## Subpart DD

— National Emission Standards for Hazardous

Air Pollutants from Off

- Site Waste and Recovery Operations

Contents §63.680 Applicability and designation of affected sources. §63.681 Definitions. §63.682 [Reserved] §63.683 Standards: General. §63.684 Standards: Off

- site material treatment. §63.685 Standards: Tanks. §63.686 Standards: Oil

- water and organic

- water separators. §63.687 Standards: Surface impoundments. §63.688 Standards: Containers. §63.689 Standards: Transfer systems. §63.690 Standards: Process vents. §63.691 Standards: Equipment leaks. §63.692 [Reserved] §63.693 Standar ds: Closed

- vent systems and control devices. §63.694 Testing methods and procedures. §63.695 Inspection and monitoring requirements. §63.696 Recordkeeping requirements. §63.6 97 Reporting requirements. §63.698 Implementation and enforcement. Table 1 to Subpart DD of Part 63

— List of Hazardous Air Pollutants (HAP) for Subpart DD Table 2 to Subpart DD of Part 63

— Applicability of Paragraphs in Subpart A of This Part 63

— General Provisions to Subpart DD Table 3 to Subpart DD of Part 63

— Tank Control Levels for Tanks at Existing Affected Sources as Required by 40 CFR 63.685(b)(1) (i) Table 4 to Subpart DD of Part 63

— Tank Control Levels for Tanks at Existing Affected Sources as Required by 40 CFR 63.685(b)(1) (ii) Table 4 5 to Subpart DD of Part 63

— Tank Control Levels for Tanks at New Affected Source s as Required by 40 CFR 63.685(b)(2)



## §63.680 Applicability and designation of affected sources.

(a) The provisions of this subpart apply to the owner and operator of a plant site for which both of the conditions specified in paragraphs (a)(1) and (a)(2) of this section are applicable. If either one of these conditions does not apply to the plant site , then the owner and operator of the plant site are not subject to the provisions of this subpart.(1) The plant site is a major source of hazardous air pollutant (HAP) emissions as defined

in 40 CFR 63.2.
(2) At the plant site is located one or more of operations that receives off

- site materials as specified in paragraph (b) of this section and the operations is one of the following waste management operations or recovery operations as specified in paragraphs (a)(2)(i) through (a)(2)(vi) of this section.
(i) A waste management operation that receives off

- site material and the operation is regulated as a hazardous waste treatment, storage, and disposal facility (TSDF) under either 40 CFR part 264 or part 265.
(ii) A waste management operation that treats wastewater which is an off

- site material and the operation is exempted from regulation as a hazardous waste treatment, storage, and disposal facility under 40 CFR 264.1(g)(6) or 40 CFR 265.1(c)(10).
(iii) A waste management operation that treats wastewat er which is an off

- site material and the operation meets both of the following conditions:
(A) The operation is subject to regulation under either section 402 or 307(b) of the Clean Water Act but is not owned by a “state” or “municipality” as defined by s ection 502(3) and 502(4), respectively, of the Clean Water Act; and

(B) The treatment of wastewater received from off

- site is the predominant activity performed at the plant site.
(iv) A recovery operation that recycles or reprocesses hazardous waste whic h is an off

site material and the operation is exempted from regulation as a hazardous waste treatment, disposal, and storage facility under 40 CFR 264.1(g)(2) or 40 CFR 265.1(c)(6).
(v) A recovery operation that recycles or reprocesses used solvent which is an off

- site material and the operation is not part of a chemical, petroleum, or other manufacturing process that is required to use air emission controls by another subpart of 40 CFR part 63 or 40 CFR part 61.
(vi) A recovery operation that re

- refines or reprocesses used oil which is an off

- site material and the operation is regulated under 40 CFR 279 subpart F

— Standards for Used Oil Processors and Refiners.
(b) For the purpose of implementing this subpart, an off

- site material is a material that meets all of the criteria specified in paragraph (b)(1) of this section but is not one of the materials specified in paragraph (b)(2) of this section.

(1) An off

- site material is a material that meets all of the criteria specified in paragraphs (b)(1)(i) throu gh (b)(1)(iii) of this section. If any one of these criteria do not apply to the material, then the material is not an off

- site material subject to this subpart.(i) The material is a waste, used oil, or used solvent as defined in §63.681 of this subpart;

(ii) The waste, used oil, or used solvent is not produced or generated within the plant site, but the material is delivered, transferred, or otherwise moved to the plant site from a location outside the boundaries of the plant site; and

(iii) The waste, used oil, or used solvent contains one or more of the hazardous air pollutants (HAP) listed in Table 1 of this subpart based on the composition of the material at the point

- of

- delivery, as defined in §63.681 of this subpart.
(2) For the purpose of impleme nting this subpart, the following materials are not off

- site materials:

(i) Household waste as defined in 40 CFR 258.2.
(ii) Radioactive mixed waste managed in accordance with all applicable regulations under Atomic Energy Act and Nuclear Waste Policy Act authorities.
(iii) Waste that is generated as a result of implementing remedial activities required under the Resource Conservation and Recovery Act (RCRA) corrective action authorities (RCRA sections 3004(u), 3004(v), or 3008(h)), Comprehensive Environmental Response, Compensation, and Liability Act (CERCLA) authorities, or similar Federal or State authorities.

(iv) Wast e containing HAP that is generated by residential households (e.g., old paint, home garden pesticides) and subsequently is collected as a community service by government agencies, businesses, or other organizations for the purpose of promoting the proper d isposal of this waste.
(v) Waste that is transferred from a chemical manufacturing plant or other facility for which both of the following conditions apply to the waste:
(A) The management of the waste at the facility is required either under part 63 subp art F

— National Emission Standards for Organic Hazardous Air Pollutants from the Synthetic Organic Chemical Manufacturing Industry or under another subpart in 40 CFR part 63 to meet the air emission control standards for process wastewater specified in 40 C FR 63.132 through 63.147; and
(B) The owner or operator of the facility from which the waste is transferred has complied with the provisions of 40 CFR 63.132(g)(1)(ii) and (g)(2).
(vi) Waste that is transferred from a chemical manufacturing plant, petroleu m refinery, or coke by

- product recovery plant which is subject to 40 CFR part 61, subpart FF

— National Emission Standards for Benzene Waste Operations, and for which both of the following conditions apply to the waste:(A) The waste is generated at a facili ty that is not exempted under the provisions of 40

CFR 61.342(a) from meeting the air emission control standards of 40 CFR part 61, subpart FF; and
(B) The owner or operator of the facility from which the waste is transferred has complied with the provisi ons of 40 CFR 61.342(f)(2).
(vii) Ship ballast water pumped from a ship to an onshore wastewater treatment facility.
(viii) Hazardous waste that is stored for 10 days or less at a transfer facility in compliance with the provisions of 40 CFR 263.12.

(c) A ffected sources

— (1) Off

- site material management units. For each operation specified in paragraphs (a)(2)(i) through (a)(2)(vi) of this section that is located at the plant site, the affected source is the entire group of off

- site material management units associated with the operation. An off

- site material management unit is a tank, container, surface impoundment, oil

water separator, organic

- water separator, or transfer system used to manage off

- site material. For the purpose of implementing the standards under this subpart, a unit that meets the definition of a tank or container but also is equipped with a vent that serves as a process vent for any of the processes listed in paragraphs (c)(2)(i) through (c)(2)(vi) of this section is not an off

- site materi al management unit but instead is a process vent and is to be included in the appropriate affected source group under paragraph (c)(2) of this section. Examples of such a unit may include, but are not limited to, a distillate receiver vessel, a primary con denser, a bottoms receiver vessel, a surge control tank, a separator tank, and a hot well.

(2) Process vents. For each operation specified in paragraphs (a)(2)(i) through (a)(2)(vi) of this section that is located at the plant site, the affected source is the entire group of process equipment associated with the process vents for the processes listed in paragraphs (c)(2)(i) through (c)(2)(vi) of this section.
(i) Distillation process used for the treatment, recycling, or recovery of off

- site material. Disti llation means a process, either batch or continuous, separating one or more off

- site material feed streams into two or more exit streams having different component concentrations from those in the feed stream or streams. The separation is achieved by the r edistribution of the components between the liquid and vapor phases as they approach equilibrium within the distillation unit.
(ii) Fractionation process used for the treatment, recycling, or recovery of off

- site material. Fractionation means a liquid mixt ure separation process or method used to separate a mixture of several volatile components of different boiling points in successive stages, each stage removing from the mixture some proportion of one of the components.

(iii) Thin

- film evaporation process used for the treatment, recycling, or recovery of off

site material. Thin

- film evaporation means a liquid mixture separation process or method that uses a heating surface consisting of a large diameter tube that may be either straight or tapered,horizonta l or vertical. Liquid is spread on the tube wall by a rotating assembly of blades that

maintain a close clearance from the wall or actually ride on the film of liquid on the wall.
(iv) Solvent extraction process used for the treatment, recycling, or recove ry of off

- site material. Solvent extraction means a separation process or method in which a solid or a solution is contacted with a liquid solvent (the material and the solvent being relatively insoluble in each other) to preferentially dissolve and transf er one or more components into the solvent.
(v) Steam stripping process used for the treatment, recycling, or recovery of off

- site material. Steam stripping means a liquid mixture separation process or method in which vaporization of the volatile component s of a liquid mixture occurs by the introduction of steam directly into the process.
(vi) Gas stripping process used for the treatment, recycling, or recovery of off

- site material. Gas stripping means a desorption process or method used to transfer one or more volatile components from a liquid mixture into a gas stream either with or without the application of heat to the liquid. Packed towers, spray towers, and bubble

- cap, sieve, or valve

type plate towers are examples of the process configurations used fo r contacting the gas and a liquid.

(3) Equipment leaks. For each operation specified in paragraphs (a)(2)(i) through (a)(2)(vi) of this section that is located at the plant site, the affected source is the entire group of equipment components for which eac h component meets all of the conditions specified in paragraphs (c)(3)(i) through (c)(3)(iii) of this section. If any one of these conditions do not apply to an equipment component, then that component is not part of the affected source for equipment leaks

. (i) The equipment component is a pump, compressor, agitator, pressure relief device, sampling connection system, open

- ended valve or line, valve, connector, or instrumentation system;
(ii) The equipment component contains or contacts off

- site material ha ving a total HAP concentration equal to or greater than 10 percent by weight; and
(iii) The equipment component is intended to operate for 300 hours or more during a calendar year in off

- site material service, as defined in §63.681 of this subpart.

(d) Fa cility

- wide exemption. The owner or operator of affected sources subject to this subpart is exempted from the requirements of §§63.682 through 63.699 of this subpart in situations when the total annual quantity of the HAP that is contained in the off

- site material received at the plant site is less than 1 megagram per year. For a plant site to be exempted under the provisions of this paragraph (d), the owner or operator must meet the requirements in paragraphs (d)(1) through (d)(3) of this section.

(1) The owner or operator must prepare an initial determination of the total annual HAP quantity in the off

- site material received at the plant site. This determination is based on the totalquantity of the HAP listed in Table 1 of this subpart as determined at th e point

- of

- delivery for each off

- site material stream.
(2) The owner or operator must prepare a new determination whenever the extent of changes to the quantity or composition of the off

- site material received at the plant site could cause the total annual HAP quantity in the off

- site material received at the plant site to exceed the limit of 1 megagram per year.
(3) The owner or operator must maintain documentation to support the owner's or operator's determination of the total annual HAP quantity in the o ff

- site material received at the plant site. This documentation must include the basis and data used for determining the HAP content of the off

- site material.

(e) Compliance dates

— (1) Existing sources. The owner or operator of an affected source that commenced construction or reconstruction before October 13, 1994, must achieve compliance with the provisions of this subpart on or before the date specified in paragraph (e)(1)(i)
, or (e)(1) (ii) or (iii) of this section as applicable to the affected source.

(i) For an affected source that commenced construction or reconstruction before October 13, 1994 and receives off

- site material for the first time before February 1, 2000, the owner or operator of this affected source must achieve compliance with the provisions of the subpart (except §§ 63. 685(b)(1) (ii) , 63.691(b), and 63.691(c) (3)(i) and (ii) of this subpart ) on or before February 1, 2000 unless an extension has been granted by the Administrator as provided in 40 CFR 63.6(i). These existing affected sources shall be in compliance with the tank requirements of §63. 685(b)(1) (ii) of this subpart two year s after the publication date of the final amendments [INSERT DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER]
, the equipment leak requirements of §63. 691(b) of this subpart one year after the publication date of the final amendments [INSERT DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER] , and the pressure relief device monitoring requirements of §63. 691 (c) ( 3)(i) and (ii) of this subpart three years after the publication date of the final amendments [INSERT DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER]

. (ii) For an affected source that commenced construction or reconstruction before October 13, 1994, but receives off

- site material for the first time on or after February 1, 2000, but before [INSERT DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER]
, the owner or operator of the affected source must achieve compliance with the provisions of this subpart (except §§ 63. 685(b)(1)(ii), 63.691(b), and 63.691(c)(3)(i) and (ii) of this subpart ) upon the first date that the affected source begins to manage off

- site material. These e xisting affected sources shall be in compliance with the tank requirements of §63. 685(b)(1) (ii) of this subpart two years after the publication date of the final amendments [INSERT DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER] , the equipment leak requirements of §63. 691(b) of this subpart one year after the publication date of the final amendments [INSERT DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER] , and the pressure relief device monitoring requirements of §63. 691 (c) ( 3)(i) and (ii) of this subpart three years after thepublication date of the final amendments [INSERT DATE OF PUBLICATION OF THE FINAL

RULE AMENDMENTS IN THE FEDERAL REGISTER]

. (i i i) For an affected source that commenced construction or reconstruction before October 13, 1994, but receives off

- site material for the first time on or after [INSERT DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER]
, the owner or operator of the affected source must achieve compliance with the provisions of this subpart (except §§ 63. 685 (b)(1) (ii) , 63.691(b), and 63.691(c) ( 3)(i) and (ii) of this subpart ) upon the first date that the affected source begins to manage off

- site material. These e xisting affected sources shall be in compliance with the tank requirements of §63. 685(b)(1) (ii) of this subpart two years after the publication date of the final amendments [INSERT DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER]
, the equipment leak requirements of §63. 691(b) of this subpart one year after the publication date of the final amendments [INSERT DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER] , and the pressure relief device monitoring requirements of §63. 691 (c) ( 3)(i) and (ii) of this subpart three years after the publication date of the final amendments [INSERT DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER]

. (2) New sources. The owner or operator of an affected source for which construction or reconstruction commences on or after October 13, 1994, must achieve compliance with the provisions of this subpart (except §§63. 685(b)( 2 ), 63.691(b), and 63.691(c) (i) and (ii) of this subpart ) on or before July 1, 1996, or upon initial startup of operations, whichever date is later as provided in 40 CFR 63.6(b). New affected sou rces that commenced construction or reconstruction after October 13 , 199 4 , but on or before [INSERT DATE OF PUBLICATION OF THE PROPOSED AMENDMENTS IN THE FEDERAL REGISTER], shall be in compliance with the tank requirements of §63. 6 85(b)(2 ) of this subpart two years after the publication date of the final amendments , the equipment leak requirements of §63. 691(b) of this subpart one after the publication date of the final amendments , and the pressure relief devi ce monitoring requirements of § 63. 691 (c) (i) and (ii) of this subpart three years after the effective date of the final amendments. New affected sources that commence construction or reconstruction after [INSERT DATE OF PUBLICATION OF THE PROPOSED AMENDMENTS IN THE FEDERAL REGISTER] , shall be in compliance with the tank requirements of §63. 685(b)(2 ) of this subpart , the equipment leak requirements of §63. 691(b) of this subpart , and the pressure relief devi ce monitoring requirements of § 63. 691 (c) ( 3)(i) and (ii) of this subpart upon initial startup or by the effective date of the final amendments, whichever is later.
(f) The provisions of 40 CFR part 63, subpart A

— General Provisions that apply and those that do not apply to this subpart are specified in Table 2 of this subpart.
(g) Applicability of this subpart . (1) The emission limitations set forth in this subpart and the emission limitations referred to in this subpart shall apply at all times except during periods of non

- operation of the affected source (or specific portion there of) resulting in cessation of the emissions to which this subpart applies.(2) The owner or operator shall not shut down items of equipment that are required or

utilized for compliance with this subpart during times when emissions are being routed to suc h items of equipment, if the shutdown would contravene requirements of this subpart applicable to such items of equipment. 

## §63.681 Definitions. All terms used in this subpart shall have the meaning given to them in this section, 40 CFR 63.2 of this part, and the Act.

Boiler means an enclosed combustion device that extracts useful energy in the form of steam and is not an incinerator or a process heater.

Bypass means diverting a process vent or closed vent system stream to the atmosphere such that it does not first pass through an emission control device.

Closed

- vent system means a system that is not open to the atmosphere and is composed of hard

piping, ductwork, connections, and, if necessary, fans, blowers, or other flow

- inducing devices that conveys gas or vapor from an emission point to a control device.

Closure device means a cap, hatch, lid, plug, seal, valve, or other type of fitting that prevents or reduces air pollutant emissions to the atmosphere by blocking an opening in a cover when the device is secured in the closed position. Closure devices include devices that are detachable from the cover (e.g., a sampling port cap), manually oper ated (e.g., a hinged access lid or hatch), or automatically operated (e.g., a spring

- loaded pressure relief valve).

Container means a portable unit used to hold material. Examples of containers include but are not limited to drums, dumpsters, roll

- off box es, bulk cargo containers commonly known as “portable tanks” or “totes”, cargo tank trucks, and tank rail cars.

Continuous record means documentation of data values measured at least once every 15 minutes and recorded at the frequency specified in this su bpart.

Continuous recorder means a data recording device that either records an instantaneous data value at least once every 15 minutes or records 15

- minutes or more frequent block averages.

