[Title 40 CFR 60.561]
[Code of Federal Regulations (annual edition) - July 1, 2009 Edition]
[Title 40 - PROTECTION OF ENVIRONMENT]
[Chapter I - ENVIRONMENTAL PROTECTION AGENCY (CONTINUED)]
[Subchapter C - AIR PROGRAMS (CONTINUED)]
[Part 60 - STANDARDS OF PERFORMANCE FOR NEW STATIONARY SOURCES--]
[Subpart Ddd - Standards of Performance for Volatile Organic Compound (VOC)]
[Sec. 60.561 - Definitions.]
[From the U.S. Government Printing Office]
40PROTECTION OF ENVIRONMENT62009-07-012009-07-01falseDefinitions.60.561Sec. 60.561PROTECTION OF ENVIRONMENTENVIRONMENTAL PROTECTION AGENCY (CONTINUED)AIR PROGRAMS (CONTINUED)STANDARDS OF PERFORMANCE FOR NEW STATIONARY SOURCES--Standards of Performance for Volatile Organic Compound (VOC)
Sec. 60.561 Definitions.
As used in this subpart, all terms not defined herein shall have the
meaning given them in the Act, in subpart A of part 60, or in subpart VV
of part 60, and the following terms shall have the specific meanings
given them.
Boiler means any enclosed combustion device that extracts useful
energy in the form of steam.
Capital expenditure means, in addition to the definition in 40 CFR
60.2, an expenditure for a physical or operational change to an existing
facility that exceeds P, the product of the facility's replacement cost,
R, and an adjusted annual asset guideline repair allowance, A, as
reflected by the following equation: P = R x A, where
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(a) The adjusted annual asset guideline repair allowance, A, is the
product of the percent of the replacement cost, Y, and the applicable
basic annual asset guideline repair allowance, B, as reflected by the
following equation: A = Y x (B / 100);
(b) The percent Y is determined from the following equation: Y = 1.0
- 0.57 log X, where X is 1986 minus the year of construction; and
(c) The applicable basic annual asset guideline repair allowance, B,
is equal to 12.5.
Car-sealed means, for purposes of these standards, a seal that is
placed on the device used to change the position of a valve (e.g., from
opened to closed) such that the position of the valve cannot be changed
without breaking the seal and requiring the replacement of the old seal
once broken with a new seal.
Closed vent system means a system that is not open to the atmosphere
and that is composed of piping, connections, and, if necessary, flow
inducing devices that transport gas or vapor from a piece or pieces of
equipment to a control device.
Continuous emissions means any gas stream containing VOC that is
generated essentially continuously when the process line or any piece of
equipment in the process line is operating.
Continuous process means a polymerization process in which reactants
are introduced in a continuous manner and products are removed either
continuously or intermittently at regular intervals so that the process
can be operated and polymers produced essentially continuously.
Control device means an enclosed combustion device, vapor recovery
system, or flare.
Copolymer means a polymer that has two different repeat units in its
chain.
Decomposition means, for the purposes of these standards, an event
in a polymerization reactor that advances to the point where the
polymerization reaction becomes uncontrollable, the polymer begins to
break down (decompose), and it becomes necessary to relieve the reactor
instantaneously in order to avoid catastrophic equipment damage or
serious adverse personnel safety consequences.
Decomposition emissions refers to those emissions released from a
polymer production process as the result of a decomposition or during
attempts to prevent a decomposition.
Emergency vent stream means, for the purposes of these standards, an
intermittent emission that results from a decomposition, attempts to
prevent decompositions, power failure, equipment failure, or other
unexpected cause that requires immediate venting of gases from process
equipment in order to avoid safety hazards or equipment damage. This
includes intermittent vents that occur from process equipment where
normal operating parameters (e.g., pressure or temperature) are exceeded
such that the process equipment can not be returned to normal operating
conditions using the design features of the system and venting must
occur to avoid equipment failure or adverse safety personnel
consequences and to minimize adverse effects of the runaway reaction.
This does not include intermittent vents that are designed into the
process to maintain normal operating conditions of process vessels
including those vents that regulate normal process vessel pressure.
End finisher means a polymerization reaction vessel operated under
very low pressures, typically at pressures of 2 mm Hg (1 in.
