(a) For an affected source complying with the requirements in subpart SS of this part 63, the terms used in this subpart and in subpart SS of this part 63 have the meaning given them in Sec. 63.981, except as specified in Sec. Sec. 63.8000(d)(5)(ii) and (7), 63.8010(c)(2), 63.8025(b), and paragraph (g) of this section.
(b) For an affected source complying with the requirements in subpart TT of this part 63, the terms used in this subpart and in subpart TT of this part 63 have the meaning given them in Sec. 63.1001.
(c) For an affected source complying with the requirements in subpart UU of this part 63, the terms used in this subpart and in subpart UU of this part 63 have the meaning given them in Sec. 63.1020.
(d) For an affected source complying with the requirements in subpart WW of this part 63, the terms used in this subpart and subpart WW of this part 63 have the meaning given them in Sec. 63.1061, except as specified in Sec. Sec. 63.8000(d)(7), 63.8010(c)(2), and paragraph (g) of this section.
(e) For an affected source complying with requirements in Sec. Sec. 63.1253, 63.1257, and 63.1258, the terms used in this subpart and in Sec. Sec. 63.1253, 63.1257, and 63.1258 have the meaning given them in Sec. 63.1251, except as specified in Sec. 63.8000(d)(7) and paragraph (g) of this section.
(f) For an affected source complying with the requirements of Sec. 63.104, the terms used in this subpart and in Sec. 63.104 have the meaning given them in Sec. 63.101, except as specified in Sec. 63.8000(d)(7) and paragraph (g) of this section.
(g) All other terms used in this subpart are defined in the CAA, in 40 CFR 63.2, and in this paragraph (g). If a term is defined in Sec. 63.2, Sec. 63.981, Sec. 63.1001, Sec. 63.1020, Sec. 63.1061, or Sec. 63.1251 and in this paragraph (g), the definition in this paragraph (g) applies for the purposes of this subpart.
Bulk loading means the loading, into a tank truck or rail car, of liquid coating products that contain one or more of the organic HAP, as defined in section 112 of the CAA, from a loading rack. A loading rack is the system used to fill tank trucks and railcars at a single geographic site.
Coating means a material such as paint, ink, or adhesive that is intended to be applied to a substrate and consists of a mixture of resins, pigments, solvents, and/or other additives, where the material is produced by a manufacturing operation where materials are blended, mixed, diluted, or otherwise formulated. Coating does not include materials made in processes where a formulation component is synthesized by chemical reaction or separation activity and then transferred to another vessel where it is formulated to produce a material used as a coating, where the synthesized or separated component is not stored prior to formulation. Typically, coatings include products described by the following North American Industry Classification System (NAICS) codes, code 325510, Paint and Coating Manufacturing, code 325520, Adhesive and Sealant Manufacturing, and code 325910, Ink Manufacturing.
Construction means the onsite fabrication, erection, or installation of an affected source. Addition of new equipment to an affected source does not constitute construction, but it may constitute reconstruction of the affected source if it satisfies the definition of reconstruction in Sec. 63.2.
Deviation means any instance in which an affected source subject to this subpart, or an owner or operator of such a source:
(1) Fails to meet any requirement or obligation established by this subpart including, but not limited to, any emission limit, operating limit, or work practice standard;
(2) Fails to meet any term or condition that is adopted to implement an applicable requirement in this subpart and that is included in the operating permit for any affected source required to obtain such a permit; or
(3) Fails to meet any emission limit, operating limit, or work practice standard in this subpart during startup, shutdown, or malfunction, regardless of whether or not such failure is permitted by this subpart.
Enhanced biological treatment system means an aerated, thoroughly mixed treatment unit(s) that contains biomass suspended in water followed by a clarifier that removes biomass from the treated water and recycles recovered biomass to the aeration unit. The mixed liquor volatile suspended solids (biomass) is greater than 1 kilogram per cubic meter throughout each aeration unit. The biomass is suspended and aerated in the water of the aeration unit(s) either by submerged air flow or mechanical agitation. A thoroughly mixed treatment unit is a unit that is designed and operated to approach or achieve uniform biomass distribution and organic compound concentration throughout the aeration unit by quickly dispersing the recycled biomass and the wastewater entering the unit.
Excess emissions means emissions greater than those allowed by the emission limit.
Group 1a storage tank means a storage tank at an existing source with a capacity greater than or equal to 20,000 gal storing material that has a maximum true vapor pressure of total organic HAP greater than or equal to 1.9 pounds per square inch, absolute (psia). Group 1a storage tank also means a storage tank at a new source with either a capacity greater than or equal to 25,000 gal storing material that has a maximum true vapor pressure of total HAP greater than or equal to 0.1 psia or a capacity greater than or equal to 20,000 gal and less than 25,000 gal storing material that has a maximum true vapor pressure of total HAP greater than or equal to 1.5 psia.