Continuous seal means a seal that forms a continuous closure that completely covers the space between the edge of the floating roof and the wall of a tank. A continuous seal may be a vapor

mounted seal, liquid

- mounted seal, or metallic shoe seal. A continuous seal may be constructed of fastened segments so as to form a continuous seal.

Control device means equipment used for recovering, removing, oxidizing, or destroying organic vapors. Examples of such equipment include but are not limited to carbon adsorbers, condenser s, vapor incinerators, flares, boilers, and process heaters.

Cover means a device or system that provides a continuous barrier over the material managed in an off

- site material management unit to prevent or reduce air pollutant emissions to theatmosphere. A cover may have openings needed for operation, inspection, sampling,

maintenance, and repair of the unit provided that each opening is closed when not in use (e.g., access hatches, sampling ports). A cover may be a separate piece of equipment which can b e detached and removed from the unit or a cover may be formed by structural features permanently integrated into the design of the unit.

Emission point means an individual tank, surface impoundment, container, oil

- water or organic

water separator, transfer system, process vent, or enclosure.

Enclosure means a structure that surrounds a tank or container, captures organic vapors emitted from the tank or container, and vents the captured vapor through a closed vent system to a control device.
External float ing roof means a pontoon

- type or double

- deck type cover that rests on the liquid surface in a tank with no fixed roof.
Fixed roof means a cover that is mounted on a unit in a stationary position and does not move with fluctuations in the level of the liqu id managed in the unit.

Flame zone means the portion of the combustion chamber in a boiler or process heater occupied by the flame envelope.
Floating roof means a cover consisting of a double deck, pontoon single deck, or internal floating cover which re sts upon and is supported by the liquid being contained, and is equipped with a continuous seal.

Flow indicator means a device that indicates whether gas is flowing, or whether the valve position would allow gas to flow in a bypass line.

Hard

- piping means pipe or tubing that is manufactured and properly installed in accordance with relevant standards and good engineering practices.
Hazardous air pollutants or HAP means the specific organic chemical compounds, isomers, and mixtures listed in Table 1 of this subpart.

Hazardous waste means a waste that is determined to be hazardous under the Resource Conservation and Recovery Act (PL 94

- 580) (RCRA), as implemented by 40 CFR parts 260 and 261.

In gas/vapor service means that a piece of equipment in off

- s ite material service contains a gas or vapor at operating conditions.
In heavy liquid service means that a piece of equipment in off

- site material service is not in gas/vapor service or in light liquid service.In light liquid service means that a piece of equipment in off

- site material service contains a liquid that meets the following conditions:
(1) The vapor pressure of one or more of the organic compounds is greater than 0.3 kilopascals at 20 °C,
(2) The total concentration of the pure organic compound s constituents having a vapor pressure greater than 0.3 kilopascals at 20 °C is equal to or greater than 20 percent by weight of the total process stream, and
(3) The fluid is a liquid at operating conditions.

N OTE : Vapor pressures may be determined by the methods described in 40 CFR 60.485(e)(1).
In liquid service means that a piece of equipment in off

- site material service is not in gas/vapor service.
Individual drain system means a stationary system used to convey wastewater streams or residuals to a was te management unit or to discharge or disposal. The term includes hard

- piping, all drains and junction boxes, together with their associated sewer lines and other junction boxes (e.g., manholes, sumps, and lift stations) conveying wastewater streams or res iduals. For the purpose of this subpart, an individual drain system is not a drain and collection system that is designed and operated for the sole purpose of collecting rainfall runoff (e.g., stormwater sewer system) and is segregated from all other indiv idual drain systems.
Internal floating roof means a cover that rests or floats on the liquid surface (but not necessarily in complete contact with it inside a tank that has a fixed roof).
Light

- material service means the container is used to manage an off

- site material for which both of the following conditions apply: the vapor pressure of one or more of the organic constituents in the off

- site material is greater than 0.3 kilopascals (kPa) at 20 °C; and the total concentration of the pure organic constitue nts having a vapor pressure greater than 0.3 kPa at 20 °C is equal to or greater than 20 percent by weight.
Liquid

- mounted seal means a foam

- or liquid

- filled continuous seal mounted in contact with the liquid in a unit.

Maximum HAP vapor pressure means the sum of the individual HAP equilibrium partial pressure exerted by an off

- site material at the temperature equal to either: the local maximum monthly average temperature as reported by the National Weather Service when the off

- site material is st ored or treated at ambient temperature; or the highest calendar

- month average temperature of the off

- site material when the off

- site material is stored at temperatures above the ambient temperature or when the off

- site material is stored or treated at temp eratures below the ambient temperature. For the purpose of this subpart, maximum HAP vapor pressure is determined using the procedures specified in §63.694(j) of this subpart.Metallic shoe seal means a continuous seal that is constructed of metal sheets w hich are held

vertically against the wall of the tank by springs, weighted levers, or other mechanisms and is connected to the floating roof by braces or other means. A flexible coated fabric (envelope) spans the annular space between the metal sheet and t he floating roof.
No detectable organic emissions means no escape of organics to the atmosphere as determined using the procedure specified in §63.694(k) of this subpart.
Off

- site material means a material that meets all of the criteria specified in paragr aph §63.680(b)(1) of this subpart but is not one of the materials specified in §63.680(b)(2) of this subpart.
Off

- site material management unit means a tank, container, surface impoundment, oil

- water separator, organic

- water separator, or transfer system u sed to manage off

- site material.
Off

- site material service means any time when a pump, compressor, agitator, pressure relief device, sampling connection system, open

- ended valve or line, valve, connector, or instrumentation system contains or contacts off

- site material.
Off

- site material stream means an off

- site material produced or generated by a particular process or source such that the composition and form of the material comprising the stream remain consistent. An off

- site material stream may be deliv ered, transferred, or otherwise moved to the plant site in a continuous flow of material (e.g., wastewater flowing through a pipeline) or in a series of discrete batches of material (e.g., a truckload of drums all containing the same off

- site material or m ultiple bulk truck loads of an off

- site material produced by the same process).

Oil

- water separator means a separator as defined for this subpart that is used to separate oil from water.
Operating parameter value means a minimum or maximum value established for a control device or treatment process parameter which, if achieved by itself or in combination with one or more other operating parameter values, determines that an owner or operator has complied with an ap plicable emission limitation or standard.

Organic

- water separator means a separator as defined for this subpart that is used to separate organics from water.

Plant site means all contiguous or adjoining property that is under common control including pro perties that are separated only by a road or other public right

- of

- way. Common control includes properties that are owned, leased, or operated by the same entity, parent entity, subsidiary, or any combination thereof. A unit or group of units within a cont iguous property that are not under common control (e.g., a wastewater treatment unit or solvent recovery unit located at the site but is sold to a different company) is a different plant site.

Point

- of

- delivery means the point at the boundary or within th e plant site where the owner or operator first accepts custody, takes possession, or assumes responsibility for the management ofan off

- site material stream managed in a waste management operation or recovery operation specified in §63.680 (a)(2)(i) throu gh (a)(2)(vi) of this subpart. The characteristics of an off

- site material stream are determined prior to combining the off

- site material stream with other off

- site material streams or with any other materials.

Point

- of

- treatment means a point after the t reated material exits the treatment process but before the first point downstream of the treatment process exit where the organic constituents in the treated material have the potential to volatilize and be released to the atmosphere. For the purpose of ap plying this definition to this subpart, the first point downstream of the treatment process exit is not a fugitive emission point due to an equipment leak from any of the following equipment components: pumps, compressors, valves, connectors, instrumentati on systems, or safety devices pressure relief devices

.
Pressure release means the emission of materials resulting from the system pressure being greater than the set pressure of the pressure relief device. This release can be one release or a series of rele ases over a short time period.
Pressure relief device or valve means a safety device used to prevent operating pressures from exceeding the maximum allowable working pressure of the process equipment. A common pressure relief device is a spring

- loaded pres sure relief valve. Devices that are actuated either by a pressure of less than or equal to 2.5 pounds per square inch gauge or by a vacuum are not pressure relief devices.

Process heater means an enclosed combustion device that transfers heat released by burning fuel directly to process streams or to heat transfer liquids other than water.

Process vent means an open

- ended pipe, stack, or duct through which a gas stream containing HAP is continuously or intermittently discharged to the atmosphere from any of the processes listed in §63.680(c)(2)(i) through (c)(2)(vi) of this section. For the purpose of this subpart, a process vent is none of the following: a pressure

- relief device vent or other vent that is used as a safety device (as defined in this section) ; an open

- ended line or other vent that is subject to the equipment leak control requirements under §63.691 of this subpart; or a stack or other vent that is used to exhaust combustion products from a boiler, furnace, process heater, incinerator, or other combustion device.

Recovery operation means the collection of off

- site material management units, process vents, and equipment components used at a plant site to manage an off

- site material stream from the point

- of

- delivery through the point where the material has been recycled, reprocessed, or re

refined to obtain the intended product or to remove the physical and chemical impurities of

concern.
Safety device means a closure device such as a pressure relief valve, frangible disc, fusible plug, or any other type of device which functions to p revent physical damage or permanent deformation to equipment by venting gases or vapors during unsafe conditions resulting from an unplanned, accidental, or emergency event. For the purpose of this subpart, a safety device is not used for routine venting o f gases or vapors from the vapor headspace underneath a cover such asduring filling of the unit or to adjust the pressure in this vapor headspace in response to normal

daily diurnal ambient temperature fluctuations. A safety device is designed to remain i n 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 equipment as determined by the owner or operator based on manufacturer recommendati ons, applicable regulations, fire protection and prevention codes, standard engineering codes and practices, or other requirements for the safe handling of flammable, combustible, explosive, reactive, or hazardous materials.

Separator means a waste managem ent unit, generally a tank, used to separate oil or organics from water. A separator consists of not only the separation unit but also the forebay and other separator basins, skimmers, weirs, grit chambers, sludge hoppers, and bar screens that are located directly after the individual drain system and prior to any additional treatment units such as an air flotation unit clarifier or biological treatment unit. Examples of a separator include, but are not limited to, an API separator, parallel

- plate intercept or, and corrugated

- plate interceptor with the associated ancillary equipment.
Single

- seal system means a floating roof having one continuous seal. This seal may be vapor

mounted, liquid

- mounted, or a metallic shoe seal.
Surface impoundment means a unit t hat is a natural topographical depression, man

- made excavation, or diked area formed primarily of earthen materials (although it may be lined with

man

- made materials), which is designed to hold an accumulation of liquids. Examples of surface impoundments i nclude holding, storage, settling, and aeration pits, ponds, and lagoons.

Tank means a stationary unit that is constructed primarily of nonearthen materials (such as wood, concrete, steel, fiberglass, or plastic) which provide structural support and is de signed to hold an accumulation of liquids or other materials.
Transfer system means a stationary system for which the predominant function is to convey liquids or solid materials from one point to another point within a waste management operation

or recov ery operation. For the purpose of this subpart, the conveyance of material using a container (as defined for this subpart) or a self

- propelled vehicle (e.g., a front

- end loader) is not a transfer system. Examples of a transfer system include but are not li mited to a pipeline, an individual drain system, a gravity

- operated conveyor (such as a chute), and a mechanically

powered conveyor (such as a belt or screw conveyor).
Temperature monitoring device means a piece of equipment used to monitor temperature and having an accuracy of ±1 percent of the temperature being monitored expressed in degrees Celsius (°C) or ±1.2 degrees °C, whichever value is greater.

Treatment process means a process in which an off

- site material stream is physically, chemically, therma lly, or biologically treated to destroy, degrade, or remove hazardous air pollutants contained in the off

- site material. A treatment process can be composed of a single unit (e.g., a steam stripper) or a series of units (e.g., a wastewater treatment system ). A treatment process can be used to treat one or more off

- site material streams at the same time.Used oil means any oil refined from crude oil or any synthetic oil that has been used and as a

result of such use is contaminated by physical or chemical i mpurities. This definition is the same definition of “used oil” in 40 CFR 279.1.

Used solvent means a mixture of aliphatic hydrocarbons or a mixture of one and two ring aromatic hydrocarbons that has been used as a solvent and as a result of such use is c ontaminated by physical or chemical impurities.

Vapor

- mounted seal means a continuous seal that is mounted such that there is a vapor space between the liquid in the unit and the bottom of the seal.
Volatile organic hazardous air pollutant concentration or VOHAP concentration means the fraction by weight of those compounds listed in Table 1 of this subpart that are in an off

- site material as measured using Method 305 in appendix A of this part and expressed in terms of parts per million (ppm). As an alte rnative to using Method 305, an owner or operator may determine the HAP concentration of an off

- site material using any one of the other test methods specified in §63.694(b)(2)(ii) of this subpart. When a test method specified in §63.694(b)(2)(ii) of this subpart other than Method 305 is used to determine the speciated HAP concentration of an off

- site material, the individual compound concentration may be adjusted by the corresponding f m305 value listed in Table 1 of this subpart to determine a VOHAP concen tration.

Waste means a material generated from industrial, commercial, mining, or agricultural operations or from community activities that is discarded, discharged, or is being accumulated, stored, or physically, chemically, thermally, or biologically tre ated prior to being discarded or discharged.

Waste management operation means the collection of off

- site material management units, process vents, and equipment components used at a plant site to manage an off

- site material stream from the point

- of

- delive ry to the point where the waste exits or is discharged from the plant site or the waste is placed for on

- site disposal in a unit not subject to this subpart (e.g., a waste incinerator, a land disposal unit).
Waste stabilization process means any physical or chemical process used to either reduce the mobility of hazardous constituents in a waste or eliminate free liquids as determined by Test Method 9095

— Paint Filter Liquids Test in “Test Methods for Evaluating Solid Waste, Physical/Chemical Methods,” EPA P ublication No. SW

- 846, Third Edition, September 1986, as amended by Update I, November 15, 1992. (As an alternative, an owner or operator may use any more recent, updated version of Method 9095 approved by the EPA.) A waste stabilization process includes m ixing the waste with binders or other materials and curing the resulting waste and binder mixture. Other synonymous terms used to refer to this process are “waste fixation” or “waste solidification.” A waste stabilization process does not include the addin g of absorbent materials to the surface of a waste, without mixing, agitation, or subsequent curing, to absorb free liquid. 

## §63.682 [Reserved]

## §63.683 Standards: General.

(a) The general standards under this section apply to owners and operators of affected sources as designated in §63.680(c) of this subpart.

(b) Off

- site material management units. (1) For each off

- site material management unit that is part of an affected source, the owner or operator must meet the requirements in either paragraph (b )(1)(i), (b)(1)(ii), or (b)(1)(iii) of this section except for those off

- site material management units exempted under paragraph (b)(2) of this section.
(i) The owner or operator controls air emissions from the off

- site material management unit in accordan ce with the applicable standards specified in §§63.685 through 63.689 of this subpart.
(ii) The owner or operator removes or destroys HAP in the off

- site material before placing the material in the off

- site material management unit by treating the material in accordance with the standards specified in §63.684 of this subpart.
(iii) The owner or operator determines before placing off

- site material in the off

- site material management unit that the average VOHAP concentration of the off

- site material is less t han 500 parts per million by weight (ppmw) at the point

- of

- delivery. The owner or operator must perform an initial determination of the average VOHAP concentration of the off

- site material using the procedures specified in §63.694(b) of this subpart. This initial determination must be performed either before the first time any portion of the off

- site material stream is placed in the unit or by the compliance date, whichever date is later. Thereafter, the owner or operator must review and update, as necessar y, this determination at least once every calendar year following the date of the initial determination for the off

- site material stream.

(2) An off

- site material management unit is exempted from the requirements in paragraph (b)(1) of this section when th e owner or operator meets one of the exemptions provided in paragraphs (b)(2)(i) through (b)(2)(iv) of this section as applicable to the unit.

(i) An off

- site material management unit is exempted from the requirements in paragraph (b)(1) of this section if the off

- site material management unit is also subject to another subpart under 40 CFR part 63 or 40 CFR part 61, and the owner or operator is controlling the HAP listed in Table 1 of this subpart that are emitted from the unit in compliance with the provi sions specified in the other applicable subpart under part 61 or part 63.
(ii) At the discretion of the owner or operator, one or a combination of off

- site material management units may be exempted from the requirements in paragraph (b)(1) of this section when these units meet the condition that the total annual quantity of HAP contained in the off

site material placed in the units exempted under this paragraph (b)(2)(ii) is less than 1 megagram per year. For the off

- site material management units selected by the owner or operator to be exempted from the requirements in paragraph (b)(1) of this section, the owner or operator must meet the requirements in paragraphs (b)(2)(ii)(A) and (b)(2)(ii)(B) of this section. An owner or operator may change the off

- site material management units selected to be exempted under this paragraph (b)(2)(ii) by preparing a new designation for the exempt

- units as required byparagraph (b)(2)(ii)(A) of this section and performing a new determination as required by

paragraph (b)(2)( ii)(B) of this section.
(A) The owner or operator must designate each of the off

- site material management units selected by the owner or operator to be exempt under paragraph (b)(2)(ii) of this section by either submitting to the Administrator a written no tification identifying the exempt

- units or permanently marking the exempt

- units at the plant site. If an owner or operator chooses to prepare and submit a written notification, this notification must include a site plan, process diagram, or other appropria te documentation identifying each of the exempt

- units. If an owner or operator chooses to permanently mark the exempt

- units, each exempt

- unit must be marked in such a manner that it can be readily identified as an exempt

- unit from the other off

- site materi al management units located at the plant site.
(B) The owner or operator must prepare an initial determination of the total annual HAP quantity in the off

- site material placed in the units exempted under this paragraph (b)(2)(ii). This determination is bas ed on the total quantity of the HAP listed in Table 1 of this subpart as determined at the point where the off

- site material is placed in each exempted unit. The owner or operator must perform a new determination whenever the extent of changes to the quant ity or composition of the off

- site material placed in the exempted units could cause the total annual HAP content in the off

- site material to exceed 1 megagram per year. The owner or operator must maintain documentation to support the most recent determina tion of the total annual HAP quantity. This documentation must include the basis and data used for determining the HAP content of the off

- site material.
(iii) A tank or surface impoundment is exempted from the requirements in paragraph (b)(1) of this secti on if the unit is used for a biological treatment process that meets the requirements in either paragraph (b)(2)(iii)(A) or (b)(2)(iii)(B) of this section and the owner or operator complies with the monitoring requirements in §63.684(e)(4) of this subpart.
(A) The HAP biodegradation efficiency (R bio ) for the biological treatment process is equal to or greater than 95 percent. The HAP biodegradation efficiency (R bio ) shall be determined in accordance with the requirements of §63.694(h) of this subpart.

