus the next month. The
initial compliance demonstration includes the results of emission
capture system and add-on control device performance tests conducted
according to Secs. 63.4164, 63.4165, and 63.4166; results of liquid-
liquid material balances conducted according to Sec. 63.4161(h);
calculations according to Sec. 63.4161 and supporting documentation
showing that, during the initial compliance period, the organic HAP
emission rate was equal to or less than the emission limit in
Sec. 63.4090(a); the operating limits established during the performance
tests and the results of the continuous parameter monitoring required by
Sec. 63.4168; and documentation of whether you developed and implemented
the work practice plan required by Sec. 63.4093.
(b) New and reconstructed affected sources. For a new or
reconstructed affected source, you must meet the requirements of
paragraphs (b)(1) through (4) this section.
(1) All emission capture systems, add-on control devices, and CPMS
you use to demonstrate compliance must be installed and operating no
later than the applicable compliance date specified in Sec. 63.4183.
Except for solvent recovery systems for which you conduct liquid-liquid
material balances according to Sec. 63.4161(h), you must conduct a
performance test of each capture system and add-on control device
according to the procedures in Secs. 63.4164, 63.4165, and 63.4166, and
establish the operating limits required by Sec. 63.4092 no later than
180 days after the applicable compliance date specified in Sec. 63.4183.
For a solvent recovery system for which you conduct liquid-liquid
material balances according to Sec. 63.4161(h), you must initiate the
first material balance no later than 180 days after the applicable
compliance date specified in Sec. 63.4183.
(2) You must develop and begin implementing the work practice plan
required by Sec. 63.4093 no later than the compliance date specified in
Sec. 63.4083.
(3) You must complete the compliance demonstration for the initial
compliance period according to the requirements of Sec. 63.4161. The
initial compliance period begins on the applicable compliance date
specified in Sec. 63.4083 and ends on the last day of the first full
month after the compliance date, or the date you conduct the performance
tests of the emission capture systems and add-on control devices, or
initiate the first liquid-liquid material balance for a solvent recovery
system; whichever is later. The initial compliance demonstration
includes the results of emission capture system and add-on control
device performance tests conducted according to Secs. 63.4164, 63.4165,
and 63.4166; results of liquid-liquid material balances conducted
according to Sec. 63.4161(h); calculations according to Sec. 63.4161 and
supporting documentation showing that, during the initial compliance
period, the organic HAP emission rate was equal to or less than the
emission limit in Sec. 63.4090(b); the operating limits established
during the performance tests and the results of the continuous parameter
monitoring required by Sec. 63.4168; and documentation of whether you
developed and implemented the work practice plan required by
Sec. 63.4093.
(4) You do not need to comply with the operating limits for the
emission capture system and add-on control device required by
Sec. 63.4092 until after you have completed the performance tests
specified in paragraph (b)(1) of this section. Instead, you must
maintain a log detailing the operation and maintenance of the emission
capture system, add-on control device, and continuous
[[Page 296]]
parameter monitors during the period between the compliance date and the
performance test. You must begin complying with the operating limits for
your affected source on the date you complete the performance tests
specified in paragraph (b)(1) of this section. This requirement does not
apply to solvent recovery systems for which you conduct liquid-liquid
material balances according to Sec. 63.4161(h).
Sec. 63.4161 How do I demonstrate initial compliance?
You may use the emission rate with add-on controls option for any
coating operation, for any group of coating operations in the affected
source, or for all of the coating operations in the affected source. You
may include both controlled and uncontrolled coating operations in a
group for which you use this option. You must use either the compliant
material option or the emission rate without add-on controls option for
any coating operation(s) in the affected source for which you do not use
this option. To demonstrate initial compliance, the coating operation(s)
for which you use the emission rate with add-on controls option must
meet the applicable emission limit in Sec. 63.4090 and the work practice
standards required in Sec. 63.4093; and each controlled coating
operation must meet the operating limits required in Sec. 63.4092. You
must meet all the requirements of this section to demonstrate initial
compliance with the emission limitations. When calculating the organic
HAP emission rate according to this section, do not include any
coatings, thinners, or cleaning materials used on coating operations for
which you use the compliant material option or the emission rate without
add-on controls option. You do not need to redetermine the mass of
organic HAP in coatings, thinners, or cleaning materials that have been
reclaimed onsite and reused in the coating operation(s) for which you
use the emission rate with add-on controls option.
(a) Except as provided in Sec. 63.4160(b)(4) and except for solvent
recovery systems for which you conduct liquid-liquid material balances
according to the requirements of Sec. 63.4161(h), you must establish and
demonstrate continuous compliance during the initial compliance period
with the operating limits required by Sec. 63.4092, using the procedures
specified in Secs. 63.4167 and 63.4168.
(b) You must develop, implement, and document your implementation of
the work practice plan required by Sec. 63.4093 during the initial
compliance period as specified in Sec. 63.4130.
(c) You must follow the procedures in paragraphs (d) through (l) of
this section to demonstrate compliance with the applicable emission
limit in Sec. 63.4090.
(d) Determine the mass fraction of organic HAP, density, volume
used, and volume fraction of coating solids. Follow the procedures
specified in Sec. 63.4151(a) through (d) to determine the mass fraction
of organic HAP, density, and volume of each coating, thinner, and
cleaning material used during the compliance period, and the volume
fraction of coating solids for each coating used during the compliance
period.
(e) Calculate the total mass of organic HAP emissions before add-on
controls. Using Equation 1 of Sec. 63.4151, calculate the total mass of
organic HAP emissions before add-on controls from all coatings,
thinners, and cleaning materials used during the compliance period in
the coating operation or group of coating operations for which you use
the emission rate with add-on controls option.
(f) Calculate the organic HAP emission reduction for each controlled
coating operation. Determine the mass of organic HAP emissions reduced
for each controlled coating operation during the compliance period. The
emissions reduction determination quantifies the total organic HAP
emissions that pass through the emission capture system and are
destroyed or removed by the add-on control device. Use the procedures in
paragraph (g) of this section to calculate the mass of organic HAP
emissions reduction for each controlled coating operation using an
emission capture system and add-on control device other than a solvent
recovery system for which you conduct liquid-liquid material balances.
For each controlled coating operation using a solvent recovery system
for which you
[[Page 297]]
conduct a liquid-liquid material balance, use the procedures in
paragraph (h) of this section to calculate the organic HAP emissions
reduction.
(g) Calculate the organic HAP emissions reduction for controlled
coating operations not using liquid-liquid material balance. For each
controlled coating operation using an emission capture system and add-on
control device other than a solvent recovery system for which you
conduct liquid-liquid material balances, calculate organic HAP emissions
reduction, using Equation 1 of this section, by applying the emission
capture system efficiency and add-on control device efficiency to the
mass of organic HAP contained in the coatings, thinners, and cleaning
materials that are used in the coating operation served by the emission
capture system and add-on control device during the compliance period.
For any period of time a deviation specified in Sec. 63.4163(c) or (d)
occurs in the controlled coating operation, including a deviation during
a period of startup, shutdown, or malfunction, you must assume zero
efficiency for the emission capture system and add-on control device.
For the purposes of completing the compliance calculations, you must
treat the materials used during a deviation on a controlled coating
operation as if they were used on an uncontrolled coating operation for
the time period of the deviation. You must not include those materials
in the calculations of organic HAP emissions reduction in Equation 1 of
this section.
[GRAPHIC] [TIFF OMITTED] TR23JY02.006
Where:
HC = mass of organic HAP emissions reduction for the
controlled coating operation during the compliance period, kg.
AI = total mass of organic HAP in the coatings used in the
controlled coating operation, kg, as calculated in Equation 1A of this
section.
BI = total mass of organic HAP in the thinners used in the
controlled coating operation, kg, as calculated in Equation 1B of this
section.
CI = total mass of organic HAP in the cleaning materials used
in the controlled coating operation during the compliance period, kg, as
calculated in Equation 1C of this section.
CE = capture efficiency of the emission capture system vented to the
add-on control device, percent. Use the test methods and procedures
specified in Secs. 63.4164 and 63.4165 to measure and record capture
efficiency.
DRE = organic HAP destruction or removal efficiency of the add-on
control device, percent. Use the test methods and procedures in
Secs. 63.4164 and 63.4166 to measure and record the organic HAP
destruction or removal efficiency.
(1) Calculate the kg of organic HAP in the coatings used in the
controlled coating operation, using Equation 1A of this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.007
Where:
AI = mass of organic HAP in the coatings used in the
controlled coating operation, kg.
Volc,i = total volume of coating, i, used, liters.
Dc,i = density of coating, i, kg per liter.
Wc,i = mass fraction of organic HAP in coating, i, kg per kg.
m = number of different coatings used.
(2) Calculate the kg of organic HAP in the thinners used in the
controlled coating operation, using Equation 1B of this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.008
Where:
[[Page 298]]
BI = mass of organic HAP in the thinners used in the
controlled coating operation, kg.
Volt,j = total volume of thinner, j, used, liters.
Dt,j = density of thinner, j, kg per liter.
Wt,j = mass fraction of organic HAP in thinner, j, kg per kg.
n = number of different thinners used.
(3) Calculate the kg of organic HAP in the cleaning materials used
in the controlled coating operation during the compliance period, using
Equation 1C of this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.009
Where:
CI = mass of organic HAP in the cleaning materials used in
the controlled coating operation, kg.
Vols,k = total volume of cleaning material, k, used, liters.
Ds,k = density of cleaning material, k, kg per liter.
Ws,k = mass fraction of organic HAP in cleaning material, k,
kg per kg.
p = number of different cleaning materials used.
(h) Calculate the organic HAP emissions reduction for controlled
coating operations using liquid-liquid material balance. For each
controlled coating operation using a solvent recovery system for which
you conduct liquid-liquid material balances, calculate the organic HAP
emissions reduction by applying the volatile organic matter collection
and recovery efficiency to the mass of organic HAP contained in the
coatings, thinners, and cleaning materials that are used in the coating
operation controlled by the solvent recovery system during the
compliance period. Perform a liquid-liquid material balance for each
compliance period as specified in paragraphs (h)(1) through (6) of this
section. Calculate the mass of organic HAP emission reduction by the
solvent recovery system as specified in paragraph (h)(7) of this
section.
(1) For each solvent recovery system, install, calibrate, maintain,
and operate according to the manufacturer's specifications, a device
that indicates the cumulative amount of volatile organic matter
recovered by the solvent recovery system each compliance period. The
device must be initially certified by the manufacturer to be accurate to
within [plusmn]2.0 percent of the mass of volatile organic matter
recovered.
(2) For each solvent recovery system, determine the mass of volatile
organic matter recovered for the compliance period, kg, based on
measurement with the device required in paragraph (h)(1) of this
section.
(3) Determine the mass fraction of volatile organic matter for each
coating used in the coating operation controlled by the solvent recovery
system during the compliance period, kg volatile organic matter per kg
coating. You may determine the volatile organic matter mass fraction
using Method 24 of 40 CFR part 60, appendix A, or an EPA approved
alternative method, or you may use information provided by the
manufacturer or supplier of the coating. In the event of any
inconsistency between information provided by the manufacturer or
supplier and the results of Method 24 of 40 CFR part 60, appendix A, or
an approved alternative method, the test method results will govern.