Group 1b storage tank means a storage tank at a new source that has a capacity greater than or equal to 10,000 gal, stores material that has a maximum true vapor pressure of total organic HAP greater than or equal to 0.02 psia, and is not a Group 1a storage tank.
Group 2 storage tank means a storage tank that does not meet the definition of a Group 1a or Group 1b storage tank.
Group 1 transfer operations means all bulk loading of coating products if the coatings contain greater than or equal to 3.0 million gallons per year (gal/yr) of HAP with a weighted average HAP partial pressure greater than or equal to 1.5 psia.
Group 2 transfer operations means bulk loading of coating products that does not meet the definition of Group 1 transfer operations, and all loading of coating products from a loading rack to other types of containers such as cans, drums, and totes.
Group 1 wastewater stream means a wastewater stream that contains total partially soluble and soluble HAP at an annual average concentration greater than or equal to 4,000 parts per million by weight (ppmw) and load greater than or equal to 750 pounds per year (lb/yr) at an existing source or greater than or equal to 1,600 ppmw and any partially soluble and soluble HAP load at a new source.
Group 2 wastewater stream means a wastewater stream that does not meet the definition of a Group 1 wastewater stream.
Halogenated vent stream means a vent stream determined to contain halogen atoms in organic compounds at a concentration greater than or equal to 20 ppmv as determined by the procedures specified in Sec. 63.8000(b).
Hydrogen halide and halogen HAP means hydrogen chloride, chlorine, and hydrogen fluoride.
In organic HAP service means that a piece of equipment either contains or contacts a fluid (liquid or gas) that is at least 5 percent by weight of total organic HAP as determined according to the provisions of Sec. 63.180(d). The provisions of Sec. 63.180(d) also specify how to determine that a piece of equipment is not in organic HAP service.
Large control device means a control device that controls total HAP emissions of greater than or equal to 10 tpy, before control.
Maximum true vapor pressure means the equilibrium partial pressure exerted by the total organic HAP in the stored or transferred liquid at the temperature equal to the highest calendar-month average of the liquid storage or transfer temperature for liquids stored or transferred above or below the ambient temperature or at the local maximum monthly average temperature as reported by the National Weather Service for liquids stored or transferred at the ambient temperature, as determined:
(1) In accordance with methods described in American Petroleum Institute Publication 2517, Evaporative Loss From External Floating-Roof Tanks (incorporated by reference as specified in Sec. 63.14 of subpart A of this part 63); or
(2) As obtained from standard reference texts; or
(3) As determined by the American Society for Testing and Materials Method D2879-83 (incorporated by reference as specified in Sec. 63.14 of subpart A of this part); or
(4) Any other method approved by the Administrator.
Partially soluble HAP means HAP listed in Table 7 of this subpart.
Point of determination (POD) means each point where process wastewater exits the miscellaneous coating operations.
Note to definition for point of determination: The regulation allows determination of the characteristics of a wastewater stream at the point of determination or downstream of the point of determination if corrections are made for changes in flow rate and annual average concentration of partially soluble and soluble HAP compounds as determined in Sec. 63.144. Such changes include losses by air emissions; reduction of annual average concentration or changes in flow rate by mixing with other water or wastewater streams; and reduction in flow rate or annual average concentration by treating or otherwise handling the wastewater stream to remove or destroy HAP.
Process vessel means any stationary or portable tank or other vessel with a capacity greater than or equal to 250 gal and in which mixing, blending, diluting, dissolving, temporary holding, and other processing steps occur in the manufacturing of a coating.
Process vessel vent means a vent from a process vessel or vents from multiple process vessels that are manifolded together into a common header, through which a HAP-containing gas stream is, or has the potential to be, released to the atmosphere. Emission streams that are undiluted and uncontrolled containing less than 50 ppmv HAP, as determined through process knowledge that no HAP are present in the emission stream or using an engineering assessment as discussed in Sec. 63.1257(d)(2)(ii), test data using Method 18 of 40 CFR part 60, appendix A, or any other test method that has been validated according to the procedures in Method 301 of appendix A of this part, are not considered process vessel vents. Flexible elephant trunk systems when used with closed vent systems and drawing ambient air (i.e., the system is not ducted, piped, or otherwise connected to the unit operations) away from operators when vessels are opened are not process vessel vents. Process vessel vents do not include vents on storage tanks, wastewater emission sources, or pieces of equipment subject to the requirements in Table 3 of this subpart. A gas stream going to a fuel gas system is not a process vessel vent. A gas stream routed to a process for a process purpose is not a process vessel vent.
Recovery device, as used in the wastewater provisions, means an individual unit of equipment used for the purpose of recovering chemicals for fuel value (i.e., net positive heating value), use, reuse, or for sale for fuel value, use, or reuse. Examples of equipment that may be recovery devices include organic removal devices such as decanters, strippers, or thin-film evaporation units. To be a recovery device, a decanter and any other equipment based on the operating principle of gravity separation must receive only multi-phase liquid streams. A recovery device is considered part of the miscellaneous coating manufacturing operations.
