[Federal Register Volume 80, Number 3 (Tuesday, January 6, 2015)]
[Rules and Regulations]
[Pages 792-815]
From the Federal Register Online via the Government Publishing Office [www.gpo.gov]
[FR Doc No: 2014-30748]
[[Page 791]]
Vol. 80
Tuesday,
No. 3
January 6, 2015
Part V
Department of Energy
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48 CFR Part 430
Energy Conservation Program for Consumer Products: Test Procedures for
Direct Heating Equipment and Pool Heaters; Final Rule
Federal Register / Vol. 80 , No. 3 / Tuesday, January 6, 2015 / Rules
and Regulations
[[Page 792]]
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DEPARTMENT OF ENERGY
10 CFR Part 430
[Docket Number EERE-2013-BT-TP-0004]
RIN 1904-AC94
Energy Conservation Program for Consumer Products: Test
Procedures for Direct Heating Equipment and Pool Heaters
AGENCY: Office of Energy Efficiency and Renewable Energy, Department of
Energy.
ACTION: Final rule.
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SUMMARY: The U.S. Department of Energy (DOE) is amending its test
procedures for vented home heating equipment and pool heaters
established under the Energy Policy and Conservation Act. This
rulemaking fulfills DOE's statutory obligation to review its test
procedures for covered products at least once every seven years. The
amendments add provisions for testing vented home heating equipment
that utilizes condensing technology, and incorporate by reference six
industry test standards to replace the outdated test standards referred
to in the existing DOE test procedure. For pool heaters, the amendments
incorporate by reference Air-Conditioning, Heating, and Refrigeration
Institute (AHRI) Standard 1160-2009, ``Performance Rating of Heat Pump
Pool Heaters,'' and ANSI/American Society of Heating, Refrigerating,
and Air-Conditioning Engineers (ASHRAE) Standard 146-2011, ``Method of
Testing and Rating Pool Heaters,'' to establish a test method for
electric pool heaters (including heat pump pool heaters). The
amendments also clarify the test procedure's applicability to oil-fired
pool heaters.
DATES: The effective date of this rule is February 5, 2015. Compliance
will be mandatory starting July 6, 2015.
The incorporation by reference of certain publications listed in
this rule is approved by the Director of the Federal Register as of
February 5, 2015. Other publications referenced were approved on
January 3, 2014.
ADDRESSES: The docket is available for review at www.regulations.gov,
including Federal Register notices, public meeting attendee lists and
transcripts, comments, and other supporting documents/materials. All
documents in the docket are listed in the www.regulations.gov index.
However, not all documents listed in the index may be publicly
available, such as information that is exempt from public disclosure.
A link to the docket Web page can be found at: http://www.regulations.gov/#!docketDetail;D=EERE-2013-BT-TP-0004. This Web
page contains a link to the docket for this rule on the
www.regulations.gov site. The www.regulations.gov Web page contains
simple instructions on how to access all documents, including public
comments, in the docket.
For information on how to review the docket, contact Ms. Brenda
Edwards at (202) 586-2945 or by email: [email protected].
FOR FURTHER INFORMATION CONTACT: Mr. John Cymbalsky, U.S. Department of
Energy, Office of Energy Efficiency and Renewable Energy, Building
Technologies Program, EE-2J, 1000 Independence Avenue SW., Washington,
DC 20585-0121. Telephone: (202) 287-1692. Email:
[email protected].
Ms. Sarah Butler, U.S. Department of Energy, Office of the General
Counsel, GC-71, 1000 Independence Avenue SW., Washington, DC 20585-
0121. Telephone: (202) 586-1777. Email: [email protected].
SUPPLEMENTARY INFORMATION: This final rule incorporates by reference
into subpart B of 10 CFR part 430, the following industry standards:
AHRI Standard 1160-2009 (``AHRI 1160''), Performance Rating of Heat
Pump Pool Heaters, 2009.
Copies of AHRI 1160 can be obtained from the Air-Conditioning,
Heating, 2111 Wilson Blvd., Suite 500, Arlington, VA 22201, 703-524-
8800, or go to http://www.ahrinet.org.
ANSI Z21.86-2008, (``ANSI Z21.86''), Vented Gas-Fired Space Heating
Appliances, Fifth Edition.
Copies of ANSI Z21.86 can be obtained from American National
Standards Institute, 25 W. 43rd Street, 4th Floor, New York, NY
10036, 212-642-4900, or go to http://www.ansi.org.
ANSI/ASHRAE Standard 103-2007, (``ASHRAE 103-2007''), Method of
Testing for Annual Fuel Utilization Efficiency of Residential
Central Furnaces and Boilers, ANSI approved March 25, 2008.
Copies of ASHRAE 103-2007 can be obtained from American Society of
Heating, Refrigerating and Air-Conditioning Engineers, Inc.,
Publication Sales, 1791 Tullie Circle, NE., Atlanta, GA 30329, 800-
527-4723 or 404-636-8400, or go to http://www.ashrae.org.
ANSI/ASHRAE Standard 146-2011 (``ASHRAE 146''), Method of Testing
and Rating Pool Heaters, ASHRAE approved February 2, 2011.
Copies of ASHRAE 146 can be obtained from American Society of
Heating, Refrigerating and Air-Conditioning Engineers, Inc.,
Publication Sales, 1791 Tullie Circle, NE., Atlanta, GA 30329, 800-
527-4723 or 404-636-8400, or go to http://www.ashrae.org.
ASTM D2156-09, (``ASTM D2156''), Standard Test Method for Smoke
Density in Flue Gases from Burning Distillate Fuels, ASTM approved
December 1, 2009.
Copies of ASTM D2156 can be obtained from American Society for
Testing and Materials International, 100 Barr Harbor Drive, P.O. Box
C700, West Conshohocken, PA 19428-2959, or go to http://www.astm.org.
UL 729-2003 (``UL 729''), Standard for Safety for Oil-Fired
Floor Furnaces, Sixth Edition, dated August 29, 2003, including
revisions through April 22, 2010.
Copies of UL 729 can be obtained from Underwriters Laboratories,
Inc., 2600 NW. Lake Rd., Camas WA 98607-8542, or go to http://www.UL.com.
UL 730-2003 (``UL 730''), Standard for Safety for Oil-Fired Wall
Furnaces, Fifth Edition, dated August 29, 2003, including revisions
through April 22, 2010.
Copies of UL 730 can be obtained from Underwriters Laboratories,
Inc., 2600 NW. Lake Rd., Camas WA 98607-8542, or go to http://www.UL.com.
UL 896-1993 (``UL 896''), Standard for Safety for Oil-Burning
Stoves, Fifth Edition, dated July 29, 1993, including revisions
through May 7, 2010.
Copies of UL 896 can be obtained from Underwriters Laboratories,
Inc., 2600 NW. Lake Rd., Camas WA 98607-8542, or go to http://www.UL.com.
Table of Contents
I. Authority and Background
II. Synopsis of the Final Rule
III. Discussion
A. Products Covered by This Final Rule
B. Dates for the Amended Test Procedure
C. Test Procedure for Direct Heating Equipment
1. Vented Home Heating Equipment Employing Condensing Technology
2. Updating of Industry Reference Standards
3. Other Issues
D. Test Procedure for Pool Heaters
1. Electric Pool Heaters
2. Other Issues
E. Compliance With Other EPCA Requirements
IV. Procedural Issues and Regulatory Review
A. Review Under Executive Order 12866
B. Review Under the Regulatory Flexibility Act
C. Review Under the Paperwork Reduction Act of 1995
D. Review Under the National Environmental Policy Act of 1969
E. Review Under Executive Order 13132
F. Review Under Executive Order 12988
G. Review Under the Unfunded Mandates Reform Act of 1995
H. Review Under the Treasury and General Government
Appropriations Act, 1999
I. Review Under Executive Order 12630
J. Review Under Treasury and General Government Appropriations
Act, 2001
K. Review Under Executive Order 13211
L. Review Under Section 32 of the Federal Energy Administration
Act of 1974
M. Congressional Notification
V. Approval of the Office of the Secretary
[[Page 793]]
I. Authority and Background
Title III, Part B \1\ of the Energy Policy and Conservation Act of
1975 (``EPCA'' or ``the Act''), Public Law 94-163 (codified at 42
U.S.C. 6291-6309) sets forth a variety of provisions designed to
improve energy efficiency and establishes the Energy Conservation
Program for Consumer Products Other Than Automobiles.\2\ These include
two covered products that are the subject of this rule: direct heating
equipment (DHE) and pool heaters. (42 U.S.C. 6292(a)(9) and (11))
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\1\ For editorial reasons, upon codification in the U.S. Code,
Part B was redesignated as Part A.
\2\ All references to EPCA in this document refer to the statute
as amended through the American Energy Manufacturing Technical
Corrections Act (AEMTCA), Pub. L. 112-210 (Dec. 18, 2012).
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Under EPCA, the energy conservation program generally consists of
four parts: (1) Testing; (2) labeling; (3) establishing Federal energy
conservation standards; and (4) certification and enforcement
procedures. The testing requirements consist of test procedures that
manufacturers of covered products must use as the basis for making
representations about the efficiency of those products, including
representations to DOE of compliance with applicable energy
conservation standards adopted pursuant to EPCA. (42 U.S.C. 6293(c); 42
U.S.C. 6295(s)) Similarly, DOE must use these test requirements to
determine whether the products comply with any relevant standards
promulgated under EPCA. (42 U.S.C. 6295(s))
Under 42 U.S.C. 6293, EPCA sets forth the criteria and procedures
that DOE must follow when prescribing or amending test procedures for
covered products. EPCA provides, in relevant part, that any test
procedures prescribed or amended under this section must be reasonably
designed to produce test results which measure energy efficiency,
energy use, or estimated annual operating cost of a covered product
during a representative average use cycle or period of use, and must
not be unduly burdensome to conduct. (42 U.S.C. 6293(b)(3))
In addition, if DOE determines that a test procedure amendment is
warranted, it must publish proposed test procedures and offer the
public an opportunity to present oral and written comments on them. (42
U.S.C. 6293(b)(2)) Finally, in any rulemaking to amend a test
procedure, DOE must determine to what extent, if any, the proposed test
procedure would alter the product's measured energy efficiency. (42
U.S.C. 6293(e)(1))
Further, the Energy Independence and Security Act of 2007 (EISA
2007) amended EPCA to require that at least once every seven years, DOE
must review test procedures for all covered products and either amend
test procedures (if the Secretary determines that amended test
procedures would more accurately or fully comply with the requirements
of 42 U.S.C. 6293(b)(3)), or publish notice in the Federal Register of
any determination not to amend a test procedure. (42 U.S.C.
6293(b)(1)(A)) Under this requirement, DOE must review the test
procedures for direct heating equipment and pool heaters not later than
December 19, 2014 (i.e., seven years after the enactment of EISA 2007).
This final rule satisfies this requirement.
This rulemaking covers two types of direct heating equipment:
vented home heating equipment and unvented home heating equipment. For
vented home heating equipment, the test procedure is located at 10 CFR
430.23(o) and 10 CFR part 430, subpart B, appendix O (Appendix O). The
vented home heating equipment test procedure includes provisions for
determining energy efficiency (annual fuel utilization efficiency
(AFUE)), as well as annual energy consumption. DOE's test procedures
for unvented home heating equipment are located at 10 CFR 430.23(g) and
10 CFR 430, subpart B, appendix G (Appendix G). For unvented heaters
that are used as the primary heating source for the home, there is a
calculation of annual energy consumption based on a single assignment
of active mode hours; there is no provision for calculation of energy
efficiency. For unvented heaters that are not used as the primary
heating source for the home, there are no provisions for calculating
either the energy efficiency or annual energy consumption.
DOE's test procedure for pool heaters is found at 10 CFR 430.23(p)
and 10 CFR part 430, subpart B, appendix P (Appendix P). The test
procedure includes provisions for determining two energy efficiency
descriptors (i.e., thermal efficiency and integrated thermal
efficiency), as well as annual energy consumption.
In addition to the test procedure review provision discussed above,
EISA 2007 also amended EPCA to require DOE to amend its test procedures
for all covered products to include measurement of standby mode and off
mode energy consumption. (42 U.S.C. 6295(gg)(2)(A)) DOE published a
final rule adopting standby mode and off mode provisions for heating
products in the Federal Register on December 17, 2012. 77 FR 74559.
That rulemaking was limited to test procedure amendments to address
standby mode and off mode requirements; it did not address non-standby/
off mode issues in DOE's existing test procedures for the covered
products. DOE addresses those issues separately in this final rule.
On October 12, 2011, DOE published in the Federal Register a
request for information (RFI) that identified and requested comment on
a number of issues regarding the test procedures for DHE (including
both vented and unvented home heating equipment) and pool heaters
(October 2011 RFI).\3\ 76 FR 63211. DOE accepted comments and
information on the October 2011 RFI until November 28, 2011, and
considered all feedback received.
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\3\ The October 2011 RFI also requested information on the need
to amend the test procedures for residential water heaters. However,
because the American Energy Manufacturing and Technical Corrections
Act amended EPCA to require that DOE develop a uniform efficiency
descriptor for residential and commercial water heaters (42 U.S.C.
6295(e)(5)), DOE is addressing test procedure updates for that
product in a separate rulemaking.
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On October 24, 2013, DOE published a notice of proposed rulemaking
(NOPR) to propose amendments for its test procedures for vented home
heating equipment and pool heaters (October 2013 NOPR). 78 FR 63410. In
the October 2013 NOPR, DOE proposed amending the test procedure to
include provisions for condensing technology in vented home heating
equipment, updating outdated references, and clarifying the pool heater
test procedure as it applies to oil-fired products. DOE also proposed
new test provisions for electric pool heaters, including electric heat
pump pool heaters. DOE did not receive comments on the RFI relating to
unvented home heating equipment and, after reviewing the test method,
did not propose any changes to the test procedure for unvented home
heating equipment in the October 2013 NOPR. Pursuant to 42 U.S.C.
6293(b)(1)(A)(ii), DOE has determined not to amend the test procedure
for unvented home heating equipment.
The October 2013 NOPR serves as the basis for this final rule. On
December 4, 2013, DOE held a public meeting to discuss the test
procedure proposals outlined in the October 2013 NOPR. DOE accepted
comments and information on the NOPR until January 7, 2014. DOE
considered the feedback received from stakeholders, which is discussed
in section III of this final rule.
II. Synopsis of the Final Rule
In this final rule, DOE amends its test procedures for vented home
heating equipment and pool heaters. The vented
[[Page 794]]
home heating equipment amendments add provisions for testing vented
heaters that utilize condensing technology and update incorporations by
reference in the existing test procedure. The pool heater amendments
incorporate by reference Air-Conditioning, Heating, and Refrigeration
Institute (AHRI) Standard 1160-2009, ``Performance Rating of Heat Pump
Pool Heaters'' (AHRI 1160) and American National Standards Insitute
(ANSI)/American Society of Heating, Refrigerating, and Air-Conditioning
Engineers (ASHRAE) Standard 146-2011, ``Method of Testing and Rating
Pool Heaters'' (ASHRAE 146), to establish testing procedures for
electric resistance and electric heat pump pool heaters. The amendments
for pool heaters also clarify the test procedure's applicability to
gas-fired and oil-fired pool heaters. The amendments and clarifications
for both product types are summarized below.
DOE amends the test procedure for vented heaters to incorporate by
reference the following six current industry standards to replace the
outdated standards referenced in the existing DOE test procedure: (1)
ANSI/ASHRAE Standard 103-2007, ``Method of Test for Annual Fuel
Utilization Efficiency of Residential Central Furnaces and Boilers''
(ASHRAE 103-2007); (2) ANSI Z21.86-2008, ``Gas-Fired Space Heating
Appliances'' (ANSI Z21.86); (3) ASTM D2156-09, ``Standard Test Method
for Smoke Density in Flue Gases from Burning Distillate Fuels'' (ASTM
D2156); (4) UL 729-2003, ``Standard for Safety for Oil-Fired Floor
Furnaces'' (UL 729); (5) UL 730-2003, ``Standard for Safety for Oil-
Fired Wall Furnaces'' (UL 730); and (6) UL 896-1993, ``Standard for
Safety for Oil-Burning Stoves'' (UL 896). DOE also establishes a test
method to determine the AFUE of vented heaters that use condensing
technology.
DOE does not adopt as part of the final rule a proposal included in
the October 2013 NOPR for a default jacket loss value for vented floor
furnaces. DOE proposed a default value of one percent for floor furnace
jacket loss (measured as a percentage of fuel input rate in Btu/h).
However, subsequent DOE testing revealed an average jacket loss of 3.05
percent with a standard deviation of 0.45 percent. Because the results
show jacket losses to be much higher than one percent, DOE will not
adopt a default value. The test procedure continues to require the
measurement of jacket losses for vented floor furnaces when determining
the AFUE.
In addition, DOE corrects multiple clerical errors and clarifies
sections that commenters identified as ambiguous or unclear in the test
procedure for vented home heating equipment. These changes are
identified and explained in section III.
In this final rule, DOE clarifies the applicability of the pool
heater test method for oil-fired products. DOE also adopts new
provisions for testing electric pool heaters, including electric heat
pump pool heaters. DOE adopts test methods for electric pool heaters by
incorporating by reference ASHRAE 146. In addition, DOE adopts test
methods for electric heat pump pool heaters by incorporating by
reference AHRI 1160, which provides a method to convert the coefficient
of performance (COP) metric used in that standard to the thermal
efficiency metric required by EPCA. (42 U.S.C. 6291(22)(E))
In any rulemaking to amend a test procedure, DOE must determine to
what extent, if any, the proposed test procedure would alter the
measured energy efficiency of any covered product from that determined
under the existing test procedure. (42 U.S.C. 6293(e)(1)) For both
vented home heating equipment and pool heaters, DOE has determined that
the proposed test procedure amendments would have a de minimis impact
on the products' measured efficiency. A full discussion of the
rationale for this conclusion is provided in section III.C.
III. Discussion
DOE received seven written comments in response to the October 2013
NOPR in addition to the comments received during the December 2013
public meeting. The commenters included: AHRI; ASHRAE; Empire Comfort
Systems (ECS); Intertek; the Natural Resources Defense Council (NRDC);
Raypak; and China WTO/TBT National Notification & Enquiry Center,
Standard and Regulation Researching Center, AQSIQ, P.R. China (CWTO).
These interested parties commented on a range of issues, including
those DOE identified in the October 2013 NOPR, as well as several other
pertinent issues. The issues on which DOE received comments, as well as
DOE's responses to those comments and the resulting changes to the test
procedures for vented home heating equipment and pool heaters, are
discussed in the following subsections C and D.
DOE notes that the U.S. Court of Appeals for the District of
Columbia (D.C. Circuit) on February 8, 2013, issued a decision vacating
the DOE definition of ``Vented hearth heater'' at 10 CFR 430.2 and
remanded the issue to DOE to interpret the challenged provisions
consistent with the court's opinion.\4\ As such, DOE amends the
definition of ``vented home heating equipment'' at 10 CFR 430.2 to
remove the term ``vented hearth heater.'' DOE did not receive comments
related to the application of the test procedure to vented hearth
heaters in response to the October 2013 NOPR. DOE plans to address the
vented hearth heaters test procedure in a separate rulemaking.