(B) T he total actual HAP mass removal rate (MR bio ) for the off

- site material treated by the biological treatment process is equal to or greater than the required HAP mass removal rate (RMR) for the off

- site material. The total actual HAP mass removal rate (MR bi o ) must be determined in accordance with the requirements of §63.694(i) of this subpart. The required HAP mass removal rate (RMR) must be determined in accordance with the requirements of §63.694(e) of this subpart.

(iv) An off

- site material management uni t is exempted from the requirements in paragraph (b)(1) of this section if the off

- site material placed in the unit is a hazardous waste that meets the conditions specified in either paragraph (b)(2)(iv)(A) or (b)(2)(iv)(B) of this section.(A) The hazardo us waste meets the numerical organic concentration limits, applicable to the

hazardous waste, as specified in 40 CFR part 268

— Land Disposal Restrictions, listed in the table, “Treatment Standards for Hazardous Waste” in 40 CFR 268.40.
(B) The organic hazar dous constituents in the hazardous waste have been treated by the treatment technology established by the EPA for the hazardous waste in 40 CFR 268.42(a), or have been removed or destroyed by an equivalent method of treatment approved by the EPA under 40 C FR 268.42(b).

(v) A tank used for bulk feed of off

- site material to a waste incinerator is exempted from the requirements specified in paragraph (b)(1) of this section if the tank meets all of the conditions specified in paragraphs (b)(2)(v)(A) through (b) (2)(v)(C) of this section.
(A) The tank is located inside an enclosure vented to a control device that is designed and operated in accordance with all applicable requirements specified under 40 CFR part 61, subpart FF

— National Emission Standards for Benzen e Waste Operations for a facility at which the total annual benzene quantity from the facility waste is equal to or greater than 10 megagrams per year;
(B) The enclosure and control device serving the tank were installed and began operation prior to July 1 , 1996; and
(C) The enclosure is designed and operated in accordance with the criteria for a permanent total enclosure as specified in “Procedure T

— Criteria for and Verification of a Permanent or Temporary Total Enclosure” under 40 CFR 52.741, appendix B. The enclosure may have permanent or temporary openings to allow worker access; passage of material into or out of the enclosure by conveyor, vehicles, or other mechanical or electrical equipment; or to direct air flow into the enclosure. The owner or opera tor must annually perform the verification procedure for the enclosure as specified in Section 5.0 to “Procedure T

— Criteria for and Verification of a Permanent or Temporary Total Enclosure.”

(c) Process vents. (1) For each process vent that is part of an a ffected source, the owner or operator must meet the requirements in either paragraph (c)(1)(i) or (c)(1)(ii) of this section except for those process vents exempted under paragraph (c)(2) of this section.
(i) The owner or operator controls air emissions fr om the process vent in accordance with the standards specified in §63.690 of this subpart.
(ii) The owner or operator determines before placing off

- site material in the process equipment associated with the process vent that the average VOHAP concentration of the off

- site material is less than ppmw at the point

- of

- delivery. The owner or operator must perform an initial determination of the average VOHAP concentration of the off

- site material using the procedures specified in §63.694(b) of this subpart befor e any portion of the off

- site material stream is placed in the unit. Thereafter, the owner or operator must review and update, as necessary, this determination at least once every calendar year following the date of the initial determination for the off

- si te material stream.(2) A process vent is exempted from the requirements of paragraph (c)(1) of this section when

the owner or operator meets one of the exemptions provided in paragraphs (c)(2)(i) through (c)(2)(iii) of this section.
(i) A process vent is exempted from the requirements in paragraph (c)(1) of this section if the process vent is also subject to another subpart under part 63 or 40 CFR part 61, and the owner or operator is controlling the HAP listed in Table 1 of this subpart that are emitted f rom the process vent in compliance with the provisions specified in the other applicable subpart under part 61 or part 63.
(ii) A process vent is exempted from the requirements specified in paragraph (c)(1) of this section if the owner or operator determin es that the process vent stream flow rate is less than 0.005 cubic meters per minute (m 3 /min) at standard conditions (as defined in 40 CFR 63.2). The process vent stream flow rate shall be determined in accordance with the procedures specified in §63.694(m ) of this subpart. Documentation must be prepared by the owner or operator and maintained at the plant site to support the determination of the process vent stream flow rate. This documentation must include identification of each process vent exempted unde r this paragraph and the test results used to determine the process vent stream flow rate.
(iii) A process vent is exempted from the requirements specified in paragraph (c)(1) of this section if the owner or operator determines that the process vent stream flow rate is less than 6.0

m 3 /min at standard conditions (as defined in 40 CFR 63.2) and the total HAP concentration is less than 20 ppmv. The process vent stream flow rate and total HAP concentration shall be determined in accordance with the procedures specified in §63.694(m) of this subpart. Documentation must be prepared by the owner or operator and maintained at the plant site to support the determination of the process vent stream flow rate and total HAP concentration. This documentation must include identification of each process vent exempted under this paragraph (c)(2)(iii) and the test results used to determine the process vent stream flow rate and total HAP concentration. The owner or operator must perform a new determination of the process vent stream flow rate and total HAP concentration when the extent of changes to operation of the unit on which the process vent is used could cause either the process vent stream flow rate to exceed the limit of 6.0 m 3 /min or the total HAP concentration to exce ed the limit of 20 ppmv.

(d) Equipment leaks. The owner or operator must control equipment leaks from each equipment component that is part of the affected source specified in §63.680(c)(3) of this subpart by implementing leak detection and control measure s in accordance with the standards specified in §63.691 of this subpart.

( e ) General Duty. At all times, the owner or operator must operate and maintain any affected source, including associated air pollution control equipment and monitoring equipment, in a manner consistent with safety and good air pollution control practices for minimizing emi ssions. The general duty to minimize emissions does not require the owner operator to make any further efforts to reduce emissions if levels required by the applicable standard have been achieved. Determination of whether a source is operating in complianc e with operation and maintenance requirements will be based on information available to the Administrator, which may include,but is not limited to, monitoring results
, review of operation and maintenance procedures, review

of operation and maintenance rec ords, and inspection of the source.

( f ) In addition to the cases listed in § 63.695(e)(4) of this subpart , deviation means any of the cases listed in paragraphs ( f )(1) through ( f

)(6) of this section.
(1) Any instance in which an affected source subject to this subpart, or an owner or operator of such a source, 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) When a performance test indi cates that emissions of a pollutant in Table 1 to this subpart are exceeding the emission standard for the pollutant specified in Table 1 to this subpart.
(3) When the average value of a monitored operating parameter, based on the data averaging period for compliance specified in § 63.695 of this subpart , does not meet the operating limit specified in § 63.693 of this subpart

. (4) When an affected source discharges directly in to the atmosphere from any of the so urces specified in paragraphs ( f )(4)(i) and (i i ) of this section.
(i) A pressure relief device, as defined in § 63.681 of this subpart

. (ii) A bypass, as defined in § 63.681 of this subpart

. (5) Any instance in which the affected source subject to this subpart, or an owner or operator of such a source, fails to meet any term or condition specified in paragraph ( f )(5)(i) or (ii) of this section.
(i) Any term or condition that is adopted to implement an applicable requirement in this subpart.
(ii) Any term or condition relating to compliance with this subp art that is included in the operating permit for an affected source to obtain such a permit.
(6) Any failure to collect required data, except for periods of monitoring system malfunctions, repairs associated with monitoring system malfunctions, and require d monitoring system quality assurance or quality control activities (including, as applicable, calibration checks and required zero and span adjustments). 

## §63.684 Standards: Off

- site material treatment.

(a) The provisions of this section apply to the tre atment of off

- site material to remove or destroy HAP for which §63.683(b)(1)(ii) of this subpart references the requirements of this section for such treatment.
(b) The owner or operator shall remove or destroy the HAP contained in off

- site material stream s to be managed in the off

- site material management unit in accordance with §63.683(b)(1)(ii) ofthis subpart using a treatment process that continuously achieves, under normal operations, one

or more of the performance levels specified in paragraphs (b)(1 ) through (b)(5) of this section (as applicable to the type of treatment process) for the range of off

- site material stream compositions and quantities expected to be treated.

(1) VOHAP concentration. The treatment process shall reduce the VOHAP concentration of the off

- site material using a means, other than by dilution, to achieve one of the following performance levels, as applicable:
(i) In the case when every off

- site material stream entering the treatment process has an average VOHAP concentration equal to or greater than 500 ppmw at the point

- of

- delivery, then the VOHAP concentration of the off

- site material shall be reduced to a level that is less than 500 ppmw at the point

- of

- treatment.
(ii) In the case when off

- site material streams entering the treatment process are a mixture of off

site material streams having an average VOHAP concentration equal to or greater than 500 ppmw at the point

- of

- delivery with off

- site material streams having aver age VOHAP concentrations less than 500 ppmw at the point

- of

- delivery, then the VOHAP concentration of the off

- site material must be reduced to a level at the point

- of

- treatment that meets the performance level specified in either paragraph (b)(1)(ii)(A) or (B) of this section.

(A) Less than the VOHAP concentration limit (C R ) established for the treatment process using the procedure specified in §63.694(d); or

(B) Less than the lowest VOHAP concentration determined for each of the off

- site material streams entering the treatment process as determined by the VOHAP concentration of the off

- site material at the point

- of

- delivery.

(2) HAP mass removal. The treatment process shall achieve a performance level such that the total quantity of HAP actually removed fr om the off

- site material stream (MR) is equal to or greater than the required mass removal (RMR) established for the off

- site material stream using the procedure specified in §63.694(e) of this subpart. The MR for the off

- site material streams shall be det ermined using the procedures specified in §63.694(f) of this subpart.

(3) HAP reduction efficiency. For any treatment process except a treatment process that uses biological degradation and is performed in an open tank or surface impoundment, the treatmen t process must achieve the applicable performance level specified in either paragraph (b)(3)(i) or (b)(3)(ii) of this section.
(i) In the case when the owner or operator determines that off

- site material stream entering the treatment process has an average VOHAP concentration less than 10,000 ppmw at the point

- of

delivery, then the treatment process shall achieve a performance level such that the total quantity of HAP in the off

- site material stream is reduced by 95 percent or more. The HAP reduction effici ency (R) for the treatment process shall be determined using the procedure specified in §63.694(g) of this subpart. The average VOHAP concentration of the off

- site material stream atthe point

- of

- delivery shall be determined using the procedure specified i n §63.694(b) of this subpart.

(ii) In the case when the off

- site material stream entering the treatment process has an average VOHAP concentration equal to or greater than 10,000 ppmw at the point

- of

- delivery, then the treatment process shall achieve a pe rformance level such that the total quantity of HAP in the off

- site material stream is reduced by 95 percent or more, and the average VOHAP concentration of the off

- site material at the point

- of

- treatment is less than 100 parts per million by weight (ppmw) . The HAP reduction efficiency (R) for the treatment process shall be determined using the procedure specified in §63.694(g) of this subpart. The average VOHAP concentration of the off

- site material stream at the point

- of

- treatment shall be determined usin g the procedure specified in §63.694(c) of this subpart.

(4) Biological degradation performed in an open tank or surface impoundment. A treatment process using biological degradation and performed in an open tank or surface impoundment must achieve the pe rformance level specified in either paragraph (b)(4)(i) or (b)(4)(ii) of this section.
(i) The HAP reduction efficiency (R) for the treatment process is equal to or greater than 95 percent, and the HAP biodegradation efficiency (R bio ) for the treatment pro cess is equal to or greater than 95 percent. The HAP reduction efficiency (R) shall be determined using the procedure specified in §63.694(g) of this subpart. The HAP biodegradation efficiency (R bio ) shall be determined in accordance with the requirements of §63.694(h) of this subpart.
(ii) The total quantity of HAP actually removed from the off

- site material stream by biological degradation (MR bio ) shall be equal to or greater than the required mass removal (RMR) established for the off

- site material stre am using the procedure specified in §63.694(e) of this subpart. The MR bio of the off

- site material stream shall be determined using the procedures specified in §63.694(i) of this subpart.

(5) Incineration. The treatment process must destroy the HAP contai ned in the off

- site material stream using one of the combustion devices specified in paragraphs (b)(5)(i) through (b)(5)( i v) of this section.
(i) An incinerator for which the owner or operator has been issued a final permit under 40 CFR part 270, and the i ncinerator is designed and operated in accordance with the requirements of 40 CFR part 264, subpart O

— Incinerators, or
(ii) An incinerator for which the owner or operator has certified compliance with the interim status requirements of 40 CFR part 265, sub part O

— Incinerators.
(iii) A boiler or industrial furnace for which the owner or operator has been issued a final permit under 40 CFR part 270, and the combustion unit is designed and operated in accordance with the requirements of 40 CFR part 266, subpart H

— Hazardous Waste Burned in Boilers and Industrial Furnaces.(iv) A boiler or industrial furnace for which the owner or operator has certified compliance with

the interim status requirements of 40 CFR part 266, subpart H Hazardous Waste Burned in Boilers and Industrial Furnaces.

(v ) An incinerator, boiler, or industrial furnace for which the owner or operator has submitted a Notification of Compliance under 40 CFR 63.1207(j) and 63. 1210(d) and complies with the requirements of 40 CFR part 63 subpart EEE at all times (including times when non

- hazardous waste is being burned).
(c) For a treatment process that removes the HAP from the off

- site material by a means other than thermal destruction or biological degradation to achieve one of the performances levels specified in paragraph (b)(1), (b)(2), or (b)(3) of this section, the owner or operator shall manage the HAP removed from the off

- site material in such a manner to minimize release of these HAP to the atmosphere, to the extent practical. Examples of HAP e mission control measures that meet the requirements of this paragraph include managing the HAP removed from the off

- site material in units that use air emission controls in accordance with the standards specified in §§63.685 through 63.689 of this subpart, as applicable to the unit.
(d) When the owner or operator treats the off

- site material to meet one of the performance levels specified in paragraphs (b)(1) through (b)(4) of this section, the owner or operator shall demonstrate that the treatment process achieves the selected performance level for the range of expected off

- site material stream compositions expected to be treated. An initial demonstration shall be performed as soon as possible but no later than 30 days after first time an owner or operator begins using the treatment process to manage off

- site material streams in accordance with the requirements of either §63.683(b)(1)(ii) or §63.683(b)(2)(ii) of this subpart as applicable to the affected off

- site material management unit or process equipmen t. Thereafter, the owner or operator shall review and update, as necessary, this demonstration at least once every calendar year following the date of the initial demonstration.
(e) When the owner or operator treats the off

- site material to meet one of the performance levels specified in paragraphs (b)(1) through (b)(4) of this section, the owner or operator shall ensure that the treatment process is achieving the applicable performance requirements by continuously monitoring the operation of the process wh en it is used to treat off

- site material by complying with paragraphs (e)(1) through (e)(3) or, for biological treatment units, paragraph (e)(4) of this section:
(1) A continuous monitoring system shall be installed and operated for each treatment that

mea sures operating parameters appropriate for the treatment process technology. This system shall include a continuous recorder that records the measured values of the selected operating parameters. The monitoring equipment shall be installed, calibrated, and maintained in accordance with the equipment manufacturer's specifications. The continuous recorder shall be a data recording device that is capable of recording either an instantaneous data value at least once every 15 minutes or an average value for inte rvals of 15 minutes or less.
(2) For each monitored operating parameter, the owner or operator shall establish a minimum operating parameter value or a maximum operating parameter value, as appropriate, to define therange of conditions at which the treatm ent process must be operated to continuously achieve the

applicable performance requirements of this section.
(3) When the treatment process is operating to treat off

- site material, the owner or operator shall inspect the data recorded by the continuous mo nitoring system on a routine basis and operate the treatment process such that the actual value of each monitored operating parameter is greater than the minimum operating parameter value or less than the maximum operating parameter value, as appropriate, established for the treatment process.
(4) When the treatment process is a biological treatment process that is complying with paragraph (b)(4) of this section, the owner or operator must establish and implement a written procedure to monitor the appropria te parameters that demonstrate proper operation of the biological treatment unit in accordance with the evaluation required in §63.694(h) of this subpart. The written procedure must list the operating parameters that will be monitored and state the frequen cy of monitoring to ensure that the biological treatment unit is operating between the minimum operating parameter values and maximum operating parameter values to establish that the biological treatment unit is continuously achieving the performance requi rement.
(f) The owner or operator must maintain records for each treatment process in accordance with the requirements of §63.696(a) of this subpart.
(g) The owner or operator must prepare and submit reports for each treatment process in accordance with th e requirements of §63.697(a) of this subpart.
(h) The Administrator may at any time conduct or request require that the owner or operator conduct testing necessary to demonstrate that a treatment process is achieving the applicable performance requirements of this section. The testing shall be conducted in accordance with the applicable requirements of this section. The Administrator may elect to have an authorized representative observe testing conducted by the owner or operator. 

## §63.685 Standards: Tanks.

(a) The provisions of this section apply to the control of air emissions from tanks for which §63.683(b)(1)(i) of this subpart references the use of this section for such air emission control.