Responsible official means responsible official as defined in 40 CFR 70.2.
Safety device means a closure device such as a pressure relief valve, frangible disc, fusible plug, or any other type of device which functions exclusively to prevent physical damage or permanent deformation to a unit or its air emission control equipment by venting gases or vapors directly to the atmosphere during unsafe conditions resulting from an unplanned, accidental, or emergency event. For the purposes of this subpart, a safety device is not used for routine venting of gases or vapors from the vapor headspace underneath a cover such as during filling of the unit or to adjust the pressure in response to normal daily diurnal ambient temperature fluctuations. A safety device is designed to remain in a closed position during normal operations and open only when the internal pressure, or another relevant parameter, exceeds the device threshold setting applicable to the air emission control equipment as determined by the owner or operator based on manufacturer recommendations, applicable regulations, fire protection and prevention codes and practices, or other requirements for the safe handling of flammable, combustible, explosive, reactive, or hazardous materials.
Shutdown means the cessation of operation of an affected source, any process vessels within an affected source, or equipment required or used to comply with this subpart if steps taken to cease operation differ from those under routine procedures for removing the vessel or equipment from service. Shutdown also applies to the emptying and degassing of storage tanks.
Small control device means a control device that controls total HAP emissions of less than 10 tpy, before control.
Soluble HAP means the HAP listed in Table 8 of this subpart.
Startup means the setting in operation of a new affected source. For new equipment added to an affected source, including equipment required or used to comply with this subpart, startup means the first time the equipment is put into operation. Startup includes the setting in operation of equipment any time the steps taken differ from routine procedures for putting the equipment into operation.
Storage tank means a tank or other vessel that is used to store organic liquids that contain one or more HAP as raw material feedstocks or products. The following are not considered storage tanks for the purposes of this subpart:
(1) Vessels permanently attached to motor vehicles such as trucks, railcars, barges, or ships;
(2) Pressure vessels designed to operate in excess of 204.9 kilopascals and without emissions to the atmosphere;
(3) Vessels storing organic liquids that contain HAP only as impurities;
(4) Wastewater storage tanks; and
(5) Process vessels.
Total organic compounds or (TOC) means the total gaseous organic compounds (minus methane and ethane) in a vent stream.
Wastewater storage tank means a stationary structure that is designed to contain an accumulation of wastewater and is constructed primarily of nonearthen materials (e.g., wood, concrete, steel, plastic) which provide structural support.
Wastewater stream means water that is discarded from miscellaneous coating manufacturing operations through a POD, and that contains an annual average concentration of total partially soluble and soluble HAP compounds of at least 1,600 ppmw at any flow rate. For the purposes of this subpart, noncontact cooling water is not considered a wastewater stream.
Work practice standard means any design, equipment, work practice, or operational standard, or combination thereof, that is promulgated pursuant to section 112(h) of the Clean Air Act. [68 FR 69185, Dec. 11, 2003, as amended at 70 FR 25682, May 13, 2005; 71 FR 58503, Oct. 4, 2006]
Sec. Table 1 to Subpart HHHHH of Part 63--Emission Limits and Work
Practice Standards for Process Vessels
As required in Sec. 63.8005, you must meet each emission limit and work practice standard in the following table that applies to your process vessels. ------------------------------------------------------------------------
And you must . . .
For each . . . You must . . .------------------------------------------------------------------------1. Portable process vessel at an a. Equip the Nonapplicable.
existing source. vessel with a
cover or lid that
must be in place
at all times when
the vessel
contains a HAP,
except for
material
additions and
sampling.------------------------------------------------------------------------2. Stationary process vessel at a. Equip the i. Considering
an existing source. vessel with a both capture and
cover or lid that any combination
must be in place of control
at all times when (except a flare),
the vessel reduce emissions
contains a HAP, of organic HAP
except for with a vapor
material existing pressure
additions and =0.6
sampling; or kPa by =75 percent by
weight, and
reduce emissions
of organic HAP
with a vapor
pressure <0.6 kPa
by =60
percent by
weight.