H2O) or less, in order to produce high viscosity
poly(ethylene terephthalate). An end finisher is preceded in a high
viscosity poly(ethylene terephthalate) process line by one or more
polymerization vessels operated under less severe vacuums, typically
between 5 and 10 mm Hg (3 and 5 in. H2O). A high viscosity
poly(ethylene terephthalate) process line may have one or more end
finishers.
Existing control device means, for the purposes of these standards,
an air pollution control device that has been in operation on or before
September 30, 1987, or that has been in operation between September 30,
1987, and January 10, 1989, on those continuous or intermittent
emissions from a process section that is marked by an ``--'' in table 1
of this subpart.
Existing control device is reconstructed means, for the purposes of
these standards, the capital expenditure of at least
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50 percent of the replacement cost of the existing control device.
Existing control device is replaced means, for the purposes of these
standards, the replacement of an existing control device with another
control device.
Expandable polystyrene means a polystyrene bead to which a blowing
agent has been added using either an in-situ suspension process or a
post-impregnation suspension process.
Experimental process line means a polymer or copolymer manufacturing
process line with the sole purpose of operating to evaluate polymer
manufacturing processes, technologies, or products. An experimental
process line does not produce a polymer or resin that is sold or that is
used as a raw material for nonexperimental process lines.
Flame zone means that portion of the combustion chamber in a boiler
occupied by the flame envelope.
Fugitive emissions equipment means each pump, compressor, pressure
relief device, sampling connection system, open-ended valve or line,
valve, and flange or other connector in VOC service and any devices or
systems required by subpart VV of this part.
Gas phase process means a polymerization process in which the
polymerization reaction is carried out in the gas phase; i.e., the
monomer(s) are gases in a fluidized bed of catalyst particles and
granular polymer.
High density polyethylene (HDPE) means a thermoplastic polymer or
copolymer comprised of at least 50 percent ethylene by weight and having
a density of greater than 0.940 gm/cm\3\3 (58.7 lb/ft\3\).
High pressure process means the conventional production process for
the manufacture of low density polyethylene in which a reaction pressure
of about 15,000 psig (103,000 kPa gauge) or greater is used.
High viscosity poly(ethylene terephthalate) means poly(ethylene
terephthalate) that has an intrinsic viscosity of 0.9 or higher and is
used in such applications as tire cord and seat belts.
Incinerator means an enclosed combustion device that is used for
destroying VOC.
In-situ suspension process means a manufacturing process in which
styrene, blowing agent, and other raw materials are added together
within a reactor for the production of expandable polystyrene.
Intermittent emissions means those gas streams containing VOC that
are generated at intervals during process line operation and includes
both planned and emergency releases.
Liquid phase process means a polymerization process in which the
polymerization reaction is carried out in the liquid phase; i.e., the
monomer(s) and any catalyst are dissolved, or suspended in a liquid
solvent.
Liquid phase slurry process means a liquid phase polymerization
process in which the monomer(s) are in solution (completely dissolved)
in a liquid solvent, but the polymer is in the form of solid particles
suspended in the liquid reaction mixture during the polymerization
reaction; sometimes called a particle form process.
Liquid phase solution process means a liquid phase polymerization
process in which both the monomer(s) and polymer are in solution
(completely dissolved) in the liquid reaction mixture.
Low density polyethylene (LDPE) means a thermoplastic polymer or
copolymer comprised of at least 50 percent ethylene by weight and having
a density of 0.940 g/cm\3\ (58.7 lb/ft\3\) or less.
Low pressure process means a production process for the manufacture
of low density polyethylene in which a reaction pressure markedly below
that used in a high pressure process is used. Reaction pressure of
current low pressure processes typically go up to about 300 psig (2,070
kPa gauge).
Low viscosity poly(ethylene terephthalate) means a poly(ethylene
terephthalate) that has an intrinsic viscosity of less than 0.75 and is
used in such applications as clothing, bottle, and film production.
Material recovery section means the equipment that recovers
unreacted or by-product materials from any process section for return to
the process line, off-site purification or treatment, or sale. Equipment
designed to separate unreacted or by-product material from the polymer
product are to be included
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in this process section, provided at least some of the material is
recovered for reuse in the process, off-site purification or treatment,
or sale, at the time the process section becomes an affected facility.