(4) Determine the density of each coating, thinner, and cleaning
material used in the coating operation controlled by the solvent
recovery system during the compliance period, kg per liter, according to
Sec. 63.4151(c).
(5) Measure the volume of each coating, thinner, and cleaning
material used in the coating operation controlled by the solvent
recovery system during the compliance period, liters.
(6) Calculate the solvent recovery system's volatile organic matter
collection and recovery efficiency, using Equation 2 of this section:
[[Page 299]]
[GRAPHIC] [TIFF OMITTED] TR23JY02.010
Where:
RV = volatile organic matter collection and recovery
efficiency of the solvent recovery system during the compliance period,
percent.
MVR = mass of volatile organic matter recovered by the
solvent recovery system during the compliance period, kg.
Voli = volume of coating, i, used in the coating operation
controlled by the solvent recovery system during the compliance period,
liters.
Di = density of coating, i, kg coating per liter coating.
CVi = mass fraction of volatile organic matter for coating,
i, kg volatile organic matter per kg coating.
Volj = volume of thinner, j, used in the coating operation
controlled by the solvent recovery system during the compliance period,
liters.
Dj = density of thinner, j, kg thinner per liter thinner.
Volk = volume of cleaning material, k, used in the coating
operation controlled by the solvent recovery system during the
compliance period, liters.
Dk = density of cleaning material, k, kg cleaning material
per liter cleaning material
m = number of different coatings used in the coating operation
controlled by the solvent recovery system during the compliance period.
n = number of different thinners used in the coating operation
controlled by the solvent recovery system during the compliance period.
p = number of different cleaning materials used in the coating operation
controlled by the solvent recovery system during the compliance period.
(7) Calculate the mass of organic HAP emissions reduction for the
coating operation controlled by the solvent recovery system during the
compliance period, using Equation 3 of this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.011
Where:
HCSR = mass of organic HAP emissions reduction for the
coating operation controlled by the solvent recovery system using a
liquid-liquid material balance during the compliance period, kg.
AI = total mass of organic HAP in the coatings used in the
coating operation controlled by the solvent recovery system, kg,
calculated using Equation 1A of this section.
BI = total mass of organic HAP in the thinners used in the
coating operation controlled by the solvent recovery system, kg,
calculated using Equation 1B of this section.
CI = total mass of organic HAP in the cleaning materials used
in the coating operation controlled by the solvent recovery system, kg,
calculated using Equation 1C of this section.
RV = volatile organic matter collection and recovery
efficiency of the solvent recovery system, percent, from Equation 2 of
this section.
(i) [Reserved]
(j) Calculate the total volume of coating solids used. Determine the
total volume of coating solids used, liters, which is the combined
volume of coating solids for all the coatings used during the compliance
period, using Equation 2 of Sec. 63.4151.
(k) Calculate the organic HAP emission rate. Determine the organic
HAP emission rate to the atmosphere, kg organic HAP per liter coating
solids used during the compliance period, using Equation 4 of this
section.
[[Page 300]]
[GRAPHIC] [TIFF OMITTED] TR23JY02.012
Where:
HHAP = organic HAP emission rate to the atmosphere during the
compliance period, kg organic HAP per liter coating solids used.
He = total mass of organic HAP emissions before add-on
controls from all the coatings, thinners, and cleaning materials used
during the compliance period, kg, determined according to paragraph (e)
of this section.
HC,i = total mass of organic HAP emissions reduction for
controlled coating operation, i, during the compliance period, kg, from
Equation 1 of this section.
HCSR,j = total mass of organic HAP emissions reduction for
controlled coating operation, j, during the compliance period, kg, from
Equation 3 of this section.
Vst = total volume of coating solids used during the
compliance period, liters, from Equation 2 of Sec. 63.4151.
q = number of controlled coating operations except those controlled with
a solvent recovery system.
r = number of coating operations controlled with a solvent recovery
system.
(l) To demonstrate initial compliance with the emission limit,
calculated using Equation 4 of this section, must be less than or equal
to the applicable emission limit in Sec. 63.4090. You must keep all
records as required by Secs. 63.4130 and 63.4131. As part of the
Notification of Compliance Status required by Sec. 63.4110, you must
identify the coating operation(s) for which you used the emission rate
with add-on controls option and submit a statement that the coating
operation(s) was (were) in compliance with the emission limitations
during the initial compliance period because the organic HAP emission
rate was less than or equal to the applicable emission limit in
Sec. 63.4090, and you achieved the operating limits required by
Sec. 63.4092 and the work practice standards required by Sec. 63.4093.
Sec. 63.4162 [Reserved]
Sec. 63.4163 How do I demonstrate continuous compliance with the emission limitations?
(a) To demonstrate continuous compliance with the applicable
emission limit in Sec. 63.4090, the organic HAP emission rate for each
compliance period determined according to the procedures in Sec. 63.4161
must be equal to or less than the applicable emission limit in
Sec. 63.4090. Each month following the initial compliance period
described in Sec. 63.4160 is a compliance period.
(b) If the organic HAP emission rate for any compliance period
exceeded the applicable emission limit in Sec. 63.4090, this is a
deviation from the emission limitation for that compliance period and
must be reported as specified in Secs. 63.4110(b)(6) and 63.4120(g).
(c) You must demonstrate continuous compliance with each operating
limit required by Sec. 63.4092 that applies to you as specified in Table
1 to this subpart.
(1) If an operating parameter is out of the allowed range specified
in Table 1 to this subpart, this is a deviation from the operating limit
that must be reported as specified in Secs. 63.4110(b)(6) and
63.4120(g).
(2) If an operating parameter deviates from the operating limit
specified in Table 1 to this subpart, then you must assume that the
emission capture system and add-on control device were achieving zero
efficiency during the time period of the deviation. For the purposes of
completing the compliance calculations specified in Sec. 63.4161, you
must treat the materials used during a deviation on a controlled coating
operation as if they were used on an uncontrolled coating operation for
the time period of the deviation. You must not include those materials
in the calculation of organic HAP emissions reductions in Equation 1 of
Sec. 63.4161.
[[Page 301]]
(d) You must meet the requirements for bypass lines in
Sec. 63.4168(b). If any bypass line is opened and emissions are diverted
to the atmosphere when the coating operation is running, this is a
deviation that must be reported as specified in Secs. 63.4110(b)(6) and
63.4120(g). For the purposes of completing the compliance calculations
specified in Sec. 63.4161, you must treat the materials used during a
deviation on a controlled coating operation as if they were used on an
uncontrolled coating operation for the time period of the deviation. You
must not include those materials in the calculation of organic HAP
emissions reductions in Equation 1 of Sec. 63.4161.
(e) You must demonstrate continuous compliance with the work
practice standards in Sec. 63.4093. If you did not develop a work
practice plan, or you did not implement the plan, or you did not keep
the records required by Sec. 63.4130(k)(9), this is a deviation from the
work practice standards that must be reported as specified in
Secs. 63.4110(b)(6) and 63.4120(g).
(f) As part of each semiannual compliance report required in
Sec. 63.4120, you must submit a statement that you were in compliance
with the emission limitations during the reporting period because the
organic HAP emission rate for each compliance period was less than or
equal to the applicable emission limit in Sec. 63.4090, and you achieved
the operating limits required by Sec. 63.4092 and the work practice
standards required by Sec. 63.4093 during each compliance period.
(g) During periods of startup, shutdown, and malfunction of the
emission capture system, add-on control device, or coating operation
that may affect emission capture or control device efficiency, you must
operate in accordance with the SSMP required by Sec. 63.4100(d).
(h) Consistent with Secs. 63.6(e) and 63.7(e)(1), deviations that
occur during a period of startup, shutdown, or malfunction of the
emission capture system, add-on control device, or coating operation
that may affect emission capture or control device efficiency are not
violations if you demonstrate to the Administrator's satisfaction that
you were operating in accordance with the SSMP. The Administrator will
determine whether deviations that occur during a period of startup,
shutdown, or malfunction are violations according to the provisions in
Sec. 63.6(e).
(i) [Reserved]
(j) You must maintain records as specified in Secs. 63.4130 and
63.4131.
Sec. 63.4164 What are the general requirements for performance tests?
(a) You must conduct each performance test required by Sec. 63.4160
according to the requirements in Sec. 63.7(e)(1) and under the
conditions in this section unless you obtain a waiver of the performance
test according to the provisions in Sec. 63.7(h).
(1) Representative coating operation operating conditions. You must
conduct the performance test under representative operating conditions
for the coating operation. Operations during periods of startup,
shutdown, or malfunction and periods of nonoperation do not constitute
representative conditions. You must record the process information that
is necessary to document operating conditions during the test and
explain why the conditions represent normal operation.
(2) Representative emission capture system and add-on control device
operating conditions. You must conduct the performance test when the
emission capture system and add-on control device are operating at a
representative flow rate, and the add-on control device is operating at
a representative inlet concentration. You must record information that
is necessary to document emission capture system and add-on control
device operating conditions during the test and explain why the
conditions represent normal operation.
(b) You must conduct each performance test of an emission capture
system according to the requirements in Sec. 63.4165 and of an add-on
control device according to the requirements in Sec. 63.4166.
(c) The performance test to determine add-on control device organic
HAP destruction or removal efficiency must consist of three runs as
specified in Sec. 63.7(e)(3) and each run must last at least 1 hour.
[[Page 302]]
Sec. 63.4165 How do I determine the emission capture system efficiency?
You must use the procedures and test methods in this section to
determine capture efficiency as part of the performance test required by
Sec. 63.4160.
(a) You may assume the capture system efficiency is 100 percent if
both of the conditions in paragraphs (a)(1) and (2) of this section are
met:
(1) The capture system meets the criteria in Method 204 of appendix
M to 40 CFR part 51 for a PTE and directs all the exhaust gases from the
enclosure to an add-on control device.
(2) All coatings, thinners, and cleaning materials used in the
coating operation are applied within the capture system; coating solvent
flash-off and coating, curing, and drying occurs within the capture
system and the removal or evaporation of cleaning materials from the
surfaces they are applied to occurs within the capture system. For
example, this criterion is not met if parts enter the open shop
environment when being moved between a spray booth and a curing oven.
(b) If the capture system does not meet both of the criteria in
paragraphs (a)(1) and (2) of this section, then you must use one of the
three protocols described in paragraphs (c), (d), and (e) of this
section to measure capture efficiency. The capture efficiency
measurements use TVH capture efficiency as a surrogate for organic HAP
capture efficiency. For the protocols in paragraphs (c) and (d) of this
section, the capture efficiency measurement must consist of three test
runs. Each test run must be at least 3 hours duration or the length of a
production run, whichever is longer, up to 8 hours. For the purposes of
this test, a production run means the time required for a single part to
go from the beginning to the end of production which includes surface
preparation activities and drying or curing time.