b. Equip the i. Reduce
vessel with a emissions of
tightly fitting organic HAP with
vented cover or a vapor pressure
lid that must be =0.6
closed at all kPa by =75 percent by
vessel contains weight, and
HAP, except for reduce emissions
material of organic HAP
additions and with a vapor
sampling. pressure <0.6 kPa
by =60
percent by
weight, by
venting emissions
through a closed-
vent system to
any combination
of control
devices (except a
flare); or
ii. Reduce
emissions of
total organic HAP
by venting
emissions from a
non-halogenated
vent stream
through a closed-
vent system to a
flare; or
iii. Reduce
emissions of
total organic HAP
by venting
emissions through
a closed-vent
system to a
condenser that
reduces the
outlet gas
temperature to:------------------------------------------------------------------------
<10 C if the
process vessel
contains HAP with
a partial
pressure <0.6
kPa, or
<2 C if the
process vessel
contains HAP with
a partial
pressure =0.6 kPa and
<17.2 kPa, or
<-5 C if the
process vessel
contains HAP with
a partial
pressure =17.2 kPa.3. Portable and stationary a. Equip the i. Reduce
process vessel at a new source. vessel with a emissions of
tightly fitting total organic HAP
vented cover or by =95
lid that must be percent by weight
closed at all by venting
times when the emissions through
vessel contains a closed-vent
HAP, except for system to any
material combination of
additions and control devices
sampling. (except a flare);
or
ii. Reduce
emissions of
total organic HAP
by venting
emissions from a
non-halogenated
vent stream
through a closed-
vent system to a
flare; or
iii. Reduce
emissions of
total organic HAP
by venting
emissions through
a closed-vent
system to a
condenser that
reduces the
outlet gas
temperature to:
<-4 C if the
process vessel
contains HAP with
a partial
pressure <0.7
kPa, or------------------------------------------------------------------------
<-20 C if the
process vessel
contains HAP with
a partial
pressure =0.7 kPa and
<17.2 kPa, or
<-30 C if the
process vessel
contains HAP with
a partial
pressure =17.2 kPa.4. Halogenated vent steam from a a. Use a halogen i. Reduce overall
process vessel subject to the reduction device emissions of
requirements of item 2 or 3 of after the hydrogen halide
this table for which you use a combustion and halogen HAP
combustion control device to control device; by =95
control organic HAP emissions. or percent; or
ii. Reduce overall
emissions of
hydrogen halide
and halogen HAP
to <=0.45
kilogram per hour
(kg/hr).
b. Use a halogen Reduce the halogen
reduction device atom mass
before the emission rate to
combustion <=0.45 kg/hr.
control device.------------------------------------------------------------------------ [68 FR 69185, Dec. 11, 2003, as amended at 70 FR 25682, May 13, 2005]
Sec. Table 2 to Subpart HHHHH of Part 63--Emission Limits for Storage
Tanks
As required in Sec. 63.8010, you must meet each emission limit in the following table that applies to your storage tanks. ------------------------------------------------------------------------
For each . . . Then you must . . .------------------------------------------------------------------------1. Group 1a storage tank..... a. Comply with the requirements of
subpart WW of this part, except as
specified in Sec. 63.8010(b); or
b. Reduce total organic HAP emissions
from the storage tank by =90
percent by weight by venting emissions
through a closed-vent system to any
combination of control devices
(excluding a flare); or
c. Reduce total organic HAP emissions
from the storage tank by venting
emissions from a non-halogenated vent
stream through a closed-vent system to a
flare.------------------------------------------------------------------------2. Group 1b storage tank..... a. Comply with the requirements of
subpart WW of this part, except as
specified in Sec. 63.8010(b); or
b. Reduce total organic HAP emissions
from the storage tank by =80
percent by weight by venting emissions
through a closed-vent system to any
combination of control devices
(excluding a flare); or
c. Reduce total organic HAP emissions
from the storage tank by venting
emissions from a non-halogenated vent
stream through a closed-vent system to a
flare.------------------------------------------------------------------------
Sec. Table 3 to Subpart HHHHH of Part 63--Requirements for Equipment
Leaks
As required in Sec. 63.8015, you must meet each requirement in the following table that applies to your equipment leaks. ------------------------------------------------------------------------
For all . . . You must . . .------------------------------------------------------------------------1. Equipment that is in a. Comply with the requirements in Sec.