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\4\ Hearth, Patio & Barbecue Ass'n v. U.S. Dep't of Energy, 706
F.3d 499, 509 (D.C. Cir. 2013).
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A. Products Covered by This Final Rule
The amendments in this final rule cover those products that meet
the definitions for vented home heating equipment and pool heaters, as
codified in 10 CFR 430.2. DOE received no comment regarding unvented
home heating equipment in response to the RFI and thus did not propose
test procedure amendments for these products in the October 2013 NOPR.
Likewise, DOE does not adopt any amendments to its test procedure for
unvented home heating equipment in this final rule.
B. Dates for the Amended Test Procedure
This final rule amends 10 CFR 430.3, 10 CFR 430.23, Appendix O to
subpart B of part 430, and Appendix P to subpart B of part 430. The
amendments to 10 CFR 430.3 and 10 CFR 430.23 are effective 30 days
after publication of this final rule. Pursuant to 42 U.S.C. 6293(c)(2),
effective 180 days after DOE prescribes or establishes a new or amended
test procedure, manufacturers must make representations of energy
efficiency, including certifications of compliance, using that new or
amended test procedure. Accordingly, all representations of energy
efficiency, including certifications of compliance, must be based on
testing conducted in accordance with the amended Appendix O and
Appendix P as of 180 days after publication of the test procedure final
rule.
C. Test Procedure for Direct Heating Equipment
This final rule amends DOE's test procedures for vented heaters to
account for this condensing technology. Condensing technology is a
design strategy that increases the efficiency of a heating appliance by
extracting additional thermal energy from the flue gases, causing the
water vapor created in the combustion process to condense. The
provisions regarding condensing technology for vented home heating
equipment are essentially the same as those contained in ASHRAE 103-
2007.
[[Page 795]]
However, because of the numerous clarifications and modifications
needed to apply the condensing technology provisions of the industry
standard for furnaces and boilers to vented home heating equipment, DOE
incorporates the condensing procedures as stand-alone amendments to
DOE's vented home heating equipment test procedure, rather than
incorporating by reference select provisions of ASHRAE 103-2007.
Consistent with 42 U.S.C. 6293(c), any representations of energy
consumption of vented home heating equipment must be based on the final
amended test procedures 180 days after the publication of this test
procedure final rule in the Federal Register. Until that time,
manufacturers must make such representations based either on the final
amended test procedures or on the previous test procedures, set forth
at 10 CFR part 430, subpart B, appendix O, revised as of January 1,
2014.
In response to the October 2013 NOPR and during the December 2013
public meeting, DOE received comments relating to vented home heating
equipment from five interested parties (Intertek, ECS, AHRI, NRDC, and
ASHRAE). The comments focused on: (1) condensate collection test
procedures, (2) updating incorporations by reference to industry
standards, and (3) other test procedure details. Regarding the first
issue, commenters generally favored incorporating condensing technology
into the test procedure, although some further clarifications were
requested. Regarding the second issue, commenters generally favored
updating incorporations by reference to more recent industry standards.
As part of DOE's overall review of test procedures, these vented home
heating equipment amendments include a complete updating of references
to industry standards used in the vented home heating equipment test
procedure and modifications to the test procedure as necessary.
Finally, regarding the third issue, the comments primarily concerned
clerical, typographical, and other minor issues present in the existing
and proposed test procedures. These issues are discussed in greater
detail below.
1. Vented Home Heating Equipment Employing Condensing Technology
DOE considered the possibility of minimizing the test burden by
reducing the time required for measuring condensate mass during steady-
state conditions. The test procedure section 3.8.1 requires that the
measurement of condensate shall be conducted during the thirty-minute
period after steady-state conditions have been established.
DOE received comments from four interested parties regarding the
order of the condensate collection test procedures for vented home
heating equipment. Comments from AHRI, ECS, Intertek, and NRDC were
generally in favor of amending the test procedure to account for
condensing technology, as the technology results in lower energy use.
AHRI and Intertek both questioned the need for separate condensation
testing as opposed to combining the testing with current steady-state
testing to decrease the test burden. (ECS, No. 7 at p.1; NRDC, No. 10
at p.1; Intertek, Public Meeting Transcript, No. 6 at p. 14; AHRI, No.
9 at p.1)
In order to reduce test burden, DOE allows for the measurement of
condensate during the establishment of the steady-state conditions (10
CFR part 430, subpart B, App. O, section 3.8.1) rather than after
establishing steady-state conditions (10 CFR part 430, subpart B, App.
O, section 3.1). DOE investigated the difference in condensate mass
collected and the rate of condensate production during the two separate
periods (i.e., during the establishment of steady-state conditions and
once steady-state conditions have been reached). Based on the
comparison of the measurements, DOE has determined that there is no
significant difference in the mass of condensate collected or the rate
of condensate production during the two separate periods. Therefore,
DOE concurs with AHRI and Intertek's comments that the condensation
collection may be performed during the steady-state test.
Accordingly, DOE adopts provisions that allow for performance of
the steady-state condensate collection test set forth in section 3.8.1
during the steady-state test set out in section 3.1 of the test
procedure. DOE amends Appendix O by adding section 3.8.1 to allow the
option for condensate measurements either concurrently with or
immediately after completion of the steady-state test.
AHRI commented that the margin of error for a measurement of
condensate mass (MC,SS) should not be more than 0.5 percent and that section 2 of the existing test procedure
should be modified to include this language. (AHRI, No.9 at p.1) DOE
agrees with the comment from AHRI as this margin of error for the
measurement of condensate mass is consistent with the margin of error
provided in the residential furnace and boiler test procedures. DOE is
using the language from section 6.6 of ASHRAE 103-2007 for this
clarification. DOE placed this phrasing in section 3.8.1 of the new
test procedure instead of in section 2.
Empire Comfort Systems and AHRI commented that there is no guidance
in the existing test procedure specifying the mode in which to test
units, especially condensing units, shipped with multiple control
modes. Further, AHRI recommended that DOE add a provision specifying
that models that provide consumers with the capability to operate the
heater in more than one mode should be tested using the mode that
represents the least efficient operation. AHRI specifically mentioned
the need for clarification when a unit has a manual mode and a
thermostat-controlled, step-modulating mode and stated that the
selection of the operational mode for testing affects the AFUE rating.
(AHRI, No.9 at p.3; ECS, No. 7 p.2; ECS, Public Meeting Transcript, No.
6, p.18-19)
DOE agrees that a clarification is necessary regarding in which
control mode to test when multiple options are present, particularly
when a unit is capable of both automatic and manual modes. Automatic
mode indicates that the unit has thermostat control and operates using
single-stage, two-stage, or step-modulating controls. In manual mode
the unit is controlled by the user. Because these appliances are most
often operated in automatic mode when both automatic and manual are
available, DOE is requiring units capable of both automatic and manual
control to be tested according to the provisions in the test procedure
for units with automatic mode. DOE added section 2.11 to the test
procedure to implement this change.
ECS and AHRI submitted comments in favor of adopting the ASHRAE 103
methodology to determine a default flue gas draft factor
(DF) value for condensing units with no off period flue
losses. This method provides the option of testing or assigning a
default draft factor of 0.05. (AHRI, No.9 at p.1; ECS, No. 7 at p.1)
DOE agrees to include the option of testing or assigning a default
value for the draft factor for units with no measureable off period
flue losses. Adopting this provision is in line with the general intent
of adopting ASHRAE103-2007 methodologies when appropriate. It also
reduces the testing burden by allowing the use of a default factor of
0.05 in some cases.
DOE incorporates a test method based on the use of a smoke stick
device to establish the absence of flow through the heat exchanger of
vented home heating equipment designed with no measurable airflow
through the heat exchanger. This test is used only to determine whether
the use of the default draft factor is appropriate (per sections
[[Page 796]]
8.8.3 and 9.10 of ASHRAE 103-2007). This test is not intended to
determine the volume of air moving through the heat exchanger. If the
test confirms the absence of airflow, then the default draft factor of
0.05 may be used. If the test results indicate the presence of airflow,
then the draft factor must be determined either through testing or as
specified in Table 1 of 10 CFR part 430, subpart B, Appendix O. DOE has
implemented these changes by adding sections 3.6.1 and 3.6.2 to the
existing test procedure and modifying sections 4.1.2 and 4.5.2 of the
existing test procedure by incorporating certain provisions from
sections 8.8.3 and 9.10 of ASHRAE 103-2007.
2. Updating of Industry Reference Standards
ASHRAE commented in favor of the DOE proposal to include by
reference ASHRAE 103-2007, as this standard best represents collective
industry knowledge and best practices. (ASHRAE, No. 5 at p.1) Because
all ASHRAE103-1993 sections referenced in this test procedure are
identical to the 2007 version, DOE is incorporating those sections from
the ASHRAE 103-2007 in the final rule in order to reference the most
current version of the standard.
AHRI commented against the proposed change to section 2.1.3 of the
test procedure, which would reference 37.1.1 of UL 896 for installing
vented room heaters, because this reference is a standard for oil-fired
heaters and makes no improvement to the current test procedure. AHRI
stated the current language to use manufacturer's instructions is more
appropriate for the overall body of units tested. This approach
reflects the variety of oil- and gas-fired appliances and the nature of
the testing conducted. (AHRI, No. 9 at p.2; AHRI, Public Meeting
Transcript, No. 6 at p.21) DOE agrees that this reference change should
not be adopted, but is adopting slight modifications to section 2.1.3
to provide that the unit under test must be installed in accordance
with the manufacturer's installation and operations (I&O) manual
provided with the unit.
AHRI commented against the proposed change to section 2.3.3 of the
existing test procedure, which would reference Table 1 of ASHRAE 103-
2007 instead of section 2.2, Table VII, of ANSI Standard Z21.11.1-1974.
AHRI proposed instead to reference Table IV of ANSI Z21.86. AHRI's
reasoning is that the Z21 series of safety standards are the source
documents for general specifications on gases used during the testing
of gas-fired appliances, including Table 1 of ASHRAE 103-1993, which
comes from Table XI in ANSI Z21.47. (AHRI, No. 9 at p.2) DOE agrees
with this proposal since Z21.86has the advantages AHRI has mentioned.
The reference in section 2.1.3 of the final rule is changed to Table IV
of ANSI Z21.86.
DOE implements a number of additional changes in this final rule.
In most cases, these changes consist of updating incorporations by
reference to a more current version of industry standards. These
updates allow for new users of the test procedures to execute the DOE
test procedures without depending on outdated standards, which may be
difficult to obtain.
In some cases, an update incorporates by reference a standard that,
in its more current version, includes several of the standards that are
incorporated by reference in the existing test procedure and used to be
published separately, but are now combined under a new title. One such
case is the standard that includes the ANSI standards for wall
furnaces, floor furnaces, and room heaters, which were once separate
standards but are now combined into a single standard. This new
standard is titled, ``Vented Gas-Fired Space Heating Appliances'' and
is referred to as ``ANSI Z21.86'' in this final rule. DOE is
incorporating by reference ANSI Z21.86-2008 to specify the testing
procedures related to circulating air adjustments, found in section 2.5
of the revised DOE test procedure, and location of temperature
measuring instrumentation, found in section 2.6.1. In addition, DOE
incorporates by reference ANSI Z21.86 to specify the installation
instructions for direct vent (section 6.1.3 and figure 6) and non-
direct vent (section 8.1.3 and figure 7 or figure 10) wall furnaces.
ANSI Z21.86 does not include installation specifications for vented
room heaters and vented floor furnaces. Accordingly, as discussed
previously, for vented room heaters the manufacturer's recommendations
as described in the installation and operations (I&O) manual provided
with the units must be used for installation. For vented floor
furnaces, the requirement in section 2.1.2 of the current test
procedure to install vented floor furnaces for testing as specified in
sections 35.1 through 35.5 of UL-729-1976 remains materially unchanged;
the updated UL test methods are the same as those in the existing test
procedure and reflect the specific installation requirements of each
appliance. Although the UL standards typically are used for oil-fired
equipment and the ANSI standards typically are used for gas-fired
equipment, in the existing DOE test procedure, where there is no
distinction between installation provisions, the UL standards are cited
in application to both gas and oil floor furnaces (i.e., section
2.1.2).
DOE incorporates by reference ASHRAE 103-2007 in three locations
within the revised test procedure--sections 2.3 Fuel supply, 2.4 Burner
adjustments, and 3.2 Jacket loss measurement--in lieu of three older
standards incorporated by reference in the existing test procedure. DOE
is updating these references to ASHRAE 103-2007 because this standard
incorporates industry consensus without the need to depend on other
references. It is not materially different from the test method used in
the current vented home heating equipment test procedure (i.e., the
AFUE test method). All referenced industry standards are listed in 10
CFR 430.3, Materials incorporated by reference. DOE concludes that
these changes and updates to materials incorporated by reference will
neither result in material differences in test results nor increase
test procedure burden.
The following is a list of the shorthand titles and full titles of
all the referenced standards used in the existing test procedure and
those used in this vented home heating equipment test procedure.
Standards Used in the Existing Test Procedures for Vented Home
Heating Equipment:
``ANSI Standard Z21.11.1-1974'' means the American National
Standard for Gas-Fired Room Heaters.
``ANSI Standard Z21.44-1973'' means the American National Standard
for Gas-Fired Gravity and Fan Type Direct Vent Wall Furnaces.
``ANSI Standard Z21.48-1976'' means the American National Standard
for Gas-Fired Gravity and Fan Type Floor Furnaces.
``ANSI Standard Z21.49-1975'' means the American National Standard
for Gas-Fired Gravity and Fan Type Vented Wall Furnaces.
``ANSI Standard Z91.1-1972'' means the American National Standard
for Performance Standards for Oil-Powered Central Furnaces.
``ANSI Standard Z11.182-1965 (R1971) (ASTM D 2156-65 (1970))''
means the standard published by the American Society of Testing and
Materials titled, ``Standard Test Method for Smoke Density in Flue
Gases from Burning Distillate Fuels.''
``UL 729-1976'' means the Underwriters Laboratories standard for
Oil-Fired Floor Furnaces.
[[Page 797]]
``UL 730-1974'' means the Underwriters Laboratories standard for
Oil-Fired Wall Furnaces.
``UL 896-1973'' means the Underwriters Laboratories standard for
Oil-Burning Stoves.
Standards Used in the Amended Test Procedure for Vented Home
Heating Equipment:
``ANSI/ASHRAE Standard 103-2007'' means the test standard published
by the American Society of Heating, Refrigerating, and Air-Conditioning
Engineers titled, ``Method of Test for Annual Fuel Utilization
Efficiency of Residential Central Furnaces and Boilers.''
``ANSI Z21.86-2008'' means the standard published by the American
National Standards Institute titled, ``Vented Gas-Fired Space Heating
Appliances.''
``ASTM D2156-09'' means the standard published by the American
Society of Testing and Materials titled, ``Standard Test Method for
Smoke Density in Flue Gases from Burning Distillate Fuels.''
``UL 729-2003'' means the test standard published by the
Underwriters Laboratory, Inc. titled, ``Standard for Safety for Oil-
Fired Floor Furnaces.''
``UL 730-2003'' means the test standard published by the
Underwriters Laboratory, Inc. titled, ``Standard for Safety for Oil-
Fired Wall Furnaces.''
3. Other Issues
AHRI and ECS commented on three typographical errors. First, in the
October 2013 NOPR, the denominator of the equation for LC,SS
in section 4.1.6.2 and the denominator of the equation for
LC in section 4.1.6.4 were supposed to read ``1053.3'' but
instead read ``1053'' and the missing ``.3'' was erroneously placed at
the end of the equation. Second, the variable CT* had been
replaced with the number ``100'' in the MS,OFF and
MF,OFF equations in 4.3.3 and 4.5.1in the existing test
procedure. Finally, values for DS for system numbers 9
through 12 were omitted in Table 1 from the existing test procedure.
(AHRI, No.9 at p.2; AHRI, Public Meeting Transcript, No. 6, p.27; ECS,
No. 7 p.1-2; ECS Public Meeting Transcript, No. 6, p.17) DOE recognizes
the errors as clerical. DOE found that the first error resulted from
the conversion to publishing format and that the error is not present
in the original document. DOE has corrected this error and to prevent
future errors, DOE will submit equations as images and request the
printing office review the document before publication. Regarding the
second error, although CT* equals 100 when the tracer gas is
a single component gas, this is not always the case. Thus, DOE agrees
that the ``100'' term should be ``CT*'' to account for
instances when the tracer gas is not a single component gas. DOE notes
that this is consistent with the text following the equation. Regarding
the third error, there is no value given for DS for system
numbers 9 through 12 as these systems are direct vent systems to which
DS does not apply. The value is intentionally omitted from
subsequent calculations and has been changed to ``0'' for clarity.
ECS commented that the ANSI Z21.86, incorporated by reference in
the revised test procedure, does not provide detailed information about
the appropriate positioning of thermocouple(s) for measuring the flue
exhaust temperature. (ECS, No. 7 p.1; ECS, Public Meeting Transcript,
No. 6, p.22) DOE disagrees. These details are in section 2.6 of the
existing test procedure.
ECS and AHRI submitted comments in favor of DOE's proposal to
include the option to set a jacket loss value for vented floor furnaces
at a default of one percent in lieu of testing. (AHRI, No.9 at p.2;
ECS, No. 7 p.1) DOE is generally in favor of simplifying the test
procedure where results would not be affected. In this case, DOE's
testing revealed an average jacket loss of 3.05 percent with a standard
deviation of 0.45 percent. DOE concluded from this testing that the
proposed default jacket loss value of one percent for vented floor
furnaces, while consistent with industry practices for other equipment,
is too low for this product. However, adopting a higher default jacket
loss value would significantly affect AFUE. Therefore, DOE does not
introduce an optional default jacket loss value for vented floor
furnaces and continues to require testing as described in section 3.2
of the existing test procedure.
Intertek and AHRI submitted comments in favor of removing the
requirement to install simulated walls and floors for performance
testing of floor furnaces. The comments argue that these requirements
are driven by safety concerns and have no effect on the efficiency
ratings, so removing the requirement will reduce test burden. (AHRI,
Public Meeting Transcript, No. 6, p.23-25; Intertek Public Meeting
Transcript, No. 6, p.23-25) DOE rejects this suggestion primarily
because DOE has no data to confirm that the performance testing is not
affected by the added walls and floors. Furthermore, in DOE's view, any
decrease in test burden resulting from elimination of this requirement
would be minimal. Manufacturers are already required to install these
simulated floors and walls during safety testing. As a result, any
decrease in test burden would affect only a small group of independent
laboratories, if any, that only conduct performance testing and thus
may not have an existing setup. Therefore, DOE is retaining these
requirements in the test procedure.
DOE corrected other typographical errors that are present in the
existing test procedure. In the equation in section 4.3.6 of appendix
O, DOE has (1) added a missing minus (``-'') sign immediately to the
right of the ``CjLj''; (2) replaced the plus
(``+'') sign between the two bracketed parts of the equation with a
multiplication (``X'') symbol; and (3) replaced the second
``Ls,OFF'' in the second bracketed part of the equation with
``LI,OFF''. In section 4.1.15, DOE corrects ``equFipped'' to
read ``equipped'' and corrects ``therostats'' to read ``thermostats.''