(c) Liquid-to-uncaptured-gas protocol using a temporary total
enclosure or building enclosure. The liquid-to-uncaptured-gas protocol
compares the mass of liquid TVH in materials used in the coating
operation, to the mass of TVH emissions not captured by the emission
capture system. Use a temporary total enclosure or a building enclosure
and the procedures in paragraphs (c)(1) through (6) of this section to
measure emission capture system efficiency using the liquid-to-
uncaptured-gas protocol.
(1) Either use a building enclosure or construct an enclosure around
the coating operation where coatings, thinners, and cleaning materials
are applied, and all areas where emissions from these applied coatings
and materials subsequently occur, such as flash-off, curing, and drying
areas. The areas of the coating operation where capture devices collect
emissions for routing to an add-on control device, such as the entrance
and exit areas of an oven or spray booth, must also be inside the
enclosure. The enclosure must meet the applicable definition of a
temporary total enclosure or building enclosure in Method 204 of
appendix M to 40 CFR part 51.
(2) Use Method 204A or 204F of appendix M to 40 CFR part 51 to
determine the mass fraction of TVH liquid input from each coating,
thinner, and cleaning material used in the coating operation during each
capture efficiency test run. To make the determination, substitute TVH
for each occurrence of the term VOC in the methods.
(3) Use Equation 1 of this section to calculate the total mass of
TVH liquid input from all the coatings, thinners, and cleaning materials
used in the coating operation during each capture efficiency test run.
[GRAPHIC] [TIFF OMITTED] TR23JY02.013
Where:
TVHused = total mass of TVH liquid input from all coatings,
thinners,
[[Page 303]]
and cleaning materials used in the coating operation during the capture
efficiency test run, kg.
TVHi = mass fraction of TVH in coating, thinner, or cleaning
material, i, that is used in the coating operation during the capture
efficiency test run, kg TVH per kg material.
Voli = total volume of coating, thinner, or cleaning
material, i, used in the coating operation during the capture efficiency
test run, liters.
Di = density of coating, thinner, or cleaning material, i, kg
material per liter material.
n = number of different coatings, thinners, and cleaning materials used
in the coating operation during the capture efficiency test run.
(4) Use Method 204D or E of appendix M to 40 CFR part 51 to measure
the total mass, kg, of TVH emissions that are not captured by the
emission capture system; they are measured as they exit the temporary
total enclosure or building enclosure during each capture efficiency
test run. To make the measurement substitute TVH for each occurrence of
the term VOC in the methods.
(i) Use Method 204D if the enclosure is a temporary total enclosure.
(ii) Use Method 204E if the enclosure is a building enclosure.
During the capture efficiency measurement, all organic compound emitting
operations inside the building enclosure, other than the coating
operation for which capture efficiency is being determined must be shut
down, but all fans and blowers must be operating normally.
(5) For each capture efficiency test run, determine the percent
capture efficiency of the emission capture system, using Equation 2 of
this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.014
Where:
CE = capture efficiency of the emission capture system vented to the
add-on control device, percent.
TVHused = total mass of TVH liquid input used in the coating
operation during the capture efficiency test run, kg.
TVHuncaptured = total mass of TVH that is not captured by the
emission capture system and that exits from the temporary total
enclosure or building enclosure during the capture efficiency test run,
kg.
(6) Determine the capture efficiency of the emission capture system
as the average of the capture efficiencies measured in the three test
runs.
(d) Gas-to-gas protocol using a temporary total enclosure or a
building enclosure. The gas-to-gas protocol compares the mass of TVH
emissions captured by the emission capture system to the mass of TVH
emissions not captured. Use a temporary total enclosure or a building
enclosure and the procedures in paragraphs (d)(1) through (5) of this
section to measure emission capture system efficiency using the gas-to-
gas protocol.
(1) Either use a building enclosure or construct an enclosure around
the coating operation where coatings, thinners, and cleaning materials
are applied and all areas where emissions from these applied coatings
and materials subsequently occur such as flash-off, curing, and drying
areas. The areas of the coating operation where capture devices collect
emissions generated by the coating operation for routing to an add-on
control device, such as the entrance and exit areas of an oven or a
spray booth, must also be inside the enclosure. The enclosure must meet
the applicable definition of a temporary total enclosure or building
enclosure in Method 204 of appendix M to 40 CFR part 51.
(2) Use Method 204B or 204C of appendix M to 40 CFR part 51 to
measure the total mass, kg, of TVH emissions captured by the emission
capture system during each capture efficiency test run as measured at
the inlet to the add-on
[[Page 304]]
control device. To make the measurement, substitute TVH for each
occurrence of the term VOC in the methods.
(i) The sampling points for the Method 204B or 204C measurement must
be upstream from the add-on control device and must represent total
emissions routed from the capture system and entering the add-on control
device.
(ii) If multiple emission streams from the capture system enter the
add-on control device without a single common duct, then the emissions
entering the add-on control device must be simultaneously measured in
each duct, and the total emissions entering the add-on control device
must be determined.
(3) Use Method 204D or 204E of appendix M to 40 CFR part 51 to
measure the total mass, kg, of TVH emissions that are not captured by
the emission capture system; they are measured as they exit the
temporary total enclosure or building enclosure during each capture
efficiency test run. To make the measurement, substitute TVH for each
occurrence of the term VOC in the methods.
(i) Use Method 204D if the enclosure is a temporary total enclosure.
(ii) Use Method 204E if the enclosure is a building enclosure.
During the capture efficiency measurement, all organic compound emitting
operations inside the building enclosure other than the coating
operation for which capture efficiency is being determined must be shut
down, but all fans and blowers must be operating normally.
(4) For each capture efficiency test run, determine the percent
capture efficiency of the emission capture system, using Equation 3 of
this section:
[GRAPHIC] [TIFF OMITTED] TR23JY02.015
Where:
CE = capture efficiency of the emission capture system vented to the
add-on control device, percent.
TVHcaptured = total mass of TVH captured by the emission
capture system as measured at the inlet to the add-on control device
during the emission capture efficiency test run, kg.
TVHuncaptured = total mass of TVH that is not captured by the
emission capture system and that exits from the temporary total
enclosure or building enclosure during the capture efficiency test run,
kg.
(5) Determine the capture efficiency of the emission capture system
as the average of the capture efficiencies measured in the three test
runs.
(e) Alternative capture efficiency protocol. As an alternative to
the procedures specified in paragraphs (c) and (d) of this section, you
may determine capture efficiency using any other capture efficiency
protocol and test methods that satisfy the criteria of either the DQO or
LCL approach as described in appendix A to subpart KK of this part.
Sec. 63.4166 How do I determine the add-on control device emission destruction or removal efficiency?
(a) For all types of add-on control devices, use the test methods as
specified in paragraphs (a)(1) through (5) of this section.
(1) Use Method 1 or 1A of appendix A to 40 CFR part 60, as
appropriate, to select sampling sites and velocity traverse points.
(2) Use Method 2, 2A, 2C, 2D, 2F, or 2G of appendix A to 40 CFR part
60, as appropriate, to measure gas volumetric flow rate.
(3) Use Method 3, 3A, or 3B of appendix A to 40 CFR part 60, as
appropriate, for gas analysis to determine dry molecular weight. You may
also use as an alternative to Method 3B, the manual method for measuring
the oxygen, carbon dioxide, and carbon monoxide content of exhaust gas
in ANSI/ASME, PTC 19.10-1981, ``Flue and Exhaust Gas Analyses''
(incorporated by reference, see Sec. 63.14).
[[Page 305]]
(4) Use Method 4 of appendix A to 40 CFR part 60 to determine stack
gas moisture.
(5) Methods for determining gas volumetric flow rate, dry molecular
weight, and stack gas moisture must be performed, as applicable, during
each test run.
(b) Measure total gaseous organic mass emissions as carbon at the
inlet and outlet of the add-on control device simultaneously, using
either Method 25 or 25A of appendix A to 40 CFR part 60, as specified in
paragraphs (b)(1) through (3) of this section. You must use the same
method for both the inlet and outlet measurements.
(1) Use Method 25 if the add-on control device is an oxidizer and
you expect the total gaseous organic concentration as carbon to be more
than 50 parts per million (ppm) at the control device outlet.
(2) Use Method 25A if the add-on control device is an oxidizer and
you expect the total gaseous organic concentration as carbon to be 50
ppm or less at the control device outlet.
(3) Use Method 25A if the add-on control device is not an oxidizer.
(c) If two or more add-on control devices are used for the same
emission stream, then you must measure emissions at the outlet of each
device. For example, if one add-on control device is a concentrator with
an outlet for the high-volume, dilute stream that has been treated by
the concentrator, and a second add-on control device is an oxidizer with
an outlet for the low-volume, concentrated stream that is treated with
the oxidizer, you must measure emissions at the outlet of the oxidizer
and the high-volume dilute stream outlet of the concentrator.
(d) For each test run, determine the total gaseous organic emissions
mass flow rates for the inlet and the outlet of the add-on control
device, using Equation 1 of this section. If there is more than one
inlet or outlet to the add-on control device, you must calculate the
total gaseous organic mass flow rate using Equation 1 of this section
for each inlet and each outlet and then total all of the inlet emissions
and total all of the outlet emissions.
[GRAPHIC] [TIFF OMITTED] TR23JY02.016
Where:
Mf = total gaseous organic emissions mass flow rate, kg/per
hour (h).
Cc = concentration of organic compounds as carbon in the vent
gas, as determined by Method 25 or Method 25A, parts per million by
volume (ppmv), dry basis.
Qsd = volumetric flow rate of gases entering or exiting the
add-on control device, as determined by Method 2, 2A, 2C, 2D, 2F, or 2G,
dry standard cubic meters/hour (dscm/h).
0.0416 = conversion factor for molar volume, kg-moles per cubic meter
(mol/m \3\) (@ 293 Kelvin (K) and 760 millimeters of mercury (mm Hg)).
(e) For each test run, determine the add-on control device organic
emissions destruction or removal efficiency, using Equation 2 of this
section.
[GRAPHIC] [TIFF OMITTED] TR23JY02.017
Where:
DRE = add-on control device organic emissions destruction or removal
efficiency, percent.
Mfi = total gaseous organic emissions mass flow rate at the
inlet(s) to the add-on control device, using Equation 1 of this section,
kg/h.
Mfo = total gaseous organic emissions mass flow rate at the
outlet(s) of the add-on control device, using Equation 1 of this
section, kg/h.
(f) Determine the emission destruction or removal efficiency of the
add-on control device as the average of the efficiencies determined in
the three test runs and calculated in Equation 2 of this section.
Sec. 63.4167 How do I establish the emission capture system and add-on control device operating limits during the performance test?
During the performance test required by Sec. 63.4160 and described
in Secs. 63.4164, 63.4165, and 63.4166, you must establish the operating
limits required by
[[Page 306]]
Sec. 63.4092 according to this section unless you have received approval
for alternative monitoring and operating limits under Sec. 63.8(f) as
specified in Sec. 63.4092.