organic HAP service at an Sec. 63.424(a) through (d) and
existing source. 63.428(e), (f), and (h)(4), except as
specified in Sec. 63.8015(b); or
b. Comply with the requirements of
subpart TT of this part; or
c. Comply with the requirements of
subpart UU of this part, except as
specified in Sec. 63.8015(c) and (d).------------------------------------------------------------------------2. Equipment that is in a. Comply with the requirements of
organic HAP service at a new subpart TT of this part; or
source. b. Comply with the requirements of
subpart UU of this part, except as
specified in Sec. 63.8015(c) and (d).------------------------------------------------------------------------ [68 FR 58190, Oct. 8, 2003, as amended at 71 FR 69021, Nov. 29, 2006]
Sec. Table 4 to Subpart HHHHH of Part 63--Emission Limits and Work
Practice Standards for Wastewater Streams
As required in Sec. 63.8020, you must meet each emission limit and work practice standard in the following table that applies to your wastewater streams. ------------------------------------------------------------------------
For each . . . You must . . .------------------------------------------------------------------------1. Wastewater tank used to Maintain a fixed roof, which may have
store a Group 1 wastewater openings necessary for proper venting of
stream. the tank, such as pressure/vacuum vent
or j-pipe vent.------------------------------------------------------------------------2. Group 1 wastewater stream. a. Convey using hard-piping and treat the
wastewater as a hazardous waste in
accordance with 40 CFR part 264, 265, or
266 either onsite or offsite; or
b. If the wastewater contains <50 ppmw of
partially soluble HAP, you may elect to
treat the wastewater in an enhanced
biological treatment system that is
located either onsite or offsite.------------------------------------------------------------------------
Sec. Table 5 to Subpart HHHHH of Part 63--Emission Limits and Work
Practice Standards for Transfer Operations
As required in Sec. 63.8025, you must meet each emission limit and work practice standard in the following table that applies to your transfer operations. ------------------------------------------------------------------------
For each . . . You must. . . .------------------------------------------------------------------------1. Group 1 transfer operation a. Reduce emissions of total organic HAP
vent stream. by =75 percent by weight by
venting emissions through a closed-vent
system to any combination of control
devices (except a flare); or
b. Reduce emissions of total organic HAP
by venting emissions from a non-
halogenated vent stream through a closed-
vent system to a flare; or
c. Use a vapor balancing system designed
and operated to collect organic HAP
vapors displaced from tank trucks and
railcars during loading and route the
collected HAP vapors to the storage tank
from which the liquid being loaded
originated or to another storage tank
connected by a common header.------------------------------------------------------------------------2. Halogenated Group 1 a. Use a halogen reduction device after
transfer operation vent the combustion device to reduce
stream for which you use a emissions of hydrogen halide and halogen
combustion device to control HAP by =95 percent by weight
organic HAP emissions. or to <=0.45 kg/hr; or
b. Use a halogen reduction device before
the combustion device to reduce the
halogen atom mass emission rate to
<=0.45 kg/hr.------------------------------------------------------------------------ Sec. Table 6 to Subpart HHHHH of Part 63--Requirements for Heat Exchange
Systems
As required in Sec. 63.8030, you must meet each requirement in the following table that applies to your heat exchange systems. ------------------------------------------------------------------------
For each . . . You must . . .------------------------------------------------------------------------Heat exchange system, as Comply with the requirements in Sec.
defined in Sec. 63.101. 63.104, except as specified in Sec.
63.8030.------------------------------------------------------------------------
Sec. Table 7 to Subpart HHHHH of Part 63--Partially Soluble Hazardous
Air Pollutants
As specified in Sec. 63.8020, the partially soluble HAP in wastewater that are subject to management and treatment requirements in this subpart are listed in the following table: ------------------------------------------------------------------------
Chemical name . . . CAS No.------------------------------------------------------------------------1. 1,1,1-Trichloroethane (methyl chloroform)............... 715562. 1,1,2,2-Tetrachloroethane............................... 793453. 1,1,2-Trichloroethane................................... 790054. 1,1-Dichloroethylene (vinylidene chloride).............. 753545. 1,2-Dibromoethane....................................... 1069346. 1,2-Dichloroethane (ethylene dichloride)................ 1070627. 1,2-Dichloropropane..................................... 788758. 1,3-Dichloropropene..................................... 5427569. 2,4,5-Trichlorophenol................................... 9595410. 2-Butanone (MEK)....................................... 7893311. 1,4-Dichlorobenzene.................................... 10646712. 2-Nitropropane......................................... 7946913. 4-Methyl-2-pentanone (MIBK)............................ 10810114. Acetaldehyde........................................... 7507015. Acrolein............................................... 10702816. Acrylonitrile.......................................... 10713117. Allyl chloride......................................... 10705118. Benzene................................................ 7143219. Benzyl chloride........................................ 10044720. Biphenyl............................................... 9252421. Bromoform (tribromomethane)............................ 7525222. Bromomethane........................................... 7483923. Butadiene.............................................. 10699024. Carbon disulfide....................................... 7515025. Chlorobenzene.......................................... 10890726. Chloroethane (ethyl chloride).......................... 7500327. Chloroform............................................. 6766328. Chloromethane.......................................... 7487329. Chloroprene............................................ 12699830. Cumene................................................. 9882831. Dichloroethyl ether.................................... 11144432. Dinitrophenol.......................................... 5128533. Epichlorohydrin........................................ 10689834. Ethyl acrylate......................................... 14088535. Ethylbenzene........................................... 