In section 4.1.8, DOE corrects ``drafthood'' to read ``draft hood.''
These and other typographical errors have been corrected in this final
rule document. These errors are obviously typographical in nature,
because similar efficiency equations in other parts of the test
procedure, as well as those used in industry standards, do not include
these errors. The relevant industry groups have determined the correct
format of this equation since its adoption and have been utilizing the
correct format when testing and rating product efficiency.
Another issue that was identified during DOE's review is the lack
of a defining equation in the calculation procedures for manually
controlled vented heaters in section 4.2.4 of the existing test
procedure. To correct this omission, DOE adds an equation describing
the weighted average steady-state efficiency ([eta]SS-WT) in
terms of the latent and sensible losses to section 4.2.4.1.
DOE identified several additional sections of the existing test
procedure that require clarification. Section 2.9 states, ``maintain
the room temperature within 5[emsp14][deg]F (2.8[deg]C) of the value TRA measured during the
steady-state performance test.'' However, while section 3.1.1 and 3.1.2
explain to establish steady state using three successive readings of
the stack or flue gas temperature taken 15 minutes apart, it does not
indicate at what time the variable TRA is established (or
whether it is an average). DOE clarifies that while the room
temperature must be continuously monitored in order to meet the
conditions specified in section 2.9, TRA is to be measured
in coincidence with the third of the three successive 15-minute
interval readings of the stack or flue gas temperatures
[[Page 798]]
taken during the steady-state tests (sections 3.1.1 and 3.1.2).
Likewise, the measurement of additional variables (TS,SS,
XCO2S, TF,SS, XCO2F) described in
section 3.1 are to coincide with the third of these three successive
15-minute interval readings.
DOE also identified that the requirements in section 2.9 for
combustion air and draft relief air temperatures require clarification.
Section 2.9 states that the ``temperature of the air for combustion and
the air for draft relief shall not differ more than
5[emsp14][deg]F from room temperature as measured above.'' DOE
clarifies that this means these temperatures shall not differ more than
5[emsp14][deg]F from the room ambient temperature at any
point in time; it does not mean 5[emsp14][deg]F with
respect to the measurement TRA. DOE also clarifies that this
requirement for the combustion air does not apply during the cool-down
tests of sections 3.3 and 3.6. These tests are conducted during shut-
down of the unit, when maintaining requirements for combustion air
temperatures are unnecessary.
DOE clarifies in sections 4.1.2 and 4.1.3 that the flue and stack
draft factors may be obtained through the test method and calculations
in sections 3.6 and 4.5, respectively, or by using the appropriate
default factors from Table 1.
The final issue identified by DOE was to clarify the applicability
of the testing and calculation method in sections 3.3 and 4.3 (tracer
gas method) for units without a thermal stack damper. The test
procedure currently prescribes that units without thermal stack dampers
be rated using the calculation method in section 4.1 or 4.2 depending
on the control type. Section 4.3 incorrectly states that as an optional
procedure all vented heaters without thermal stack dampers can elect to
use the AFUE calculation method described in 4.3.
DOE reviewed the use of the tracer gas method as described in 4.3
for units without thermal stack dampers. DOE believes manufacturers do
not use the tracer gas method to test units without thermal stack
dampers and do not use such testing results to calculate the AFUE for
such units. In previous rulemakings for vented home heating equipment,
DOE did not receive public comments regarding the applicability of
section 4.3, and DOE has not received waiver requests that would
indicate that there are any instances in which the calculation methods
of 4.1 cannot be used for units without thermal stack dampers,
suggesting that an alternative test method is unnecessary for these
units.
DOE performed testing on several representative units to determine
the applicability of sections 4.1, 4.2, and 4.3 to units with and
without stack dampers. The AFUE values were generated twice for each
unit, once using the results from the tracer gas method, and once using
the calculation method in 4.1 (for units equipped without manual
controls or thermal stack dampers) or 4.2 (for models equipped with
manual controls). The results are presented in Table 3.1 below and show
an average 2.6 percent higher AFUE when using the tracer gas method in
section 4.3 as opposed to the calculation method in 4.1.
Table 3.1--Difference in AFUE in Units of Vented Home Heating Equipment
When Tested Using Tracer Gas Method and Standard Method
------------------------------------------------------------------------
Difference in
AFUE
------------------------------------------------------------------------
Unit A.................................................. 3.3
Unit B.................................................. 3.2
Unit C.................................................. 1.2
------------------------------------------------------------------------
The sign of the AFUE change is consistent with the operation of the
system with the stack damper removed or forced open because the flue
gases would more freely move with the damper open resulting in higher
loss. This fundamental design difference along with the differences in
AFUE values from the testing show that the calculation methods are not
equivalent and so only one should be allowed for each design.
Further, 10 CFR 430.23, Test procedures for the measurement of
energy and water consumption, states clearly that the tracer gas
calculation method in section 4.3 applies to ``vented heaters equipped
with thermal stack dampers,'' and that section 4.1 applies to vented
heaters ``without either manual controls or thermal stack dampers.''
Thus, DOE considers this a clarification of, rather than a modification
to, the current test procedure.
For the reasons described previously, DOE clarifies that the
optional use of the tracer gas method does not apply to units without
thermal stack dampers. DOE has determined this clarification will not
impose any additional burden on manufacturers, since units without
thermal stack dampers are already commonly rated using the calculation
method in 4.1 or 4.2. Moreover, DOE has determined that disallowing the
tracer gas method for units without thermal stack dampers will not
affect efficiency ratings, since it is highly unlikely that
manufacturers have rated units without thermal stack dampers using the
tracer gas test method previously.
D. Test Procedure for Pool Heaters
DOE's existing test procedure for pool heaters is found at 10 CFR
430.23(p) and 10 CFR part 430, subpart B, appendix P (existing test
procedure).
In its definition of ``efficiency descriptor,'' EPCA specifies that
for pool heaters, the efficiency descriptor shall be ``thermal
efficiency'' (42 U.S.C. 6291(22)(E)). Current energy conservation
standards for pool heaters do not account for standby mode and off mode
energy use. As part of a recent test procedure rulemaking, DOE
prescribed a new efficiency metric for pool heaters, titled
``integrated thermal efficiency.'' 77 FR 74559 (Dec. 17, 2012). This
prescribed integrated thermal efficiency (TEI) metric builds
on the existing thermal efficiency metric to include electrical energy
consumption during standby mode and off mode operation, as required by
EISA 2007. (42 U.S C. 6295(gg)(2)(A))
Because certain types of pool heaters are powered by energy sources
other than gas, DOE requested comments in the October 2011 RFI
regarding the appropriateness of prescribing the currently incorporated
ANSI Z21.56 test method, titled ``Gas-Fired Pool Heaters,'' for testing
pool heaters that operate with electricity (including electric heat
pump pool heaters) or oil. 76 FR 63211, 63215-16 (Oct. 12, 2011). In
the October 2011 RFI, DOE tentatively concluded that the test procedure
for pool heaters at 10 CFR part 430, subpart B, appendix P already
contains provisions to allow the ANSI Z21.56 test method to be applied
to oil-fired pool heaters, and, therefore, no further action is
necessary for those products. DOE received no comments that were
contrary to this conclusion.
Prior to the October 2011 RFI, in a December 2009 NOPR for energy
conservation standards for heating products, DOE concluded that, as
currently drafted, the DOE test procedure for pool heaters is not
suitable for measuring energy efficiency for electric pool heaters
(including electric heat pump pool heaters). 74 FR 65852, 65866-67
(Dec. 11, 2009). In the October 2011 RFI, DOE noted that for electric
pool heaters (including those units using electric heat pump
technology), the fuel source is electricity (measured in watts) instead
of gas (measured in Btu/h), but ``thermal efficiency,'' as required
under EPCA and determined using ANSI Z21.56, is a
[[Page 799]]
measure of heat delivered to the water at the heater outlet (in Btu/h)
divided by the heat input (in Btu/h) of the fuel. 76 FR 63211, 63215 16
(Oct. 12, 2011). It is technologically feasible to develop an
integrated thermal efficiency rating for an electric heat pump pool
heater by converting the power input in watts to the input in Btu/h
(which can be done for both the power used during active mode and the
power used during standby mode and off mode).
Currently, electric heat pumps for space heating are typically
rated using industry standards for coefficient of performance (COP).
DOE notes that when an integrated thermal efficiency metric as
described above is applied to electric heat pump pool heaters, the
calculated results are efficiency ratings of more than 100 percent.
This may necessitate some reeducation among consumers to alleviate any
confusion resulting from changing labeling from COP to integrated
thermal efficiency. Furthermore, the test procedure still includes
provisions for calculating heat pump pool heater COP. Another
consideration for electric heat pump pool heaters is that performance
depends upon the ambient temperature and humidity, so environmental
conditions for testing are much more important for electric heat pump
pool heaters than for gas-fired pool heaters, oil-fired pool heaters,
or electric resistance pool heaters.
In response to the October 2013 NOPR and during the December 2013
public meeting, DOE received comments from four interested parties
(Raypak, AHRI, NRDC, and CWTO). The comments focused primarily on the
inclusion of electric resistance and electric heat pump pool heaters
into the pool heater test procedure. The main issues of concern stem
from implementing common metrics over all pool heater types. More
specifically, the base operating hours, efficiency metrics, and
different features of electric resistance and electric heat pump pool
heaters as compared to traditional gas fired pool heaters drew comments
and discussion.
1. Electric Pool Heaters
AHRI commented that the nomenclature in the proposed subsection
1.6, `Hybrid Pool Heater,' in which the term `hybrid' refers to a
combination gas and electric pool heater, may cause confusion because
hybrid is already used to refer to an electric heat pump for other
product classes. (AHRI, Public Meeting Transcript, No. 6 at p. 33-34)
DOE found that the term hybrid most commonly refers to pool heaters
that use solar energy in conjunction with a traditional gas or electric
pool heater. In addition, certain electric heat pump pool heaters and
combination electric heat pump and electric resistance heating pool
heaters are referred to as hybrid heat pumps. DOE reviewed this issue
and found that appliances that used the term hybrid or a variant of it
have relatively low market penetration. Furthermore, other appliances
that use the term ``hybrid,'' or a variant of it, generally have an
additional qualifier such as ``hybrid solar pool heater'' or ``hybrid
heat pump.'' Given that gas pool heaters and electric heat pump pool
heaters comprise the large majority of pool heaters today, DOE believes
that `hybrid pool heater' is an intuitive name for a pool heater that
combines the functionality of gas and electric heat pump pool heaters.
Therefore, DOE is adopting this nomenclature.
In response to DOE's proposal to introduce the integrated thermal
efficiency metric as an efficiency descriptor for pool heaters, Raypak
commented that implementing a new metric has the potential to confuse
customers and will create a significant burden on pool heater
manufacturers, which are primarily small business entities. In
addition, Raypak commented that thermal efficiency does not address
energy prices. (Raypak, No. 8 at pp. 1-2)
DOE believes that the confusion to customers caused by the
introduction of the new integrated thermal efficiency metric should be
minimal, as other parameters such as COP can continue to be used in the
manufacturers' literature if such parameters are determined pursuant to
the applicable DOE test procedure. DOE does not believe that
implementing the integrated thermal efficiency metric represents an
undue burden on manufacturers. The integrated thermal efficiency metric
incorporates the COP as determined by the current industry standard
AHRI 1160 and therefore changes in test set-up or methods will be
minimal. Also, DOE does not recognize the changes in labeling as unduly
burdensome. DOE agrees that the new integrated thermal efficiency
metric does not directly address energy price. However, it is DOE's
intent for this metric to provide information about the unit's
efficiency, not overall cost to the consumer. Therefore, DOE is not
incorporating energy price into the integrated thermal efficiency
metric.
AHRI and Raypak commented that the current burner operating hour
(BOH) value of 104 hours is inappropriate for this test procedure as it
is specific to gas-fired pool heaters. They further state that the
current BOH value does not apply to heat pump pool heaters because of
typical industry sizing conventions, which are that gas-fired pool
heaters have a significantly higher heating capacity than heat pump
pool heaters sized for the same pool. (AHRI, No. 9 at p. 3; Raypak, No.
8 at p. 1)
Regarding the use of an average burner operating hours (BOH) value
of 104 hours, DOE understands that the output capacity of the pool
heater is typically selected based on the specific pool
characteristics, namely pool size (surface area) and the ambient
conditions.\5\ DOE found that some pool heater sizing conventions list
similar sizing guidelines for both gas-fired \6\ and electric heat pump
\7\ pool heaters. Therefore, if a pool heater's output capacity is
properly selected relative to the pool's load requirement, then the
actual burner operating time will be similar whether gas-fired or
electric. Therefore, DOE is not changing the BOH value for electric
heat pump pool heaters.
---------------------------------------------------------------------------
\5\ See Dep't of Energy, Heat Pump Swimming Pool Heaters (May
29, 2012), http://energy.gov/energysaver/articles/heat-pump-swimming-pool-heaters Dep't of Energy, Gas Swimming Pool Heaters
(June 10, 2014), http://energy.gov/energysaver/articles/gas-swimming-pool-heaters.
\6\ See In the Swim, Calculating Approximate Heater Size,
https://www.intheswim.com/landing/whichsizeheater.aspx.
\7\ See AquaCal, How Can I Size My Swimming Pool Heat Pump?
(July 22, 2013), http://www.aquacal.com/blog/post/127-How-Can-I-Size-My-Swimming-Pool-Heat-Pump-.
---------------------------------------------------------------------------
AHRI commented that the integrated thermal efficiency metric is not
appropriate for many reasons, including, primarily, that standby mode
and off mode energy consumption in pool heaters provides no heating
benefit and distorts the relevance of thermal efficiency ratings. AHRI
also provided potential alternatives, such as using heating seasonal
efficiency (EFFYHS) or simply modifying the existing average
annual electrical energy consumption (EAE) calculation.
(AHRI, No. 9 at pp. 5-6)
EPCA requires DOE to include the standby energy consumption in the
existing metrics unless ``such an integrated test procedure is
technically infeasible.'' (42 U.S.C. 6295(gg)(2)(A)) Previous test
procedures also accounted for the standby energy consumption for pool
heaters with continuous pilot lights in the EFFYHS term.
However, EFFYHS is not appropriate as a naming convention
for the new metric because it is specific to the heating season and the
new metric also includes non-heating season effects.
AHRI's suggestion to modify the EAE calculation is
consistent with the test procedure in this final rule. The standby
[[Page 800]]
and off mode electrical energy is accounted for in
EAE,Standby,off, which is a component of EAE.
However, EAE does not include fuel energy consumption and is
therefore not a comprehensive energy efficiency metric for all pool
heaters. The TEI metric is a more complete representation of
the energy efficiency of pool heaters because it includes both fuel and
electricity energy consumption.
AHRI also commented that the new integrated thermal efficiency
metric cannot be used for sizing. (AHRI, No. 9 at pp. 3-6) DOE agrees
that pool heaters should not be sized based on integrated thermal
efficiency. Instead, pool heaters should be sized based on the pool
heater capacity and the thermal efficiency (ET), which is
part of this test procedure, and can continue to be used for sizing.
DOE also points out that the industry can use thermal efficiency in
addition to integrated thermal efficiency when communicating marketing
and sizing information to consumers.
AHRI further commented that prescribing TEI as the new
energy efficiency metric will impose an enormous and needless burden on
manufacturers and disrupt the marketplace. (AHRI, No. 9 at pp. 3-6) DOE
believes that the additional testing burdens of measuring standby are
minimal. Specifically, the test procedure specifies monitoring the
standby energy consumption for an additional 60 minutes using the
existing set-up for other parts of the test procedures. In addition,
AHRI commented that they recognize the 2007 amendments to EPCA allow
DOE latitude and discretion to prescribe a separate test procedure to
determine standby mode and off mode energy use, as well as a separate
energy conservation standard for standby mode and off mode energy
consumption. AHRI further interprets this to mean there is no mandate
that DOE must integrate the standby and off mode consumption into the
thermal efficiency, citing Sections 325(gg)(3)(B) and Subsection
325(gg)(2)(A)(ii). Lastly, AHRI suggested the possibility of using an
annual consumption metric as a replacement for thermal efficiency.
(AHRI, No. 9 at p. 5)
DOE reviewed this issue and reaffirms that in its definition of
``efficiency descriptor,'' EPCA specifies that the efficiency
descriptor for pool heaters shall be ``thermal efficiency.'' (42 U.S.C.
6291(22)(E)) EPCA requires DOE to include the standby energy
consumption in the existing metrics unless ``such an integrated test
procedure is technically infeasible.'' (42 U.S.C. 6295(gg)(2)(A)) DOE
has the option to create a separate standard for standby and off mode
consumption only if incorporation into a standard is ``not feasible.''
(42 U.S.C. 6295(gg)(3)(B)) In the case of pool heaters, DOE determined
that it is technically feasible to measure standby and off mode
consumption and incorporate those measurements into the thermal
efficiency metric.
CWTO submitted two comments that concern the inclusion of
electrical power (PE) in the seasonal useful output (EOUT)
equation. CWTO questioned applying thermal efficiency to rated fuel
input capacity and electrical power in section 5.4.3 of the pool heater
test procedure. CWTO stated that if EOUT was only based on
absorbed heat it would be more intuitive. (CWTO, No 11 at p.3) It is
DOE's position that for all pool heaters, contrary to some other
appliances, the electrical components in active mode provide useful
energy that justifies including them into that equation in addition to
the more familiar QIN. This is true for both gas-fired and
electric pool heaters. In addition, because these components are
present and active during thermal efficiency testing, including their
energy use in the overall integrated thermal efficiency is necessary.
This formulation also allows for the integration of standby and off
mode energy consumption into the metric. Finally, this formulation
applies equally to gas-fired, oil-fired, electric resistance, and
electric heat pump pool heaters.
Through this final rule, DOE adds test methods that apply to
electric heat pump and electric resistance pool heaters. DOE amends its
pool heater test procedure by adding a test method for electric heat
pump pool heaters that references AHRI Standard 1160-2009,
``Performance Rating of Heat Pump Pool Heaters,'' and ANSI/ASHRAE
Standard 146-2011, ``Method of Testing and Rating Pool Heaters.'' In
addition, DOE amends its pool heater test procedure by adding a test
method for electric resistance pool heaters that references ASHRAE146.
DOE concludes that incorporation of these industry test standards is
appropriate as they represent current best practices for these pool
heater products.
Although DOE prescribes amended test procedures in this final rule,
manufacturers are not required to certify compliance for electric heat
pump and electric resistance pool heaters until such time as DOE sets
minimum energy conservation standards for those products (which would
include energy consumption in active, standby, and off modes). Prior to
DOE setting energy conservation standards for electric heat pump and
electric resistance pool heaters, any representations as to the energy
efficiency or energy use of those products made after 180 days after
the publication of this test procedure final rule must be based on this
amended test procedure. Manufacturers of electric heat pump pool
heaters may use the COP metric as measured by the DOE test procedure
being adopted in this final rule in addition to the integrated thermal
efficiency metric for making efficiency representations.