(a) Thermal oxidizers. If your add-on control device is a thermal
oxidizer, establish the operating limits according to paragraphs (a)(1)
and (2) of this section.
(1) During the performance test, you must monitor and record the
combustion temperature at least once every 15 minutes during each of the
three test runs. You must monitor the temperature in the firebox of the
thermal oxidizer or immediately downstream of the firebox before any
substantial heat exchange occurs.
(2) Use the data collected during the performance test to calculate
and record the average combustion temperature maintained during the
performance test. This average combustion temperature is the minimum
operating limit for your thermal oxidizer.
(b) Catalytic oxidizers. If your add-on control device is a
catalytic oxidizer, establish the operating limits according to either
paragraphs (b)(1) and (2) or paragraphs (b)(3) and (4) of this section.
(1) During the performance test, you must monitor and record the
temperature just before the catalyst bed and the temperature difference
across the catalyst bed at least once every 15 minutes during each of
the three test runs.
(2) Use the data collected during the performance test to calculate
and record the average temperature just before the catalyst bed and the
average temperature difference across the catalyst bed maintained during
the performance test. These are the minimum operating limits for your
catalytic oxidizer.
(3) As an alternative to monitoring the temperature difference
across the catalyst bed, you may monitor the temperature just before the
catalyst bed and implement a site-specific inspection and maintenance
plan for your catalytic oxidizer as specified in paragraph (b)(4) of
this section. During the performance test, you must monitor and record
the temperature just before the catalyst bed at least once every 15
minutes during each of the three test runs. Use the data collected
during the performance test to calculate and record the average
temperature just before the catalyst bed during the performance test.
This is the minimum operating limit for your catalytic oxidizer.
(4) You must develop and implement an inspection and maintenance
plan for your catalytic oxidizer(s) for which you elect to monitor
according to paragraph (b)(3) of this section. The plan must address, at
a minimum, the elements specified in paragraphs (b)(4)(i) through (iii)
of this section.
(i) Annual sampling and analysis of the catalyst activity (i.e.,
conversion efficiency) following the manufacturer's or catalyst
supplier's recommended procedures.
(ii) Monthly inspection of the oxidizer system including the burner
assembly and fuel supply lines for problems and, as necessary, adjusting
the equipment to assure proper air-to-fuel mixtures.
(iii) Annual internal and monthly external visual inspection of the
catalyst bed to check for channeling, abrasion, and settling. If
problems are found, you must take corrective action consistent with the
manufacturer's recommendations and conduct a new performance test to
determine destruction efficiency according to Sec. 63.4166.
(c) Carbon adsorbers. If your add-on control device is a carbon
absorber, establish the operating limits according to paragraphs (c)(1)
and (2) of this section.
(1) You must monitor and record the total regeneration desorbing gas
(e.g., steam or nitrogen) mass flow for each regeneration cycle and the
carbon bed temperature after each carbon bed regeneration and cooling
cycle for the regeneration cycle either immediately preceding or
immediately following the performance test.
(2) The operating limits for your carbon absorber are the minimum
total desorbing gas mass flow recorded during the regeneration cycle and
the maximum carbon bed temperature recorded after the cooling cycle.
(d) Condensers. If your add-on control device is a condenser,
establish the operating limits according to paragraphs (d)(1) and (2) of
this section.
[[Page 307]]
(1) During the performance test, you must monitor and record the
condenser outlet (product side) gas temperature at least once every 15
minutes during each of the three test runs.
(2) Use the data collected during the performance test to calculate
and record the average condenser outlet (product side) gas temperature
maintained during the performance test. This average condenser outlet
gas temperature is the maximum operating limit for your condenser.
(e) Concentrators. If your add-on control device includes a
concentrator, you must establish operating limits for the concentrator
according to paragraphs (e)(1) through (4) of this section.
(1) During the performance test, you must monitor and record the
desorption concentrate stream gas temperature at least once every 15
minutes during each of the three runs of the performance test.
(2) Use the data collected during the performance test to calculate
and record the average temperature. This is the minimum operating limit
for the desorption concentrate gas stream temperature.
(3) During the performance test, you must monitor and record the
pressure drop of the dilute stream across the concentrator at least once
every 15 minutes during each of the three runs of the performance test.
(4) Use the data collected during the performance test to calculate
and record the average pressure drop. This is the maximum operating
limit for the dilute stream across the concentrator.
(f) Emission capture system. For each capture device that is not
part of a PTE that meets the criteria of Sec. 63.4165(a), establish an
operating limit for either the gas volumetric flow rate or duct static
pressure as specified in paragraphs (f)(1) and (2) of this section. The
operating limit for a PTE is specified in Table 1 to this subpart.
(1) During the capture efficiency determination required by
Sec. 63.4160 and described in Secs. 63.4164 and 63.4165, you must
monitor and record either the gas volumetric flow rate or the duct
static pressure for each separate capture device in your emission
capture system at least once every 15 minutes during each of the three
test runs at a point in the duct between the capture device and the add-
on control device inlet.
(2) Calculate and record the average gas volumetric flow rate or
duct static pressure for the three test runs for each capture device.
This average gas volumetric flow rate or duct static pressure is the
minimum operating limit for that specific capture device.
Sec. 63.4168 What are the requirements for continuous parameter monitoring system installation, operation, and maintenance?
(a) General. You must install, operate, and maintain each CPMS
specified in paragraphs (c), (e), (f), and (g) of this section according
to paragraphs (a)(1) through (6) of this section. You must install,
operate, and maintain each CPMS specified in paragraphs (b) and (d) of
this section according to paragraphs (a)(3) through (5) of this section.
(1) The CPMS must complete a minimum of one cycle of operation for
each successive 15-minute period. You must have a minimum of four
equally spaced successive cycles of CPMS operation in 1 hour.
(2) You must determine the average of all recorded readings for each
successive 3-hour period of the emission capture system and add-on
control device operation except as specified in paragraph (a)(6) of this
section.
(3) You must record the results of each inspection, calibration, and
validation check of the CPMS.
(4) You must maintain the CPMS at all times and have available
necessary parts for routine repairs of the monitoring equipment.
(5) You must operate the CPMS and collect emission capture system
and add-on control device parameter data at all times that a controlled
coating operation is operating except during monitoring malfunctions,
associated repairs, and required quality assurance or control activities
(including, if applicable, calibration checks and required zero and span
adjustments).
(6) You must not use emission capture system or add-on control
device
[[Page 308]]
parameter data recorded during monitoring malfunctions, associated
repairs, out-of-control periods, or required quality assurance or
control activities when calculating data averages. You must use all the
data collected during all other periods in calculating the data averages
for determining compliance with the emission capture system and add-on
control device operating limits.
(7) A monitoring malfunction is any sudden, infrequent, not
reasonably preventable failure of the CPMS to provide valid data.
Monitoring failures that are caused in part by poor maintenance or
careless operation are not malfunctions. Except for periods of required
quality assurance or control activities, any period during which the
CPMS fails to operate and record data continuously as required by
paragraph (a)(1) of this section, or generates data that cannot be
included in calculating averages as specified in paragraph (a)(6) of
this section, is a deviation from the monitoring requirements.
(b) Capture system bypass line. You must comply with the
requirements of paragraphs (a)(3) through (5) and (b)(1) and (2) of this
section for each emission capture system that contains bypass lines that
could divert emissions away from the add-on control device to the
atmosphere.
(1) You must monitor or secure the valve or closure mechanism
controlling the bypass line in a nondiverting position in such a way
that the valve or closure mechanism cannot be opened without creating a
record that the valve was opened. The method used to monitor or secure
the valve or closure mechanism must meet one of the requirements
specified in paragraphs (b)(1)(i) through (iv) of this section.
(i) Flow control position indicator. Install, calibrate, maintain,
and operate according to the manufacturer's specifications a flow
control position indicator that takes a reading at least once every 15
minutes and provides a record indicating whether the emissions are
directed to the add-on control device or diverted from the add-on
control device. The time of occurrence and flow control position must be
recorded, as well as every time the flow direction is changed. The flow
control position indicator must be installed at the entrance to any
bypass line that could divert the emissions away from the add-on control
device to the atmosphere.
(ii) Car-seal or lock-and-key valve closures. Secure any bypass line
valve in the closed position with a car-seal or a lock-and-key type
configuration. You must visually inspect the seal or closure mechanism
at least once every month to ensure that the valve is maintained in the
closed position and the emissions are not diverted away from the add-on
control device to the atmosphere.
(iii) Valve closure monitoring. Ensure that any bypass line valve is
in the closed (non-diverting) position through monitoring of valve
position at least once every 15 minutes. You must inspect the monitoring
system at least once every month to verify that the monitor will
indicate valve position.
(iv) Automatic shutdown system. Use an automatic shutdown system in
which the coating operation is stopped when flow is diverted by the
bypass line away from the add-on control device to the atmosphere when
the coating operation is running. You must inspect the automatic
shutdown system at least once every month to verify that it will detect
diversions of flow and shutdown the coating operation.
(2) If any bypass line is opened, you must include a description of
why the bypass line was opened and the length of time it remained open
in the semiannual compliance reports required in Sec. 63.4120.
(c) Thermal oxidizers and catalytic oxidizers. If you are using a
thermal oxidizer or catalytic oxidizer as an add-on control device
(including those used with concentrators or with carbon adsorbers to
treat desorbed concentrate streams), you must comply with the
requirements in paragraphs (a) and (c)(1) through (3) of this section:
(1) For a thermal oxidizer, install a gas temperature monitor in the
firebox of the thermal oxidizer or in the duct immediately downstream of
the firebox before any substantial heat exchange occurs.
(2) For a catalytic oxidizer, install a gas temperature monitor in
the gas stream immediately before the catalyst bed, and if you establish
operating
[[Page 309]]
limits according to Sec. 63.6167(b)(1) and (2), also install a gas
temperature monitor in the gas stream immediately after the catalyst
bed.
(3) For each gas temperature monitoring device, you must comply with
the requirements in paragraphs (c)(3)(i) through (vii) of this section.
(i) Locate the temperature sensor in a position that provides a
representative temperature.
(ii) Use a temperature sensor with a measurement sensitivity of 4
degrees Fahrenheit or 0.75 percent of the temperature value, whichever
is larger.
(iii) Shield the temperature sensor system from electromagnetic
interference and chemical contaminants.
(iv) If a gas temperature chart recorder is used, it must have a
measurement sensitivity in the minor division of at least 20 degrees
Fahrenheit.
(v) Perform an electronic calibration at least semiannually
according to the procedures in the manufacturer's owners manual.
Following the electronic calibration, you must conduct a temperature
sensor validation check in which a second or redundant temperature
sensor placed nearby the process temperature sensor must yield a reading
within 30 degrees Fahrenheit of the process temperature sensor's
reading.
(vi) Any time the sensor exceeds the manufacturer's specified
maximum operating temperature range, either conduct calibration and
validation checks or install a new temperature sensor.
(vii) At least monthly, inspect components for integrity and
electrical connections for continuity, oxidation, and galvanic
corrosion.