(b) According to the date an affected source commenced construction or reconstruction and the date an affected source receives off

- site material for the first time as established in §63.680(e)(i)

- (iii) of this subpart
, T t he owner or operator shall control air emissions from each tank subject to this section in accordance with either paragraph (b)(1)(i) o r (ii) of this section the following applicable requirements:

. (1) (i) For a tank that is part of an existing affected sou rce but the tank is not used to manage off

site material having a maximum HAP vapor pressure kilopascal (kPa) that is equal to or greater than 76.6 kPa nor is the tank used for a waste stabilization process as defined in §63.681 of this subpart, the owner or operator shall determine whether the tank is required to use either TankLevel 1 controls or Tank Level 2 controls as specified for the tank by Table 3 of this subpart

based on the off

- site material maximum HAP vapor pressure and
, the tank's design capa city. The owner or operator shall control air emissions from a tank required by Table 3 to use Tank Level 1 controls in accordance with the requirements of paragraph (c) of this section. The owner or operator shall control air emissions from a tank require d by Table 3 to use Tank Level 2 controls in accordance with the requirements of paragraph (d) of this section.

( ii) For a tank that is part of an existing affected source but the tank is not used for a waste stabilization process as defined in §63.681 of this subpart, the owner or operator shall determine whether the tank is required to use either Tank Level 1 controls or Tank Level 2 controls as specified for the tank by Table 4 of this subpart based on the off

- site material maximum HAP vapor pressure and the tank's design capacity. The owner or operator shall control air emissions from a tank required by Table 4 to use Tank Level 1 controls in accordance with the requirements of paragraph (c) of this section. The owner or operator shall control air emissions from a tank required by Table 4 to use Tank Level 2 controls in accordance with the requirements of paragraph (d) of this section.

(2) For a tank that is part of a new affected source but the tank is not used to manage off

- site material having a maximum HAP vapor pressure that is equal to or greater than 76.6 kPa nor is the tank used for a waste stabilization proces s as defined in §63.681 of this subpart, the owner or operator shall determine whether the tank is required to use either Tank Level 1 controls or Tank Level 2 controls as specified for the tank by Table 4 5 of this subpart based on the off

- site material maximum HAP vapor pressure and the tank's design capacity. The owner or operator shall control air emissions from a tank required by Table 5 4 to use Tank Level 1 controls in accordance with the requirements o f paragraph (c) of this section. The owner or operator shall control air emissions from a tank required by Table 4 5 to use Tank Level 2 controls in accordance with the requirements of paragraph (d) of this section.

(3) For a tank that is used for a waste stabilization process, the owner or operator shall control air emissions from the tank by using Tank Level 2 controls in accordance with the requirements of paragraph (d) of this section.
(4) For a tank that manages off

- site material having a maximum HAP vapor pressure that is equal to or greater than 76.6 kPa, the owner or operator must control air emissions by using one of the tanks specified in paragraphs (b)(4)(i) through (b)(4)(iii) of this section.
(i) A tank vented through a closed

- vent system to a control device in accordance with the requirements specified in paragraph (g) of this section;
(ii) A pressure tank designed and operated in accordance with the requirements specified in paragraph (h) of this section; or(iii) A tank located inside an enclosure that is vented through a closed

- vent system to an enclosed

combustion control device in accordance with the requirements specified in paragraph (i) of this section.
(c) Owners and operators controlling air emissions from a tank using Tank Level 1 controls shall meet the following requirements:
(1) The owner or operator shall determine the maximum HAP vapor pressure for an off

- site material to be managed in the tank using Tank Level 1 controls before the first time the off

- site material is placed in the tank. The maximum HAP vapor pressure shall be determined using the procedures specified in §63.694(j) of this subpart. Thereafter, the owner or operator shall perform a new determination whenever changes to the off

- site material managed in the tank could potentially cause the maximum HAP vapor pressure to increase to a level that is equal to or greater than the maximum HAP vapor pressure limit for the tank design capacity category specified in Table 3
, or Table 4 or Table 5 of this subpart, as applic able to the tank.
(2) The owner or operator must control air emissions from the tank in accordance with the requirements in either paragraph (c)(2)(i), (c)(2)(ii), or (c)(2)(iii) of this section, as applicable to the tank.
(i) The owner or operator contro ls air emissions from the tank in accordance with the provisions specified in subpart 00 OO of 40 CFR part 63

— National Emission Standards for Tanks

— Level 1
, except that § § 40 CFR 63.902(c)(2) and (c)(3) shall not apply for the purposes of this subpart.

(ii) As an alternative to meeting the requirements in paragraph (c)(2)(i) of this section, an owner or operator may control air emissions from the tank in accordance with the provisions for Tank Level 2 controls as specified in paragraph (d) of this section.

(i ii) As an alternative to meeting the requirements in paragraph (c)(2)(i) of this section when a tank is used as an interim transfer point to transfer off

- site material from containers to another off

- site material management unit, an owner or operator may c ontrol air emissions from the tank in accordance with the requirements in paragraphs (c)(2)(iii)(A) and (c)(2)(iii)(B) of this section. An example of such a tank is an in

- ground tank into which organic

- contaminated debris is dumped from roll

- off boxes or d ump trucks, and then this debris is promptly transferred from the tank to a macroencapsulation unit by a backhoe.
(A) During those periods of time when the material transfer activity is occurring, the tank may be operated without a cover.

(B) At all other times, air emissions from the tank must be controlled in accordance with the provisions specified in 40 CFR part 67, subpart 00 OO

— National Emission Standards for Tanks

— Level 1
, except that § § 40 CFR 63.902(c)(2) and (c)(3) shall not apply for the purposes of this subpart

. (d) Owners and operators controlling air emissions from a tank using Tank Level 2 controls shall use one of the following tanks:(1) A fixed

- roof tank equipped with an internal floating roof in accordance with the requirements

specified i n paragraph (e) of this section;
(2) A tank equipped with an external floating roof in accordance with the requirements specified in paragraph (f) of this section;
(3) A tank vented through a closed

- vent system to a control device in accordance with the requirements specified in paragraph (g) of this section;
(4) A pressure tank designed and operated in accordance with the requirements specified in paragraph (h) of this section; or
(5) A tank located inside an enclosure that is vented through a closed

- vent system to an enclosed combustion control device in accordance with the requirements specified in paragraph (i) of this section.
(e) The owner or operator who elects to control air emissions from a tank using a fixed

- roof with an internal floating roof shall meet the requirements specified in paragraphs (e)(1) through (e)(3) of this section.
(1) The tank shall be equipped with a fixed roof and an internal floating roof in accordanc e with the following requirements:
(i) The internal floating roof shall be designed to float on the liquid surface except when the floating roof must be supported by the leg supports.
(ii) The internal floating roof shall be equipped with a continuous se al between the wall of the tank and the floating roof edge that meets either of the following requirements:
(A) A single continuous seal that is either a liquid

- mounted seal or a metallic shoe seal, as defined in §63.681 of this subpart; or

(B) Two conti nuous seals mounted one above the other. The lower seal may be a vapor

- mounted seal.
(iii) The internal floating roof shall meet the following specifications:
(A) Each opening in a noncontact internal floating roof except for automatic bleeder vents (vac uum breaker vents) and the rim space vents is to provide a projection below the liquid surface.
(B) Each opening in the internal floating roof shall be equipped with a gasketed cover or a gasketed lid except for leg sleeves, automatic bleeder vents, rim s pace vents, column wells, ladder wells, sample wells, and stub drains.(C) Each penetration of the internal floating roof for the purpose of sampling shall have a slit

fabric cover that covers at least 90 percent of the opening.

(D) Each automatic bleede r vent and rim space vent shall be gasketed.
(E) Each penetration of the internal floating roof that allows for passage of a ladder shall have a gasketed sliding cover.
(F) Each penetration of the internal floating roof that allows for passage of a colum n supporting the fixed roof shall have a flexible fabric sleeve seal or a gasketed sliding cover.
(2) The owner or operator shall operate the tank in accordance with the following requirements:
(i) When the floating roof is resting on the leg supports, th e process of filling, emptying, or refilling shall be continuous and shall be accomplished as soon as practical.
(ii) Automatic bleeder vents are to be set closed at all times when the roof is floating, except when the roof is being floated off or is bein g landed on the leg supports.
(iii) Prior to filling the tank, each cover, access hatch, gauge float well or lid on any opening in the internal floating roof shall be bolted or fastened closed (i.e., no visible gaps). Rim spaces vents are to be set to ope n only when the internal floating roof is not floating or when the pressure beneath the rim exceeds the manufacturer's recommended setting.
(3) The owner or operator shall inspect the internal floating roof in accordance with the procedures specified in § 63.695(b) of this subpart.
(f) The owner or operator who elects to control tank emissions by using an external floating roof shall meet the requirements specified in paragraphs (f)(1) through (f)(3) of this section.
(1) The owner or operator shall design the external floating roof in accordance with the following requirements:
(i) The external floating roof shall be designed to float on the liquid surface except when the floating roof must be supported by the leg supports.
(ii) The floating roof shall b e equipped with two continuous seals, one above the other, between the wall of the tank and the roof edge. The lower seal is referred to as the primary seal, and the upper seal is referred to as the secondary seal.
(A) The primary seal shall be a liquid

- m ounted seal or a metallic shoe seal, as defined in §63.681 of this subpart. The total area of the gaps between the tank wall and the primary seal shall not exceed 212 square centimeters (cm2) per meter of tank diameter, and the width of any portion of thes e gaps shall not exceed 3.8 centimeters (cm). If a metallic shoe seal is used for the primary seal, the metallic shoe seal shall be designed so that one end extends into the liquid in the tankand the other end extends a vertical distance of at least 61 ce ntimeters (24 inches) above the

liquid surface.
(B) The secondary seal shall be mounted above the primary seal and cover the annular space between the floating roof and the wall of the tank. The total area of the gaps between the tank wall and the secondar y seal shall not exceed 21.2 square centimeters (cm2) per meter of tank diameter, and the width of any portion of these gaps shall not exceed 1.3 centimeters (cm).
(iii) The external floating roof shall be meet the following specifications:
(A) Except fo r automatic bleeder vents (vacuum breaker vents) and rim space vents, each opening in a noncontact external floating roof shall provide a projection below the liquid surface.
(B) Except for automatic bleeder vents, rim space vents, roof drains, and leg sleeves, each opening in the roof shall be equipped with a gasketed cover, seal, or lid.
(C) Each access hatch and each gauge float wells shall be equipped with covers designed to be bolted or fastened when the cover is secured in the closed position.
(D) Each automatic bleeder vent and each rim space vents shall be equipped with a gasket.
(E) Each roof drain that empties into the liquid managed in the tank shall be equipped wi th a slotted membrane fabric cover that covers at least 90 percent of the area of the opening.
(F) Each unslotted and slotted guide pole well shall be equipped with a gasketed sliding cover or a flexible fabric sleeve seal.
(G) Each unslotted guide pole shall be equipped with a gasketed cap on the end of the pole.
(H) Each slotted guide pole shall be equipped with a gasketed float or other device which closes off the surface from the atmosphere.
(I) Each gauge hatch and each sample well shall be equippe d with a gasketed cover.
(2) The owner or operator shall operate the tank in accordance with the following requirements:
(i) When the floating roof is resting on the leg supports, the process of filling, emptying, or refilling shall be continuous and shal l be accomplished as soon as practical.
(ii) Except for automatic bleeder vents, rim space vents, roof drains, and leg sleeves, each opening in the roof shall be secured and maintained in a closed position at all times except when the closure device must be open for access.
(iii) Covers on each access hatch and each gauge float well shall be bolted or fastened when secured in the closed position.(iv) Automatic bleeder vents shall be set closed at all times when the roof is floating, except

when the roof is being floated off or is being landed on the leg supports.
(v) Rim space vents shall be set to open only at those times that the roof is being floated off the roof leg supports or when the pressure beneath the rim seal exceeds the manufacturer's

recomm ended setting.
(vi) The cap on the end of each unslotted guide pole shall be secured in the closed position at all times except when measuring the level or collecting samples of the liquid in the tank.
(vii) The cover on each gauge hatch or sample well s hall be secured in the closed position at all times except when the hatch or well must be opened for access.
(viii) Both the primary seal and the secondary seal shall completely cover the annular space between the external floating roof and the wall of th e tank in a continuous fashion except during inspections.
(3) The owner or operator shall inspect the external floating roof in accordance with the procedures specified in §63.695(b) of this subpart.
(g) The owner or operator who controls tank air emissi ons by venting to a control device shall meet the requirements specified in paragraphs (g)(1) through (g)(3) of this section.
(1) The tank shall be covered by a fixed roof and vented directly through a closed

- vent system to a control device in accordance with the following requirements:
(i) The fixed roof and its closure devices shall be designed to form a continuous barrier over the entire surface area of the liquid in the tank.
(ii) Each opening in the fixed roof not vented to the control device shall be equipped with a closure device. If the pressure in the vapor headspace underneath the fixed roof is less than atmospheric pressure when the control device is operating, the closure devices shall be designed to operate such that when the closure device i s secured in the closed position there are no visible cracks, holes, gaps, or other open spaces in the closure device or between the perimeter of the cover opening and the closure device. If the pressure in the vapor headspace underneath the fixed roof is equal to or greater than atmospheric pressure when the control device is operating, the closure device shall be designed to operate with no detectable organic emissions.

(iii) The fixed roof and its closure devices shall be made of suitable materials that will minimize exposure of the off

- site material to the atmosphere, to the extent practical, and will maintain the integrity of the equipment throughout its intended service life. Factors to be considered when selecting the materials for and designing the fixed roof and closure devices shall include: organic vapor permeability, the effects of any contact with the liquid and its vapor managed in the tank; the effects of outdoor exposure to wind, moisture, and sunlight; and the operating practices used for th e tank on which the fixed roof is installed.(iv) The closed

- vent system and control device shall be designed and operated in accordance

with the requirements of §63.693 of this subpart.

(2) Whenever an off

- site material is in the tank, the fixed roof sh all be installed with each closure device secured in the closed position and the vapor headspace underneath the fixed roof vented to the control device except that as follows:

(i) V v enting to the control device is not required, and opening of closure devices or removal of the fixed roof is allowed at the following times:

( A i ) To provide access to the tank for performing routine inspection, maintenance, or other activities needed for normal operations. Examples of such activities include those times when a worker needs to open a port to sample liquid in the tank, or when a wor ker needs to open a hatch to maintain or repair equipment. Following completion of the activity, the owner or operator shall promptly secure the closure device in the closed position or reinstall the cover, as applicable, to the tank.

( B ii ) To remove accu mulated sludge or other residues from the bottom of the tank.
(ii) Opening of a safety device, as defined in §63.681 of this subpart, is allowed at any time conditions require it to do so to avoid an unsafe condition s

. (3) The owner or operator shall inspect and monitor the air emission control equipment in accordance with the procedures specified in §63.695 of this subpart.
(h) The owner or operator who elects to control tank air emissions by using a pressure tank shal l meet the following requirements.
(1) The tank shall be designed not to vent to the atmosphere as a result of compression of the vapor headspace in the tank during filling of the tank to its design capacity.
(2) All tank openings shall be equipped with closure devices designed to operate with no detectable organic emissions as determined using the procedure specified in §63.694(k) of this subpart.

(3) Whenever an off

- site material is in the tank, the tank shall be operated as a closed system that does no t vent to the atmosphere except at those times when purging of inerts from the tank is required and the purge stream is routed to a closed

- vent system and control device designed and operated in accordance with the requirements of § 63.693 of this subpart.
under either of the following conditions as specified in paragraph (h)(3)(i) or (h)(3)(ii) of this section.
(i) At those times when opening of a safety device, as defined in §63.681 of this subpart, is required to avoid an unsafe condition.(ii) At those times when purging of inerts from the tank is required and the purge stream is

routed to a closed

- vent system and control device designed and operated in accordance with the requirements of §63.693 of this subpart.
(i) The owner or operator who elects to c ontrol air emissions by using an enclosure vented through a closed

- vent system to an enclosed combustion control device shall meet the requirements specified in paragraphs (i)(1) through ( 4 3 ) of this section.

(1) The tank shall be located inside an enclosu re. The enclosure shall be designed and operated in accordance with the criteria for a permanent total enclosure as specified in “Procedure T

— Criteria for and Verification of a Permanent or Temporary Total Enclosure” under 40 CFR 52.741, appendix B. The en closure may have permanent or temporary openings to allow worker access; passage of material into or out of the enclosure by conveyor, vehicles, or other mechanical means; entry of permanent mechanical or electrical equipment; or to direct airflow into the enclosure. The owner or operator shall perform the verification procedure for the enclosure as specified in Section 5.0 to “Procedure T

— Criteria for and Verification of a Permanent or Temporary Total Enclosure” initially when the enclosure is first instal led and, thereafter, annually.
(2) The enclosure shall be vented through a closed

- vent system to an enclosed combustion control device that is designed and operated in accordance with the standards for either a vapor incinerator, boiler, or process heater specified in §63.693 of this subpart.
(3) Opening of a safety device, as defined in §63.681 of this subpart, is allowed at any time conditions require it to do so to avoid an unsafe condition

. ( 4 3 ) The owner or operator shall inspect and monitor the clos ed

- vent system and control device as specified in §63.693. 

## §63.686 Standards: Oil

- water and organic

- water separators.

(a) The provisions of this section apply to the control of air emissions from oil

- water separators and organic

- water separators for which §63.683(b)(1)(i) of this subpart references the use of this section for such air emission control.

(b) The owner or o perator shall control air emissions from each separator subject to this section by using one of the following:
(1) A floating roof in accordance with all applicable provisions specified in 40 CFR 63 subpart VV

— National Emission Standards for Oil

- Water Sep arators and Organic

- Water Separators
, except that § § 40 CFR 63.1043(c)(2), 63.1044(c)(2) and 63.1045(b)(3)(i) shall not apply for the purposes of this subpart . For portions of the separator where it is infeasible to install and operate a floating roof, such as over a weir mechanism, the owner or operator shall comply with the requirements specified in paragraph (b)(2) of this section.(2) A fixed

- roof that is vented through a closed

- vent system to a control device in accordance

with all applicable provision s specified in 40 CFR 63 subpart VV

— National Emission Standards for Oil

- Water Separators and Organic

- Water Separators , except that 63.1043(c)(2), 63.1044(c)(2) and 63.1045(b)(3)(i) shall not apply for the purposes of this subpart

. (3) A pressurized separator that operates as a closed system in accordance with all applicable provisions specified in 40 CFR part 63, subpart VV

— National Emission Standards for Oil

- Water Separators and Organic

- Water Separators , except that 63.1043(c)(2), 63.1044(c)(2) and 63.1045(b)(3)(i) shall not apply for the purposes of this subpart

. 