Otherwise such equipment are to be assigned to one of the other process
sections, as appropriate. Equipment that treats recovered materials are
to be included in this process section, but equipment that also treats
raw materials are not to be included in this process section. The latter
equipment are to be included in the raw materials preparation section.
If equipment is used to return unreacted or by-product material directly
to the same piece of process equipment from which it was emitted, then
that equipment is considered part of the process section that contains
the process equipment. If equipment is used to recover unreacted or by-
product material from a process section and return it to another process
section or a different piece of process equipment in the same process
section or sends it off-site for purification, treatment, or sale, then
such equipment are considered part of a material recovery section.
Equipment used for the on-site recovery of ethylene glycol from
poly(ethylene terephthalate) plants, however, are not included in the
material recovery section, but are covered under the standards
applicable to the polymerization reaction section (Sec. 60.562-
1(c)(1)(ii)(A) or (2)(ii)(A)).
Operating day means, for the purposes of these standards, any
calendar day during which equipment used in the manufacture of polymer
was operating for at least 8 hours or one labor shift, whichever is
shorter. Only operating days shall be used in determining compliance
with the standards specified in Sec. 60.562-1(c)(1)(ii)(B), (1)(ii)(C),
(2)(ii)(B), and (2)(ii)(C). Any calendar day in which equipment is used
for less than 8 hours or one labor shift, whichever is less, is not an
``operating day'' and shall not be used as part of the rolling 14-day
period for determining compliance with the standards specified in Sec.
60.562-1(c)(1)(ii)(B), (1)(ii)(C), (2)(ii)(B), and (2)(ii)(C).
Polyethylene means a thermoplastic polymer or copolymer comprised of
at least 50 percent ethylene by weight; see low density polyethylene and
high density polyethylene.
Poly(ethylene terephthalate) (PET) means a polymer or copolymer
comprised of at least 50 percent bis-(2-hydroxyethyl)-terephthalate
(BHET) by weight.
Poly(ethylene terephthalate) (PET) manufacture using dimethyl
terephthalate means the manufacturing of poly(ethylene terephthalate)
based on the esterification of dimethyl terephthalate (DMT) with
ethylene glycol to form the intermediate monomer bis-(2-hydroxyethyl)-
terephthalate (BHET) that is subsequently polymerized to form PET.
Poly(ethylene terephthalate) (PET) manufacture using terephthalic
acid means the manufacturing of poly(ethylene terephthalate) based on
the esterification reaction of terephthalic acid (TPA) with ethylene
glycol to form the intermediate monomer bis-(2-hydroxyethyl)-
terephthalate (BHET) that is subsequently polymerized to form PET.
Polymerization reaction section means the equipment designed to
cause monomer(s) to react to form polymers, including equipment designed
primarily to cause the formation of short polymer chains (oligomers or
low polymers), but not including equipment designed to prepare raw
materials for polymerization, e.g., esterification vessels. For the
purposes of these standards, the polymerization reaction section begins
with the equipment used to transfer the materials from the raw materials
preparation section and ends with the last vessel in which
polymerization occurs. Equipment used for the on-site recovery of
ethylene glycol from poly(ethylene terephthalate) plants, however, are
included in this process section, rather than in the material recovery
process section.
Polypropylene (PP) means a thermoplastic polymer or copolymer
comprised of at least 50 percent propylene by weight.
Polystyrene (PS) means a thermoplastic polymer or copolymer
comprised of at least 80 percent styrene or para-methylstyrene by
weight.
Post-impregnation suspension process means a manufacturing process
in which polystyrene beads are first
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formed in a suspension process, washed, dried, or otherwise finished and
then added with a blowing agent to another reactor in which the beads
and blowing agent are reacted to produce expandable polystyrene.
Process heater means a device that transfers heat liberated by
burning fuel to fluids contained in tubular coils, including all fluids
except water that is heated to produce steam.
Process line means a group of equipment assembled that can operate
independently if supplied with sufficient raw materials to produce
polypropylene, polyethylene, polystyrene, (general purpose, crystal, or
expandable) or poly(ethylene terephthalate) or one of their copolymers.
A process line consists of the equipment in the following process
sections (to the extent that these process sections are present at a
plant): raw materials preparation, polymerization reaction, product
finishing, product storage, and material recovery.