(d) Carbon adsorbers. If you are using a carbon adsorber as an add-
on control device, you must monitor the total regeneration desorbing gas
(e.g., steam or nitrogen) mass flow for each regeneration cycle, the
carbon bed temperature after each regeneration and cooling cycle, and
comply with paragraphs (a)(3) through (5) and (d)(1) and (2) of this
section.
(1) The regeneration desorbing gas mass flow monitor must be an
integrating device having a measurement sensitivity of plus or minus 10
percent, capable of recording the total regeneration desorbing gas mass
flow for each regeneration cycle.
(2) The carbon bed temperature monitor must have a measurement
sensitivity of 1 percent of the temperature recorded or 1 degree
Fahrenheit, whichever is greater, and must be capable of recording the
temperature within 15 minutes of completing any carbon bed cooling
cycle.
(e) Condensers. If you are using a condenser, you must monitor the
condenser outlet (product side) gas temperature and comply with
paragraphs (a) and (e)(1) and (2) of this section.
(1) The gas temperature monitor must have a measurement sensitivity
of 1 percent of the temperature recorded or 1 degree Fahrenheit,
whichever is greater.
(2) The temperature monitor must provide a gas temperature record at
least once every 15 minutes.
(f) Concentrators. If you are using a concentrator, such as a
zeolite wheel or rotary carbon bed concentrator, you must comply with
the requirements in paragraphs (a) and (f)(1) and (2) of this section.
(1) You must install a temperature monitor in the desorption gas
stream. The temperature monitor must meet the requirements in paragraphs
(a) and (c)(3) of this section.
(2) You must install a device to monitor pressure drop across the
zeolite wheel or rotary carbon bed. The pressure monitoring device must
meet the requirements in paragraphs (a) and (f)(2)(i) through (vii) of
this section.
(i) Locate the pressure sensor(s) in or as close to a position that
provides a representative measurement of the pressure.
(ii) Minimize or eliminate pulsating pressure, vibration, and
internal and external corrosion.
(iii) Use a gauge with a minimum tolerance of 0.5 inch of water or a
transducer with a minimum tolerance of 1 percent of the pressure range.
(iv) Check the pressure tap daily.
(v) Using a manometer, check gauge calibration quarterly and
transducer calibration monthly.
(vi) Conduct calibration checks anytime the sensor exceeds the
manufacturer's specified maximum operating pressure range or install a
new pressure sensor.
[[Page 310]]
(vii) At least monthly, inspect components for integrity, electrical
connections for continuity, and mechanical connections for leakage.
(g) Emission capture systems. The capture system monitoring system
must comply with the requirements in paragraph (a) of this section and
the applicable requirements in paragraphs (g)(1) and (2) of this
section.
(1) For each flow measurement device, you must meet the requirements
in paragraphs (a) and (g)(1)(i) through (iv) of this section.
(i) Locate a flow sensor in a position that provides a
representative flow measurement in the duct from each capture device in
the emission capture system to the add-on control device.
(ii) Reduce swirling flow or abnormal velocity distributions due to
upstream and downstream disturbances.
(iii) Conduct a flow sensor calibration check at least semiannually.
(iv) At least monthly, inspect components for integrity, electrical
connections for continuity, and mechanical connections for leakage.
(2) For each pressure drop measurement device, you must comply with
the requirements in paragraphs (a) and (g)(2)(i) through (vi) of this
section.
(i) Locate the pressure sensor(s) in or as close to a position that
provides a representative measurement of the pressure drop across each
opening you are monitoring.
(ii) Minimize or eliminate pulsating pressure, vibration, and
internal and external corrosion.
(iii) Check pressure tap pluggage daily.
(iv) Using an inclined manometer with a measurement sensitivity of
0.0002 inch water, check gauge calibration quarterly and transducer
calibration monthly.
(v) Conduct calibration checks any time the sensor exceeds the
manufacturer's specified maximum operating pressure range or install a
new pressure sensor.
(vi) At least monthly, inspect components for integrity, electrical
connections for continuity, and mechanical connections for leakage.
Other Requirements and Information
Sec. 63.4180 Who implements and enforces this subpart?
(a) This subpart can be implemented and enforced by us, the EPA, or
a delegated authority such as your State, local, or tribal agency. If
the EPA Administrator has delegated authority to your State, local, or
tribal agency, then that agency (as well as the EPA) has the authority
to implement and enforce this subpart. You should contact your EPA
Regional Office to find out if implementation and enforcement of this
subpart is delegated to your State, local, or tribal agency.
(b) In delegating implementation and enforcement authority of this
subpart to a State, local, or tribal agency under subpart E of this
part, the authorities contained in paragraph (c) of this section are
retained by the EPA Administrator and are not transferred to the State,
local, or tribal agency.
(c) The authorities that will not be delegated to State, local, or
tribal agencies are listed in paragraphs (c)(1) through (4) of this
section.
(1) Approval of alternatives to the work practice standards in
Sec. 63.4093 under Sec. 63.6(g).
(2) Approval of major alternatives to test methods under
Sec. 63.7(e)(2)(ii) and (f) and as defined in Sec. 63.90.
(3) Approval of major alternatives to monitoring under Sec. 63.8(f)
and as defined in Sec. 63.90.
(4) Approval of major alternatives to recordkeeping and reporting
under Sec. 63.10(f) and as defined in Sec. 63.90.
Sec. 63.4181 What definitions apply to this subpart?
Terms used in this subpart are defined in the CAA, in 40 CFR 63.2,
the General Provisions of this part, and in this section as follows:
Add-on control device means an air pollution control device, such as
a thermal oxidizer or carbon absorber, that reduces pollution in an air
stream by destruction or removal before discharge to the atmosphere.
Adhesive means any chemical substance that is applied for the
purpose of bonding two surfaces together.
Capture device means a hood, enclosure, room, floor sweep, or other
means
[[Page 311]]
of containing or collecting emissions and directing those emissions into
an add-on control device.
Capture efficiency or capture system efficiency means the portion
(expressed as a percentage) of the pollutants from an emission source
that is delivered to an add-on control device.
Capture system means one or more capture devices intended to collect
emissions generated by a coating operation in the use of coatings and
cleaning materials, both at the point of application and at subsequent
points where emissions from the coatings and cleaning materials occur,
such as flashoff, drying, or curing. As used in this subpart, multiple
capture devices that collect emissions generated by a coating operation
are considered a single capture system.
Cleaning material means a solvent used to remove contaminants and
other materials such as dirt, grease, oil, and dried or wet coating
(e.g., depainting) from a substrate before or after coating application
or from equipment associated with a coating operation such as spray
booths, spray guns, racks, tanks, and hangers. Thus, it includes
cleaning materials used for substrates or equipment or both.
Coating means a material applied to a substrate for decorative,
protective, or functional purposes. For the purposes of this subpart,
coatings include paints, porcelain enamels, sealants, caulks, inks,
adhesives, and maskants. Decorative, protective, or functional materials
that consist only of protective oils, acids, bases, or any combination
of these substances are not considered coatings for the purposes of this
subpart.
Coating operation means equipment used to apply cleaning materials
to a substrate to prepare it for coating application or to remove dried
coating (surface preparation), to apply coating to a substrate (coating
application) and to dry or cure the coating after application, or to
clean coating operation equipment (equipment cleaning). A single coating
operation may include any combination of these types of equipment but
always includes at least the point at which a coating or cleaning
material is applied and all subsequent points in the affected source
where organic HAP emissions from that coating or cleaning material
occur. There may be multiple coating operations in an affected source.
Applications of coatings using hand-held, nonrefillable aerosol
containers, touchup markers, or marking pens are not coating operations
for the purposes of this subpart.
Coating solids means the nonvolatile portion of the coating that
makes up the dry film.
Continuous parameter monitoring system means the total equipment
that may be required to meet the data acquisition and availability
requirements of this subpart used to sample, condition (if applicable),
analyze, and provide a record of coating operation, capture system, or
add-on control device parameters.
Controlled coating operation means a coating operation from which
some or all of the organic HAP emissions are routed through an emission
capture system and add-on control device.
Deviation means any instance in which an affected source subject to
this subpart or an owner or operator of such a source:
(1) Fails to meet any requirement or obligation established by this
subpart including but not limited to any emission limit, or operating
limit, or work practice standard;
(2) Fails to meet any term or condition that is adopted to implement
an applicable requirement in this subpart and that is included in the
operating permit for any affected source required to obtain such a
permit; or
(3) Fails to meet any emission limit, or operating limit, or work
practice standard in this subpart during startup, shutdown, or
malfunction regardless of whether or not such failure is permitted by
this subpart.
Emission limitation means an emission limit, operating limit, or
work practice standard.
Enclosure means a structure that surrounds a source of emissions and
captures and directs the emissions to an add-on control device.
Exempt compound means a specific compound that is not considered a
VOC due to negligible photochemical reactivity. The exempt compounds are
listed in 40 CFR 51.100(s).
[[Page 312]]
Facility maintenance means the routine repair or refurbishing
(including surface coating) of the tools, equipment, machinery, and
structures that comprise the infrastructure of the facility or that are
necessary for the facility to function in its intended capacity. It does
not mean cleaning of equipment that is part of a large appliances
coating operation.
Heat transfer coil means a tube-and-fin assembly used in large
appliance products to remove heat from a circulating fluid.
Large appliance part means a component of a large appliance product
except for the wider use parts excluded under Sec. 63.4081(d)(1).
Large appliance product means, but is not limited to, any of the
following products (except as provided under Sec. 63.4081(d)(3))
manufactured for household, recreational, institutional, commercial, or
industrial use:
(1) Cooking equipment (ovens, ranges, and microwave ovens but not
including toasters, counter-top grills, and similar small products);
(2) Refrigerators, freezers, and refrigerated cabinets and cases;
(3) Laundry equipment (washers, dryers, drycleaning machines, and
pressing machines);
(4) Dishwashers, trash compactors, and water heaters; and
(5) HVAC units, air-conditioning (except motor vehicle) units, air-
conditioning and heating combination units, comfort furnaces, and
electric heat pumps.
Specifically excluded are heat transfer coils and large commercial
and industrial chillers.
Large commercial and industrial chillers means, for the purposes of
this subpart, equipment designed to produce chilled water for use in
commercial or industrial HVAC systems.
Manufacturer's formulation data means data on a material (such as a
coating) that are supplied by the material manufacturer based on
knowledge of the ingredients used to manufacture that material, rather
than based on testing of the material with the test methods specified in
Sec. 63.4141. Manufacturer's formulation data may include, but are not
limited to, information on density, organic HAP content, volatile
organic matter content, and coating solids content.
Mass fraction of organic HAP means the ratio of the mass of organic
HAP to the mass of a material in which it is contained, expressed as kg
organic HAP per kg of material.
Month means a calendar month or a pre-specified period of 28 to 35
days to allow for flexibility in recordkeeping when data are based on a
business accounting period.