## §63.687 Standards: Surface impoundments.

(a) The provisions of this section apply to the control of air emissions from surface impoundments for which §63.683(b)(1)(i) of this subpart references the use of this section for such air emission control.
(b) The owner or operator shall control air emi ssions from each surface impoundment subject to this section by using one of the following:
(1) A floating membrane cover in accordance with the applicable provisions specified in 40 CFR 63 subpart QQ

— National Emission Standards for Surface Impoundments , e xcept that 63.942(c)(2) and (c)(3) and 63.943(c)(2) shall not apply for the purposes of this subpart ; or
(2) A cover that is vented through a closed

- vent system to a control device in accordance with all applicable provisions specified in 40 CFR 63 subpar t QQ

— National Emission Standards for Surface Impoundments , except that 63.942(c)(2) and (c)(3) and 63.943(c)(2) shall not apply for the purposes of this subpart

. 

## §63.688 Standards: Containers.

(a) The provisions of this section apply to the control of a ir emissions from containers for which §63.683(b)(1)(i) of this subpart references the use of this section for such air emission control.
(b) The owner or operator shall control air emissions from each container subject to this section in accordance with the following requirements, as applicable to the container, except when the special provisions for waste stabilization processes specified in paragraph (c) of this section apply to the container.
(1) For a container having a design capacity greater than 0. 1 m 3 and less than or equal to 0.46 m 3

, the owner or operator must control air emissions from the container in accordance with the requirements in either paragraph (b)(1)(i) or (b)(1)(ii) of this section.
(i) The owner or operator controls air emissions fr om the container in accordance with the standards for Container Level 1 controls as specified in 40 CFR part 63, subpart PP

— NationalEmission Standards for Containers , except that 63.922(d)(4) and (d)(5) and 63.923(d)(4) and

(d)(5) shall not apply for the purposes of this subpart

. (ii) As an alternative to meeting the requirements in paragraph (b)(1)(i) of this section, an owner or operator may choose to control air emissions from the container in accordance with the standards for either Container Level 2 c ontrols or Container Level 3 controls as specified in subpart PP of this part 63

— National Emission Standards for Containers , except that 63.922(d)(4) and (d)(5) and 63.923(d)(4) and (d)(5) shall not apply for the purposes of this subpart

. (2) For a contain er having a design capacity greater than 0.46 m 3 and the container is not in light

material service as defined in §63.681 of this subpart, the owner or operator must control air emissions from the container in accordance with the requirements in either par agraph (b)(1)(i) or (b)(1)(ii) of this section.
(3) For a container having a design capacity greater than 0.46 m 3 and the container is in light

material service as defined in §63.681 of this subpart, the owner or operator must control air emissions from th e container in accordance with the requirements in either paragraph (b)(3)(i) or (b)(3)(ii) of this section.
(i) The owner or operator controls air emissions from the container in accordance with the standards for Container Level 2 controls as specified in 40 CFR part 63, subpart PP

— National Emission Standards for Containers , except that 63.922(d)(4) and (d)(5) and 63.923(d)(4) and (d)(5) shall not apply for the purposes of this subpart

. (ii) As an alternative to meeting the requirements in paragraph (b)(3) (i) of this section, an owner or operator may choose to control air emissions from the container in accordance with the standards for Container Level 3 controls as specified in 40 CFR part 63, subpart PP

— National Emission Standards for Containers.

(c) When a container subject to this subpart and having a design capacity greater than 0.1 m 3 is used for treatment of an off

- site material by a waste stabilization process as defined in §63.681 of this subpart, the owner or operator shall control air emissions fr om the container at those times during the process when the off

- site material in the container is exposed to the atmosphere in accordance with the standards for Container Level 3 controls as specified in 40 CFR part 63, subpart PP

— National Emission Standar ds for Containers. 

## §63.689 Standards: Transfer systems.

(a) The provisions of this section apply to the control of air emissions from transfer systems for which §63.683(b)(1)(i) of this subpart references the use of this section for such air emission

con trol.
(b) For each transfer system that is subject to this section and is an individual drain system, the owner or operator shall control air emissions in accordance with the standards specified in 40 CFR part 63, subpart RR

— National Emission Standards fo r Individual Drain Systems.(c) For each transfer system that is subject to this section but is not an individual drain system,

the owner or operator shall control air emissions by using one of the transfer systems specified in paragraphs (c)(1) through (c )(3) of this section.
(1) A transfer system that uses covers in accordance with the requirements specified in paragraph (d) of this section.
(2) A transfer system that consists of continuous hard

- piping. All joints or seams between the pipe sections shall be permanently or semi

- permanently sealed (e.g., a welded joint between two sections of metal pipe or a bolted and gasketed flange).
(3) A transfer system that is enclosed and vented through a closed

- vent system to a control device in accordance with the r equirements specified in paragraphs (c)(3)(i) and (c)(3)(ii) of this section.
(i) The transfer system is designed and operated such that an internal pressure in the vapor headspace in the enclosure is maintained at a level less than atmospheric pressure wh en the control device is operating, and

(ii) The closed

- vent system and control device are designed and operated in accordance with the requirements of §63.693 of this subpart.
(d) Owners and operators controlling air emissions from a transfer system usin g covers in accordance with the provisions of paragraph (c)(1) of this section shall meet the requirements specified in paragraphs (d)(1) through (d)(6) of this section.
(1) The cover and its closure devices shall be designed to form a continuous barrier over the entire surface area of the off

- site material as it is conveyed by the transfer system except for the openings at the inlet and outlet to the transfer system throu gh which the off

- site material passes. The inlet and outlet openings used for passage of the off

- site material through the transfer system shall be the minimum size required for practical operation of the transfer system.

(2) The cover shall be installed in a manner such that there are no visible cracks, holes, gaps, or other open spaces between cover section joints or between the interface of the cover edge and its mounting.
(3) Except for the inlet and outlet openings to the transfer system through whic h the off

- site material passes, each opening in the cover shall be equipped with a closure device designed to operate such that when the closure device is secured in the closed position there are no visible cracks, holes, gaps, or other open spaces in the closure device or between the perimeter of the opening and the closure device.

(4) The cover and its closure devices shall be made of suitable materials that will minimize exposure of the off

- site material to the atmosphere, to the extent practical, and w ill maintain the integrity of the equipment throughout its intended service life. Factors to be considered when selecting the materials for and designing the cover and closure devices shall include: organicvapor permeability; the effects of any contact wi th the material or its vapors conveyed in the

transfer system; the effects of outdoor exposure to wind, moisture, and sunlight; and the operating practices used for the transfer system on which the cover is installed.

(5) Whenever an off

- site material is in the transfer system, the cover shall be installed with each closure device secured in the closed position
, except the as specified in paragraph (d)(5)(i) or (d)(5)(ii) of this section.

(i) O o pening of closure devices or removal of the cover is allowed to provide access to the transfer system for performing routine inspection, maintenance, repair, or other activities needed for normal operations. Examples of such activities include those times when a worker needs to open a hatch or remove the cover to repair conveyance equipment mounted under the cover or to clear a blockage of material inside the system. Following completion of the activity, the owner or operator shall promptly secure the closu re device in the closed position or reinstall the cover, as applicable.
(ii) Opening of a safety device, as defined in §63.681 of this subpart, is allowed at any time conditions require it to do so to avoid an unsafe condition

. (6) The owner or operator shall inspect the air emission control equipment in accordance with the requirements specified in §63.695 of this subpart. 

## §63.690 Standards: Process vents.

(a) The provisions of this section apply to the control of air emissions from process vents for which §63.683(c)(1)(i) of this subpart references the use of this section for such air emission control.
(b) The owner or operator must route the vent stream from each affected process vent through a closed

- vent system to a control device that meets the st andards specified in §63.693 of this subpart. For the purpose of complying with this paragraph (b), a primary condenser is not a control device; however, a second condenser or other organic recovery device that is operated downstream of the primary condens er is considered a control device. 

## §63.691 Standards: Equipment leaks.

(a) The provisions of this section apply to the control of air emissions from equipment leaks for which §63.683(d) references the use of this section for such air emissions control.

(b) According to the date an affected source commenced construction or reconstruction and the date an affected source receives off

- site material for the first time
, as established in §63.680(e)(i)

- (iii) of this subpart
, t T he owner or operator shall control the HAP emitted from equipment leaks in accordance with the applicable provisions specified in either paragraph (b)(1) or (b)(2) of this section.(1) (i) The owner or operator controls the HAP emitted from equipment leaks in accordance with

§61.24 2 1 through §61.247 in 40 CFR part 61, subpart V

— National Emission Standards for Equipment Leaks
, with the difference noted in paragraphs (b)( 2 1 )( ii i) and (iv) of this section for the purposes of this subpart ; or
(2 ii ) The owner or operator controls the HAP emitted from equipment leaks in accordance with §63.16 2 1 through §63.182 in 40 CFR part 63, subpart H

— National Emission Standards for Organic Hazardous Air Pollutants from Equipment Leaks , with the differences noted in paragraphs (b)(2)(i) through (iv) of this section for the purposes of this subpart

. (iii) On or after [THE DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER ], for the purpose of complying with the requirements of 40 CFR 61.242

- 6(a)(2), the open end is sealed when instru ment monitoring of the open

- ended valve or line conducted according to Method 21 of 40 CFR part 60, appendix A indicates no readings of 500 ppm or greater.

(iv) On or after [THE DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER ], for the purpose of complying with the requirements of 40 CFR 61.242

- 6(d), o pen

- ended valves or lines in an emergency shutdown system which are designed to open automatically in the event of a process upset and that are exempt from the requirements in 4 0 CFR 61.242

- 6(a), (b)
, and (c) must comply with the requirements in §63. 693(c)(2) of this subpart

.

(2) The owner or operator controls the HAP emitted from equipment leaks in accordance with § 63.161 through § 63. 183 in 40 CFR part 63, subpart H

– National Emission Standards for Organic Hazardous Air Pollutants f or Equipment Leaks
, with the differences noted in paragraphs (b) (2)(i) through (v ) of this section for the purposes of this subpart.

( i ) F or each valve in gas/vapor or in light liquid service, as defined in § 63. 681 of this subpart
, that is part of an affected source under this subpart, an instrument reading that defines a leak is 500 ppm or greater as detected by Method 21 of 40 CFR part 60, appendix A

. ( ii ) F or each pump in light liquid service, as defined in § 63. 681 of this subpart
, that is part of an affected source under this subpart, an instrument readin g that defines a leak is 1 ,000 ppm or greater as detected by Method 21 of 40 CFR part 60, appendix A. Repair is not required unless an instrument reading of 2,000 ppm or greater is detected.

(iii ) On or after [THE DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN THE FEDERAL REGISTER ], for the purpose of complying with the requirements of 40 CFR 63.167 ( a ) (2) , the o pen end is sealed when instrument monitoring of the open

- ended valve or line conducted according to Method 21 of 40 CFR part 60, appendix A indicates no readings of 500 ppm or greater.(iv) On or after [THE DATE OF PUBLICATION OF THE FINAL RULE AMENDMENTS IN

THE FEDERAL REGISTER ], for the purpose of complying with the requirements of 40 CFR 6 3

. 167 (d), o pen

- ended valves or lines in an emergency shutdown system which are designed to open automatically in the event of a process upset and that are exempt from the requirements in 40 CFR 6 3.167 (a), (b) and (c) must comply with the requirements in §63. 693(c)(2) of this subpart.

(v ) For the purposes of this subpart, t he pressure relief device requirements of § 63.691(c) of this subpart rather than those of 40 CFR 63.165 shall apply.

(c) Requirements for pressure relief devices

. Except as provided in paragraph (c)(4) of this section, the owner or operator must comply with the requirements specified in paragraphs (c)(1) through ( 3 ) of this section for pressure relief devices in off

- site material service

. (1) Operating requirements

. Except during a pressure release event , operate each pressure relief device in off

- site material gas or vapor service with an instrument reading of less than 500 ppm above background as detected by Method 21 of 40 CFR part 60, a ppendix A.

(2) Pressure release requirements

. For pressure relief devices in off

- site material gas or vapor
s ervice, the owner or operator must comply with either paragraph (c )(2)(i) or (ii) of this section following a pressure release , as applicable.
(i) If the pressure relief device does not consist of or include a rupture disk, the pressure relief device shall be returned to a condition indicated by an instrument reading of less than 500 ppm above background, as detected by Method 21 of 40 CFR part 60, appendix A, no later than 5 calendar days after the pressure rel ease device returns to off

- site material service f

ollowing a pressure release , except as provided in 40 CFR 63.171

. (ii) If the pressure relief device consists of or includes a rupture disk
, except as provided in 40 CFR 63.171, install a replacement disk as soon as practicable but no later than 5 calendar days after the pressure release

. (3) Pressure release management

. Except as provided in paragraph (c)(4) of this section, emissions of HAP listed in Table 1 of this subpart may not be discharged directly to the atmosphere from pressure relief devices in off

- site material service, and a ccording to the date an affected source commenced construction or reconstruction and the date an affected source receives off

- site material for the first time
, as established in §63.680(e)(i)

- (iii) of this subpart
, the owner or operator must comply with the requirements specified in paragraphs (c)(3)(i) and (ii) of this section for all pressure relief devices in off

- site material service.
(i) The owner or operator m ust equip each pressure relief device in off

- site material service with a device(s) or use a monitoring system that is capable of : 1) identifying the pressure release; 2) recording the time and duration of each pressure release ; and 3) notifying operators immediately that a pressure release is occurring. The device or monitoring system may be either specific to the pressure release device itself or may be associated with the process system or piping, sufficient to indicate a pressure release to the atmosphe re. Examples of these types of devices ormonitoring systems include, but are not limited to, a rupture disk indicator, magnetic sensor,

motion detector on the pressure relief valve stem, flow monitor, pressure monitor , or parametric monitoring system

. (ii) If any pressure relief device in off

- site material service releases directly to the atmosphere as a result of a pressure release event, the owner or operator must calculate the quantity of HAP listed in Table 1 of this subpart released during each pr essure release event and report this quantity as required i n § 63.697(b)(5) of this subpart . Calculations may be based on data from the pressure relief device monitoring alone or in combination with process parameter monitoring data and process knowledge.

(4) Pressure relief devices routed to a drain system, process or control device

. If a pressure relief device in off

- site material service is designed and operated to route all pressure releases through a closed vent system to a drain system, process or con trol device , paragraphs (c)(1), (2), and (3) of this section do not apply

. T he closed vent system and the process or control device (if applicable) must meet the requirements of § 63. 693 of this subpart . The drain system (if applicable) must meet the requirements of §63. 689 of this subpart

. 

## §63.692 [Reserved]
§63.693 Standards: Closed

- vent systems and control devices.

(a) The provisions of this section apply to closed

- vent systems and control devices used to control air emissions for which another standard references the use of this section for such air emission control.

(b) For each closed

- vent system and control device used to comply with this section, the owner or operator shall meet the following requirements:
(1) The owner or operator must use a closed

- vent system that meets the requirements specified in paragraph (c) of this section.
(2) The owner or operator must use a control device that meets the requirements specified in paragraphs (d) through (h) of this section as applicable to the type a nd design of the control device selected by the owner or operator to comply with the provisions of this section.
(3) Whenever gases or vapors containing HAP are vented routed from a tank through a closed

vent system connected to a control device used to comply with this section the requirements of paragraph §63.6 8 5( b ) (1), (2) or (3) of this subpart
, the control device must be operating except as provided for at those times listed in either paragraph s (b)(3)(i) or and (b)(3)(ii) of this section.(i) T he control device may only be bypassed for the purpose of performing planned routine

maintenance of the closed

- vent system or control device in situations when the routine maintenance cannot be performed during periods that the emission point tank emissions are vented to the control device

. is shutdown.

(ii) On an annual basis, the total time that the closed

- vent system or control device is bypassed to perform routine maintenance shall n ot exceed 240 hours per each calendar year.
(ii) The control device may be bypassed for the purpose of correcting a malfunction of the closed

- vent system or control device. The owner or operator shall perform the adjustments or repairs necessary to correct the malfunction as soon as practicable after the malfunction is detected.
(4) The owner or operator must inspect and monitor each closed

- vent system in accordance with the requirements specified in either paragraph (b)(4)(i) or (b)(4)(ii) of this s ection.
(i) The owner or operator inspects and monitors the closed

- vent system in accordance with the requirements specified in §63.695(c) of this subpart, and complies with the applicable recordkeeping requirements in §63.696 of this subpart and the appli cable reporting requirements in §63.697 of this subpart.
(ii) As an alternative to meeting the requirements specified in paragraph (b)(4)(i) of this section, the owner or operator may choose to inspect and monitor the closed

- vent system in accordance with the requirements under 40 CFR part 63, subpart H

— National Emission Standards for Organic Hazardous Air Pollutants for Equipment Leaks as specified in 40 CFR 63.172(f) through (h), and complies with the applicable recordkeeping requirements in 40 CFR 63.181 and the applicable reporting requirements in 40 CFR 63.182.
(5) The owner or operator must monitor the operation of each control device in accordance with the requirements specified in paragraphs (d) through (h) of this section as applicable to the type

a nd design of the control device selected by the owner or operator to comply with the provisions of this section.
(6) The owner or operator shall maintain records for each control device in accordance with the requirements of §63.696 of this subpart.