Process section means the equipment designed to accomplish a general
but well-defined task in polymer production. Process sections include
raw materials preparation, polymerization reaction, material recovery,
product finishing, and product storage and may be dedicated to a single
process line or common to more than one process line.
Process unit means equipment assembled to perform any of the
physical and chemical operations in the production of polypropylene,
polyethylene, polystyrene, (general purpose, crystal, or expandable), or
poly(ethylene terephthalate) or one of their copolymers. A process unit
can operate independently if supplied with sufficient feed or raw
materials and sufficient storage facilities for the product. Examples of
process units are raw materials handling and monomer recovery.
Product finishing section means the equipment that treats, shapes,
or modifies the polymer or resin to produce the finished end product of
the particular facility, including equipment that prepares the product
for product finishing. For the purposes of these standards, the product
finishing section begins with the equipment used to transfer the
polymerized product from the polymerization reaction section and ends
with the last piece of equipment that modifies the characteristics of
the polymer. Product finishing equipment may accomplish product
separation, extruding and pelletizing, cooling and drying, blending,
additives introduction, curing, or annealing. Equipment used to separate
unreacted or by-product material from the product are to be included in
this process section, provided the material separated from the polymer
product is not recovered at the time the process section becomes an
affected facility. If the material is being recovered, then the
separation equipment are to be included in the material recovery
section. Product finishing does not include polymerization, the physical
mixing of the pellets to obtain a homogenous mixture of the polymer
(except as noted below), or the shaping (such as fiber spinning,
molding, or fabricating) or modification (such as fiber stretching and
crimping) of the finished end product. If physical mixing occurs in
equipment located between product finishing equipment (i.e., before all
the chemical and physical characteristics have been ``set'' by virtue of
having passed through the last piece of equipment in the product
finishing section), then such equipment are to be included in this
process section. Equipment used to physically mix the finished product
that are located after the last piece of equipment in the product
finishing section are part of the product storage section.
Product storage section means the equipment that is designed to
store the finished polymer or resin end product of the particular
facility. For the purposes of these standards, the product storage
section begins with the equipment used to transfer the finished product
out of the product finishing section and ends with the containers used
to store the final product. Any equipment used after the product
finishing section to recover unreacted or by-product material are to be
considered part of a material recovery section. Product storage does not
include any intentional modification of the characteristics of any
polymer or resin product, but does include equipment that provide a
uniform mixture of product, provided such equipment are used after the
last product finishing
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piece of equipment. This process section also does not include the
shipment of a finished polymer or resin product to another facility for
further finishing or fabrication.
Raw materials preparation section means the equipment located at a
polymer manufacturing plant designed to prepare raw materials, such as
monomers and solvents, for polymerization. For the purposes of these
standards, this process section begins with the equipment used to
transfer raw materials from storage and recovered material from material
recovery process sections, and ends with the last piece of equipment
that prepares the material for polymerization. The raw materials
preparation section may include equipment that accomplishes
purification, drying, or other treatment of raw materials or of raw and
recovered materials together, activation of catalysts, and
esterification including the formation of some short polymer chains
(oligomers), but does not include equipment that is designed primarily
to accomplish the formation of oligomers, the treatment of recovered
materials alone, or the storage of raw materials.
Recovery system means an individual unit or series of material
recovery units, such as absorbers, condensers, and carbon adsorbers,
used for recovering volatile organic compounds.
Total organic compounds (TOC) means those compounds measured
according to the procedures specified in Sec. 60.564.
Vent stream means any gas stream released to the atmosphere directly
from an emission source or indirectly either through another piece of
process equipment or a material recovery device that constitutes part of
the normal recovery operations in a polymer process line where potential
emissions are recovered for recycle or resale, and any gas stream
directed to an air pollution control device. The emissions released from
an air pollution control device are not considered a vent stream unless,
as noted above, the control device is part of the normal material
recovery operations in a polymer process line where potential emissions
are recovered for recycle or resale.
Volatile organic compounds (VOC) means, for the purposes of these
standards, any reactive organic compounds as defined in Sec. 60.2
Definitions.
[55 FR 51035, Dec. 11, 1990; 56 FR 9178, Mar. 5, 1991; 56 FR 12299, Mar.
22, 1991; 65 FR 61767, Oct. 17, 2000]