2. Other Issues
In addition to the changes for electric pool heaters described in
the previous section, DOE also clarifies that the DOE test procedure is
applicable to oil-fired pool heaters, despite the incorporation of a
test method (ANSI Z21.56) titled ``Gas-Fired Pool Heaters.'' Section
4.1.1 of that test method contains a provision to compute the energy
used when oil is the fuel, as opposed to natural gas. In addition, DOE
is clarifying the definition of the equilibrium term used in the active
mode thermal efficiency testing. This clarification has been inserted
into section 2.1 of existing test procedure, as listed in the
regulatory text. Finally, DOE has added clarifications regarding burner
input rate error, equilibrium conditions, water temperature rise,
seasonal off switch, and recirculating pump to the existing test
procedure as listed in the regulatory text.
E. Compliance With Other EPCA Requirements
As mentioned in the preamble at section II, in amending a test
procedure, EPCA directs DOE to determine to what extent, if any, the
amended test procedure would alter the measured energy efficiency or
measured energy use of a covered product as determined under the
current test procedure. (42 U.S.C. 6293(e)(1)) The current energy
conservation standards for vented home heating equipment and pool
heaters are based on existing test procedure efficiency metrics--AFUE
and thermal efficiency (Et), respectively.
The test procedure amendments for vented home heating equipment in
this final rule do not contain changes that will alter the measured
energy efficiency of equipment. Rather, the changes represent either
clarifications that would improve the uniform application of the test
procedures for certain product types or provisions to cover new product
types. Any change in the reported efficiency of currently covered
products that might be associated with these clarifications is expected
to be de minimis.
[[Page 801]]
Consistent with 42 U.S.C. 6293(c), any representations of energy
consumption of vented home heating equipment must be based on any final
amended test procedures no later than 180 days after the publication of
the test procedure final rule in the Federal Register. Until that time,
manufacturers must make such representations based either on the final
amended test procedure or on the previous test procedure, set forth at
10 CFR part 430, subpart B, appendix O as contained in 10 CFR parts 200
to 499 edition revised as of January 1, 2014. Consistent with 42 U.S.C.
6291(8), representations of energy consumption includes representations
regarding the measures of energy use (including, for this product,
active mode, standby mode, and off mode energy use), annual operating
cost, energy efficiency (including, for this product, AFUE), or other
measure of energy consumption. DOE notes that manufacturers must use
the same test procedure for all representations of energy efficiency,
including certifications of compliance.
This final rule does not include any changes to the current standby
mode and off mode testing procedures and calculations for vented home
heating equipment as established in the December 2012 final rule. 77 FR
74559 (Dec. 17, 2012). Although fossil fuel standby mode and off mode
energy consumption were already captured in the existing AFUE metric,
the December 2012 final rule required manufacturers to use the new test
procedures for determining electrical standby mode and off mode energy
consumption in Appendix O beginning on June 17, 2013. Certifications of
compliance with the electrical standby mode and off mode energy
consumption standards are not required until the compliance date of DOE
standards that include electrical standby mode and off mode energy
consumption.
The test procedure amendments in this final rule for pool heaters
do not alter the measured efficiency of equipment covered by the
existing test procedure. This final rule provides a new test method for
electric resistance and electric heat pump pool heaters. However,
electric resistance and electric heat pump pool heaters are not
currently subject to energy conservation standards by DOE. Therefore,
DOE has concluded that there is no need to address the impact of these
amendments on current energy conservation standards for pool heaters.
Consistent with 42 U.S.C. 6293(c), any representations of energy
consumption of pool heaters must be based on any final amended
procedures and calculations in appendix P starting 180 days after the
publication of any final amended test procedures in the Federal
Register. Until that time, manufacturers of gas-fired and oil-fired
pool heaters may make such representations based either on the final
amended test procedures or on the previous test procedures, set forth
at 10 CFR part 430, subpart B, appendix P as contained in the 10 CFR
parts 200 to 499 edition revised as of January 1, 2014. Consistent with
42 U.S.C. 6291(8), representations of energy consumption include
representations of measures of energy use (including for this product,
active mode, standby mode, and off mode energy use), annual operating
cost, energy efficiency (including for this product, thermal efficiency
(Et), or integrated thermal efficiency (TEI)), or
other measure of energy consumption. Again, DOE notes that
manufacturers must use the same test procedure for all representations
of energy efficiency, including certifications of compliance.
There are currently no energy conservation standards for electric
resistance pool heaters, electric heat pump pool heaters, or oil-fired
pool heaters. Upon the compliance date of any final energy conservation
standards for these types of pool heaters, use of any final test
procedures in appendix P will be required to demonstrate compliance.
There are also currently no energy conservation standards for the
standby mode and off mode energy use of gas-fired pool heaters. Upon
the compliance date of any energy conservation standards that
incorporate standby mode and off mode energy consumption for gas-fired
pool heaters (i.e., for this product, a standard expressed as
integrated thermal efficiency (TEI)), use of any final test
procedures in appendix P will be required to demonstrate compliance.
IV. Procedural Issues and Regulatory Review
A. Review Under Executive Order 12866
The Office of Management and Budget has determined that test
procedure rulemakings do not constitute ``significant regulatory
actions'' under section 3(f) of Executive Order 12866, ``Regulatory
Planning and Review,'' 58 FR 51735 (Oct. 4, 1993). Accordingly, this
regulatory action is not subject to review under the Executive Order by
the Office of Information and Regulatory Affairs (OIRA) in the Office
of Management and Budget (OMB).
B. Administrative Procedure Act
Pursuant to the decision in Hearth, Patio & Barbecue Ass'n v. U.S.
Dep't of Energy, 706 F.3d 499 (D.C. Cir. 2013), DOE removed the
definition of ``vented hearth heater'' from 10 CFR 430.2 to reflect the
Court's order vacating the regulatory definition of ``vented hearth
heater.'' 79 FR 43927 (July 29, 2014). As such, in this final rule, DOE
is removing the cross references to ``vented hearth heater'' from the
definition of ``vented home heating equipment'' at 10 CFR 430.2. DOE
has determined, pursuant to 5 U.S.C. 553(b)(B), that prior notice and
an opportunity for public comment on this final rule are unnecessary.
DOE is not exercising any of the discretionary authority that the
Congress has provided to the Secretary of Energy in EPCA. DOE,
therefore, finds that good cause exists to waive prior notice and an
opportunity to comment for this rulemaking.
C. Review Under the Regulatory Flexibility Act
The Regulatory Flexibility Act (5 U.S.C. 601 et seq., as amended by
the Small Business Regulatory Enforcement Fairness Act of 1996)
requires preparation of an initial regulatory flexibility analysis
(IFRA) for any rule that by law must be proposed for public comment and
a final regulatory flexibility analysis (FRFA) for any such rule that
an agency adopts as a final rule, unless the agency certifies that the
rule, if promulgated, will not have a significant economic impact on a
substantial number of small entities. A regulatory flexibility analysis
examines the impact of the rule on small entities and considers
alternative ways of reducing negative effects. Also, as required by
Executive Order 13272, ``Proper Consideration of Small Entities in
Agency Rulemaking,'' 67 FR 53461 (August 16, 2002), DOE published
procedures and policies on February 19, 2003, to ensure that the
potential impacts of its rules on small entities are properly
considered during the DOE rulemaking process. 68 FR 7990. DOE has made
its procedures and policies available on the Office of the General
Counsel's Web site at: www.energy.gov/gc.
This final rule amends DOE's test procedures that will be used to
determine compliance with energy conservation standards for vented home
heating equipment and pool heaters. For vented home heating equipment,
the amendments add provisions for testing models that utilize
condensing technology and incorporate by reference the most appropriate
or recent versions of several industry standards referenced in the DOE
test procedure for the purposes of test set-up and installation
specifications. For pool heaters, the amendments incorporate by
reference
[[Page 802]]
AHRI 1160 and ASHRAE 146 to establish testing procedures for electric
(including electric heat pump) pool heaters. The amendments for pool
heaters also clarify the test procedure's applicability to oil-fired
pool heaters. DOE reviewed this final rule under the provisions of the
Regulatory Flexibility Act and the policies and procedures published on
February 19, 2003. 68 FR 7990.
1. Reasons for, Objectives of, and Legal Basis for the Final Rule
The reasons for, objectives of, and legal basis for the final rule
are stated elsewhere in the preamble and are not repeated here.
2. Description and Estimated Number of Small Entities Regulated
For the manufacturers of the covered products, the Small Business
Administration (SBA) has set a size threshold, which defines those
entities classified as ``small businesses'' for the purposes of the
statute. DOE used the SBA's small business size standards to determine
whether any small entities would be subject to the requirements of the
rule. 65 FR 30836, 30848-49 (May 15, 2000), as amended at 65 FR 53533,
53544-45 (Sept. 5, 2000) and codified at 13 CFR part 121. The SBA size
standards are listed by North American Industry Classification System
(NAICS) code and industry description and are available at http://www.sba.gov/idc/groups/public/documents/sba_homepage/serv_sstd_tablepdf.pdf. Vented home heating equipment and pool heater
manufacturing are classified under NAICS 333414--``Heating Equipment
(except Warm Air Furnaces) Manufacturing.'' The SBA sets a threshold of
500 employees or less for an entity to be considered as a small
business for both of these categories.\8\
---------------------------------------------------------------------------
\8\ In the December 2009 NOPR, DOE mistakenly listed gas-fired
pool heater manufacturing under NAICS code 335228. 74 FR 65852,
65984 (Dec. 11, 2009). The correct classification for pool heater
manufacturing is NAICS 333414. Both NAICS categories have the same
500 employee limit.
---------------------------------------------------------------------------
To estimate the number of companies that could be small business
manufacturers of products covered by this rulemaking, DOE conducted a
market survey using available public information to identify potential
small manufacturers. DOE's research involved reviewing several industry
trade association membership directories (e.g., AHRI \9\), product
databases (e.g., AHRI \10\ and CEC \11\ databases), individual company
Web sites, and marketing research tools (e.g., Hoovers \12\ reports) to
create a list of all domestic small business manufacturers of heating
products covered by this rulemaking. DOE identified 2 manufacturers of
vented home heating equipment and 5 manufacturers of pool heaters
(including electric heat pump pool heater manufacturers) that can be
considered small businesses.
---------------------------------------------------------------------------
\9\ See http://www.ahrinet.org/ahri+members.aspx.
\10\ See http://www.ahridirectory.org/ahriDirectory/pages/home.aspx.
\11\ See http://www.appliances.energy.ca.gov/.
\12\ See http://www.hoovers.com/.
---------------------------------------------------------------------------
3. Description and Estimate of Compliance Requirements
a. Vented Home Heating Equipment
DOE amends its test procedure for vented home heating equipment to
incorporate by reference the most recent or appropriate version of six
industry standards to replace the outdated standards referenced in the
existing DOE test procedure as described in section III. C.2. of this
document. These updates result in no material change to DOE's test
procedure for vented home heating equipment.
In addition, DOE amends the test procedure to include a test method
to determine the AFUE of vented home heating equipment that use
condensing technology. The AFUE test method may add a modest cost to
testing for manufacturers of such products. The test can be conducted
in the same test facility and simultaneous to the former AFUE test
requirements, but some additional testing and calculation is required
to accurately determine AFUE. Specifically, this test procedure
requires a condensate collection test to be conducted on vented heaters
utilizing condensing technologies. The duration of the condensate
collection test time would be 30 minutes for steady-state testing, if
conducted subsequent to all other steady-state testing and 1-2 hours
for cyclic testing. In some cases, only steady-state testing is
required (i.e., all manually-controlled vented heaters and those vented
heaters not utilizing the optional tracer gas procedures). In such
cases, the condensation test provisions would not require any
additional time because the test procedure allows for the condensate
collection to be conducted simultaneously with the other steady-state
test requirements of section 3.1. Vented home heaters are tested
utilizing the optional tracer gas procedures and are required to
conduct both steady-state and cyclic condensate collection procedures.
DOE estimates that the additional testing for condensing units adds a
maximum of three hours to the AFUE test. DOE estimates that lab
technicians on average, are paid at a rate of $27.50 per hour.\13\
Therefore, DOE estimates the added cost will be a maximum of $82.50 per
test unit, which is modest in comparison to the overall cost of product
development and certification.
---------------------------------------------------------------------------
\13\ ``Lab Technician Salary.'' Job Search. N.p., n.d. Web. 22
Aug. 2014. http://www.indeed.com/salary/Lab-Technician.html.
---------------------------------------------------------------------------
b. Pool Heaters
DOE amends its test procedure for pool heaters to adopt provisions
for testing electric pool heaters, including electric heat pump pool
heaters. In addition, DOE amends the test procedure to incorporate by
reference AHRI 1160 and ASHRAE 146 for both electric resistance and
electric heat pump pool heaters. These pool heaters are not currently
regulated by DOE, but DOE's research showed that all identified
domestic small business manufacturers of electric heat pump pool
heaters already rate COP and capacity according to the rating
conditions specified in AHRI 1160 and typically at an additional rating
point outside of the AHRI 1160 test conditions. In addition, DOE notes
that ANSI/ASHRAE Standard 90.1-2010 contains efficiency levels for
electric heat pump pool heaters and specifies AHRI 1160 as the test
method. Several States (e.g., Florida, California) also have minimum
efficiency requirements for electric heat pump pool heaters, which is
another factor that may drive manufacturers to rate their products for
efficiency. Because manufacturers of electric heat pump pool heaters
are already rating their products using AHRI 1160 due to the ANSI/
ASHRAE Standard 90.1-2010 requirements and State efficiency
requirements, DOE does not believe that including an electric heat pump
pool heater test method that references the industry standard will
cause significant, if any, additional burden to manufacturers. The
additional burdens for measuring standby consist of one 60 minute
period where the electricity use is metered. For a technician making an
average of $37.50 per hour, this results in an added cost of $37.50,
which is not significant in comparison to the overall cost of product
development and certification.
For electric resistance pool heaters, the test method in ASHRAE
146--is comparable to that for gas-fired and oil-fired pool heaters in
the existing DOE test method. Since the new test method in this final
rule is essentially the same as the existing test method used by the
industry and incorporated by reference, it is not expected that the new
rule will add to the burden of manufacturers of electric resistance
pool heaters.
[[Page 803]]
4. Duplication, Overlap, and Conflict With Other Rules and Regulations
DOE is not aware of any rules or regulations that duplicate,
overlap, or conflict with the rule being adopted today.
5. Significant Alternatives to the Rule
As noted earlier in the preamble, this rule is largely based upon
the industry testing procedures already in place for vented home
heating equipment and pool heaters. DOE believes the amendments will be
useful for both consumers and industry, and are consistent with the
Department's goals and statutory requirements, while also minimizing
the economic burden on manufacturers. After a full review of the test
procedure and comments received from the NOPR and public meeting, DOE
has incorporated changes to the vented home heating equipment test
procedure as discussed in section III. and listed in the regulatory
text, including adding a condensation collection test, adding a test to
determine default draft factor eligibility, and updating references to
the most recent or appropriate version. DOE has incorporated changes to
the pool heater test procedure as listed in the regulatory text
including adding test provisions for electric resistance and electric
heat pump pool heaters and incorporating a new metric, integrated
thermal efficiency, which incorporates standby losses. DOE has
determined that there is no further need for alternative test methods
for this test procedure.
D. Review Under the Paperwork Reduction Act of 1995
Manufacturers of vented home heating equipment and pool heaters
must certify to DOE that their products comply with all applicable
energy conservation standards. In certifying compliance, manufacturers
must test their products according to the DOE test procedures for
vented home heating equipment and pool heaters, including any
amendments adopted for those test procedures, on the date that
compliance is required. DOE has established regulations for the
certification and recordkeeping requirements for all covered consumer
products and commercial equipment, including vented home heating
equipment and pool heaters. 76 FR 12422 (March 7, 2011). The
collection-of-information requirement for certification and
recordkeeping is subject to review and approval by OMB under the
Paperwork Reduction Act (PRA). This requirement has been approved by
OMB under OMB control number 1910-1400. Public reporting burden for the
certification is estimated to average 30 hours per response, including
the time for reviewing instructions, searching existing data sources,
gathering and maintaining the data needed, and completing and reviewing
the collection of information.
Notwithstanding any other provision of the law, no person is
required to respond to, nor shall any person be subject to a penalty
for failure to comply with, a collection of information subject to the
requirements of the PRA, unless that collection of information displays
a currently valid OMB Control Number.
E. Review Under the National Environmental Policy Act of 1969
In this final rule, DOE is amending the test procedure that it
expects will be used to develop and implement future energy
conservation standards for vented home heating equipment and pool
heaters. DOE has determined that this rule falls into a class of
actions that are categorically excluded from review under the National
Environmental Policy Act of 1969 (42 U.S.C. 4321 et seq.) and DOE's
implementing regulations at 10 CFR part 1021. Specifically, this final
rule amends the existing test procedures without affecting the amount,
quality, or distribution of energy usage, and, therefore, would not
result in any environmental impacts. Thus, this rulemaking is covered
by Categorical Exclusion A5 under 10 CFR part 1021, subpart D, which
applies to any rulemaking that interprets or amends an existing rule
without changing the environmental effect of that rule. Accordingly,
neither an environmental assessment nor an environmental impact
statement is required.
F. Review Under Executive Order 13132
Executive Order 13132, ``Federalism,'' 64 FR 43255 (August 10,
1999), imposes certain requirements on Federal agencies formulating and
implementing policies or regulations that preempt State law or that
have Federalism implications. The Executive Order requires agencies to
examine the constitutional and statutory authority supporting any
action that would limit the policymaking discretion of the States, and
to carefully assess the necessity for such actions. The Executive Order
also requires agencies to have an accountable process to ensure
meaningful and timely input by State and local officials in the
development of regulatory policies that have Federalism implications.
On March 14, 2000, DOE published a statement of policy describing the
intergovernmental consultation process it will follow in the
development of such regulations. 65 FR 13735. DOE has examined this
final rule and has determined that it will not have a substantial
direct effect on the States, on the relationship between the national
government and the States, or on the distribution of power and
responsibilities among the various levels of government. EPCA governs
and prescribes Federal preemption of State regulations as to energy
conservation for the products that are the subject of this final rule.
States can petition DOE for exemption from such preemption to the
extent, and based on criteria, set forth in EPCA. (42 U.S.C. 6297(d))
No further action is required by Executive Order 13132.
G. Review Under Executive Order 12988
Regarding the review of existing regulations and the promulgation
of new regulations, section 3(a) of Executive Order 12988, ``Civil
Justice Reform,'' 61 FR 4729 (Feb. 7, 1996), imposes on Federal
agencies the general duty to adhere to the following requirements: (1)
Eliminate drafting errors and ambiguity; (2) write regulations to
minimize litigation; (3) provide a clear legal standard for affected
conduct rather than a general standard; and (4) promote simplification
and burden reduction. Regarding the review required by section 3(a),
section 3(b) of Executive Order 12988 specifically requires that
Executive agencies make every reasonable effort to ensure that the
regulation: (1) Clearly specifies the preemptive effect, if any; (2)
clearly specifies any effect on existing Federal law or regulation; (3)
provides a clear legal standard for affected conduct while promoting
simplification and burden reduction; (4) specifies the retroactive
effect, if any; (5) adequately defines key terms; and (6) addresses
other important issues affecting clarity and general draftsmanship
under any guidelines issued by the Attorney General. Section 3(c) of
Executive Order 12988 requires Executive agencies to review regulations
in light of applicable standards in sections 3(a) and 3(b) to determine
whether they are met or it is unreasonable to meet one or more of them.