10041436. Ethylene oxide......................................... 7521837. Ethylidene dichloride.................................. 7534338. Hexachlorobenzene...................................... 11874139. Hexachlorobutadiene.................................... 8768340. Hexachloroethane....................................... 6772141. Methyl methacrylate.................................... 8062642. Methyl-t-butyl ether................................... 163404443. Methylene chloride..................................... 7509244. N-hexane............................................... 11054345. N,N-dimethylaniline.................................... 12169746. Naphthalene............................................ 9120347. Phosgene............................................... 7544548. Propionaldehyde........................................ 12338649. Propylene oxide........................................ 7556950. Styrene................................................ 10042551. Tetrachloroethylene (perchloroethylene)................ 12718452. Tetrachloromethane (carbon tetrachloride).............. 5623553. Toluene................................................ 10888354. Trichlorobenzene (1,2,4-).............................. 12082155. Trichloroethylene...................................... 79016
56. Trimethylpentane....................................... 54084157. Vinyl acetate.......................................... 10805458. Vinyl chloride......................................... 7501459. Xylene (m)............................................. 10838360. Xylene (o)............................................. 9547661. Xylene (p)............................................. 106423------------------------------------------------------------------------ [68 FR 69185, Dec. 11, 2003, as amended at 70 FR 25683, May 13, 2005]
Sec. Table 8 to Subpart FFFF of Part 63--Soluble Hazardous Air
Pollutants
As specified in Sec. 63.8020, the soluble HAP in wastewater that are subject to management and treatment requirements of this subpart are listed in the following table: ------------------------------------------------------------------------
Chemical name . . . CAS No.------------------------------------------------------------------------1. Acetonitrile............................................ 750582. Acetophenone............................................ 988623. Diethyl sulfate......................................... 646754. Dimethyl hydrazine (1,1)................................ 571475. Dimethyl sulfate........................................ 777816. Dinitrotoluene (2,4).................................... 1211427. Dioxane (1,4)........................................... 1239118. Ethylene glycol dimethyl ether.......................... 1107149. Ethylene glycol monobutyl ether acetate................. 11207210. Ethylene glycol monomethyl ether acetate............... 11049611. Isophorone............................................. 7859112. Methanol............................................... 6756113. Nitrobenzene........................................... 9895314. Toluidine (o-)......................................... 9553415. Triethylamine.......................................... 121448------------------------------------------------------------------------ [68 FR 69185, Dec. 11, 2003, as amended at 70 FR 25683, May 13, 2005]
Sec. Table 9 to Subpart HHHHH of Part 63--Requirements for Reports
As required in Sec. 63.8075(a) and (b), you must submit each report that applies to you on the schedule shown in the following table: ------------------------------------------------------------------------
The report must You must submit
You must submit a . . . contain . . . the report . . .------------------------------------------------------------------------1. Precompliance report......... The information At least 6 months
specified in Sec. prior to the
63.8075(c). compliance date;
or for new
sources, with the
application for
approval of
construction or
reconstruction.------------------------------------------------------------------------2. Notification of compliance The information No later than 150
status report. specified in Sec. days after the
63.8075(d). compliance date
specified in Sec.
63.7995.------------------------------------------------------------------------3. Compliance report............ The information Semiannually
specified in Sec. according to the
63.8075(e). requirements in
Sec.
63.8075(b).------------------------------------------------------------------------
Sec. Table 10 to Subpart HHHHH of Part 63--Applicability of General
Provisions to Subpart HHHHH
As specified in Sec. 63.8095, the parts of the General Provisions that apply to you are shown in the following table: ----------------------------------------------------------------------------------------------------------------
Citation Subject Explanation----------------------------------------------------------------------------------------------------------------Sec. 63.1............................. Applicability.............. Yes.Sec. 63.2............................. Definitions................ Yes.Sec. 63.3............................. Units and Abbreviations.... Yes.Sec. 63.4............................. Prohibited Activities...... Yes.Sec. 63.5............................. Construction/Reconstruction Yes.Sec. 63.6(a).......................... Applicability.............. Yes.Sec. 63.6(b)(1)-(4)................... Compliance Dates for New Yes.
and Reconstructed sources.Sec. 63.6(b)(5)....................... Notification............... Yes.Sec. 63.6(b)(6)....................... [Reserved].................
Sec. 63.6(b)(7)....................... Compliance Dates for New Yes.
and Reconstructed Area
Sources That Become Major.Sec. 63.6(c)(1)-(2)................... Compliance Dates for Yes.
Existing Sources.Sec. 63.6(c)(3)-(4)................... [Reserved].................Sec. 63.6(c)(5)....................... Compliance Dates for Yes.
Existing Area Sources That
Become Major.Sec. 63.6(d).......................... [Reserved].................Sec. 63.6(e)(1)-(2)................... Operation & Maintenance.... Yes.Sec. 63.6(e)(3)(i), (ii), and (v) SSMP....................... Yes, except information regarding Group 2
through (viii). emission points and equipment leaks is
not required in the SSMP, as specified
in Sec. 63.8080(f).Sec. 63.6(e)(3)(iii) and (iv)......... Recordkeeping and Reporting No, Sec. Sec. 63.998(d)(3) and
During Startup, Shutdown, 63.998(c)(1)(ii)(D) through (G) specify
and Malfunction (SSM). the recordkeeping requirement for SSM
events, and Sec. 63.8075(e)(5)
specifies reporting requirements.Sec. 63.6(e)(3)(ix)................... Title V permit............. Yes.Sec. 63.6(f)(1)....................... Compliance Except During Yes.