Organic HAP content means the mass of organic HAP per volume of
coating solids for a coating, calculated using Equation 2 of
Sec. 63.4141. The organic HAP content is determined for the coating in
the condition it is in when received from its manufacturer or supplier
and does not account for any alteration after receipt.
Permanent total enclosure (PTE) means a permanently installed
enclosure that meets the criteria of Method 204 of appendix M, 40 CFR
part 51, for a PTE and that directs all the exhaust gases from the
enclosure to an add-on control device.
Protective oil means an organic material that is applied to a
substrate for the purpose of providing lubrication or protection from
corrosion without forming a solid film. This definition of protective
oils includes, but is not limited to, lubricating oils, evaporative oils
(including those that evaporate completely), and extrusion oils.
Research or laboratory facility means a facility whose primary
purpose is for research and development of new processes and products
conducted under the close supervision of technically trained personnel
and is not engaged in the manufacture of final or intermediate products
for commercial purposes, except in a de minimis manner.
Responsible official means responsible official as defined in 40 CFR
70.2.
Startup, initial means the first time equipment is brought online in
a facility.
Surface preparation means use of a cleaning material on a portion of
or all of a substrate including use of cleaning material to remove dried
coating which is sometimes called ``depainting.''
Temporary total enclosure means an enclosure constructed for the
purpose
[[Page 313]]
of measuring the capture efficiency of pollutants emitted from a given
source as defined in Method 204 of appendix M, 40 CFR part 51.
Thinner means an organic solvent that is added to a coating after
the coating is received from the supplier.
Total volatile hydrocarbon (TVH) means the total amount of
nonaqueous volatile organic matter determined according to Methods 204
and 204A through 204F of appendix M to 40 CFR part 51 and substituting
the term TVH each place in the methods where the term VOC is used. The
TVH includes both VOC and non-VOC.
Uncontrolled coating operation means a coating operation from which
no organic HAP emissions are routed through an emission capture system
and add-on control device.
Volatile organic compound (VOC) means any compound defined as VOC in
40 CFR 51.100(s).
Volume fraction of coating solids means the ratio of the volume of
coating solids (also known as volume of nonvolatiles) to the volume of
coating, expressed as liters of coating solids per liter of coating.
Wastewater means water that is generated in a coating operation and
is collected, stored, or treated prior to being discarded or discharged.
Table 1 to Subpart NNNN of Part 63--Operating Limits if Using the
Emission Rate With Add-On Controls Option
[If you are required to comply with operating limits by Sec. 63.4092,
you must comply with the applicable operating limits in the following
table]
------------------------------------------------------------------------
And you must
demonstrate
You must meet the continuous
For following device . . . following operating compliance with the
limit . . . operating limit by .
. .
------------------------------------------------------------------------
1. thermal oxidizer......... a. the average i. collecting the
combustion combustion
temperature in any temperature data
3-hour period must according to Sec.
not fall below the 63.4168(c);
combustion ii. reducing the
temperature limit data to 3-hour
established block averages; and
according to Sec. iii. maintaining the
63.4167(a). 3-hour average
combustion
temperature at or
above the
combustion
temperature limit.
2. catalytic oxidizer....... a. the average i. collecting the
temperature temperature data
measured just according to Sec.
before the catalyst 63.4168(c);
bed in any 3-hour ii. reducing the
period must not data to 3-hour
fall below the block before the
limit established averages; and
according to Sec. iii. maintaining the
63.4167(b); and 3-hour average
either. temperature before
the catalyst bed at
or above the
temperature limit.
b. ensure that i. collecting the
average temperature temperature data
difference across according to Sec.
the catalyst bed in 63.4168(c);
any 3-hour period ii. reducing the
does not fall below data to 3-hour
the temperature block difference
difference limit across averages;
established and
according to Sec. iii. maintaining the
63.4167(b)(2); or. 3-hour average
temperature
difference at or
above the
temperature
difference limit.
c. develop and i. maintaining an up-
implement an to-date inspection
inspection and and maintenance
maintenance plan plan, records of
according to Sec. annual catalyst
63.4167(b)(4). activity checks,
records monthly
inspections of the
oxidizer system,
and records of the
annual internal
inspections of the
catalyst bed. If a
problem is
discovered during a
monthly or annual
inspection required
by Sec.
63.4167(b)(4), you
must take
corrective action
as soon as
practicable
consistent with the
manufacturer's
recommendations.
3. carbon adsorber.......... a. the total i. measuring the
regeneration total regeneration
desorbing gas desorbing gas
(e.g., steam or (e.g., steam or
nitrogen) mass flow nitrogen) mass flow
for each carbon bed for each
regeneration cycle regeneration cycle
must not fall below according to Sec.
the total 63.4168(d); and
regeneration ii. maintaining the
desorbing gas mass total regeneration
flow limit desorbing gas mass
established flow at or above
according to Sec. the mass flow
63.4167(c). limit.
[[Page 314]]
b. the temperature i. measuring the
of the carbon bed, temperature of the
after completing carbon bed after
each regeneration completing each
and any cooling regeneration and
cycle, must not any cooling cycle
exceed the carbon according to Sec.
bed temperature 63.4168(d); and
limit established ii. operating the
according to Sec. carbon beds such
63.4167(c). that each carbon
bed is not returned
to service until
the recorded
temperature of the
carbon bed is at or
below the
temperature limit.
4. condenser................ a. the average i. collecting the
condenser outlet condenser outlet
(product side) gas (product side) gas
temperature in any temperature
3-hour period must according to Sec.
not exceed the 63.4168(e);
temperature limit ii. reducing the
established data to 3-hour
according to Sec. block averages; and
63.4167(d). iii. maintaining the
3-hour average gas
exceed the
temperature at the
outlet at or below
the temperature
limit.
5. concentrators, including a. the average gas i. collecting the
zeolite wheels and rotary temperature of the temperature data
carbon adsorbers. desorption according to
concentrate stream 63.4168(f);
in any 3-hour ii. reducing the
period must not data to 3-hour
fall below the block averaged; and
limit established iii. maintaining the
according to Sec. 3-hour average
63.4167(e). temperature at or
above the
temperature limit.
b. the average i. collecting the
pressure drop of pressure drop data
the dilute stream according to
across the 63.4168(f); and
concentrator in any ii. reducing the
3-hour period must pressure drop data
not fall below the to across the 3-
limit established hour block
according to Sec. averages; and
63.4167(e). iii. maintaining the
3-hour average
pressure drop at or
above the pressure
drop limit.
6. emission capture system a. the direction of i. collecting the
that is a PTE according to the air flow at all direction of air
Sec. 63.4165(a). times must be into flow, and either
the enclosure; and the facial velocity
either. of air through all
natural draft
openings according
to Sec.
63.4168(g)(1) or
the pressure drop
across the
enclosure according
to Sec.
63.4168(g)(2); and
ii. maintaining the
facial velocity of
air flow through
all natural draft
openings or the
pressure drop at or
above the facial
velocity limit or
pressure drop
limit, and
maintaining the
direction of air
flow into the
enclosure at all
times.
b. the average See item 6.a. of
facial velocity of this table.
air through all
natural draft
openings in the
enclosure must be
at least 200 feet
per minute; or.
c. the pressure drop See item 6.a. of
across the this table.
enclosure must be
at least 0.007 inch
H2O, as established
in Method 204 of
appendix M to 40
CFR part 51.
7. emission capture system a. the average gas i. collecting the
that is not a PTE according volumetric flow gas volumetric flow
to Sec. 63.4165(a). rate or duct static rate or duct static
pressure in each pressure for each
duct between a capture device
capture device and according to Sec.
add-on control 63.4168(g);
device inlet in any ii. reducing the
3-hour period must data to 3-hour
not fall below the block averages; and
average volumetric iii. maintaining the
flow rate or duct 3-hour average gas
static pressure volumetric flow
limit established rate or duct static
for that capture pressure for each
device according to capture device at
Sec. 63.4167(f). or above the gas
volumetric flow
rate or duct static
pressure limit.
------------------------------------------------------------------------
Table 2 to Subpart NNNN of Part 63--Applicability of General Provisions
to Subpart NNNN
[You must comply with the applicable General Provisions requirements according to the following table]
----------------------------------------------------------------------------------------------------------------
Applicable to subpart
Citation Subject NNNN Explanation
----------------------------------------------------------------------------------------------------------------
Sec. 63.1(a)(1)-(14)............... General Applicability.. Yes..................... .......................
Sec. 63.1(b)(1)-(3)................ Initial Applicability Yes..................... Applicability to
Determination. subpart NNNN is also
specified in Sec.
63.4081.
Sec. 63.1(c)(1).................... Applicability After Yes..................... .......................
Standard Established.
Sec. 63.1(c)(2)-(3)................ Applicability of Permit No...................... Area sources are not
Program for Area subject to subpart
Sources. NNNN.
Sec. 63.1(c)(4)-(5)................ Extensions and Yes..................... .......................
Notifications.
[[Page 315]]
Sec. 63.1(e)....................... Applicability of Permit Yes..................... .......................
Program Before
Relevant Standard is
Set.
Sec. 63.2.......................... Definitions............ Yes..................... Additional definitions
are Specified in Sec.
63.4181.
Sec. 63.3(a)-(c)................... Units and Abbreviations Yes..................... .......................
Sec. 63.4(a)(1)-(5)................ Prohibited Activities.. Yes..................... .......................
Sec. 63.4(b)-(c)................... Circumvention/ Yes..................... .......................
Severability.
Sec. 63.5(a)....................... Construction/ Yes..................... .......................
Reconstruction.
Sec. 63.5(b)(1)-(6)................ Requirements for Yes..................... .......................
Existing, Newly
Constructed, and
Reconstructed Sources.
Sec. 63.5(d)....................... Application for Yes..................... .......................
Approval of
Construction/
Reconstruction.
Sec. 63.5(e)....................... Approval of Yes..................... .......................
Construction/
Reconstruction.
Sec. 63.5(f)....................... Approval of Yes..................... .......................
Construction/
Reconstruction Based
on Prior State Review.
Sec. 63.6(a)....................... Compliance With Yes..................... .......................
Standards and
Maintenance
Requirements--
Applicability.
Sec. 63.6(b)(1)-(7)................ Compliance Dates for Yes..................... Section 63.4083
New and Reconstructed specifies the
Sources. compliance dates.
Sec. 63.6(c)(1)-(5)................ Compliance Dates for Yes..................... Section 63.4083
Existing Sources. specifies the
compliance dates.
Sec. 63.6(e)(1)-(2)................ Operation and Yes..................... .......................
Maintenance.
Sec. 63.6(e)(3).................... SSMP................... Yes..................... Only sources using an
add--on control device
to comply with the
standard must complete
SSMP.
Sec. 63.6(f)(1).................... Compliance Except Yes..................... Applies only to sources
During Startup, using an and add--on
Shutdown, and control device to
Malfunction. comply with the
standards.
Sec. 63.6(f)(2)-(3)................ Methods for Determining Yes..................... .......................
Compliance.
Sec. 63.6(g)(1)-(3)................ Use of an Alternative Yes..................... .......................