DOE has completed the required review and determined that, to the
extent permitted by law, this final rule meets the relevant standards
of Executive Order 12988.
H. Review Under the Unfunded Mandates Reform Act of 1995
Title II of the Unfunded Mandates Reform Act of 1995 (UMRA)
requires
[[Page 804]]
each Federal agency to assess the effects of Federal regulatory actions
on State, local, and Tribal governments and the private sector. Public
Law 104-4, sec. 201 (codified at 2 U.S.C. 1531). For regulatory actions
likely to result in a rule that may cause the expenditure by State,
local, and Tribal governments, in the aggregate, or by the private
sector of $100 million or more in any one year (adjusted annually for
inflation), section 202 of UMRA requires a Federal agency to publish a
written statement that estimates the resulting costs, benefits, and
other effects on the national economy. (2 U.S.C. 1532(a), (b)) The UMRA
also requires a Federal agency to develop an effective process to
permit timely input by elected officers of State, local, and Tribal
governments on a ``significant intergovernmental mandate,'' and
requires an agency plan for giving notice and opportunity for timely
input to potentially affected small governments before establishing any
requirements that might significantly or uniquely affect them. On March
18, 1997, DOE published a statement of policy on its process for
intergovernmental consultation under UMRA. 62 FR 12820. (This policy is
also available at www.gc.doe.gov/gc/office-general-counsel.) This final
rule, which modifies the test procedures for vented home heating
equipment and for pool heaters, contains neither an intergovernmental
mandate, nor a mandate that may result in the expenditure by State,
local, and Tribal governments, in the aggregate, or by the private
sector, of $100 million or more in any year. Accordingly, no further
assessment or analysis is required under UMRA.
I. Review Under the Treasury and General Government Appropriations Act,
1999
Section 654 of the Treasury and General Government Appropriations
Act, 1999 (Pub. L. 105-277) requires Federal agencies to issue a Family
Policymaking Assessment for any rule that may affect family well-being.
This final rule concerning test procedures would not have any impact on
the autonomy or integrity of the family as an institution. Accordingly,
DOE has concluded that it is not necessary to prepare a Family
Policymaking Assessment.
J. Review Under Executive Order 12630
Pursuant to Executive Order 12630, ``Governmental Actions and
Interference with Constitutionally Protected Property Rights,'' 53 FR
8859 (March 18, 1988), DOE has determined that this final rule will not
result in any takings that might require compensation under the Fifth
Amendment to the U.S. Constitution.
K. Review Under Treasury and General Government Appropriations Act,
2001
Section 515 of the Treasury and General Government Appropriations
Act, 2001 (44 U.S.C. 3516 note) provides for Federal agencies to review
most disseminations of information to the public under information
quality guidelines established by each agency pursuant to general
guidelines issued by OMB. OMB's guidelines were published at 67 FR 8452
(Feb. 22, 2002), and DOE's guidelines were published at 67 FR 62446
(Oct. 7, 2002). DOE has reviewed this final rule under the OMB and DOE
guidelines and has concluded that it is consistent with applicable
policies in those guidelines.
L. Review Under Executive Order 13211
Executive Order 13211, ``Actions Concerning Regulations That
Significantly Affect Energy Supply, Distribution, or Use,'' 66 FR 28355
(May 22, 2001), requires Federal agencies to prepare and submit to OIRA
at OMB, a Statement of Energy Effects for any significant energy
action. A ``significant energy action'' is defined as any action by an
agency that promulgates or is expected to lead to promulgation of a
final rule, and that: (1) Is a significant regulatory action under
Executive Order 12866, or any successor order; and (2) is likely to
have a significant adverse effect on the supply, distribution, or use
of energy; or (3) is designated by the Administrator of OIRA as a
significant energy action. For any proposed significant energy action,
the agency must give a detailed statement of any adverse effects on
energy supply, distribution, or use should the proposal be implemented,
and of reasonable alternatives to the action and their expected
benefits on energy supply, distribution, and use.
This regulatory action to amend the test procedure for measuring
the energy efficiency of vented home heating equipment and pool heaters
is not a significant regulatory action under Executive Order 12866 or
any successor order. Moreover, it will not have a significant adverse
effect on the supply, distribution, or use of energy, nor has it been
designated as a significant energy action by the Administrator of OIRA.
Therefore, it is not a significant energy action, and, accordingly, DOE
has not prepared a Statement of Energy Effects for this rulemaking.
M. Review Under Section 32 of the Federal Energy Administration Act of
1974
Under section 301 of the Department of Energy Organization Act
(Pub. L. 95-91; 42 U.S.C. 7101 et seq.), DOE must comply with all laws
applicable to the former Federal Energy Administration, including
section 32 of the Federal Energy Administration Act of 1974 (Pub. L.
93-275), as amended by the Federal Energy Administration Authorization
Act of 1977 (Pub. L. 95-70). (15 U.S.C. 788; FEAA) Section 32
essentially provides, in relevant part, that, where a proposed rule
authorizes or requires use of commercial standards, the notice of
proposed rulemaking must inform the public of the use and background of
such standards. In addition, section 32(c) requires DOE to consult with
the Attorney General and the Chairman of the Federal Trade Commission
(FTC) concerning the impact of the commercial or industry standards on
competition.
This final rule incorporates testing methods contained in the
following commercial standards: (1) ANSI/ASHRAE Standard 103-2007,
``Method of Test for Annual Fuel Utilization Efficiency of Residential
Central Furnaces and Boilers''; (2) ANSI Z21.86-2008, ``Vented Gas-
Fired Space Heating Appliances''; (3) ASTM D2156-09, ``Standard Test
Method for Smoke Density in Flue Gases from Burning Distillate Fuels'';
(4) UL 729-2003, ``Standard for Safety for Oil-Fired Floor Furnaces'';
(5) UL 730-2003, ``Standard for Safety for Oil-Fired Wall Furnaces'';
(6) UL 896-1993, ``Standard for Safety for Oil-Burning Stoves''; (7)
AHRI 1160-2009, ``Performance Rating of Heat Pump Pool Heaters''; and
(8) ANSI/ASHRAE Standard 146-2011, ``Method of Testing and Rating Pool
Heaters.'' While the test procedures are not exclusively based on these
standards, components of the test procedures are adopted directly from
these standards without amendment. The Department has evaluated these
standards and is unable to conclude whether they fully comply with the
requirements of section 32(b) of the FEAA, (i.e., that they were
developed in a manner that fully provides for public participation,
comment, and review). DOE has consulted with the Attorney General and
the Chairman of the FTC concerning the impact on competition of
requiring manufacturers to use the test methods contained in these
standards, and neither recommended against incorporation of these
standards.
[[Page 805]]
N. Congressional Notification
As required by 5 U.S.C. 801, DOE will report to Congress on the
promulgation of this rule before its effective date. The report will
state that it has been determined that the rule is not a ``major rule''
as defined by 5 U.S.C. 804(2).
V. Approval of the Office of the Secretary
The Secretary of Energy has approved publication of this final
rule.
List of Subjects in 10 CFR Part 430
Administrative practice and procedure, Confidential business
information, Energy conservation, Household appliances, Imports,
Incorporation by reference, Intergovernmental relations, Small
businesses.
Issued in Washington, DC, on December 23, 2014.
Kathleen B. Hogan,
Deputy Assistant Secretary for Energy Efficiency, Energy Efficiency and
Renewable Energy.
For the reasons stated in the preamble, DOE amends part 430 of
Chapter II, Subchapter D of Title 10, Code of Federal Regulations, as
set forth below:
PART 430--ENERGY CONSERVATION PROGRAM FOR CONSUMER PRODUCTS
0
1. The authority citation for part 430 continues to read as follows:
Authority: 42 U.S.C. 6291-6309; 28 U.S.C. 2461 note.
0
2. Section 430.2 is amended by revising the definition of ``vented home
heating equipment or vented heater'' to read as follows:
Sec. 430.2 Definitions.
* * * * *
Vented home heating equipment or vented heater means a class of
home heating equipment, not including furnaces, designed to furnish
warmed air to the living space of a residence, directly from the
device, without duct connections (except that boots not to exceed 10
inches beyond the casing may be permitted) and includes: vented wall
furnace, vented floor furnace, and vented room heater.
* * * * *
0
3. Section 430.3 is amended by:
0
a. Redesignating paragraphs (d)(18) as (d)(19), (t) as (v), and (i)
through (s) as (j) through (t), respectively; and
0
b. Adding paragraphs (b)(2), (d)(18), (f)(13), (i), and (u).
0
c. Revising paragraph (f)(11).
The revisions and additions read as follows:
Sec. 430.3 Materials incorporated by reference.
* * * * *
(b) * * *
(2) AHRI Standard 1160-2009 (``AHRI 1160''), Performance Rating of
Heat Pump Pool Heaters, 2009, IBR approved for appendix P to subpart B.
* * * * *
(d) * * *
(18) ANSI Z21.86-2008, (``ANSI Z21.86''), Vented Gas-Fired Space
Heating Appliances, Fifth Edition, approved March 28, 2008, IBR
approved for appendix O to subpart B.
* * * * *
(f) * * *
(11) ANSI/ASHRAE Standard 103-2007, (``ASHRAE 103-2007''), Method
of Testing for Annual Fuel Utilization Efficiency of Residential
Central Furnaces and Boilers, ANSI approved March 25, 2008, IBR
approved for appendices O and AA to subpart B.
* * * * *
(13) ANSI/ASHRAE Standard 146-2011 (``ASHRAE 146''), Method of
Testing and Rating Pool Heaters, ASHRAE approved February 2, 2011, IBR
approved for appendix P to subpart B.
* * * * *
(i) ASTM. American Society for Testing and Materials International,
100 Barr Harbor Drive, P.O. Box C700, West Conshohocken, PA 19428-2959
(www.astm.org)
(1) ASTM D2156-09, (``ASTM D2156''), Standard Test Method for Smoke
Density in Flue Gases from Burning Distillate Fuels, ASTM approved
December 1, 2009, IBR approved for appendix O to subpart B.
(2) [Reserved]
* * * * *
(u) UL. Underwriters Laboratories, Inc., 2600 NW. Lake Rd., Camas,
WA 98607-8542 (www.UL.com)
(1) UL 729-2003 (``UL 729''), Standard for Safety for Oil-Fired
Floor Furnaces, Sixth Edition, dated August 29, 2003, including
revisions through April 22, 2010, IBR approved for appendix O to
subpart B.
(2) UL 730-2003 (``UL 730''), Standard for Safety for Oil-Fired
Wall Furnaces, Fifth Edition, dated August 29, 2003, including
revisions through April 22, 2010, IBR approved for appendix O to
subpart B.
(3) UL 896-1993 (``UL 896''), Standard for Safety for Oil-Burning
Stoves, Fifth Edition, dated July 29, 1993, including revisions through
May 7, 2010, IBR approved for appendix O to subpart B.
0
4. Section 430.23 is amended by revising paragraphs (o) and (p) to read
as follows:
Sec. 430.23 Test procedures for the measurement of energy and water
consumption.
* * * * *
(o) Vented home heating equipment. (1) When determining the annual
fuel utilization efficiency (AFUE) of vented home heating equipment
(see the note at the beginning of appendix O), expressed in percent
(%), calculate AFUE in accordance with section 4.1.17 of appendix O of
this subpart for vented heaters without either manual controls or
thermal stack dampers; in accordance with section 4.2.6 of appendix O
of this subpart for vented heaters equipped with manual controls; or in
accordance with section 4.3.7 of appendix O of this subpart for vented
heaters equipped with thermal stack dampers.
(2) When estimating the annual operating cost for vented home
heating equipment, calculate the sum of:
(i) The product of the average annual fuel energy consumption, in
Btus per year for natural gas, propane, or oil fueled vented home
heating equipment, determined according to section 4.6.2 of appendix O
of this subpart, and the representative average unit cost in dollars
per Btu for natural gas, propane, or oil, as appropriate, as provided
pursuant to section 323(b)(2) of the Act; plus
(ii) The product of the average annual auxiliary electric energy
consumption in kilowatt-hours per year determined according to section
4.6.3 of appendix O of this subpart, and the representative average
unit cost in dollars per kilowatt-hours as provided pursuant to section
323(b)(2) of the Act. Round the resulting sum to the nearest dollar per
year.
(3) When estimating the operating cost per million Btu output for
gas or oil vented home heating equipment with an auxiliary electric
system, calculate the product of:
(i) The quotient of one million Btu divided by the sum of:
(A) The product of the maximum fuel input in Btus per hour as
determined in sections 3.1.1 or 3.1.2 of appendix O of this subpart
times the annual fuel utilization efficiency in percent as determined
in sections 4.1.17, 4.2.6, or 4.3.7 of this appendix (as appropriate)
divided by 100, plus
(B) The product of the maximum electric power in watts as
determined in section 3.1.3 of appendix O of this subpart times the
quantity 3.412; and
(ii) The sum of:
(A) the product of the maximum fuel input in Btus per hour as
determined in
[[Page 806]]
sections 3.1.1 or 3.1.2 of this appendix times the representative unit
cost in dollars per Btu for natural gas, propane, or oil, as
appropriate, as provided pursuant to section 323(b)(2) of the Act; plus
(B) the product of the maximum auxiliary electric power in
kilowatts as determined in section 3.1.3 of appendix O of this subpart
times the representative unit cost in dollars per kilowatt-hour as
provided pursuant to section 323(b)(2) of the Act. Round the resulting
quantity to the nearest 0.01 dollar per million Btu output.
(p) Pool heaters. (1) Determine the thermal efficiency
(Et) of a pool heater expressed as a percent (%) in
accordance with section 5.1 of appendix P to this subpart.
(2) Determine the integrated thermal efficiency (TEI) of
a pool heater expressed as a percent (%) in accordance with section 5.4
of appendix P to this subpart.
(3) When estimating the annual operating cost of pool heaters,
calculate the sum of:
(i) The product of the average annual fossil fuel energy
consumption, in Btus per year, determined according to section 5.2 of
appendix P to this subpart, and the representative average unit cost in
dollars per Btu for natural gas or oil, as appropriate, as provided
pursuant to section 323(b)(2) of the Act; plus
(ii) The product of the average annual electrical energy
consumption in kilowatt-hours per year determined according to section
5.3 of appendix P to this subpart and converted to kilowatt-hours using
a conversion factor of 3412 Btus = 1 kilowatt-hour, and the
representative average unit cost in dollars per kilowatt-hours as
provided pursuant to section 323(b)(2) of the Act. Round the resulting
sum to the nearest dollar per year.
* * * * *
0
5. Appendix O to subpart B of part 430 is amended by:
0
a. Revising the note at the beginning of appendix O;
0
b. Redesignating section 1.33 (following 1.37) as 1.39;
0
c. Redesignating sections 1.5 through 1.37 as 1.6 through 1.38;
0
d. Adding section 1.5;
0
e. Revising sections 1.27, 2.1.1, 2.1.2, 2.1.3, 2.2.2;
0
f. Adding section 2.2.4;
0
g. Revising section 2.3.1, 2.3.2, 2.3.3, 2.3.4, 2.4.2, 2.5.1;
0
h. Removing in section 2.6.1 in the last paragraph ``ANSI Z21.49-1975,
section 2.14.'' and adding in its place ``Part VIII section 8.7 of ANSI
Z21.86 (incorporated by reference, see Sec. 430.3)'';
0
i. Removing in section 2.6.2 in the first paragraph ``Figure 34.4 of UL
730-1974, or Figures 35.1 and 35.2 of UL 729-1976'' and adding in its
place ``Figure 36.4 of UL 730, or Figure 38.1 and 38.2 of UL 729
(incorporated by reference, see Sec. 430.3)'' and removing in the last
paragraph ``sections 35.12 through 35.17 of UL 730-1974'' and adding in
its place ``sections 37.5.8 through 37.5.18 of UL 730 (incorporated by
reference, see Sec. 430.3)'';
0
j. Revising section 2.9;
0
k. Adding section 2.11;
0
l. Revising sections 3.1.1, 3.1.2, 3.2, 3.3;
0
m. Adding sections 3.6.1, 3.6.2, 3.6.2.1, 3.6.2.2, 3.6.2.2.1,
3.6.2.2.2, 3.6.2.3, 3.6.2.4, 3.6.2.4.1, 3.6.2.4.2, 3.6.2.4.3, 3.8,
3.8.1, 3.8.2;
0
n. Revising sections 4.1, 4.1.2, 4.1.3, 4.1.6;
0
o. Adding sections 4.1.6.1, 4.1.6.2, 4.1.6.3, and 4.1.6.4;
0
p. Revising sections 4.1.8, 4.1.10, 4.1.15, 4.1.16, 4.2.1, 4.2.2,
4.2.4.1, 4.3, 4.3.1, 4.3.2, 4.3.3, 4.3.4, 4.3.5, 4.3.6, 4.5.1, 4.5.2,
4.5.3 and Table 1.
These additions and revisions read as follows:
Appendix O to Subpart B of Part 430--Uniform Test Method for Measuring
the Energy Consumption of Vented Home Heating Equipment
Note: On and after July 6, 2015, any representations made with
respect to the energy use or efficiency of vented home heating
equipment must be made in accordance with the results of testing
pursuant to this appendix. On and after this date, if a manufacturer
makes representations of standby mode and off mode energy
consumption, then testing must also include the provisions of this
appendix related to standby mode and off mode energy consumption.
Until July 6, 2015, manufacturers must test vented home heating
equipment in accordance with this appendix or appendix O as it
appeared at 10 CFR part 430, subpart B revised as of January 1,
2014. Any representations made with respect to the energy use or
efficiency of such vented home heating equipment must be made in
accordance with whichever version is selected. DOE notes that,
because testing under this appendix O is required as of July 6,
2015, manufacturers may wish to begin using this test procedure
immediately.
* * * * *
1.5 ``Condensing vented heater'' means a vented heater that,
during the laboratory tests prescribed in this appendix, condenses
part of the water vapor in the flue gases.
* * * * *
1.27 ``Single-stage thermostat'' means a thermostat that cycles
a burner at the maximum heat input rate and off.
* * * * *
2.1.1 Vented wall furnaces (including direct vent systems).
Install non-direct vent gas fueled vented wall furnaces as specified
in section 8.1.3 and figure 7 or figure 10 of ANSI Z21.86
(incorporated by reference, see Sec. 430.3). Install direct vent
gas fueled vented wall furnaces as specified in section 6.1.3 and
figure 6 of ANSI Z21.86 (incorporated by reference, see Sec.
430.3). Install oil fueled vented wall furnaces as specified in
section 36.1 of UL 730 (incorporated by reference, see Sec. 430.3).
2.1.2 Vented floor furnaces. Install vented floor furnaces for
test as specified in section 38.1 of UL 729 (incorporated by
reference, see Sec. 430.3).