SSM.Sec. 63.6(f)(2)-(3)................... Methods for Determining Yes.
Compliance.Sec. 63.6(g)(1)-(3)................... Alternative Standard....... Yes.Sec. 63.6(h).......................... Opacity/Visible Emission Only for flares for which Method 22
(VE) Standards. observations are required as part of a
flare compliance assessment.Sec. 63.6(i)(1)-(14).................. Compliance Extension....... Yes.Sec. 63.6(j).......................... Presidential Compliance Yes.
Exemption.Sec. 63.7(a)(1)-(2)................... Performance Test Dates..... Yes, except substitute 150 days for 180
days.Sec. 63.7(a)(3)....................... CAA Section 114 Authority.. Yes, and this paragraph also applies to
flare compliance assessments as
specified under Sec. 63.997(b)(2).Sec. 63.7(b)(1)....................... Notification of Performance Yes.
Test.Sec. 63.7(b)(2)....................... Notification of Yes.
Rescheduling.Sec. 63.7(c).......................... Quality Assurance/Test Plan Yes, except the test plan must be
submitted with the notification of the
performance test if the control device
controls process vessels.Sec. 63.7(d).......................... Testing Facilities......... Yes.Sec. 63.7(e)(1)....................... Conditions for Conducting Yes, except that performance tests for
Performance Tests. process vessels must be conducted under
worst-case conditions as specified in
Sec. 63.8005.Sec. 63.7(e)(2)....................... Conditions for Conducting Yes.
Performance Tests.Sec. 63.7(e)(3)....................... Test Run Duration.......... Yes.Sec. 63.7(f).......................... Alternative Test Method.... Yes.Sec. 63.7(g).......................... Performance Test Data Yes.
Analysis.Sec. 63.7(h).......................... Waiver of Tests............ Yes.Sec. 63.8(a)(1)....................... Applicability of Monitoring Yes.
Requirements.Sec. 63.8(a)(2)....................... Performance Specifications. Yes.Sec. 63.8(a)(3)....................... [Reserved].................Sec. 63.8(a)(4)....................... Monitoring with Flares..... Yes.Sec. 63.8(b)(1)....................... Monitoring................. Yes.Sec. 63.8(b)(2)-(3)................... Multiple Effluents and Yes.
Multiple Monitoring
Systems.Sec. 63.8(c)(1)....................... Monitoring System Operation Yes.
and Maintenance.Sec. 63.8(c)(1)(i).................... Maintain and operate CMS... Yes.Sec. 63.8(c)(1)(ii)................... Routine repairs............ Yes.Sec. 63.8(c)(1)(iii).................. SSMP for CMS............... Yes.Sec. 63.8(c)(2)-(3)................... Monitoring System Yes.
Installation.Sec. 63.8(c)(4)....................... Requirements............... Only for CEMS; requirements for CPMS are
specified in referenced subpart SS of 40
CFR part 63. This subpart does not
contain requirements for continuous
opacity monitoring systems (COMS).Sec. 63.8(c)(4)(i).................... CMS Requirements........... No. This subpart does not require COMS.Sec. 63.8(c)(4)(ii)................... CMS requirements........... Yes.Sec. 63.8(c)(5)....................... COMS Minimum Procedures.... No. This subpart does not contain opacity
or VE limits.Sec. 63.8(c)(6)....................... CMS Requirements........... Only for CEMS; requirements for CPMS are
specified in referenced subpart SS of 40
CFR part 63.Sec. 63.8(c)(7)-(8)................... CMS Requirements........... Only for CEMS. Requirements for CPMS are
specified in referenced subpart SS of 40
CFR part 63.
Sec. 63.8(d).......................... CMS Quality Control........ Only for CEMS; requirements for CPMS are
specified in referenced subpart SS of 40
CFR part 63.Sec. 63.8(e).......................... CMS Performance Evaluation. Section 63.8(e)(6)(ii) does not apply
because this subpart does not require
COMS. Other sections apply only for
CEMS; requirements for CPMS are
specified in referenced subpart SS of 40
CFR part 63.Sec. 63.8(f)(1)-(5)................... Alternative Monitoring Yes, except you may also request approval
Method. using the precompliance report.Sec. 63.8(f)(6)....................... Alternative to Relative Only for CEMS.
Accuracy Test.Sec. 63.8(g)(1)-(4)................... Data Reduction............. Only when using CEMS, except Sec.
63.8(g)(2) does not apply because data
reduction requirements for CEMS are
specified in Sec. 63.8000(d)(4)(iv).
The requirements for COMS do not apply
because this subpart has no opacity or
VE limits.Sec. 63.8(g)(5)....................... Data Reduction............. No. Requirements for CEMS are specified
in Sec. 63.8000(d)(4).