(7) Th e owner or operator shall prepare and submit reports for each control device in accordance with the requirements of §63.697 of this subpart.
(8) In the case when an owner or operator chooses to use a design analysis to demonstrate compliance of a control d evice with the applicable performance requirements specified in this section as provided for in paragraphs (d) through (g) of this section, the Administrator may require request that the design analysis be revised or amended by the owner or operator to corr ect any deficiencies identified by the Administrator. If the owner or operator and the Administrator do not agree on the acceptability of using the design analysis (including any changes required requested by the Administrator) to demonstrate that the contr ol device achieves theapplicable performance requirements, then the disagreement must be resolved using the results

of a performance test conducted by the owner or operator in accordance with the requirements of §63.694(l) of this subpart. The Administrat or may choose to have an authorized representative observe the performance test conducted by the owner or operator. Should the results of this performance test not agree with the determination of control device performance based on the design analysis, the n the results of the performance test will be used to establish compliance with this subpart.

(c) Closed

- vent system requirements.
(1) The vent stream required to be controlled shall be conveyed to the control device by either of the following closed

- vent systems:
(i) A closed

- vent system that is designed to operate with no detectable organic emissions using the procedure specified in §63.694(k) of this subpart; or

(ii) A closed

- vent system that is designed to operate at a pressure below atmospheric pressu re. The system shall be equipped with at least one pressure ga u ge or other pressure measurement device that can be read from a readily accessible location to verify that negative pressure is being maintained in the closed

- vent system when the control devic e is operating.

(2) In situations when the closed

- vent system includes bypass devices that could be used to divert a vent stream from the closed

- vent system to the atmosphere at a point upstream of the control device inlet, each bypass device must be equipped with either a flow indicator as specified in paragraph (c)(2)(i) of this section or a seal or locking device as specified in paragraph (c)(2)(ii) of this section

. , For the purpose of complying with this paragraph (c)(2), low leg drains, high point bleeds, analyzer vents, open

- ended valves or lines, or pressure relief valves needed for safety reasons are not subject to the requirements of this paragraph (c)(2). except as provided for in paragraph (c )( 2 )(iii) of this section:

(i) If a flow indicator is used, the indicator must be installed at the entrance to the bypass line used to divert the vent stream from the closed

- vent system to the atmosphere. The flow indicator must indicate a reading at least once every 15 minutes. The owner or operator must maintain records of the following information: hourly records of whether the flow indicator was operating and whether flow was detected at any time during the hour; and records of all periods when flow is detected or the flow indicator is not operating.

(i i) If a seal or locking device is used to comply with paragraph (c)(2) of this section, the device shall be placed on the mechanism by which the bypass device position is controlled ( e.g., valve handle, damper lever) when the bypass device is in the closed position such that the bypass device cannot be opened without breaking the seal or removing the lock. Examples of such devices include, but are not limited to, a car

- seal or a lock

- and

- ke y configuration valve.

(iii) Equipment needed for safety reasons, including l ow leg drains, open

- ended valves and lines not in emergency shutdown systems , and pressure relief devices subject to the requirements of§63.69 1 ( c ) of this subpart are not subject to the requirements of paragraph s (c) (2)(i) and (ii) of

this section.
(d) Carbon adsorption control device requirements.
(1) The carbon adsorption system must achieve the performance specifications in either paragraph (d)(1)(i) or (d)(1)(ii) of this section.
(i) Recover 95 percent or more, on a weight

- basis, of the total organic compounds (TOC), less methane and ethane, contained in the vent stream entering the carbon adsorption system; or
(ii) Recover 95 percent or more, on a weight

- basis, of the tot al HAP listed in Table 1 of this subpart contained in the vent stream entering the carbon adsorption system.
(2) The owner or operator must demonstrate that the carbon adsorption system achieves the performance requirements in paragraph (d)(1) of this sect ion by either performing a performance test as specified in paragraph (d)(2)(i) of this section or a design analysis as specified in paragraph (d)(2)(ii) of this section.
(i) An owner or operator choosing to use a performance test to demonstrate compliance must conduct the test in accordance with the requirements of §63.694(l) of this subpart.
(ii) An owner or operator choosing to use a design analysis to demonstrate compliance must include as part of this design analysis the information specified in either paragraph (d)(2)(ii)(A) or (d)(2)(ii)(B) of this section as applicable to the carbon adsorption system design.
(A) For a regenerable carbon adsorption system, the design analysis shall address the vent stream composition, constituent concentrations, flow rate, relative humidity, and temperature and shall establish the design exhaust vent stream organic compound concentration, adsorption cycle time, number and capacity of carbon beds, type and working capacity of activated carbon used for carbon beds, desig n total regeneration steam flow over the period of each complete carbon bed regeneration cycle, design carbon bed temperature after regeneration, design carbon bed regeneration time, and design service life of the carbon.
(B) For a nonregenerable carbon ad sorption system (e.g., a carbon canister), the design analysis shall address the vent stream composition, constituent concentrations, flow rate, relative humidity, and temperature and shall establish the design exhaust vent stream organic compound concentr ation, carbon bed capacity, activated carbon type and working capacity, and design carbon replacement interval based on the total carbon working capacity of the control device and emission point operating schedule.
(3) The owner or operator must monitor th e operation of the carbon adsorption system in accordance with the requirements of §63.695(e) using one of the continuous monitoring systems specified in paragraphs (d)(3)(i) through (iii) of this section. Monitoring the operation of a nonregenerable carbo n adsorption system ( e.g., a carbon canister) using a continuous monitoringsystem is not required when the carbon canister or the carbon in the control device is replaced on

a regular basis according to the requirements in paragraph (d)(4)(iii) of this se ction.
(i) For a regenerative

- type carbon adsorption system:
(A) A continuous parameter monitoring system to measure and record the average total regeneration stream mass flow or volumetric flow during each carbon bed regeneration cycle. The integrating re generating stream flow monitoring device must have an accuracy of ±10 percent; and
(B) A continuous parameter monitoring system to measure and record the average carbon bed temperature for the duration of the carbon bed steaming cycle and to measure the ac tual carbon bed temperature after regeneration and within 15 minutes of completing the cooling cycle. The accuracy of the temperature monitoring device must be ±1 percent of the temperature being measured, expressed in degrees Celsius or ±5 °C, whichever i s greater.
(ii) A continuous monitoring system to measure and record the daily average concentration level of organic compounds in the exhaust gas stream from the control device. The organic monitoring system must comply either with Performance Specificati on 8 or 9 in 40 CFR part 60, appendix B. The relative accuracy provision of Performance Specification 8, Sections 2.4 and 3 need not be conducted.
(iii) A continuous monitoring system that measures other alternative operating parameters upon approval of th e Administrator as specified in 40 CFR 63.8(f)(1) through (f)(5) of this part.
(4) The owner or operator shall manage the carbon used for the carbon adsorption system, as follows:
(i) Following the initial startup of the control device, all carbon in the c ontrol device shall be replaced with fresh carbon on a regular, predetermined time interval that is no longer than the carbon service life established for the carbon adsorption system. The provisions of this paragraph (d)(4)(i) do not apply to a nonregener able carbon adsorption system ( e.g., a carbon canister) for which the carbon canister or the carbon in the control device is replaced on a regular basis according to the requirements in paragraph (d)(4)(iii) of this section.
(ii) The spent carbon removed f rom the carbon adsorption system must be either regenerated, reactivated, or burned in one of the units specified in paragraphs (d)(4)(ii)(A) through (d)(4)(ii)(G) of this section.
(A) Regenerated or reactivated in a thermal treatment unit for which the ow ner or operator has been issued a final permit under 40 CFR part 270 that implements the requirements of 40 CFR part 264, subpart X.
(B) Regenerated or reactivated in a thermal treatment unit equipped with and operating air emission controls in accordance with this section.(C) Regenerated or reactivated in a thermal treatment unit equipped with and operating organic

air emission controls in accordance with a national emission standard for hazardous air pollutants under another subpart in 40 CFR part 63 or 40 CFR part 61.
(D) Burned in a hazardous waste incinerator for which the owner or operator has been issued a final permit under 40 CFR part 270 that implements the requirements of 40 CFR part 264, subpart O.

(E) Burned in a hazardous waste incinerator for which the owner or operator has designed and operates the incinerator in accordance with the interim status requirements of 40 CFR part 265, subpart O.
(F) Burned in a boiler or industrial furnace for which the owner or operator has been issued a final pe rmit under 40 CFR part 270 that implements the requirements of 40 CFR part 266, subpart H.
(G) Burned in a boiler or industrial furnace for which the owner or operator has designed and operates the unit in accordance with the interim status requirements of 40 CFR part 266, subpart H.
(iii) As an alternative to meeting the requirements in paragraphs (d)(3) and (d)(4)(i) of this section, an owner or operator of a nonregenerable carbon adsorption system may choose to replace on a regular basis the carbon canis ter or the carbon in the control device using the procedures in either paragraph (d)(4)(iii)(A) or (d)(4)(iii)(B) of this section. For the purpose of complying with this paragraph (d)(4)(iii), a nonregenerable carbon adsorption system means a carbon adsorp tion system that does not regenerate the carbon bed directly onsite in the control device, such as a carbon canister. The spent carbon removed from the nonregenerable carbon adsorption system must be managed according to the requirements in paragraph (d)(4 )(ii) of this section.
(A) Monitor the concentration level of the organic compounds in the exhaust vent from the carbon adsorption system on a regular schedule, and when carbon breakthrough is indicated, immediately replace either the existing carbon canis ter with a new carbon canister or replace the existing carbon in the control device with fresh carbon. Measurement of the concentration level of the organic compounds in the exhaust vent stream must be made with a detection instrument that is appropriate f

or the composition of organic constituents in the vent stream and is routinely calibrated to measure the organic concentration level expected to occur at breakthrough. The monitoring frequency must be daily or at an interval no greater than 20 percent of t he time required to consume the total carbon working capacity established as a requirement of paragraph (d)(2)(ii)(B) of this section, whichever is longer.
(B) Replace either the existing carbon canister with a new carbon canister or replace the existing

c arbon in the control device with fresh carbon at a regular, predetermined time interval that is less than the design carbon replacement interval established as a requirement of paragraph (d)(2)(ii)(B) of this section.(e) Condenser control device requireme nts.

(1) The condenser must achieve the performance specifications in either paragraph (e)(1)(i) or (e)(1)(ii) of this section.
(i) Recover 95 percent or more, on a weight

- basis, of the total organic compounds (TOC), less methane and ethane, contained in t he vent stream entering the condenser; or
(ii) Recover 95 percent or more, on a weight

- basis, of the total HAP, listed in Table 1 of this subpart, contained in the vent stream entering the condenser.
(2) The owner or operator must demonstrate that the cond enser achieves the performance requirements in paragraph (e)(1) of this section by either performing a performance test as specified in paragraph (e)(2)(i) of this section or a design analysis as specified in paragraph (e)(2)(ii) of this section.

(i) An ow ner or operator choosing to use a performance tests to demonstrate compliance must conduct the test in accordance with the requirements of §63.694(l) of this subpart.
(ii) An owner or operator choosing to use a design analysis to demonstrate compliance must include as part of this design analysis the following information: description of the vent stream composition, constituent concentrations, flow rate, relative humidity, and temperature; and specification of the design outlet organic compound concentra tion level, design average temperature of the condenser exhaust vent stream, and the design average temperatures of the coolant fluid at the condenser inlet and outlet.
(3) The owner or operator must monitor the operation of the condenser in accordance wit h the requirements of §63.695(e) of this subpart using one of the continuous monitoring systems specified in paragraphs (e)(3)(i) through (e)(3)(iii) of this section.
(i) A continuous parameter monitoring system to measure and record the daily average temp erature of the exhaust gases from the control device. The accuracy of the temperature monitoring device shall be ±1 percent of the temperature being measured, expressed in degrees Celsius or ±5 °C, whichever is greater.
(ii) A continuous monitoring system to measure and record the daily average concentration level of organic compounds in the exhaust gas stream from the control device. The organic monitoring system must comply either with Performance Specification 8 or 9 in 40 CFR part 60, appendix B. The r elative accuracy provision of Performance Specification 8, Sections 2.4 and 3 need not be conducted.
(iii) A continuous monitoring system that measures other alternative operating parameters upon approval of the Administrator as specified in 40 CFR 63.8(f) (1) through (f)(5) of this part.
(f) Vapor incinerator control device requirements.(1) The vapor incinerator must achieve the performance specifications in either paragraph

(f)(1)(i), (f)(1)(ii), or (f)(1)(iii) of this section.
(i) Destroy the total organ ic compounds (TOC), less methane and ethane, contained in the vent stream entering the vapor incinerator either:
(A) By 95 percent or more, on a weight

- basis, or

(B) To achieve a total incinerator outlet concentration for the TOC, less methane and ethane, of less than or equal to 20 ppmv on a dry basis corrected to 3 percent oxygen.
(ii) Destroy the HAP listed in Table 1 of this subpart contained in the vent stream entering the vapor incinerator either:
(A) By 95 percent or more, on a total HAP weight

- basis , or
(B) To achieve a total incinerator outlet concentration for the HAP, listed in Table 1 of this subpart, of less than or equal to 20 ppmv on a dry basis corrected to 3 percent oxygen.
(iii) Maintain the conditions in the vapor incinerator combustion ch amber at a residence time of 0.5 seconds or longer and at a temperature of 760°C or higher.
(2) The owner or operator must demonstrate that the vapor incinerator achieves the performance requirements in paragraph (f)(1) of this section by either performing a performance test as specified in paragraph (f)(2)(i) of this section or a design analysis as specified in paragraph (f)(2)(ii) of this section.
(i) An owner or operator choosing to use a performance test to demonstrate compliance must conduct the test i n accordance with the requirements of §63.694(l) of this subpart.
(ii) An owner or operator choosing to use a design analysis to demonstrate compliance must include as part of this design analysis the information specified in either paragraph (f)(2)(ii)(A) or (f)(2)(ii)(B) of this section as applicable to the vapor incinerator design.
(A) For a thermal vapor incinerator, the design analysis shall address the vent stream composition, constituent concentrations, and flow rate and shall establish the design mi nimum and average temperatures in the combustion chamber and the combustion chamber residence time.
(B) For a catalytic vapor incinerator, the design analysis shall address the vent stream composition, constituent concentrations, and flow rate and shall es tablish the design minimum and average temperatures across the catalyst bed inlet and outlet, and the design service life of the catalyst.
(3) The owner or operator must monitor the operation of the vapor incinerator in accordance with the requirements of §63.695(e) of this subpart using one of the continuous monitoring systemsspecified in paragraphs (f)(3)(i) through (f)(3)(iv) of this section as applicable to the type of

vapor incinerator used.
(i) For a thermal vapor incinerator, a continuous parameter monitoring system to measure and record the daily average temperature of the exhaust gases from the control device. The accuracy of the temperature monitoring device must be ±1 percent of the temperature being measured, expressed in degrees Celsius of ±0.5 °C, whichever is greater.
(ii) For a catalytic vapor incinerator, a temperature monitoring device capable of monitoring temperature at two locations equipped with a continuous recorder. One temperature sensor shall be installed in the vent stream at the n earest feasible point to the catalyst bed inlet and a second temperature sensor shall be installed in the vent stream at the nearest feasible point to the catalyst bed outlet.
(iii) For either type of vapor incinerator, a continuous monitoring system to me asure and record the daily average concentration of organic compounds in the exhaust vent stream from the control device. The organic monitoring system must comply either with Performance Specification 8 or 9 in 40 CFR part 60, appendix B. The relative acc uracy provision of Performance Specification 8, Sections 2.4 and 3 need not be conducted.
(iv) For either type of vapor incinerator, a continuous monitoring system that measures alternative operating parameters other than those specified in paragraph (f)(3 )(i) or (f)(3)(ii) of this section upon approval of the Administrator as specified in 40 CFR 63.8(f)(1) through (f)(5) of this part.
(g) Boilers and process heaters control device requirements.
(1) The boiler or process heater must achieve the performance specifications in either paragraph (g)(1)(i), (g)(1)(ii), (g)(1)(iii), (g)(1)(iv), or (g)(1)(v) of this section.
(i) Destroy the total organic compounds (TOC), less methane and ethane, contained in the vent stream introduced into the flame zone of the boil er or process heater either:
(A) By 95 percent or more, on a weight

- basis, or
(B) To achieve in the exhausted combustion gases a total concentration for the TOC, less methane and ethane, of less than or equal to 20 parts ppmv on a dry basis corrected to 3 percent oxygen.
(ii) Destroy the HAP listed in Table 1 of this subpart contained in the vent stream entering the vapor incinerator either:
(A) By 95 percent or more, on a total HAP weight

- basis, or(B) To achieve in the exhausted combustion gases a total concentration for the HAP, listed in

Table 1 of the subpart, of less than or equal to 20 ppmv on a dry basis corrected to 3 percent oxygen.
(iii) Introduce the vent stream into the flame zone of the boiler or process heater and maintain the conditions in the combustion chamber at a residence time of 0.5 seconds or longer and at a temperature of 760°C or higher.
(iv) Introduce the vent stream with the fuel that provides the predominate heat input to the boiler or process heater (i.e., the primary fuel); or
(v) Introduce the vent stream to a boiler or process heater for which the owner or operator either has been issued a final permit under 40 CFR part 270 and complies with the requirements of 40 CFR part 266, subpart H of this chapter; or has certified compl iance with the interim status requirements of 40 CFR part 266, subpart H of this ch apter ; or has submitted a Notification of Compliance under 40 CFR 63.1207(j) and 63. 1210(d) and complies with the requirements of 40 CFR part 63 subpart EEE at all times (including times when non

- hazardous waste is being burned)

. (2) The owner or operator must demonstrate that the boiler or process heater achieves the performance specifications in paragraph (g)(1) of this section chosen by the owner or operator using the a pplicable method specified in paragraph (g)(2)(i) or (g)(2)(ii) of this section.
(i) If an owner or operator chooses to comply with the performance specifications in either paragraph (g)(1)(i), (g)(1)(ii), or (g)(1)(iii) of this section, the owner or opera tor must demonstrate compliance with the applicable performance specifications by either performing a performance test as specified in paragraph (g)(2)(i)(A) of this section or a design analysis as specified in paragraph (g)(2)(i)(B) of this section.