2.1.3 Vented room heaters. Install vented room heaters for test
in accordance with the manufacturer's installation and operations
(I&O) manual provided with the unit.
* * * * *
2.2.2 Oil fueled vented home heating equipment (excluding direct
vent systems). Use flue connections for oil fueled vented floor
furnaces as specified in section 38.2 of UL 729, sections 36.2 of UL
730 for oil fueled vented wall furnaces, and sections 37.1.2 and
37.1.3 of UL 896 (all incorporated by reference, see Sec. 430.3)
for oil fueled vented room heaters.
* * * * *
2.2.4 Condensing vented heater, additional flue requirements.
The flue pipe installation must not allow condensate formed in the
flue pipe to flow back into the unit. An initial downward slope from
the unit's exit, an offset with a drip leg, annular collection
rings, or drain holes must be included in the flue pipe installation
without disturbing normal flue gas flow. Flue gases should not flow
out of the drain with the condensate. For condensing vented heaters
that do not include means for collection of condensate, a means to
collect condensate must be supplied by the test lab for the purposes
of testing.
* * * * *
2.3.1 Natural gas. For a gas fueled vented heater, maintain the
gas supply to the unit under test at a normal inlet test pressure
immediately ahead of all controls at 7 to 10 inches water column.
Maintain the regulator outlet pressure at normal test pressure
approximately at that recommended by the manufacturer. Use natural
gas having a specific gravity of approximately 0.65 and a higher
heating value within 5 percent of 1,025 Btu's per
standard cubic foot. Determine the actual higher heating value in
Btu's per standard cubic foot for the natural gas to be used in the
test with an error no greater than one percent.
2.3.2 Propane gas. For a propane-gas fueled vented heater,
maintain the gas supply to the unit under test at a normal inlet
pressure of 11 to 13 inches water column and a specific gravity of
approximately 1.53. Maintain the regulator outlet pressure, on units
so equipped, approximately at that recommended by the manufacturer.
Use propane having a specific gravity of approximately 1.53 and a
higher heating value within 5 percent of 2,500 Btu's per
standard cubic foot. Determine the actual higher heating value in
Btu's per standard
[[Page 807]]
cubic foot for the propane to be used in the test
2.3.3 Other test gas. Use other test gases with characteristics
as described in Table 4 of ANSI Z21.86 (incorporated by reference,
see Sec. 430.3). Use gases with a measured higher heating value
within 5 percent of the values specified in the Tables
section of ANSIZ21.86. Determine the actual higher heating value of
the gas used in the test with an error no greater than one percent.
2.3.4 Oil supply. For an oil fueled vented heater, use No. 1
fuel oil (kerosene) for vaporizing-type burners and either No. 1 or
No. 2 fuel oil, as specified by the manufacturer in the I&O manual
provided with the unit, for mechanical atomizing type burners. Use
test fuel conforming to the specifications given in Tables 2 and 3
of ASHRAE 103-2007 (incorporated by reference, see Sec. 430.3).
Measure the higher heating value of the test fuel within 1 percent.
* * * * *
2.4.2 Oil burner adjustments. Adjust the burners of oil fueled
vented heaters to give the CO2 reading recommended by the
manufacturer and an hourly Btu input, during the steady-state
performance test described below, which is within 2
percent of the heater manufacturer's specified normal hourly Btu
input rating. On units employing a power burner, do not allow smoke
in the flue to exceed a No. 1 smoke during the steady-state
performance test as measured by the procedure in ASTM D2156
(incorporated by reference, see Sec. 430.3). If, on units employing
a power burner, the smoke in the flue exceeds a No. 1 smoke during
the steady-state test, readjust the burner to give a lower smoke
reading, and, if necessary a lower CO2 reading, and start
all tests over. Maintain the average draft over the fire and in the
flue during the steady-state performance test at that recommended by
the manufacturer within 0.005 inches of water gauge. Do
not make additional adjustments to the burner during the required
series of performance tests. The instruments and measuring apparatus
for this test are described in section 6 and shown in Figure 8 of
ASHRAE 103-2007 (incorporated by reference, see Sec. 430.3).
* * * * *
2.5.1 Forced air vented wall furnaces (including direct vent
systems). During testing, maintain the air flow through the heater
as specified by the manufacturer in the I&O manual provided with the
unit and operate the vented heater with the outlet air temperature
between 80[emsp14][deg]F and 130[emsp14][deg]F above room
temperature. If adjustable air discharge registers are provided,
adjust them so as to provide the maximum possible air restriction.
Measure air discharge temperature as specified in section 8.7 of
ANSI Z21.86 (incorporated by reference, see Sec. 430.3).
* * * * *
2.9 Room ambient temperature. The room ambient temperature shall
be the arithmetic average temperature of the test area, determined
by measurement with four No. 24 AWG bead-type thermocouples with
junctions shielded against radiation, located approximately at 90-
degree positions on a circle circumscribing the heater or heater
enclosure under test, in a horizontal plane approximately at the
vertical midpoint of the appliance or test enclosure, and with the
junctions approximately 24 inches from sides of the heater or test
enclosure and located so as not to be affected by other than room
air.
The value TRA is the room ambient temperature
measured at the last of the three successive readings taken 15
minutes apart described in section 3.1.1 or 3.1.2 as applicable.
During the time period required to perform all the testing and
measurement procedures specified in section 3.0 of this appendix,
maintain the room ambient temperature within 5[emsp14][deg]F (2.8 C) of the value
TRA. At no time during these tests shall the room ambient
temperature exceed 100[emsp14][deg]F (37.8 C) or fall below
65[emsp14][deg]F (18.3 C).
Locate a thermocouple at each elevation of draft relief inlet
opening and combustion air inlet opening at a distance of
approximately 24 inches from the inlet openings. The temperature of
the air for combustion and the air for draft relief shall not differ
more than 5[emsp14][deg]F from the room ambient
temperature as measured above at any point in time. This requirement
for combustion air inlet temperature does not need to be met once
the burner is shut off during the testing described in sections 3.3
and 3.6 of this appendix.
* * * * *
2.11 Equipment with multiple control modes. For equipment that
has both manual and automatic thermostat control modes, test the
unit according to the procedure for its automatic control mode, i.e.
single-stage, two stage, or step-modulating.
* * * * *
3.1.1 Gas fueled vented home heating equipment (including direct
vent systems). Set up the vented heater as specified in sections
2.1, 2.2, and 2.3 of this appendix. The draft diverter shall be in
the normal open condition and the stack shall not be insulated.
(Insulation of the stack is no longer required for the vented heater
test.) Begin the steady-state performance test by operating the
burner and the circulating air blower, on units so equipped, with
the adjustments specified by sections 2.4.1 and 2.5 of this
appendix, until steady-state conditions are attained as indicated by
three successive readings taken 15 minutes apart with a temperature
variation of not more than 3[emsp14][deg]F (1.7 C) in
the stack gas temperature for vented heaters equipped with draft
diverters or 5[emsp14][deg]F (2.8 C) in the flue gas
temperature for vented heaters equipped with either draft hoods or
direct vent systems. The measurements described in this section are
to coincide with the last of these 15 minute readings.
On units employing draft diverters, measure the room temperature
(TRA) as described in section 2.9 of this appendix and
measure the steady-state stack gas temperature (TS,SS)
using the nine thermocouples located in the 5 foot test stack as
specified in section 2.6.1 of this appendix. Secure a sample of the
stack gases in the plane where TS,SS is measured or
within 3.5 feet downstream of this plane. Determine the
concentration by volume of carbon dioxide (XCO2S) present
in the dry stack gas. If the location of the gas sampling differs
from the temperature measurement plane, there shall be no air leaks
through the stack between these two locations.
On units employing draft hoods or direct vent systems, measure
the room temperature (TRA) as described in section 2.9 of
this appendix and measure the steady-state flue gas temperature
(TF,SS), using the nine thermocouples located in the flue
pipe as described in section 2.6.1 of this appendix. Secure a sample
of the flue gas in the plane of temperature measurement and
determine the concentration by volume of CO2
(XCO2F) present in dry flue gas. In addition, for units
employing draft hoods, secure a sample of the stack gas in a
horizontal plane in the five foot test stack located one foot from
the test stack inlet; and determine the concentration by volume of
CO2 (XCO2S) present in dry stack gas.
Determine the steady-state heat input rate (Qin) including pilot
gas by multiplying the measured higher heating value of the test gas
by the steady-state gas input rate corrected to standard conditions
of 60[emsp14][deg]F and 30 inches of mercury. Use measured values of
gas temperature and pressure at the meter and the barometric
pressure to correct the metered gas flow rate to standard
conditions.
After the above test measurements have been completed on units
employing draft diverters, secure a sample of the flue gases at the
exit of the heat exchanger(s) and determine the concentration of
CO2 (XCO2F) present. In obtaining this sample
of flue gas, move the sampling probe around or use a sample probe
with multiple sampling ports in order to assure that an average
value is obtained for the CO2 concentration. For units
with multiple heat exchanger outlets, measure the CO2
concentration in a sample from each outlet to obtain the average
CO2 concentration for the unit. A manifold (parallel
connected sampling tubes) may be used to obtain this sample.
For heaters with single-stage thermostat control (wall mounted
electric thermostats), determine the steady-state efficiency at the
maximum fuel input rate as specified in section 2.4 of this
appendix.
For gas fueled vented heaters equipped with either two stage
control or step-modulating control, determine the steady-state
efficiency at the maximum fuel input rate and at the reduced fuel
input rate, as specified in section 2.4.1 of this appendix.
For manually controlled gas fueled vented heaters with various
input rates, determine the steady-state efficiency at a fuel input
rate that is within 5 percent of 50 percent of the
maximum rated fuel input rate as indicated on the nameplate of the
unit or in the manufacturer's installation and operation manual
shipped with the unit. If the heater is designed to use a control
that precludes operation at other than maximum rated fuel input rate
(single firing rate) determine the steady state efficiency at the
maximum rated fuel input rate only.
3.1.2 Oil fueled vented home heating equipment (including direct
vent systems). Set up and adjust the vented heater as specified in
sections 2.1, 2.2, and 2.3.4 of this appendix. Begin the steady-
state performance test by operating the burner and the
[[Page 808]]
circulating air blower, on units so equipped, with the adjustments
specified by sections 2.4.2 and 2.5 of this appendix, until steady-
state conditions are attained as indicated by a temperature
variation of not more than 5[emsp14][deg]F (2.8 C) in
the flue gas temperature in three successive readings taken 15
minutes apart. The measurements described in this section are to
coincide with the last of these 15 minutes readings.
For units equipped with power burners, do not allow smoke in the
flue to exceed a No. 1 smoke during the steady-state performance
test as measured by the procedure described in ASTM D2156
(incorporated by reference, see Sec. 430.3). Maintain the average
draft over the fire and in the breeching during the steady-state
performance test at that recommended by the manufacturer 0.005 inches of water gauge.
Measure the room temperature (TRA) as described in
section 2.9 of this appendix. Measure the steady-state flue gas
temperature (TF,SS) using nine thermocouples located in
the flue pipe as described in section 2.6.2 of this appendix. From
the plane where TF,SS was measured, collect a sample of
the flue gas and determine the concentration by volume of
CO2 (XCO2F) present in dry flue gas. Measure
and record the steady-state heat input rate (Qin).
For manually controlled oil fueled vented heaters, determine the
steady-state efficiency at a fuel input rate that is within 5 percent of 50 percent of the maximum fuel input rate; or, if
the design of the heater is such that the fuel input rate cannot be
set to 5 percent of 50 percent of the maximum rated fuel
input rate, determine the steady-state efficiency at the minimum
rated fuel input rate as measured in section 3.1.2 of this appendix
for manually controlled oil fueled vented heaters.
* * * * *
3.2 Jacket loss measurement. Conduct a jacket loss test for
vented floor furnaces. Measure the jacket loss (Lj) in
accordance with ASHRAE 103-2007 section 8.6 (incorporated by
reference, see Sec. 430.3), applying the provisions for furnaces
and not the provisions for boilers.
3.3 Measurement of the off-cycle losses for vented heaters
equipped with thermal stack dampers. Unless specified otherwise, the
thermal stack damper should be at the draft diverter exit collar.
Attach a five foot length of bare stack to the outlet of the damper.
Install thermocouples as specified in section 2.6.1 of this
appendix.
For vented heaters equipped with single-stage thermostats,
measure the off-cycle losses at the maximum fuel input rate. For
vented heaters equipped with two stage thermostats, measure the off-
cycle losses at the maximum fuel input rate and at the reduced fuel
input rate. For vented heaters equipped with step-modulating
thermostats, measure the off-cycle losses at the reduced fuel input
rate.
Allow the vented heater to heat up to a steady-state condition.
Feed a tracer gas at a constant metered rate into the stack directly
above and within one foot above the stack damper. Record tracer gas
flow rate and temperature. Measure the tracer gas concentration in
the stack at several locations in a horizontal plane through a
cross-section of the stack at a point sufficiently above the stack
damper to ensure that the tracer gas is well mixed in the stack.
Continuously measure the tracer gas concentration and
temperature during a 10-minute cool-down period. Shut the burner off
and immediately begin measuring tracer gas concentration in the
stack, stack temperature, room temperature, and barometric pressure.
Record these values as the midpoint of each one-minute interval
between burner shut-down and ten minutes after burner shut-down.
Meter response time and sampling delay time shall be considered in
timing these measurements.
* * * * *
3.6.1 Procedure for determining (DF and
DP) of vented home heating equipment with no measurable
airflow. On units whose design is such that there is no measurable
airflow through the combustion chamber and heat exchanger when the
burner(s) is off (as determined by the test procedure in section
3.6.2 of this appendix), DF and DP may be set
equal to 0.05.
3.6.2 Test Method to Determine Whether the Use of the Default
Draft Factors (DF and DP) of 0.05 is Allowed.
Manufacturers may use the following test protocol to determine
whether air flows through the combustion chamber and heat exchanger
when the burner(s) is off using a smoke stick device. The default
draft factor of 0.05 (as allowed per section 3.6.1 of this appendix)
may be used only for units determined pursuant to this protocol to
have no air flow through the combustion chamber and heat exchanger.
3.6.2.1 Test Conditions. Wait for two minutes following the
termination of the vented heater's on-cycle.
3.6.2.2 Location of Test Apparatus
3.6.2.2.1 After all air currents and drafts in the test chamber
have been minimized, position the operable smoke stick/pencil as
specified, based on the following equipment configuration: for
horizontal combustion air intakes, approximately 4 inches from the
vertical plane at the termination of the intake vent and 4 inches
below the bottom edge of the combustion air intake, or for vertical
combustion air intakes, approximately 4 inches horizontal from vent
perimeter at the termination of the intake vent and 4 inches down
(parallel to the vertical axis of the vent). In the instance where
the boiler combustion air intake is closer than 4 inches to the
floor, place the smoke device directly on the floor without impeding
the flow of smoke.
3.6.2.2.2 Monitor the presence and the direction of the smoke
flow.
3.6.2.3 Duration of Test. Continue monitoring the release of
smoke for no less than 30 seconds.
3.6.2.4 Test Results
3.6.2.4.1 During visual assessment, determine whether there is
any draw of smoke into the combustion air intake.
3.6.2.4.2 If absolutely no smoke is drawn into the combustion
air intake, the vented heater meets the requirements to allow use of
the default draft factor of 0.05 pursuant to Section 8.8.3 and/or
9.10 of ASHRAE 103-2007 (incorporated by reference, see Sec.
430.3).
3.6.2.4.3 If there is any smoke drawn into the intake, use of
default draft factor of 0.05 is prohibited. Proceed with the methods
of testing as prescribed in section 3.6 of this appendix, or select
the appropriate default draft factor from Table 1.
* * * * *
3.8 Condensing vented heaters--measurement of condensate under
steady-state and cyclic conditions. Attach condensate drain lines to
the vented heater as specified in the manufacturer's I&O manual
provided with the unit. The test unit shall be level prior to all
testing. A continuous downward slope of drain lines from the unit
shall be maintained. The drain lines must facilitate uninterrupted
flow of condensate during the test. The condensate collection
container must be glass or polished stainless steel to facilitate
removal of interior deposits. The collection container shall have a
vent opening to the atmosphere, be dried prior to each use, and be
at room ambient temperature. The humidity of the room air shall at
no time exceed 80 percent relative humidity. For condensing units
not designed for collecting and draining condensate, drain lines
must be provided during testing that meet the criteria set forth in
this section 3.8. Units employing manual controls and units not
tested under the optional tracer gas procedures of sections 3.3 and
3.6 of this appendix shall only conduct the steady-state condensate
collection test.
3.8.1 Steady-state condensate collection test. Begin steady-
state condensate collection concurrently with or immediately after
completion of the steady-state testing of section 3.1 of this
appendix. The steady-state condensate collection period shall be 30
minutes. Condensate mass shall be measured immediately at the end of
the collection period to minimize evaporation loss from the sample.
Record fuel input during the 30-minute condensate collection steady-
state test period. Measure and record fuel higher heating value
(HHV), temperature, and pressures necessary for determining fuel
energy input (Qc,ss). The fuel quantity and HHV shall be
measured with errors no greater than 1 percent.
Determine the mass of condensate for the steady-state test
(Mc,ss) in pounds by subtracting the tare container
weight from the total container and condensate weight measured at
the end of the 30-minute condensate collection test period. The
error associated with the mass measurement instruments shall not
exceed 0.5 percent of the quantity measured.
For units with step-modulating or two stage controls, the
steady-state condensate collection test shall be conducted at both
the maximum and reduced input rates.
3.8.2 Cyclic condensate collection tests. If existing controls
do not allow for cyclical operation of the tested unit, control
devices shall be installed to allow cyclical operation of the vented
heater. Run three consecutive test cycles. For each cycle, operate
the unit until flue gas temperatures at the end of each on-cycle,
rounded to the nearest whole number, are within 5[deg]F of each
other for two consecutive cycles. On-cycle and off-cycle times are 4
minutes and 13 minutes respectively. Control of ON and OFF operation
actions shall be within 6 seconds of the scheduled time.
For fan-type vented heaters, maintain circulating air adjustments
[[Page 809]]
as specified in section 2.5 of this appendix. Begin condensate
collection at one minute before the on-cycle period of the first
test cycle. Remove the container one minute before the end of each
off-cycle period. Measure condensate mass for each test-cycle. The
error associated with the mass measurement instruments shall not
exceed 0.5 percent of the quantity measured.
Fuel input shall be recorded during the entire test period
starting at the beginning of the on-time period of the first cycle
to the beginning of the on-time period of the second cycle, from the
beginning of the on-time period of the second cycle to the beginning
of the on-time period of the third cycle, etc., for each of the test
cycles. Fuel HHV, temperature, and pressure necessary for
determining fuel energy input, Qc, shall be recorded.
Determine the mass of condensate for each cycle, Mc, in
pounds. If at the end of three cycles, the sample standard deviation
is within 20 percent of the mean value for three cycles, use total
condensate collected in the three cycles as Mc; if not,
continue collection for an additional three cycles and use the total
condensate collected for the six cycles as Mc. Determine
the fuel energy input, Qc, during the three or six test
cycles, expressed in Btu.