Standard.
Sec. 63.6(h)....................... Compliance With Opacity/ No...................... Subpart NNNN does not
Visible Emission establish opacity
standards. standards and does not
require continuous
opacity monitoring
systems (COMS).
Sec. 63.6(i)(1)-(16)............... Extension of Compliance Yes..................... .......................
Sec. 63.6(j)....................... Presidential Compliance Yes..................... .......................
Exemption.
Sec. 63.7(a)(1).................... Performance Test Yes..................... Applies to all affected
Requirements-- sources. Additional
Applicability. requirements for
performance testing
are specified in Secs.
63.4164, 63.4165, and
63.4166.
Sec. 63.7(a)(2).................... Performance Test Yes..................... Applies only to
Requirements--Dates. performance tests for
caputre system and
control device
efficiency at sources
using these to comply
with the standards.
Section 63.4160
specifies the schedule
for performance test
requirements that are
earlier than those
specified in Sec.
63.7(a)(2).
Sec. 63.7(a)(3).................... Performance Tests Yes..................... .......................
Required By the
Administrator.
Sec. 63.7(b)-(e)................... Performance Test Yes..................... Applies only to
Requirements-- performance tests for
Notification, Quality capture system and add-
Assurance Facilities on control device
Necessary for Safe efficiency at sources
Testing, Conditions using these to comply
During Test. with the standard.
Sec. 63.7(f)....................... Performance Test Yes..................... Applies to all test
Requirements--Use of methods except those
Alternative Test used to determine
Method. capture system
efficiency.
[[Page 316]]
Sec. 63.7(g)-(h)................... Performance Test Yes..................... Applies only to
Requirements--Data performance tests for
Analysis, capture system and add-
Recordkeeping, on control device
Reporting, Waiver of efficiency at sources
Test. using these to comply
with the standard.
Sec. 63.8(a)(1)-(3)................ Monitoring Requirements- Yes..................... Applies only to
-Applicability. monitoring of capture
system and add-on
control device
efficiency at sources
using these to comply
with the standard.
Additional
requirements for
monitoring are
specified in Sec.
63.4168.
Sec. 63.8(a)(4).................... Additional Monitoring No...................... Subpart NNNN does not
Requirements. have monitoring
requirements for
flares.
Sec. 63.8(b)....................... Conduct of Monitoring.. Yes..................... .......................
Sec. 63.8(c)(1)-(3)................ Continuous Monitoring Yes..................... Applies only to
Systems (CMS) monitoring of capture
Operation and system and add-on
Maintenance. control device
efficiency at sources
using these to comply
with the standard.
Additional
requirements for CMS
operations and
maintenance are
specified in Sec.
63.4168.
Sec. 63.8(c)(4).................... CMS.................... No...................... Section 63.4168
specifies the
requirements for the
operation of CMS for
capture systems and
add-on control devices
at sources using these
to comply.
Sec. 63.8(c)(5).................... COMS................... No...................... Subpart NNNN does not
have opacity or
visible emission
standards.
Sec. 63.8(c)(6).................... CMS Requirements....... No...................... Section 63.4168
specifies the
requirements for
monitoring systems for
capture systems and
add-on control devices
at sources using these
to comply.
Sec. 63.8(c)(7).................... CMS Out-of-Control Yes..................... .......................
Periods.
Sec. 63.8(c)(8).................... CMS Out-of-Control No...................... Section 63.4120
Periods and Reporting. requires reporting of
CMS out-of-control
periods.
Sec. 63.8(d)-(e)................... Quality Control Program No...................... Subpart NNNN does not
and CMS Performance require the use of
Evaluation. continuous emissions
monitoring systems.
Sec. 63.8(f)(1)-(5)................ Use of an Alternative Yes..................... .......................
Monitoring Method.
Sec. 63.8(f)(6).................... Alternative to Relative No...................... Subpart NNNN does not
Accuracy Test. require the use of
continuous emissions
monitoring systems.
Sec. 63.8(g)(1)-(5)................ Data Reduction......... No...................... Sections 63.4167 and
63.4168 specify
monitoring data
reduction.
Sec. 63.9(a)-(d)................... Notification Yes..................... .......................
Requirements.
Sec. 63.9(e)....................... Notification of Yes..................... Applies only to capture
Performance Test. system and add-on
control device
performance tests at
sources using these to
comply with the
standard.
Sec. 63.9(f)....................... Notification of Visible No...................... Subpart NNNN does not
Emissions/Opacity Test. have opacity or
visible emission
standards.
Sec. 63.9(g)(1)-(3)................ Additional No...................... Subpart NNNN does not
Notifications When require the use of
Using CMS. continuous emissions
monitoring systems.
Sec. 63.9(h)....................... Notification of Yes..................... Section 63.4110
Compliance Status. specifies the dates
for submitting the
notification of
compliance status.
Sec. 63.9(i)....................... Adjustment of Submittal Yes..................... .......................
Deadlines.
Sec. 63.9(j)....................... Change in Previous Yes..................... .......................
Information.
[[Page 317]]
Sec. 63.10(a)...................... Recordkeeping/Reporting- Yes..................... .......................
-Applicability and
General Information.
Sec. 63.10(b)(1)................... General Recordkeeping Yes..................... Additional requirements
Requirements. are specified in Secs.
63.4130 and 63.4131.
Sec. 63.10(b)(2)(i)-(v)............ Recordkeeping Relevant Yes..................... Requirements for
to Startup, Shutdown, startup, shutdown, and
and Malfunction malfunction records
Periods and CMS. only apply to add-on
control devices used
to comply with the
standard.
Sec. 63.10(b)(2)(vi)-(xi).......... ....................... Yes..................... .......................
Sec. 63.10(b)(2)(xii).............. Records................ Yes..................... .......................
Sec. 63.10(b)(2)(xiii)............. ....................... No...................... Subpart NNNN does not
require the use of
continuous emissions
monitoring systems.
Sec. 63.10(b)(2)(xiv).............. ....................... Yes..................... .......................
Sec. 63.10(b)(3)................... Recordkeeping Yes.....................
Requirements for
Applicability
Determinations.
Sec. 63.10(c)(1)-(6)............... Additional Yes..................... .......................
Recordkeeping
Requirements for
Sources with CMS.
Sec. 63.10(c)(7)-(8)............... ....................... No...................... The same records are
required in Sec.
63.4120(a)(7).
Sec. 63.10(c)(9)-(15).............. ....................... Yes..................... .......................
Sec. 63.10(d)(1)................... General Reporting Yes..................... Additional requirements
Requirements. are specified in Sec.
63.4120.
Sec. 63.10(d)(2)................... Report of Performance Yes..................... Additional requirements
Test Results. are specified in Sec.
63.4120(b).
Sec. 63.10(d)(3)................... Reporting Opacity or No...................... Subpart NNNN does not
Visible Emissions require opacity or
Observations. visible emissions
observations.
Sec. 63.10(d)(4)................... Progress Reports for Yes..................... .......................
Sources With
Compliance Extensions.
Sec. 63.10(d)(5)................... Startup, Shutdown, and Yes..................... Applies only to add-on
Malfunction Reports. control devices at
sources using these to
comply with the
standard.
Sec. 63.10(e)(1)-(2)............... Additional CMS Reports. No...................... Subpart NNNN does not
require the use of
continuous emissions
monitoring systems.
Sec. 63.10(e)(3)................... Excess Emissions/CMS No...................... Section 63.4120(b)
Performance Reports. specifies the contents
of periodic compliance
reports.
Sec. 63.10(e)(4)................... COMS Data Reports...... No...................... Subpart NNNN does not
specify requirements
for opacity or COMS.
Sec. 63.10(f)...................... Recordkeeping/Reporting Yes..................... .......................
Waiver.
Sec. 63.11......................... Control Device No...................... Subpart NNNN does not
Requirements/Flares. specify use of flares
for compliance.
Sec. 63.12......................... State Authority and Yes..................... .......................
Delegations.
Sec. 63.13......................... Addresses.............. Yes..................... .......................
Sec. 63.14......................... Incorporation by Yes..................... .......................
Reference.
Sec. 63.15......................... Availability of Yes..................... .......................
Information/
Confidentiality.
----------------------------------------------------------------------------------------------------------------
Table 3 to Subpart NNNN of Part 63--Default Organic HAP Mass Fraction
for Solvents and Solvent Blends
[You may use the mass fraction values in the following table for solvent blends for which you do not have test
data or manufacturer's formulation data.]
----------------------------------------------------------------------------------------------------------------
Average
Solvent/solvent blend CAS. No. organic HAP Typical organic HAP, percent by
mass fraction mass
----------------------------------------------------------------------------------------------------------------
1. Toluene.................................... 108-88-3 1.0 Toluene.
2. Xylene(s).................................. 1330-20-7 1.0 Xylenes, ethylbenzene.
3. Hexane..................................... 110-54-3 0.5 n-hexane.
4. n-Hexane................................... 110-54-3 1.0 n-hexane.
5. Ethylbenzene............................... 100-41-4 1.0 Ethylbenzene.
6. Aliphatic 140.............................. .............. 0 None.
7. Aromatic 100............................... .............. 0.02 1% xylene, 1% cumene.
8. Aromatic 150............................... .............. 0.09 Naphthalene.
9. Aromatic naphtha........................... 64742-95-6 0.02 1% xylene, 1% cumene.
[[Page 318]]
10. Aromatic solvent.......................... 64742-94-5 0.1 Naphthalene.
11. Exempt mineral spirits.................... 8032-32-4 0 None.
12. Ligroines (VM & P)........................ 8032-32-4 0 None.
13. Lactol spirits............................ 64742-89-6 0.15 Toluene.
14. Low aromatic white spirit................. 64742-82-1 0 None.
15. Mineral spirits........................... 64742-88-7 0.01 Xylenes.
16. Hydrotreated naphtha...................... 64742-48-9 0 None.
17. Hydrotreated light distillate............. 64742-47-8 0.001 Toluene.
18. Stoddard solvent.......................... 8052-41-3 0.01 Xylenes.
19. Super high-flash naphtha.................. 64742-95-6 0.05 Xylenes.
20. Varsol[reg] solvent....................... 8052-49-3 0.01 0.5% xylenes, 0.5% ethylbenzene.
21. VM & P naphtha............................ 64742-89-8 0.06 3% toluene, 3% xylene.
22. Petroleum distillate mixture.............. 68477-31-6 0.08 4% naphthalene, 4% biphenyl.
----------------------------------------------------------------------------------------------------------------
Table 4 to Subpart NNNN of Part 63--Default Organic HAP Mass Fraction
for Petroleum Solvent Groups a
[You may use the mass fraction values in the following table for solvent
blends for which you do not have test data or manufacturer's formulation
data.]
------------------------------------------------------------------------
Average
Solvent type organic HAP Typical organic HAP,
mass fraction percent by mass
------------------------------------------------------------------------
Aliphatic \b\..................... 0.03 1% Xylene, 1%
Toluene, and 1%
Ethylbenzene.