(A) A n owner or operator choosing to use a performance test to demonstrate compliance must conduct the test in accordance with the requirements of §63.694(l) of this subpart.
(B) An owner or operator choosing to use a design analysis to demonstrate compliance m ust include as part of this design analysis the following information: description of the vent stream composition, constituent concentrations, and flow rate; specification of the design minimum and average flame zone temperatures and combustion zone reside nce time; and description of the method and location by which the vent stream is introduced into the flame zone.
(ii) If an owner or operator chooses to comply with the performance specifications in either paragraph (g)(1)(iv) or (g)(1)(v) of this section, the owner or operator must demonstrate compliance by maintaining the records that document that the boiler or process heater is designed and operated in accordance with the applicable requirements of this section.
(3) For a boiler or process heater comply ing with the performance specifications in either paragraph (g)(1)(i), (g)(1)(ii), or (g)(1)(iii) of this section, the owner or operator must monitor the operation of a boiler or process heater in accordance with the requirements of §63.695(e) ofthis subp art using one of the continuous monitoring systems specified in paragraphs (g)(3)(i)

through (g)(3)(iii) of this section.
(i) A continuous parameter monitoring system to measure and record the daily average combustion zone temperature. The accuracy of the temperature sensor must be ±1 percent of the temperature being measured, expressed in degrees Celsius or ±0.5 °C, whichever is greater;
(ii) A continuous monitoring system to measure and record the daily average concentration of organic compounds in the ex haust vent stream from the control device. The organic monitoring system must comply either with Performance Specification 8 or 9 in 40 CFR part 60, appendix B. The relative accuracy provision of Performance Specification 8, Sections 2.4 and 3 need not be conducted.
(iii) A continuous monitoring system that measures alternative operating parameters other than those specified in paragraph (g)(3)(i) or (g)(3)(ii) of this section upon approval of the Administrator as specified in 40 CFR 63.8(f)(1) through (f)( 5) of this part.
(h) Flare control device requirements.
(1) The flare must be designed and operated in accordance with the requirements in 40 CFR 63.11(b).
(2) The owner or operator must demonstrate that the flare achieves the requirements in paragraph (h) (1) of this section by performing the procedures specified in paragraph (h)(2)(i) of this section. A previous compliance demonstration for the flare that meets all of the conditions specified in paragraph (h)(2)(ii) of this section may be used by an owner or operator to demonstrate compliance with this paragraph (h)(2).
(i) To demonstrate that a flare achieves the requirements in paragraph (h)(1) of this section, the owner or operator performs all of the procedures specified in paragraphs (h)(2)(i)(A) throu gh (h)(2)(i)(C) of this section.
(A) The owner or operator conducts a visible emission test for the flare in accordance with the requirements specified in 40 CFR 63.11(b)(4).
(B) The owner or operator determines the net heating value of the gas being combu sted in the flare in accordance with the requirements specified in 40 CFR 63.11(b)(6); and
(C) The owner or operator determines the flare exit velocity in accordance with the requirements applicable to the flare design as specified in 40 CFR 63.11(b)(7) o r 40 CFR 63.11(b)(8).
(ii) A previous compliance demonstration for the flare may be used by an owner or operator to demonstrate compliance with paragraph (h)(2) of this section provided that all conditions for the compliance determination and subsequent fl are operation are met as specified in paragraphs (h)(2)(ii)(A) and (h)(2)(ii)(B) of this section.(A) The owner or operator conducted the compliance determination using the procedures

specified in paragraph (h)(2)(i) of this section.
(B) No flare operating parameter or process changes have occurred since completion of the compliance determination which could affect the compliance determination results.
(3) The owner or operator must monitor the operation of the flare using a heat sensing monitoring device ( including but not limited to a thermocouple, ultraviolet beam sensor, or infrared sensor) that continuously detects the presence of a pilot flame. The owner or operator must record, for each 1

- hour period, whether the monitor was continuously operating and whether a pilot flame was continuously present during each hour as required in §63.696(b)(3) of this subpart. 

## §63.694 Testing methods and procedures.

(a) This section specifies the testing methods and procedures required for this subpart to perform the following:
(1) To determine the average VOHAP concentration for off

- site material streams at the point

- of

delivery for compliance with standards specifi ed §63.683 of this subpart, the testing methods and procedures are specified in paragraph (b) of this section.
(2) To determine the average VOHAP concentration for treated off

- site material streams at the point

- of

- treatment for compliance with standards s pecified §63.684 of this subpart, the testing methods and procedures are specified in paragraph (c) of this section.
(3) To determine the treatment process VOHAP concentration limit (C R ) for compliance with standards specified §63.684 of this subpart, the testing methods and procedures are specified in paragraph (d) of this section.
(4) To determine treatment process required HAP removal rate (RMR) for compliance with standards specified §63.684 of this subpart, the testing methods and procedures are spec ified in paragraph (e) of this section.
(5) To determine treatment process actual HAP removal rate (MR) for compliance with standards specified §63.684 of this subpart, the testing methods and procedures are specified in paragraph (f) of this section.

(6 ) To determine treatment process required HAP reduction efficiency (R) for compliance with standards specified in §63.684 of this subpart, the testing methods and procedures are specified in paragraph (g) of this section.
(7) To determine treatment proces s required HAP biodegradation efficiency (R bio ) for compliance with standards specified in §63.684 of this subpart, the testing methods and procedures are specified in paragraph (h) of this section.(8) To determine treatment process required actual HAP m ass removal rate (MR bio ) for

compliance with standards specified in§63.684 of this subpart, the testing methods and procedures are specified in paragraph (i) of this section.
(9) To determine maximum organic HAP vapor pressure of off

- site materials in tan ks for compliance with the standards specified in §63.685 of this subpart, the testing methods and procedures are specified in paragraph (j) of this section.
(10) To determine no detectable organic emissions, the testing methods and procedures are specifi ed in paragraph (k) of this section.

(11) To determine closed

- vent system and control device performance for compliance with the standards specified in §63.693 of this subpart, the testing methods and procedures are specified in paragraph (l) of this sect ion.
(12) To determine process vent stream flow rate and total organic HAP concentration for compliance with the standards specified in §63.693 of this subpart, the testing methods and procedures are specified in paragraph (m) of this section.
(b) Testing methods and procedures to determine average VOHAP concentration of an off

- site material stream at the point

- of

- delivery.
(1) The average VOHAP concentration of an off

- site material at the point

- of

- delivery shall be determined using either direct measurem ent as specified in paragraph (b)(2) of this section or by knowledge as specified in paragraph (b)(3) of this section.

(2) Direct measurement to determine VOHAP concentration

— (i) Sampling. Samples of the off

site material stream shall be collected from th e container, pipeline, or other device used to deliver the off

- site material stream to the plant site in a manner such that volatilization of organics contained in the sample is minimized and an adequately representative sample is collected and maintained for analysis by the selected method.
(A) The averaging period to be used for determining the average VOHAP concentration for the off

- site material stream on a mass

- weighted average basis shall be designated and recorded. The averaging period can represent any time interval that the owner or operator determines is appropriate for the off

- site material stream but shall not exceed 1 year.
(B) A sufficient number of samples, but no less than four samples, shall be collected to represent the complete range of HAP compositions and HAP quantities that occur in the off

- site material stream during the entire averaging period due to normal variations in the operating conditions for the source or process generating the off

- site material stream. Examples of such norma l variations are seasonal variations in off

- site material quantity or fluctuations in ambient temperature.
(C) All samples shall be collected and handled in accordance with written procedures prepared by the owner or operator and documented in a site samp ling plan. This plan shall describe the procedure by which representative samples of the off

- site material stream are collected such thata minimum loss of organics occurs throughout the sample collection and handling process and by

which sample integrity is maintained. A copy of the written sampling plan shall be maintained

on

- site in the plant site operating records. An example of an acceptable sampling plan includes a plan incorporating sample collection and handling procedures in accordance with the req uirements specified in “Test Methods for Evaluating Solid Waste, Physical/Chemical Methods,” EPA Publication No. SW

- 846 or Method 25D in 40 CFR part 60, appendix A.

(ii) Analysis. Each collected sample must be prepared and analyzed in accordance with one of the following methods as applicable to the sampled off

- site material for the purpose of measuring the HAP listed in Table 1 of this subpart:
(A) Method 305 in 40 CFR part 63, appendix A.
(B) Method 25D in 40 CFR part 60, appendix A.

(C) Method 624 in 40 CFR part 136, appendix A. If this method is used to analyze one or more compounds that are not on the method's published list of approved compounds, the Alternative Test Procedure specified in 40 CFR 136.4 and 40 CFR 136.5 must be followed.

(D) Method 625 in 40 CFR part 136, appendix A. For the purpose of using this method to comply with this subpart, the owner or operator must perform corrections to these compounds based on the “accuracy as recovery” using the factors in Table 7 of the method. If this met hod is used to analyze one or more compounds that are not on the method's published list of approved compounds, the Alternative Test Procedure specified in 40 CFR 136.4 and 40 CFR 136.5 must be followed.
(E) Method 1624 in 40 CFR part 136, appendix A.

(F) Method 1625 in 40 CFR part 136, appendix A.
(G) Method 8260 in “Test Methods for Evaluating Solid Waste, Physical/Chemical Methods,” EPA Publication No. SW

- 846, Third Edition, September 1986, as amended by Update I, November 15, 1992. As an alternative, an owner or operator may use any more recent, updated version of Method 8260 approved by the EPA. For the purpose of using Method 8260 to comply with this subpart, the owner or operator must maintain a formal quality assurance program consistent with section 8 of Method 8260, and this program must include the following elements related to measuring the concentrations of volatile compounds:

( 1 ) Documentation of site

- specific procedures to minimize the loss of compounds due to volatilization, biodegradation, re action, or sorption during the sample collection, storage, and preparation steps.

( 2 ) Documentation of specific quality assurance procedures followed during sampling, sample preparation, sample introduction, and analysis.( 3 ) Measurement of the average acc uracy and precision of the specific procedures, including

field duplicates and field spiking of the off

- site material source before or during sampling with compounds having similar chemical characteristics to the target analytes.
(H) Method 8270 in “Test M ethods for Evaluating Solid Waste, Physical/Chemical Methods,” EPA Publication No. SW

- 846, Third Edition, September 1986, as amended by Update I, November 15, 1992. As an alternative, an owner or operator may use any more recent, updated version of Method 8270 approved by the EPA. For the purpose of using Method 8270 to comply with this subpart, the owner or operator must maintain a formal quality assurance program consistent with Method 8270, and this program must include the following elements related to measuring the concentrations of volatile compounds:

( 1 ) Documentation of site

- specific procedures to minimize the loss of compounds due to volatilization, biodegradation, reaction, or sorption during the sample collection, storage, and preparation steps.

( 2 ) Documentation of specific quality assurance procedures followed during sampling, sample preparation, sample introduction, and analysis.

( 3 ) Measurement of the average accuracy and precision of the specific procedures, including field duplicates and fiel d spiking of the off

- site material source before or during sampling with compounds having similar chemical characteristics to the target analytes.
(I) Any other analysis method that has been validated in accordance with the procedures specified in section 5.1 and section 5.3 and the corresponding calculations in section 6.1 or section 6.3 of Method 301 in appendix A in 40 CFR part 63. The data are acceptable if they meet the criteria specified in section 6.1.5 or section 6.3.3 of Method 301. If correction i s required under section 6.3.3 of Method 301, the data are acceptable if the correction factor is within the range of 0.7 to 1.30. Other sections of Method 301 are not required.

(iii) Calculations. The average VOHAP concentration (C) on a mass

- weighted bas is shall be calculated by using the results for all samples analyzed in accordance with paragraph (b)(2)(ii) of this section and the following equation. An owner or operator using a test method that provides species

- specific chemical concentrations may adj ust the measured concentrations to the corresponding concentration values which would be obtained had the off

- site material samples been analyzed using Method 305. To adjust these data, the measured concentration for each individual HAP chemical species co ntained in the off

- site material is multiplied by the appropriate species

- specific adjustment factor (f m305 ) listed in Table 1 of this subpart.

Where:
C = Average VOHAP concentration of the off

- site material at the point

- of

- delivery on a mass

weighted basis, ppmw.i = Individual sample “i” of the off

- site material.
n = Total number of samples of the off

- site material collected (at least 4) for the averaging period (not to exceed 1 year).

Q i = Mass quantity of off

- site material stream represented by C i , kg/hr.

Q T = Total mass quantity of off

- site material during the averaging period, kg/hr.

C i = Measured VOHAP concentration of sample “i” as determined in accordance with the requirements of §63.694(a), ppmw.
(3) Knowledge of the off

- site material to det ermine VOHAP concentration.
(i) Documentation shall be prepared that presents the information used as the basis for the owner's or operator's knowledge of the off

- site material stream's average VOHAP concentration. Examples of information that may be used as the basis for knowledge include: material balances for the source or process generating the off

- site material stream; species

- specific chemical test data for the off

- site material stream from previous testing that are still applicable to the current of f

- site material stream; previous test data for other locations managing the same type of off

- site material stream; or other knowledge based on information in documents such as manifests, shipping papers, or waste certification notices.

(ii) If test data ar e used as the basis for knowledge, then the owner or operator shall document the test method, sampling protocol, and the means by which sampling variability and analytical variability are accounted for in the determination of the average VOHAP concentratio n. For example, an owner or operator may use HAP concentration test data for the off

- site material stream that are validated in accordance with Method 301 in 40 CFR part 63, appendix A of this part as the basis for knowledge of the off

- site material.

(iii ) An owner or operator using species

- specific chemical concentration test data as the basis for knowledge of the off

- site material may adjust the test data to the corresponding average VOHAP concentration value which would be obtained had the off

- site mate rial samples been analyzed using Method 305. To adjust these data, the measured concentration for each individual HAP chemical species contained in the off

- site material is multiplied by the appropriate species

specific adjustment factor (f m305 ) listed in Table 1 of this subpart.
(iv) In the event that the Administrator and the owner or operator disagree on a determination of the average VOHAP concentration for an off

- site material stream using knowledge, then the results from a determination of VOHAP conc entration using direct measurement as specified in paragraph (b)(2) of this section shall be used to establish compliance with the applicable requirements of this subpart. The Administrator may perform or require request that the owner or operator perform t his determination using direct measurement.
(c) Determination of average VOHAP concentration of an off

- site material stream at the point

of

- treatment.(1) Sampling. Samples of the off

- site material stream shall be collected at the point

- of

- treatment in a manner such that volatilization of organics contained in the sample is minimized and an adequately representative sample is collected and maintained for analysis by the selected method.
(i) The averaging period to be used for determining the average VOHAP concentration for the off

- site material stream on a mass

- weighted average basis shall be designated and recorded. The averaging period can represent any time interval that the owner or operator determines is appropriate for the off

- site material stream but shall not exceed 1 year.
(ii) A sufficient number of samples, but no less than four samples, shall be collected to represent the complete range of HAP compositions and HAP quantities that occur in the off

- site material stream during the entire averaging p eriod due to normal variations in the operating conditions for the treatment process. Examples of such normal variations are seasonal variations in off

- site material quantity or fluctuations in ambient temperature.
(iii) All samples shall be collected and handled in accordance with written procedures prepared by the owner or operator and documented in a site sampling plan. This plan shall describe the procedure by which representative samples of the off

- site material stream are collected such that a minimum loss of organics occurs throughout the sample collection and handling process and by which sample integrity is maintained. A copy of the written sampling plan shall be maintained

on

- site in the plant site operating records. An example of an acceptable sam pling plan includes a plan incorporating sample collection and handling procedures in accordance with the requirements specified in “Test Methods for Evaluating Solid Waste, Physical/Chemical Methods,” EPA Publication No. SW

- 846 or Method 25D in 40 CFR par t 60, appendix A.

(2) Analysis. Each collected sample must be prepared and analyzed in accordance with one of the methods specified in paragraphs (b)(2)(ii)(A) through (b)(2)(ii)(I) of this section, as applicable to the sampled off

- site material, for the p urpose of measuring the HAP listed in Table 1 of this subpart.

(3) Calculations. T h e a v e r a g e V O H A P c o n c e n t r a t i o n ( C ̅ ) a m a s s

- weighted basis shall be calculated by using the results for all samples analyzed in accordance with paragraph (c)(2) of this sectio n and the following equation. An owner or operator using a test method that provides species

- specific chemical concentrations may adjust the measured concentrations to the corresponding concentration values which would be obtained had the off

- site material samples been analyzed using Method 305. To adjust these data, the measured concentration for each individual HAP chemical species contained in the off

- site material is multiplied by the appropriate species

- specific adjustment factor (f m305 ) listed in Tabl e 1 of this subpart.

Where:

C ̅ = A v e r a g e V O H A P c o n c e n t r a t i o n o f t h e o f f

- site material on a mass

- weighted basis, ppmw.i = Individual sample “i” of the off

- site material.
n = Total number of samples of the off

- site material collected (at least 4) for the averaging period (not to exceed 1 year).

Q i = Mass quantity of off

- site material stream represented by C i , kg/hr.

Q T = Total mass quantity of off

- site material during the averaging period, kg/hr.

C i = Measured VOHAP concentration of sample “i” as determin ed in accordance with the requirements of §63.694(a), ppmw.

(d) Determination of treatment process VOHAP concentration limit (C R ). (1) All of the off

- site material streams entering the treatment process shall be identified.
(2) The average VOHAP concentra tion of each off

- site material stream at the point

- of

- delivery shall be determined using the procedures specified in paragraph (b) of this section.

(3) The VOHAP concentration limit (C R ) shall be calculated by using the results determined for each individ ual off

- site material stream and the following equation:

where:

C R =VOHAP concentration limit, ppmw.

x=Individual off

- site material stream “x” that has a VOHAP concentration less than 500 ppmw at the point

- of

- delivery.
y=Individual off

- site material str eam “y” that has a VOHAP concentration equal to or greater than 500 ppmw at the point

- of

- delivery.

m=Total number of “x” off

- site material streams treated by process.
n=Total number of “y” off

- site material streams treated by process.

Q
x =Total mass quan tity of off

- site material stream “x”, kg/yr.