4.0 Calculations
4.1 Annual fuel utilization efficiency for gas fueled or oil
fueled vented home heating equipment equipped without manual
controls or with multiple control modes as per 2.11 and without
thermal stack dampers. The following procedure determines the annual
fuel utilization efficiency for gas fueled or oil fueled vented home
heating equipment equipped without manual controls and without
thermal stack dampers.
* * * * *
4.1.2 Off-cycle flue gas draft factor. Based on the system
number, determine the off-cycle flue gas draft factor
(DF) from Table 1 of this appendix or the test method and
calculations of sections 3.6 and 4.5 of this appendix.
4.1.3 Off-cycle stack gas draft factor. Based on the system
number, determine the off-cycle stack gas draft factor
(Ds) from Table 1 of this appendix or from the test
method and calculations of sections 3.6 and 4.5 of this appendix,.
* * * * *
4.1.6 Latent heat loss. For non-condensing vented heaters,
obtain the latent heat loss (LL,A) from Table 2 of this
appendix. For condensing vented heaters, calculate a modified latent
heat loss (LL,A*) as follows:
For steady-state conditions:
LL,A*= LL,A-LG,SS +
LC,SS
where:
LL,A = Latent heat loss, based on fuel type, from Table 2
of this appendix,
LG,SS = Steady-state latent heat gain due to condensation
as determined in section 4.1.6.1 of this appendix, and
LC,SS = Steady-state heat loss due to hot condensate
going down the drain as determined in 4.1.6.2 of this appendix.
For cyclic conditions: (only for vented heaters tested under the
optional tracer gas procedures of section 3.3 or 3.6)
LL,A*= LL,A-LG + LC
where:
LL,A = Latent heat loss, based on fuel type, from Table 2
of this appendix,
LG = Latent heat gain due to condensation under cyclic
conditions as determined in section 4.1.6.3 of this appendix, and
LC = Heat loss due to hot condensate going down the drain
under cyclic conditions as determined in section 4.1.6.4 of this
appendix.
4.1.6.1 Latent heat gain due to condensation under steady-state
conditions. Calculate the latent heat gain (LG,SS)
expressed as a percent and defined as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.017
where:
100 = conversion factor to express a decimal as a percent,
1053.3 = latent heat of vaporization of water, Btu per pound,
Mc,ss = mass of condensate for the steady-state test as
determined in section 3.8.1 of this appendix, pounds, and
Qc,ss = fuel energy input for steady-state test as
determined in section 3.8.1 of this appendix, Btu.
4.1.6.2 Heat loss due to hot condensate going down the drain
under steady-state conditions. Calculate the steady-state heat loss
due to hot condensate going down the drain (LC,SS)
expressed as a percent and defined as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.018
where:
LG,SS = Latent heat gain due to condensation under
steady-state conditions as defined in section 4.1.6.1 of this
appendix,
1.0 = specific heat of water, Btu/lb-[deg]F,
TF,SS = Flue (or stack) gas temperature as defined in
section 3.1 of this appendix, [deg]F,
70 = assumed indoor temperature, [deg]F,
0.45 = specific heat of water vapor, Btu/lb-[deg]F, and
45 = average outdoor temperature for vented heaters, [deg]F.
4.1.6.3 Latent heat gain due to condensation under cyclic
conditions. (only for vented heaters tested under the optional
tracer gas procedures of section 3.3 or 3.6 of this appendix)
Calculate the latent heat gain (LG) expressed as a
percent and defined as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.019
where:
100 = conversion factor to express a decimal as a percent,
1053.3 = latent heat of vaporization of water, Btu per pound,
Mc = mass of condensate for the cyclic test as determined
in 3.8.2 of this appendix, pounds, and
Qc = fuel energy input for cyclic test as determined in
3.8.2 of this appendix, Btu.
4.1.6.4 Heat loss due to hot condensate going down the drain
under cyclic conditions. (only for vented heaters tested under the
optional tracer gas procedures of section 3.3 or 3.6 of this
appendix) Calculate the cyclic heat loss due to hot condensate going
down the drain (LC) expressed as a percent and defined
as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.020
where:
LG = Latent heat gain due to condensation under cyclic
conditions as defined in section 4.1.6.3 of this appendix,
1.0 = specific heat of water, Btu/lb-[deg]F,
TF,SS = Flue (or stack) gas temperature as defined in
section 3.1 of this appendix,
70 = assumed indoor temperature, [deg]F,
0.45 = specific heat of water vapor, Btu/lb-[deg]F, and
45 = average outdoor temperature for vented heaters, [deg]F.
* * * * *
4.1.8 Ratio of combustion and relief air mass flow rate to
stoichiometric air mass flow rate. For vented heaters equipped with
either an integral draft diverter or a draft hood, determine the
ratio of combustion and relief air mass flow rate to stoichiometric
air mass flow rate (RT,S), and defined as:
RT,S = A + [B/XCO2S]
where:
A = as determined from Table 2 of this appendix,
[[Page 810]]
B = as determined from Table 2 of this appendix, and
XCO2S = as defined in section 3.1 of this appendix.
* * * * *
4.1.10 Steady-state efficiency. For vented heaters equipped with
single-stage thermostats, calculate the steady-state efficiency
(excluding jacket loss), [eta]SS, expressed in percent
and defined as:
[eta]SS = 100-LL,A-LS,SS,A
where:
LL,A = latent heat loss, as defined in section 4.1.6 of
this appendix (for condensing vented heaters LL,A* for
steady-state conditions), and
LS,SS,A = sensible heat loss at steady-state operation,
as defined in section 4.1.9 of this appendix.
For vented heaters equipped with either two stage controls or
with step-modulating controls, calculate the steady-state efficiency
at the reduced fuel input rate, [eta]SS-L, expressed in
percent and defined as:
[eta]SS-L = 100-LL,A-LS,SS,A
where:
LL,A = latent heat loss, as defined in section 4.1.6 of
this appendix (for condensing vented heaters LL,A* for
steady-state conditions at the reduced firing rate), and
LS,SS,A = sensible heat loss at steady-state operation,
as defined in section 4.1.9 of this appendix, in which
LS,SS,A is determined at the reduced fuel input rate.
For vented heaters equipped with two stage controls, calculate
the steady-state efficiency at the maximum fuel input rate,
[eta]SS-H, expressed in percent and defined as:
[eta]SS-H = 100-LL,A-LS,SS,A
where:
LL,A = latent heat loss, as defined in section 4.1.6 of
this appendix (for condensing vented heaters LL,A* for
steady-state conditions at the maximum fuel input rate), and
LS,SS,A = sensible heat loss at steady-state operation,
as defined in section 4.1.9 of this appendix, in which
LS,SS,A is measured at the maximum fuel input rate.
For vented heaters equipped with step-modulating thermostats,
calculate the weighted-average steady-state efficiency in the
modulating mode, [eta]SS-MOD, expressed in percent and
defined as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.021
where:
[eta]SS-H = steady-state efficiency at the maximum fuel
input rate, as defined in section 4.1.10 of this appendix,
[eta]SS-L = steady-state efficiency at the reduced fuel
input rate, as defined in section 4.1.10 of this appendix,
TOA* = average outdoor temperature for vented heaters
with step-modulating thermostats operating in the modulating mode
and is obtained from Table 3 or Figure 1 of this appendix, and
TC = balance point temperature which represents a
temperature used to apportion the annual heating load between the
reduced input cycling mode and either the modulating mode or maximum
input cycling mode and is obtained either from Table 3 of this
appendix or calculated by the following equation:
TC = 65-[(65-15)R]
where:
65 = average outdoor temperature at which a vented heater starts
operating,
15 = national average outdoor design temperature for vented heaters,
and
R = ratio of reduced to maximum heat output rates, as defined in
section 4.1.13 of this appendix.
* * * * *
4.1.15 Fraction of heating load at maximum operating mode or
noncycling mode. For vented heaters equipped with either two stage
thermostats or step-modulating thermostats, determine the fraction
of heating load at the maximum operating mode or noncycling mode
(X2) expressed as a decimal and listed in Table 3 of this
appendix or obtained from Figure 2 of this appendix.
4.1.16 Weighted-average steady-state efficiency. For vented
heaters equipped with single-stage thermostats, the weighted-average
steady-state efficiency ([eta]SS-WT) is equal to
[eta]SS, as defined in section 4.1.10 of this appendix.
For vented heaters equipped with two stage thermostats,
[eta]SS-WT is defined as:
[eta]SS-WT = X1[eta]SS-L +
X2[eta]SS-H
where:
X1 = as defined in section 4.1.14 of this appendix
[eta]SS-L = as defined in section 4.1.10 of this appendix
X2 = as defined in section 4.1.15 of this appendix
[eta]SS-H = as defined in section 4.1.10 of this appendix
For vented heaters equipped with step-modulating controls,
[eta]SS-WT is defined as:
[eta]SS-WT = X1[eta]SS-L +
X2[eta]SS-MOD
where:
X1 = as defined in section 4.1.14 of this appendix
[eta]SS-L = as defined in section 4.1.10 of this appendix
X2 = as defined in section 4.1.15 of this appendix
[eta]SS-MOD = as defined in section 4.1.10 of this
appendix
* * * * *
4.2.1 Average ratio of stack gas mass flow rate to flue gas mass
flow rate at steady-state operation. For vented heaters equipped
with either direct vents or direct exhaust or that are outdoor
units, the average ratio of stack gas mass flow rate to flue gas
mass flow rate at steady-state operation (S/F) shall be equal to
unity. (S/F=1) For all other types of vented heaters, calculate (S/
F) defined as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.022
where:
RT,S = as defined in section 4.1.8 of this appendix with
XCO2s as measured in section 3.1. of this appendix
RT,F = as defined in section 4.1.7 of this appendix with
XCO2F as measured in section 3.1. of this appendix
4.2.2 Multiplication factor for infiltration loss during burner
on-cycle. Calculate the multiplication factor for infiltration loss
during burner on-cycle (KI,ON) defined as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.023
where:
100 = converts a decimal fraction into a percent
0.24 = specific heat of air
A/F = stoichiometric air/fuel ratio, determined in accordance with
Table 2 of this appendix
S/F = as defined in section 4.2.1 of this appendix
0.7 = infiltration parameter
RT,F = as defined in section 4.1.7 of this appendix
HHVA = average higher heating value of the test fuel,
determined in accordance with Table 2 of this appendix
* * * * *
4.2.4.1 For manually controlled heaters with various input rates
the weighted average
[[Page 811]]
steady-state efficiency ([eta]SS-WT), is determined as
follows:
[eta]SS-WT = 100-LL,A-LS,SS,A
where:
LL,A = latent heat loss, as defined in section 4.1.6 of
this appendix (for condensing vented heaters, LL,A* for
steady-state conditions), and
LS,SS,A = steady-state efficiency at the reduced fuel
input rate, as defined in section 4.1.9 of this appendix and where
LL,A and LS,SS,A are determined:
(1) at 50 percent of the maximum fuel input rate as measured in
either section 3.1.1 of this appendix for manually controlled gas
vented heaters or section 3.1.2 of this appendix for manually
controlled oil vented heaters, or
(2) at the minimum fuel input rate as measured in either section
3.1.1 of this appendix for manually controlled gas vented heaters or
section 3.1.2 of this appendix for manually controlled oil vented
heaters if the design of the heater is such that the 5
percent of 50 percent of the maximum fuel input rate cannot be set,
provided this minimum rate is no greater than \2/3\ of the maximum
input rate of the heater.
* * * * *
4.3 Annual fuel utilization efficiency by the tracer gas method.
The annual fuel utilization efficiency shall be determined by the
following tracer gas method for all vented heaters equipped with
thermal stack dampers.
4.3.1 On-cycle sensible heat loss. For vented heaters equipped
with single-stage thermostats, calculate the on-cycle sensible heat
loss (LS,ON) expressed as a percent and defined as:
LS,ON = LS,SS,A
where:
LS,SS,A = as defined in section 4.1.9 of this appendix
For vented heaters equipped with two stage thermostats, calculate
LS,ON defined as:
LS,ON = X1LS,SS,A-red +
X2LS,SS,A-max
where:
X1 = as defined in section 4.1.14 of this appendix
LS,SS,A-red = as defined as LS,SS,A in section
4.1.9 of this appendix at the reduced fuel input rate
X2 = as defined in section 4.1.15 of this appendix
LS,SS,A-max = as defined as LS,SS,A in section
4.1.9 of this appendix at the maximum fuel input rate
For vented heaters with step-modulating controls, calculate
LS,ON defined as:
LS,ON = X1LS,SS,A-red +
X2LS,SS,A-avg
where:
X1 = as defined in section 4.1.14 of this appendix
LLS,SS,A-red = as defined in section 4.3.1 of this
appendix
X2 = as defined in section 4.1.15 of this appendix
LS,SS,A-avg = average sensible heat loss for step-
modulating vented heaters operating in the modulating mode
[GRAPHIC] [TIFF OMITTED] TR06JA15.024
where:
LS,SS,A-avg = as defined in section 4.3.1 of this
appendix
TC = as defined in section 4.1.10 of this appendix
TOA* = as defined in section 4.1.10 of this appendix
15 = as defined in section 4.1.10 of this appendix
4.3.2 On-cycle infiltration heat loss. For vented heaters
equipped with single-stage thermostats, calculate the on-cycle
infiltration heat loss (LI,ON) expressed as a percent and
defined as:
LI,ON = KI,ON(70-45)
where:
KI,ON = as defined in section 4.2.2 of this appendix
70 = as defined in section 4.2.3 of this appendix
45 = as defined in section 4.2.3 of this appendix
For vented heaters equipped with two stage thermostats,
calculate LI,ON defined as:
LI,ON = X1KI,ON-Max(70-
TOA*) + X2KI,ON,red(70-
TOA)
where:
X1 = as defined in section 4.1.14 of this appendix
KI,ON-max = as defined as KI,ON in section
4.2.2 of this appendix at the maximum heat input rate
70 = as defined in section 4.2.3 of this appendix
TOA* = as defined in section 4.3.4 of this appendix
KI,ON,red = as defined as KI,ON in section
4.2.2 of this appendix at the minimum heat input rate
TOA = as defined in section 4.3.4 of this appendix
X2 = as defined in section 4.1.15 of this appendix
For vented heaters equipped with step-modulating thermostats,
calculate LI,ON defined as:
LI,ON = X1KI,ON-avg(70-
TOA*) + X2KI,ON,red(70-
TOA)
where:
X1 = as defined in section 4.1.14 of this appendix
[GRAPHIC] [TIFF OMITTED] TR06JA15.025
70 = as defined in section 4.2.3 of this appendix
TOA* = as defined in section 4.3.4 of this appendix
X2 = as defined in section 4.1.15 of this appendix
TOA = as defined in section 4.3.4 of this appendix
4.3.3 Off-cycle sensible heat loss. For vented heaters equipped
with single-stage thermostats, calculate the off-cycle sensible heat
loss (LS,OFF) at the maximum fuel input rate. For vented
heaters equipped with step-modulating thermostats, calculate
LS,OFF defined as:
LS,OFF = X1 LS,OFF,red
where:
X1 = as defined in section 4.1.14 of this appendix, and
LS,OFF,red = as defined as LS,OFF in section
4.3.3 of this appendix at the reduced fuel input rate.
For vented heaters equipped with two stage controls, calculate
LS,OFF defined as:
LS,OFF = X1 LS,OFF,red
+X2 LS,OFF,Max
where:
X1 = as defined in section 4.1.14 of this appendix,
LS,OFF,red = as defined as LS,OFF in section
4.3.3 of this appendix at the reduced fuel input rate,
X2 = as defined in section 4.1.15 of this appendix, and
LS,OFF,Max = as defined as LS,OFF in section
4.3.3 of this appendix at the maximum fuel input rate.
Calculate the off-cycle sensible heat loss (LS,OFF)
expressed as a percent and defined as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.026
where:
100 = conversion factor for percent,
0.24 = specific heat of air in Btu per pound--[deg]F,
Qin = fuel input rate, as defined in section 3.1 of this
appendix in Btu per minute (as appropriate for the firing rate),
[[Page 812]]
ton = average burner on-time per cycle and is 20 minutes,
[Sigma] mS,OFF (TS,OFF -TRA) =
summation of the ten values (for single-stage or step-modulating
models) or twenty values (for two tage models) of the quantity,
mS,OFF (TS,OFF -TRA), measured in
accordance with section 3.3 of this appendix, and
mS,OFF = stack gas mass flow rate pounds per minute.
[GRAPHIC] [TIFF OMITTED] TR06JA15.027
TS,OFF = stack gas temperature measured in accordance
with section 3.3 of this appendix,
TRA = average room temperature measured in accordance
with section 3.3 of this appendix,
PB = barometric pressure in inches of mercury,
VT = flow rate of the tracer gas through the stack in
cubic feet per minute,
CT* = concentration by volume of the active tracer gas in
the mixture in percent and is 100 when the tracer gas is a single
component gas,
CT = concentration by volume of the active tracer gas in
the diluted stack gas in percent,
TT = temperature of the tracer gas entering the flow
meter in degrees Fahrenheit, and
(TT +460) = absolute temperature of the tracer gas
entering the flow meter in degrees Rankine.
4.3.4 Average outdoor temperature. For vented heaters equipped
with single-stage thermostats, the average outdoor temperature
(TOA) is 45[emsp14][deg]F. For vented heaters equipped
with either two stage thermostats or step-modulating thermostats,
TOA during the reduced operating mode is obtained from
Table 3 or Figure 1 of this appendix. For vented heaters equipped
with two stage thermostats, TOA* during the maximum
operating mode is obtained from Table 3 or Figure 1 of this
appendix.
4.3.5 Off-cycle infiltration heat loss. For vented heaters
equipped with single stage thermostats, calculate the off-cycle
infiltration heat loss (LI,OFF) at the maximum fuel input
rate. For vented heaters equipped with step-modulating thermostats,
calculate LI,OFF defined as:
LI,OFF = X1LI,OFF,red
where:
X1 = as defined in section 4.1.14 of this appendix
LI,OFF,red = as defined in LI,OFF in section
4.3.5 of this appendix at the reduced fuel input rate
For vented heaters equipped with two stage thermostats,
calculate LI,OFF defined as:
LI,OFF = X1LI,OFF,red +
X2LI,OFF,max
where:
X1 = as defined in section 4.1.14 of this appendix
LI,OFF,red = as defined as LI,OFF in section
4.3.5 of this appendix at the reduced fuel input rate
X2 = as defined in section 4.1.15 of this appendix
LI,OFF,Max = as defined as LI,OFF in section
4.3.5 of this appendix at the maximum fuel input rate
Calculate the off-cycle infiltration heat loss
(LI,OFF) expressed as a percent and defined as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.028
where:
100 = conversion factor for percent
0.24 = specific heat of air in Btu per pound--[deg]F
1.3 = dimensionless factor for converting laboratory measured stack
flow to typical field conditions
0.7 = infiltration parameter
70 = assumed average indoor air temperature, [deg]F
TOA = average outdoor temperature as defined in section
4.3.4 of this appendix
Qin = fuel input rate, as defined in section 3.1 of this
appendix in Btu per minute (as appropriate for the firing rate)
ton = average burner on-time per cycle and is 20 minutes
[Sigma] mS,OFF = summation of the twenty values of the
quantity, mS,OFF, measured in accordance with section 3.3
of this appendix
mS,OFF = as defined in section 4.3.3 of this appendix
4.3.6 Part-load fuel utilization efficiency. Calculate the part-
load fuel utilization efficiency ([eta]u) expressed as a
percent and defined as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.029
where:
Cj = 2.8, adjustment factor,
Lj = jacket loss as defined in section 4.1.5,
LL,A = Latent heat loss, as defined in section 4.1.6 of
this appendix (for condensing vented heaters LL,A* for
cyclic conditions),
ton = Average burner on time which is 20 minutes,
LS,ON = On-cycle sensible heat loss, as defined in
section 4.3.1 of this appendix,
LS,OFF = Off-cycle sensible heat loss, as defined in
section 4.3.3 of this appendix,
LI,ON = On-cycle infiltration heat loss, as defined in
section 4.3.2 of this appendix,
LI,OFF = Off-cycle infiltration heat loss, as defined in
section 4.3.5 of this appendix,
PF = Pilot fraction, as defined in section 4.1.4 of this
appendix, and
tOFF = average burner off-time per cycle, which is 20
minutes.