Requirements for CPMS are specified in
referenced subpart SS of 40 CFR part 63.Sec. 63.9(a).......................... Notification Requirements.. Yes.Sec. 63.9(b)(1)-(5)................... Initial Notifications...... Yes.Sec. 63.9(c).......................... Request for Compliance Yes.
Extension.Sec. 63.9(d).......................... Notification of Special Yes.
Compliance Requirements
for New Source.Sec. 63.9(e).......................... Notification of Performance Yes.
Test.Sec. 63.9(f).......................... Notification of VE/Opacity No. This subpart does not contain opacity
Test. or VE limits.Sec. 63.9(g).......................... Additional Notifications Only for CEMS; requirements for CPMS are
When Using CMS. specified in referenced subpart SS of 40
CFR part 63.Sec. 63.9(h)(1)-(6)................... Notification of Compliance Yes, except this subpart has no opacity
Status. or VE limits, and Sec. 63.9(h)(2) does
not apply because Sec. 63.8075(d)
specifies the required contents and due
date of the notification of compliance
status report.Sec. 63.9(i).......................... Adjustment of Submittal Yes.
Deadlines.Sec. 63.9(j).......................... Change in Previous No, Sec. 63.8075(e)(8) specifies
Information. reporting requirements for process
changes.Sec. 63.10(a)......................... Recordkeeping/Reporting.... Yes.Sec. 63.10(b)(1)...................... Recordkeeping/Reporting.... Yes.Sec. 63.10(b)(2)(i)-(iv).............. Records related to SSM..... No, Sec. Sec. 63.998(d)(3) and
63.998(c)(1)(ii)(D) through (G) specify
recordkeeping requirements for periods
of SSM.Sec. 63.10(b)(2)(iii)................. Records related to Yes.
maintenance of air
pollution control
equipment.Sec. 63.10(b)(2)(vi), (x), and (xi)... CMS Records................ Only for CEMS; requirements for CPMS are
specified in referenced subpart SS of 40
CFR part 63.Sec. 63.10(b)(2)(vii)-(ix)............ Records.................... Yes.Sec. 63.10(b)(2)(xii)................. Records.................... Yes.Sec. 63.10(b)(2)(xiii)................ Records.................... Yes.Sec. 63.10(b)(2)(xiv)................. Records.................... Yes.Sec. 63.10(b)(3)...................... Records.................... Yes.Sec. 63.10(c)(1)-(6),(9)-(15)......... Records.................... Only for CEMS; requirements for CPMS are
specified in referenced subpart SS of 40
CFR part 63.Sec. 63.10(c)(7)-(8).................. Records.................... No. Recordkeeping requirements are
specified in Sec. 63.8080.Sec. 63.10(d)(1)...................... General Reporting Yes.
Requirements.Sec. 63.10(d)(2)...................... Report of Performance Test Yes.
Results.Sec. 63.10(d)(3)...................... Reporting Opacity or VE No. This subpart does not contain opacity
Observations. or VE limits.Sec. 63.10(d)(4)...................... Progress Reports........... Yes.Sec. 63.10(d)(5)(i)................... SSM Reports................ No, Sec. 63.8075(e)(5) and (6) specify
the SSM reporting requirements.Sec. 63.10(d)(5)(ii).................. Immediate SSM reports...... No.Sec. 63.10(e)(1)-(2).................. Additional CMS Reports..... Only for CEMS, but Sec. 63.10(e)(2)(ii)
does not apply because this subpart does
not require COMS.Sec. 63.10(e)(3)...................... Reports.................... No. Reporting requirements are specified
in Sec. 63.8075.Sec. 63.10(e)(3)(i)-(iii)............. Reports.................... No. Reporting requirements are specified
in Sec. 63.8075.Sec. 63.10(e)(3)(iv)-(v).............. Excess Emissions Reports... No. Reporting requirements are specified
in Sec. 63.8075.Sec. 63.10(e)(3)(vi-viii)............. Excess Emissions Report and No. Reporting requirements are specified
Summary Report. in Sec. 63.8075.Sec. 63.10(e)(4)...................... Reporting COMS data........ No. This subpart does not contain opacity
or VE limits.
Sec. 63.10(f)......................... Waiver for Recordkeeping/ Yes.
Reporting.Sec. 63.11............................ Control and work practice Yes
requirements.Sec. 63.12............................ Delegation................. Yes.Sec. 63.13............................ Addresses.................. Yes.Sec. 63.14............................ Incorporation by Reference. Yes.Sec. 63.15............................ Availability of Information Yes.---------------------------------------------------------------------------------------------------------------- [68 FR 69185, Dec. 11, 2003, as amended at 71 FR 20468, Apr. 20, 2006; 73 FR 78216, Dec. 22, 2008] Subpart IIIII_National Emission Standards for Hazardous Air Pollutants:
Mercury Emissions From Mercury Cell Chlor-Alkali Plants
Source: 68 FR 70928, Dec. 19, 2003, unless otherwise noted.
What This Subpart Covers