Aromatic \c\...................... 0.06 4% Xylene, 1%
Toluene, and 1%
Ethylbenzene.
------------------------------------------------------------------------
\a\ Use this table only if the solvent blend does not match any of the
solvent blends in Table 3 to this subpart and you only know whether
the blend is aliphatic or aromatic.
\b\ e.g., Mineral Spirits 135, Mineral Spirits 150 EC, Naphtha, Mixed
Hydrocarbon, Aliphatic Hydrocarbon, Aliphatic Naphtha, Naphthol
Spirits, Petroleum Spirits, Petroleum Oil, Petroleum Naphtha, Solvent
Naphtha, Solvent Blend.
\c\ e.g., Medium-flash Naphtha, High-flash Naphtha, Aromatic Naphtha,
Light Aromatic Naphtha, Light Aromatic Hydrocarbons, Aromatic
Hydrocarbons, Light Aromatic Solvent.
Subpart OOOO--National Emission Standards for Hazardous Air Pollutants:
Printing, Coating, and Dyeing of Fabrics and Other Textiles
Source: 68 FR 32189, May 29, 2003, unless otherwise noted.
What This Subpart Covers
Sec. 63.4280 What is the purpose of this subpart?
This subpart establishes national emission standards for hazardous
air pollutants (NESHAP) for fabric and other textiles printing, coating
and dyeing operations. This subpart also establishes requirements to
demonstrate initial and continuous compliance with the emission
limitations.
Sec. 63.4281 Am I subject to this subpart?
(a) Except as provided in paragraphs (c) and (d) of this section,
the source category to which this subpart applies is the printing,
coating, slashing, dyeing or finishing of fabric and other textiles, and
it includes the subcategories listed in paragraphs (a)(1) through (3) of
this section.
(1) The coating and printing subcategory includes any operation that
coats or prints fabric or other textiles. Coating and printing
operations are defined in Sec. 63.4371. Coated and printed substrates
are used in products including, but not limited to, architectural
structures, apparel, flexible hoses, hot-air balloons, lightweight
liners, luggage, military fabric, rainwear, sheets, tents, threads and
V-belts. The coating and printing subcategory includes any fabric or
other textile web coating line that also performs coating on another
substrate unless such coating is specifically excluded from this subpart
by another NESHAP in this part or is exempted from the requirements of
this subpart based on the criteria in paragraph (e) of this section. Web
coating lines exclusively dedicated to coating
[[Page 319]]
or printing fabric and other textiles are subject to this subpart.
(2) The slashing subcategory includes any operation with slashing
operations as defined in Sec. 63.4371. In the slashing process, sizing
compounds are applied to warp yarn to bind the fiber together and
stiffen the yarn to provide abrasion resistance during weaving.
(3) The dyeing and finishing subcategory includes any operation that
dyes or finishes a fabric or other textiles. Dyeing and finishing
operations are defined in Sec. 63.4371. Dyed and finished textiles are
used in a wide range of products including, but not limited to, apparel,
carpets, high-performance industrial fabrics, luggage, military fabrics,
outer wear, sheets, towels, and threads.
(b) You are subject to this subpart if you own or operate a new,
reconstructed, or existing affected source, as defined in Sec. 63.4282,
that is a major source, is located at a major source, or is part of a
major source of hazardous air pollutants (HAP). Major source is defined
in Sec. 63.2 of this part.
(c) This subpart does not apply to coating, printing, slashing,
dyeing, or finishing operations that meet any of the criteria of
paragraphs (c)(1) through (5) of this section.
(1) Coating and printing, slashing, or dyeing and finishing
operations conducted at a source that uses only regulated materials that
contain no organic HAP as defined in Sec. 63.4371.
(2) Coating, printing, slashing, dyeing, or finishing that occurs at
research or laboratory operations or that is part of janitorial,
building, and facility maintenance operations.
(3) Coating, printing, slashing, dyeing, or finishing operations
used by a facility and not for commerce, unless organic HAP emissions
from the coating, printing, slashing, dyeing or finishing operations are
as high as the major source HAP emissions specified in paragraph (b) of
this section.
(4) Fabric and other textile substrate web coating or printing
operations conducted at ambient temperatures that do not involve drying
or curing equipment such as ovens, tenter frames, steam cans, or dryers.
(5) Coating, printing, slashing, dyeing, or finishing operations
performed on-site at installations owned or operated by the Armed Forces
of the United States (including the Coast Guard and the National Guard
of any State).
(d) Web coating lines specified in paragraphs (d)(1) through (3) of
this section are not part of the affected source of this subpart.
(1) Any web coating operation that is part of the affected source of
subpart JJJJ of this part (national emission standards for hazardous air
pollutants for paper and other web coating). This would include any web
coating line that coats both a paper and other web substrate and a
fabric or other textile substrate for use in flexible packaging,
pressure sensitive tape and abrasive materials, or any web coating line
laminating a fabric substrate to paper.
(2) Any web coating operation that is part of the affected source of
subpart XXXX of this part (NESHAP for tire manufacturing). This would
include any web coating line that applies coatings to both tire cord and
to textile cord used in the production of belts and hoses.
(3) Coating, slashing, dyeing, or finishing operations at a
synthetic fiber manufacturing facility included in the affected source
of another subpart of this part, such as subpart F (NESHAP for the
synthetic organic chemical manufacturing industry) or subpart JJJ
(NESHAP for group IV polymers and resins).
(e) Any web coating line that coats both fabric and other textiles,
and another substrate such as paper, must comply with the subpart of
this part that applies to the predominant activity conducted on the
affected source. Predominant activity for this subpart is 90 percent of
the mass of substrate coated during the compliance period. (For example,
a web coating line that coats 90 percent or more of a paper substrate,
and 10 percent or less of a fabric or other textile substrate, would be
subject to 40 CFR 63, subpart JJJJ.)
Sec. 63.4282 What parts of my plant does this subpart cover?
(a) This subpart applies to each new, reconstructed, and existing
affected source within each of the three subcategories listed in
Sec. 63.4281(a).
[[Page 320]]
(b) The affected source for the web coating and printing subcategory
is the collection of all of the items listed in paragraphs (b)(1)
through (5) of this section that are used in fabric and other textiles
web coating and printing operations. The regulated materials for the web
coating and printing subcategory are the coating, printing, thinning and
cleaning materials used in the affected source.
(1) All web coating and printing equipment used to apply cleaning
materials to a substrate on the coating or printing line to prepare it
for coating or printing material application, to apply coating or
printing materials to a substrate and to dry or cure the coating or
printing materials, or equipment used to clean web coating/printing
operation equipment;
(2) All containers used for storage and vessels used for mixing
coating, printing, thinning, or cleaning materials;
(3) All equipment and containers used for conveying coating,
printing, thinning, or cleaning materials;
(4) All containers used for storage, and all equipment and
containers used for conveying waste materials generated by a coating or
printing operation; and
(5) All equipment, structures, and/or devices(s) used to convey,
treat, or dispose of wastewater streams or residuals generated by a
coating or printing operation.
(c) The affected source for the slashing subcategory is the
collection of all of the items listed in paragraphs (c)(1) through (5)
of this section that are used in slashing operations. The regulated
materials for the slashing subcategory are the slashing materials used
in the affected source.
(1) All slashing equipment used to apply and dry size on warp yarn;
(2) All containers used for storage and vessels used for mixing
slashing materials;
(3) All equipment and containers used for conveying slashing
materials;
(4) All containers used for storage and all equipment and containers
used for conveying waste materials generated by a slashing operation;
and
(5) All equipment, structures, and/or devices(s) used to convey,
treat, or dispose of wastewater streams or residuals generated by a
slashing operation.
(d) The affected source for the dyeing and finishing subcategory is
the collection of all of the items listed in paragraphs (d)(1) through
(5) of this section that are used in dyeing and finishing operations.
The regulated materials for the dyeing and finishing subcategory are the
dyeing and finishing materials used in the affected source.
(1) All dyeing and finishing equipment used to apply dyeing or
finishing materials, to fix dyeing materials to the substrate, to rinse
the textile substrate, or to dry or cure the dyeing or finishing
materials;
(2) All containers used for storage and vessels used for mixing
dyeing or finishing materials;
(3) All equipment and containers used for conveying dyeing or
finishing materials;
(4) All containers used for storage, and all equipment and
containers used for conveying, waste materials generated by a dyeing or
finishing operation; and
(5) All equipment, structures, and/or devices(s) used to convey,
treat, or dispose of wastewater streams or residuals generated by a
dyeing or finishing operation.
(e) An affected source is a new source if it meets the criteria in
paragraph (e)(1) of this section and the criteria in either paragraph
(e)(2) or (3) of this section.
(1) You commenced the construction of the source after July 11,
2002.
(2) The web coating and printing, slashing, or dyeing and finishing
operation is performed at a source where no web coating and printing,
slashing, or dyeing and finishing operation was previously performed.
(3) The web coating and printing, slashing, or dyeing and finishing
operation is performed in a subcategory in which no web coating and
printing, slashing, or dyeing and finishing operation was previously
performed.
(f) An affected source is reconstructed if you meet the criteria as
defined in Sec. 63.2.
(g) An affected source is existing if it is not new or
reconstructed.
[[Page 321]]
Sec. 63.4283 When do I have to comply with this subpart?
The date by which you must comply with this subpart is called the
compliance date. The compliance date for each type of affected source is
specified in paragraphs (a) through (c) of this section. The compliance
date begins the initial compliance period during which you conduct the
initial compliance demonstration described in Secs. 63.4320, 63.4330,
63.4340, and 63.4350.
(a) For a new or reconstructed affected source, the compliance date
is the applicable date in paragraph (a)(1) or (2) of this section:
(1) If the initial startup of your new or reconstructed affected
source is before May 29, 2003, the compliance date is May 29, 2003.
(2) If the initial startup of your new or reconstructed affected
source occurs after May 29, 2003, the compliance date is the date of
initial startup of your affected source.
(b) For an existing affected source, the compliance date is the date
3 years after May 29, 2003.
(c) For an area source that increases its emissions or its potential
to emit such that it becomes a major source of HAP emissions, the
compliance date is specified in paragraphs (c)(1) and (2) of this
section.
(1) For any portion of the source that becomes a new or
reconstructed affected source subject to this subpart, the compliance
date is the date of initial startup of the affected source or May 29,
2003, whichever is later.
(2) For any portion of the source that becomes an existing affected
source subject to this subpart, the compliance date is the date 1 year
after the area source becomes a major source or 3 years after May 29,
2003, whichever is later.
(d) You must meet the notification requirements in Sec. 63.4310
according to the dates specified in that section and in subpart A of
this part. Some of the notifications must be submitted before the
compliance dates described in paragraphs (a) through (c) of this
section.
Emission Limitations
Sec. 63.4290 What emission limits must I meet?
You must meet the emission limit for the subcategory or
subcategories present in your facility. The three subcategories are: Web
coating and printing, slashing, and dyeing and finishing. Table 1 to
this subpart presents the emission limits for a new or reconstructed
affected source and for an existing affected source in each subcategory.