* * * * *
4.5.1 Optional procedure for determining DP for vented home
heating equipment. Calculate the ratio (DP) of the rate
of flue gas mass through the vented heater during the off-period,
MF,OFF(TF,SS), to the rate of flue gas mass
flow during the on-period, MF,SS(TF,SS), and
defined as:
DP = MF,OFF(TF,SS)/
MF,SS(TF,SS)
For vented heaters in which no draft is maintained during the
steady-state or cool down tests, MF,OFF(TF,SS)
is defined as:
[GRAPHIC] [TIFF OMITTED] TR06JA15.030
For oil fueled vented heaters in which an imposed draft is
maintained, as described in section 3.6 of this appendix,
MF,OFF(TF,SS) is defined as:
MF,OFF(TF,SS) =
MF,OFF(T*F,OFF)
where:
TF,SS = as defined in section 3.1.1 of this appendix,
[[Page 813]]
T*F,OFF = flue gas temperature during the off-period
measured in accordance with section 3.6 of this appendix in degrees
Fahrenheit, and
TRA = as defined in section 2.9 of this appendix.
[GRAPHIC] [TIFF OMITTED] TR06JA15.031
PB = barometric pressure measured in accordance with
section 3.6 of this appendix in inches of mercury,
VT = flow rate of tracer gas through the vented heater
measured in accordance with section 3.6 of this appendix in cubic
feet per minute,
CT = concentration by volume of tracer gas present in the
flue gas sample measured in accordance with section 3.6 of this
appendix in percent,
CT* = concentration by volume of the active tracer gas in
the mixture in percent and is 100 when the tracer gas is a single
component gas,
TT = the temperature of the tracer gas entering the flow
meter measured in accordance with section 3.6 of this appendix in
degrees Fahrenheit, and
(TT + 460) = absolute temperature of the tracer gas
entering the flow meter in degrees Rankine.
MF,SS(TF,SS) =
Qin[RT,F(A/F)+1]/[60HHVA]
Qin = as defined in section 3.1 of this appendix,
RT,F = as defined in section 4.1.7 of this appendix,
A/F = as defined in section 4.2.2 of this appendix, and
HHVA = as defined in section 4.2.2 of this appendix.
4.5.2 Optional procedure for determining off-cycle draft factor
for flue gas flow for vented heaters. For systems numbered 1 through
10, calculate the off-cycle draft factor for flue gas flow
(DF) defined as:
DF = DP
For systems numbered 11 or 12: DF = DP
DO
For systems complying with section 3.6.1 or 3.6.2, DF =
0.05
Where:
DP = as defined in section 4.5.1. of this appendix, and
DO = as defined in section 4.4 of this appendix.
4.5.3 Optional procedure for determining off-cycle draft factor
for stack gas flow for vented heaters. Calculate the off-cycle draft
factor for stack gas flow (DS) defined as:
For systems numbered 1 or 2: DS = 1.0
For systems numbered 3 or 4: DS = (DP+0.79)/
1.4
For systems numbered 5 or 6: DS = DO
For systems numbered 7 or 8 and if DO(S/
F)<1:DS = DO DP
For systems numbered 7 or 8 and if DO(S/F)>1:
DS = DO DP+[0.85-DO
DP] [DO(S/F)-1]/[S/F-1]
where:
DP = as defined in section 4.5.1 or 3.6.1 of this
appendix, as applicable
DO = as defined in section 4.4 of this appendix
* * * * *
Table 1--Off-Cycle Draft Factors for Flue Gas Flow (DF) and for Stack Gas Flow (DS) for Vented Home Heating
Equipment Equipped Without Thermal Stack Dampers
----------------------------------------------------------------------------------------------------------------
System number (DF) (DS) Burner type Venting system type \1\
----------------------------------------------------------------------------------------------------------------
1............... 1.0.................. 1.0.................. Atmospheric.......... Draft hood or diverter.
2............... 0.4.................. 1.0.................. Power................ Draft hood or diverter.
3............... 1.0.................. 1.0.................. Atmospheric.......... Barometric draft
regulator.
4............... 0.4.................. 0.85................. Power................ Barometric draft
regulator.
5............... 1.0.................. DO................... Atmospheric.......... Draft hood or diverter
with damper.
6............... 0.4.................. DO................... Power................ Draft hood or diverter
with damper.
7............... 1.0.................. DO................... Atmospheric.......... Barometric draft
regulator with damper.
8............... 0.4.................. DODP................. Power................ Barometric draft
regulator with damper.
9............... 1.0.................. 0.................... Atmospheric.......... Direct vent.
10.............. 0.4.................. 0.................... Power................ Direct vent.
11.............. DO................... 0.................... Atmospheric.......... Direct vent with damper.
12.............. 0.4 DO............... 0.................... Power................ Direct vent with damper.
----------------------------------------------------------------------------------------------------------------
\1\ Venting systems listed with dampers means electromechanical dampers only.
* * * * *
0
6. Revise Appendix P to subpart B of part 430 to read as follows:
Appendix P to Subpart B of Part 430--Uniform Test Method for Measuring
the Energy Consumption of Pool Heaters
Note: On and after July 6, 2015, any representations made with
respect to the energy use or efficiency of all pool heaters must be
made in accordance with the results of testing pursuant to this
appendix. On and after this date, if a manufacturer makes
representations of standby mode and off mode energy consumption,
then testing must also include the provisions of this appendix
related to standby mode and off mode energy consumption. Until July
6, 2015, manufacturers must test gas-fired pool heaters in
accordance with this appendix, or appendix P as it appeared at 10
CFR part 430, subpart B revised as of January 1, 2014. Any
representations made with respect to the energy use or efficiency of
such pool heaters must be in accordance with whichever version is
selected. DOE notes that, because testing under this appendix P must
be completed as of July 6, 2015, manufacturers may wish to begin
using this test procedure immediately.
1. Definitions.
1.1 Active mode means the condition during the pool heating
season in which the pool heater is connected to the power source,
and the main burner, electric resistance element, or heat pump is
activated to heat pool water.
1.2 Coefficient of performance (COP), as applied to heat pump
pool heaters, means the ratio of heat output in kW to the total
power input in kW.
1.3 Electric heat pump pool heater means an appliance designed
for heating nonpotable water and employing a compressor, water-
cooled condenser, and outdoor air coil.
1.4 Electric resistance pool heater means an appliance designed
for heating nonpotable water and employing electric resistance
heating elements.
1.5 Fossil fuel-fired pool heater means an appliance designed
for heating nonpotable water and employing natural gas or oil
burners.
1.6 Hybrid pool heater means an appliance designed for heating
nonpotable water and employing both a heat pump (compressor, water-
cooled condenser, and outdoor air coil) and a fossil fueled burner
as heating sources.
1.7 Off mode means the condition during the pool non-heating
season in which the pool heater is connected to the power source,
[[Page 814]]
and neither the main burner, nor the electric resistance elements,
nor the heat pump is activated, and the seasonal off switch, if
present, is in the ``off'' position.
1.8 Seasonal off switch means a switch that results in different
energy consumption in off mode as compared to standby mode.
1.9 Standby mode means the condition during the pool heating
season in which the pool heater is connected to the power source,
and neither the main burner, nor the electric resistance elements,
nor the heat pump is activated.
2. Test method.
2.1 Active mode.
2.1.1 Fossil fuel-fired pool heaters. The test method for
testing fossil fuel-fired pool heaters in active mode is as
specified in section 2.10 of ANSI Z21.56 (incorporated by reference,
see Sec. 430.3), with the following additional clarifications.
1. Burner input rate is adjusted as specified in section 2.3.3
of ANSI Z21.56,
2. Equilibrium is defined as in section 9.1.3 of ASHRAE 146
(incorporated by reference; see Sec. 430.3)
3. Units are only to be tested using a recirculating loop and a
pump if: the use of the recirculating loop and pump are listed as
required; a minimum flow rate is specified in the installation or
operation manual provided with the unit; the pump is packaged with
the unit by the manufacturer; or such use is required for testing.
4. A water temperature rise of less than 40[deg] F is allowed
only as specified in the installation or operation manual(s)
provided with the unit.
2.1.2 Electric resistance pool heaters. The test method for
testing electric resistance pool heaters in active mode is as
specified in ASHRAE 146 (incorporated by reference; see Sec.
430.3).
2.1.3 Electric heat pump pool heaters. The test method for
testing electric heat pump pool heaters in active mode is as
specified in AHRI 1160 (incorporated by reference; see Sec. 430.3),
which references ASHRAE 146 (incorporated by reference; see Sec.
430.3).
2.1.4 Hybrid pool heaters. [Reserved]
2.2 Standby mode. The test method for testing the energy
consumption of pool heaters in standby mode is as described in
sections 3 through 5 of this appendix.
2.3 Off mode.
2.3.1 Pool heaters with a seasonal off switch. For pool heaters
with a seasonal off switch, no off mode test is required.
2.3.2 Pool heaters without a seasonal off switch. For pool
heaters without a seasonal off switch, the test method for testing
the energy consumption of the pool heater is as described in
sections 3 through 5 of this appendix.
3. Test conditions.
3.1 Active mode.
3.1.1 Fossil fuel-fired pool heaters. Establish the test
conditions specified in section 2.10 of ANSI Z21.56 (incorporated by
reference; see Sec. 430.3).
3.1.2 Electric resistance pool heaters. Establish the test
conditions specified in section 9.1.4 of ASHRAE 146 (incorporated by
reference; see Sec. 430.3).
3.1.3 Electric heat pump pool heaters. Establish the test
conditions specified in section 5 of AHRI 1160. The air temperature
surrounding the unit shall be at the ``High Air Temperature--Mid
Humidity (63% RH)'' level specified in section 6 of AHRI 1160
(incorporated by reference, see Sec. 430.3) (80.6 [deg]F [27.0
[deg]C] Dry-Bulb, 71.2 [deg]F [21.8 [deg]C]).
3.1.4 Hybrid pool heaters. [Reserved]
3.2 Standby mode and off mode. After completing the active mode
tests described in sections 3.1 and 4.1 of this appendix, reduce the
thermostat setting to a low enough temperature to put the pool
heater into standby mode. Reapply the energy sources and operate the
pool heater in standby mode for 60 minutes.
4. Measurements
4.1 Active mode
4.1.1 Fossil fuel-fired pool heaters. Measure the quantities
delineated in section 2.10 of ANSI Z21.56 (incorporated by
reference; see Sec. 430.3). The measurement of energy consumption
for oil-fired pool heaters in Btu is to be carried out in
appropriate units (e.g., gallons).
4.1.2 Electric resistance pool heaters. Measure the quantities
delineated in section 9.1.4 of ASHRAE 146 (incorporated by
reference; see Sec. 430.3) during and at the end of the 30-minute
period when water is flowing through the pool heater.
4.1.3 Electric heat pump pool heaters. Measure the quantities
delineated in section 9.1.1 and Table 2 of ASHRAE 146 (incorporated
by reference; see Sec. 430.3). Record the elapsed time,
tHP, from the start of electric power metering to the
end, in minutes.
4.1.4 Hybrid pool heaters. [Reserved]
4.2 Standby mode. For all pool heaters, record the average
electric power consumption during the standby mode test,
PW,SB, in W, in accordance with section 5 of IEC 62301
(incorporated by reference; see Sec. 430.3). For fossil fuel-fired
pool heaters, record the fossil fuel energy consumption during the
standby test, Qp, in Btu. (Milli-volt electrical
consumption need not be considered in units so equipped.) Ambient
temperature and voltage specifications in section 4.1 of this
appendix shall apply to this standby mode testing. Round the
recorded standby power (PW,SB) to the second decimal
place, and for loads greater than or equal to 10 W, record at least
three significant figures.
4.3 Off mode.
4.3.1 Pool heaters with a seasonal off switch. For pool heaters
with a seasonal off switch, the average electric power consumption
during the off mode, PW,OFF = 0, and the fossil fuel
energy consumed during the off mode, Qoff = 0.
4.3.2 Pool heaters without a seasonal off switch. For all pool
heaters without a seasonal off switch, record the average electric
power consumption during the standby/off mode test,
PW,OFF = PW,SB, in W, in accordance with
section 5 of IEC 62301 (incorporated by reference; see Sec. 430.3).
For fossil fuel-fired pool heaters without a seasonal off switch,
record the fossil fuel energy consumption during the off mode test,
Qoff (= Qp), in Btu. (Milli-volt electrical
consumption need not be considered in units so equipped.) Ambient
temperature and voltage specifications in section 4.1 of this
appendix shall apply to this off mode testing. Round the recorded
off mode power (PW,OFF) to the second decimal place, and
for loads greater than or equal to 10 W, record at least three
significant figures.
5. Calculations.
5.1 Thermal efficiency.
5.1.1 Fossil fuel-fired pool heaters. Calculate the thermal
efficiency, Et (expressed as a percent), as specified in
section 2.10 of ANSI Z21.56 (incorporated by reference; see Sec.
430.3). The expression of fuel consumption for oil-fired pool
heaters shall be in Btu.
5.1.2 Electric resistance pool heaters. Calculate the thermal
efficiency, Et (expressed as a percent), as specified in
section 11.1 of ASHRAE 146 (incorporated by reference; see Sec.
430.3).
5.1.3 Electric heat pump pool heaters. Calculate the COP
according to section 11.1 of ASHRAE 146. Calculate the thermal
efficiency, Et (expressed as a percent): Et =
COP.
5.1.4 Hybrid pool heaters. [Reserved]
5.2 Average annual fossil fuel energy for pool heaters. For
electric resistance and electric heat pump pool heaters, the average
annual fuel energy for pool heaters, EF =0.
For fossil fuel-fired pool heaters, the average annual fuel
energy for pool heaters, EF, is defined as:
EF = BOH QIN + (POH-BOH)QPR + (8760
- POH) Qoff,R
Where:
BOH = average number of burner operating hours = 104 h,
POH = average number of pool operating hours = 4,464 h,
QIN = rated fuel energy input as defined according to
section 2.10.1 or section 2.10.2 of ANSI, Z21.56 (incorporated by
reference; see Sec. 430.3), as appropriate. (For electric
resistance and electric heat pump pool heaters, QIN =
0.),
QPR = average energy consumption rate of continuously
operating pilot light, if employed, = (QP/1 h),
QP = energy consumption of continuously operating pilot
light, if employed, as measured in section 4.2 of this appendix, in
Btu,
8760 = number of hours in one year,
Qoff,R = average off mode fossil fuel energy consumption
rate = Qoff/(1 h), and
Qoff = off mode energy consumption as defined in section
4.3 of this appendix.
5.3 Average annual electrical energy consumption for pool
heaters. The average annual electrical energy consumption for pool
heaters, EAE, is expressed in Btu and defined as:
(1) EAE = EAE,active +
EAE,standby,off
(2) EAE,active = BOH * PE
(3) EAE,standby,off = (POH-BOH) PW,SB(Btu/h) +
(8760-POH) PW,OFF(Btu/h)
where:
EAE,active = electrical consumption in the active mode,
EAE,standby,off = auxiliary electrical consumption in the
standby mode and off mode,
PE = 2Ec, for fossil fuel-fired heaters tested according
to section 2.10.1 of ANSI Z21.56 (incorporated by reference; see
[[Page 815]]
Sec. 430.3) and for electric resistance pool heaters, in Btu/h,
= 3.412 PErated, for fossil fuel-fired heaters tested
according to section 2.10.2 of ANSI Z21.56, in Btu/h,
= Ec,HP * (60/tHP), for electric heat pump
pool heaters, in Btu/h.
Ec = electrical consumption in Btu per 30 min. This
includes the electrical consumption (converted to Btus) of the pool
heater and, if present, a recirculating pump during the 30-minute
thermal efficiency test. The 30-minute thermal efficiency test is
defined in section 2.10.1 of ANSI Z21.56 for fossil fuel-fired pool
heaters and section 9.1.4 of ASHRAE 146 (incorporated by reference;
see Sec. 430.3) for electric resistance pool heaters.
2 = conversion factor to convert unit from per 30 min. to per h.
PErated = nameplate rating of auxiliary electrical
equipment of heater, in Watts
Ec,HP = electrical consumption of the electric heat pump
pool heater (converted to equivalent unit of Btu), including the
electrical energy to the recirculating pump if used, during the
thermal efficiency test, as defined in section 9.1 of ASHRAE 146, in
Btu.
tHP = elapsed time of data recording during the thermal
efficiency test on electric heat pump pool heater, as defined in
section 9.1 of ASHRAE 146, in minutes.
BOH = as defined in section 5.2 of this appendix,
POH = as defined in section 5.2 of this appendix,
PW,SB (Btu/h) = electrical energy consumption rate during
standby mode expressed in Btu/h = 3.412 PW,SB, Btu/h,
PW,SB = as defined in section 4.2 of this appendix,
PW,OFF (Btu/h) = electrical energy consumption rate
during off mode expressed in Btu/h = 3.412 PW,OFF, Btu/h,
and
PW,OFF = as defined in section 4.3 of this appendix.
5.4 Integrated thermal efficiency.
5.4.1 Calculate the seasonal useful output of the pool heater
as:
EOUT = BOH[(Et/100)(QIN + PE)]
where:
BOH = as defined in section 5.2 of this appendix,
Et = thermal efficiency as defined in section 5.1 of this
appendix,
QIN = as defined in section 5.2 of this appendix,
PE = as defined in section 5.3 of this appendix, and
100 = conversion factor, from percent to fraction.
5.4.2 Calculate the annual input to the pool heater as:
EIN = EF + EAE
where:
EF = as defined in section 5.2 of this appendix, and
EAE = as defined in section 5.3 of this appendix.
5.4.3 Calculate the pool heater integrated thermal efficiency
(TEI) (in percent).
TEI = 100(EOUT/EIN)
where:
EOUT = as defined in section 5.4.1 of this appendix,
EIN = as defined in section 5.4.2 of this appendix, and
100 = conversion factor, from fraction to percent.
[FR Doc. 2014-30748 Filed 1-5-15; 8:45 am]
BILLING CODE 6450-01-P