Q y =Total mass quantity of off

- site material stream “y”, kg/yr.

C ̅

x =VOHAP concentration of off

- site material stream “x” at the point

- of

- delivery, ppmw.(e) Determination of required HAP mass removal rate (RMR).

(1) Each individual stream containing HAP that enters the treatment process shall be identified.
(2) The average VOHAP concentration at the point

- of

- delivery for each stream identified in paragraph (e)(1) of this section shall be determined using the test methods and procedures specified in paragraph (b) of this section.
(3) For each stream identified in paragraph (e)(1) of this section that has an average VOHAP concentration equal to or greater than 500 ppmw at the point

- of

- delivery, the average volumetri c flow rate and the density of the off

- site material stream at the point

- of

- delivery shall be determined.
(4) The required HAP mass removal rate (RMR) shall be calculated by using the average VOHAP concentration, average volumetric flow rate, and density d etermined in paragraph (e)(3) of this section for each stream and the following equation:

Where:
RMR = Required HAP mass removal rate, kg/hr.
y = Individual stream “y” that has a VOHAP concentration equal to or greater than 500 ppmw at the point

- of

- deliv ery as determined in §63.694(b).
n = Total number of “y” streams treated by process.

V y = Average volumetric flow rate of stream “y” at the point

- of

- delivery, m 3 /hr.

k y = Density of stream “y”, kg/m 3

.
C ̅ y = Average VOHAP concentration of stream “y” at the point

- of

- delivery as determined in §63.694(b)(2), ppmw.

(f) Determination of actual HAP mass removal rate (MR).

(1) The actual HAP mass removal rate (MR) shall be determined based on results for a minimum of three consecutive runs. The sampling time for ea ch run shall be at least 1 hour.(2) The HAP mass flow entering the process (E b ) and the HAP mass flow exiting the process (E
a )

shall be determined using the test methods and procedures specified in paragraphs (g)(2) through (g)(4) of this section.

(3) The actual mass removal rate shall be calculated using the HAP mass flow rates determined in paragraph (f)(2) of this section and the following equation:

MR = E b −E
a
where:
MR = Actual HAP mass removal rate, kg/hr.

E b = HAP mass flow entering process as determ ined in paragraph (f)(2) of this section, kg/hr.

E
a = HAP mass flow exiting process as determined in paragraph (f)(2) of this section, kg/hr.
(g) Determination of treatment process HAP reduction efficiency (R).
(1) The HAP reduction efficiency (R) for a tr eatment process shall be determined based on results for a minimum of three consecutive runs.
(2) Each individual stream containing HAP that enters the treatment process shall be identified. Each individual stream containing HAP that exits the treatment pr ocess shall be identified. The owner or operator shall prepare a sampling plan for measuring the identified streams that accurately reflects the retention time of the material in the process.

(3) For each run, information shall be determined for each strea m identified in paragraph (g)(2) of this section as specified in paragraphs (g)(3)(i) through (g)(3)(iii) of this section.
(i) The mass quantity shall be determined for each stream identified in paragraph (g)(2) of this section as entering the process (Q b ). The mass quantity shall be determined for each stream identified in paragraph (g)(2) of this section as exiting the process (Q
a ).
(ii) The average VOHAP concentration at the point

- of

- delivery shall be determined for each stream entering the process (C b ) (as identified in paragraph (g)(2) of this section) using the test methods and procedures specified in paragraph (b) of this section.
(iii) The average VOHAP concentration at the point

- of

- treatment shall be determined for each stream exiting the process ( C
a ) (as identified in paragraph (g)(2) of this section) using the test methods and procedures specified in paragraph (c) of this section.
(4) The HAP mass flow entering the process (E b ) and the HAP mass flow exiting the process (E
a ) shall be calculated usi ng the results determined in paragraph (g)(3) of this section and the following equations:Where:

E b = HAP mass flow entering process, kg/hr.

E
a = HAP mass flow exiting process, kg/hr.

m = Total number of runs (at least 3)
j = Individual run “j”

Q bj = Ma ss quantity of material entering process during run “j”, kg/hr.

Q aj = Average mass quantity of material exiting process during run “j”, kg/hr.

C aj = Average VOHAP concentration of material exiting process during run “j” as determined in §63.694(c), ppmw.

C bj = Average VOHAP concentration of material entering process during run “j” as determined in §63.694(b)(2), ppmw.
(5) The HAP reduction efficiency (R) shall be calculated using the HAP mass flow rates determined in paragraph (g)(4) of this section and the following equation:

Where:
R = HAP reduction efficiency, percent.

E b = HAP mass flow entering process as determined in paragraph (g)(4) of this section, kg/hr.

E
a = HAP mass flow exiting process as determined in accordance with the requirements of paragraph (g)(4) of this section, kg/hr.
(h) Determination of HAP biodegradation efficiency (R bio ).
(1) The fraction of HAP biodegraded (F bio ) shall be determined using o ne of the procedures specified in appendix C of this part 63.(2) The HAP biodegradation efficiency (R bio ) shall be calculated by using the following equation:

R bio −F bio ×100

where:

R bio = HAP biodegradation efficiency, percent.

F bio = Fraction of HAP biodegraded as determined in paragraph (h)(1) of this section.

(i) Determination of actual HAP mass removal rate (MR bio ).

(1) The actual HAP mass removal rate (MR bio ) shall be determined based on results for a minimum of three consecutiv e runs. The sampling time for each run shall be at least 1 hour.
(2) The HAP mass flow entering the process (E b ) shall be determined using the test methods and procedures specified in paragraphs (g)(2) through (g)(4) of this section.

(3) The fraction of HA P biodegraded (F bio ) shall be determined using the procedure specified in 40 CFR part 63, appendix C of this part.
(4) The actual mass removal rate shall be calculated by using the HAP mass flow rates and fraction of HAP biodegraded determined in paragraph s (i)(2) and (i)(3), respectively, of this section and the following equation:

MR bio =Eb×F bio

Where:

MR bio = Actual HAP mass removal rate, kg/hr.

E b = HAP mass flow entering process, kg/hr.

F bio = Fraction of HAP biodegraded.
(j) Determination of maximum HA P vapor pressure for off

- site material in a tank. (1) The maximum HAP vapor pressure of the off

- site material composition managed in a tank shall be determined using either direct measurement as specified in paragraph (j)(2) of this section or by knowledge of the off

- site material as specified by paragraph (j)(3) of this section.
(2) Direct measurement to determine the maximum HAP vapor pressure of an off

- site material.
(i) Sampling. A sufficient number of samples shall be collected to be representative o f the off

site material contained in the tank. All samples shall be collected and handled in accordance with written procedures prepared by the owner or operator and documented in a site sampling plan. This plan shall describe the procedure by which repres entative samples of the off

- site material iscollected such that a minimum loss of organics occurs throughout the sample collection and

handling process and by which sample integrity is maintained. A copy of the written sampling plan shall be maintained on

- site in the plant site operating records. An example of an acceptable sampling plan includes a plan incorporating sample collection and handling procedures in accordance with the requirements specified in “Test Methods for Evaluating Solid Waste, Physical /Chemical Methods,” EPA Publication No. SW

- 846 or Method 25D in 40 CFR part 60, appendix A.
(ii) Analysis. Any one of the following methods may be used to analyze the samples and compute the maximum HAP vapor pressure of the off

- site material:

(A) Method 25E in 40 CFR part 60 appendix A;
(B) Methods described in American Petroleum Institute Bulletin 2517, “Evaporation Loss from External Floating Roof Tanks,”;

(C) Methods obtained from standard reference texts;

(D) ASTM Method 2879

- 83; or
(E) Any other method approved by the Administrator.

(3) Use of knowledge to determine the maximum HAP vapor pressure of the off

- site material. Documentation shall be prepared and recorded that presents the information used as the basis for the owner's or operator's kn owledge that the maximum HAP vapor pressure of the off

- site material is less than the maximum vapor pressure limit listed in Table 3
, or Table 4 or Table 5 of this subpart for the applicable tank design capacity category. Examples of information that may be used include: the off

- site material is generated by a process for which at other locations it previously has been determined by direct measurement that t he off

- site material maximum HAP vapor pressure is less than the maximum vapor pressure limit for the appropriate tank design capacity category. In the event that the Administrator and the owner or operator disagree on a determination of the maximum HAP va por pressure for an off

- site material stream using knowledge, then the results from a determination of HAP vapor pressure using direct measurement as specified in paragraph (j)(2 ) of this section shall be used to establish compliance with the applicable re quirements of this subpart. The Administrator may perform or require that the owner or operator perform this determination using direct measurement.
(k) Procedure for determining no detectable organic emissions for the purpose of complying with this subpar t.
(1) The test shall be conducted in accordance with the procedures specified in Method 21 of 40 CFR part 60, appendix A. Each potential leak interface (i.e., a location where organic vapor leakage could occur) on the cover and associated closure devices shall be checked. Potential leak interfaces that are associated with covers and closure devices include, but are not limited to: the interface of the cover and its foundation mounting; the periphery of any opening on the coverand its associated closure de vice; and the sealing seat interface on a spring

- loaded pressure

-

relief valve.
(2) The test shall be performed when the unit contains a material having a total organic concentration representative of the range of concentrations for the materials expected to be managed in the unit. During the test, the cover and closure devices shall be secured in the closed position.
(3) The detection instrument shall meet the performance criteria of Method 21 of 40 CFR part 60, appendix A, except the instrument response f actor criteria in section 3.1.2(a) 8.1.1 of Method 21 shall be for the weighted average composition of the organic constituents in the material placed in the unit at the time of monitoring , not for each individual organic constituent.

(4) The detection instrument shall be calibrated before use on each day of its use by the procedures specified in Method 21 of 40 CFR part 60, appendix A.
(5) Calibration gases shall be as follows:
(i) Zero air (less than 10 ppmv hydrocarbon in air); and

(ii) A mixture of methane or n

- hexane in air at a concentration of approximately, but less than, 10,000 ppmv.
(6) An owner or operator may choose to adjust or not adjust the detection instrument readings to account for the background organic concentration level. If an owner or operator chooses to adjust the instrument readings for the background level, the background level value must be determined according to the procedures in Method 21 of 40 CFR part 60, appendix A.
(7) Each potential leak interface shall be checked by tra versing the instrument probe around the potential leak interface as close to the interface as possible, as described in Method 21. In the case when the configuration of the cover or closure device prevents a complete traverse of the interface, all accessib le portions of the interface shall be sampled. In the case when the configuration of the closure device prevents any sampling at the interface and the device is equipped with an enclosed extension or horn (e.g., some pressure relief devices), the instrumen t probe inlet shall be placed at approximately the center of the exhaust area to the atmosphere.
(8) An owner or operator must determine if a potential leak interface operates with no detectable emissions using the applicable procedure specified in paragra ph (k)(8)(i) or (k)(8)(ii) of this section.
(i) If an owner or operator chooses not to adjust the detection instrument readings for the background organic concentration level, then the maximum organic concentration value measured by the detection instrumen t is compared directly to the applicable value for the potential leak interface as specified in paragraph (k)(9) of this section.(ii) If an owner or operator chooses to adjust the detection instrument readings for the

background organic concentration leve l, the value of the arithmetic difference between the maximum organic concentration value measured by the instrument and the background organic concentration value as determined in paragraph (k)(6) of this section is compared with the applicable value for the potential leak interface as specified in paragraph (k)(9) of this section.
(9) A potential leak interface is determined to operate with no detectable emissions using the applicable criteria specified in paragraphs (k)(9)(i) and (k)(9)(ii) of this secti on.
(i) For a potential leak interface other than a seal around a shaft that passes through a cover opening, the potential leak interface is determined to operate with no detectable organic emissions if the organic concentration value determined in paragra ph (k)(8) is less than 500 ppmv.
(ii) For a seal around a shaft that passes through a cover opening, the potential leak interface is determined to operate with no detectable organic emissions if the organic concentration value determined in paragraph (k)(8 ) is less than 10 ,000 ppmv.
(l) Control device performance test procedures. Performance tests shall be conducted under such conditions as the Administrator specifies to the owner or operator based on representative performance of the affected source for th e period being tested. Representative conditions exclude periods of startup and shutdown unless specified by the Administrator or an applicable subpart. The owner or operator may not conduct performance tests during periods of malfunction. The owner or ope rator must record the process information that is necessary to document operating conditions during the test and include in such record an explanation to support that such conditions represent normal operation. Upon request, the owner or operator shall mak e available to the Administrator such records as may be necessary to determine the conditions of performance tests.
(1) Method 1 or 1A of 40 CFR part 60, appendix A, as appropriate, shall be used for selection of the sampling sites at the inlet and outlet of the control device.
(i) To determine compliance with a control device percent reduction requirement, sampling sites shall be located at the inlet of the control device as specified in paragraphs (l)(1)(i)(A) and (l)(1)(i)(B) of this section, and at the outlet of the control device.
(A) The control device inlet sampling site shall be located after the final product recovery device.
(B) If a vent stream is introduced with the combustion air or as an auxiliary fuel into a boiler or process heater, the lo cation of the inlet sampling sites shall be selected to ensure that the measurement of total HAP concentration or TOC concentration, as applicable, includes all vent streams and primary and secondary fuels introduced into the boiler or process heater.

(ii ) To determine compliance with an enclosed combustion device concentration limit, the sampling site shall be located at the outlet of the device.(2) The gas volumetric flow rate shall be determined using Method 2, 2A, 2C, or 2D , 2F, or 2G

of 40 CFR part 60, appendix A, as appropriate.
(3) To determine compliance with the control device percent reduction requirement, the owner or operator shall use Method 18 of 40 CFR part 60, appendix A of this chapter to measure the HAP in Table 1 of thi s subpart or Method 25A of 40 CFR 60, appendix A of this chapter to measure TOC. Method 18 may be used to measure methane and ethane
, and the measured concentration may be subtracted from the Method 25A measurement. ; a A lternatively, any other method or da ta that has been validated according to the applicable procedures in Method 301 in 40 CFR part 63, appendix A of this part may be used. The following procedures shall be used to calculate percent reduction efficiency:

(i) A minimum of three sample runs mu st be performed. The minimum sampling time for each run shall be 1 hour

. For Method 18, in whi ch either an integrated sample or a minimum of four grab samples shall be taken. If grab sampling is used, then the samples shall be taken at approximately equal intervals in time such as 15 minute intervals during the run.

(ii) The mass rate of either TOC ( minus methane and ethane) or total HAP (E i and E
o ,respectively) shall be computed.
(A) The following equations shall be used:

Where:

C ij , C oj = Concentration of sample component j of the gas stream at the inlet and outlet of the control device, respe ctively, dry basis, parts per million by volume.

E i , E
o = Mass rate of TOC (minus methane and ethane) or total HAP at the inlet and outlet of the control device, respectively, dry basis, kilogram per hour.

M ij , M oj = Molecular weight of sample component j of the gas stream at the inlet and outlet of the control device, respectively, gram/gram

- mole.

Q i , Q
o = Flow rate of gas stream at the inlet and outlet of the control device, respectively, dry standard cubic meter per minute.

K 2 = Constant, 2.494×10 −6 (parts per million) −1 (gram

- mole per standard cubic meter) (kilogram/gram) (minute/hour), where standard temperature (gram

- mole per standard cubic meter) is 20 °C.(B) When the TOC mass rate is calculated, the averag e concentration reading all organic

compounds (minus methane and ethane) measured by Method 18 25A of 40 CFR part 60, appendix A shall be summed used in using the equation in paragraph (l)(3)(ii)(A) of this section.
(C) When the total HAP mass rate is calculated, only the HAP constituents shall be summed using the equation in paragraph (l)(3)(ii)(A) of this section.
(iii) The percent reduction in TOC (minus methane and ethane) or total HAP shall be calculated as foll ows:

where:

R cd =Control efficiency of control device, percent.

E i =Mass rate of TOC (minus methane and ethane) or total HAP at the inlet to the control device as calculated under paragraph (l)(3)(ii) of this section, kilograms TOC per hour or kilograms HAP per hour.

E
o =Mass rate of TOC (minus methane and ethane) or total HAP at the outlet of the control device, as calculated under paragraph (l)(3)(ii) of this section, kilograms TOC per hour or kilograms HAP per hour.
(iv) If the vent stream entering a boiler or process heater is introduced with the combustion air or as a secondary fuel, the weight

- percent reduction of total HAP or TOC (minus methane and ethane) across the device shall be determined by comparing the TOC (minus methane and ethane) or tota l HAP in all combusted vent streams and primary and secondary fuels with the TOC (minus methane and ethane) or total HAP exiting the device, respectively.
(4) To determine compliance with the enclosed combustion device total HAP concentration limit of thi s subpart, the owner or operator shall use Method 18 of 40 CFR part 60, appendix A to

measure the total H AP in Table 1 of this subpart or Method 25A of 40 CFR part 60, a ppendix A to measure TOC. Method 18 may be used to measure methane and ethane and the m easured concentration may be subtracted from the Method 25A measurement. either TOC (minus methane and ethane) or total HAP. Alternatively, any other method or data that has been validated according to Method 301 in appendix A of this part, may be used. The following procedures shall be used to calculate parts per million by volume concentration, corrected to 3 percent oxygen:
(i) A minimum of three sample runs must be performed. The minimum sampling time for each run shall be 1 hour . For Method 18, in which either an integrated sample or a minimum of four grab samples shall be taken. If grab sampling is used, then the samples shall be taken at approximately equal intervals in time, such as 15 minute intervals during the run.(ii) The TOC concentration or total HAP concentration shall be calculated according to

paragraph (m)(4)(ii)(A) or (m)(4)(ii)(B) of this section.

(A) The TOC concentration (C TOC ) is the sum of the average concentration readings of the individual components and shall be computed for each run using the following equation: provided by Method 25 A of 40 CFR part 60, appendix A, minus the concentration of methane and ethane.

where:

C TOC =Concentration of total organic compounds minus methane and ethane, dry basis, parts per million by volume.

C ji =Concentration of sample components j of sample i, dry basis, parts per million by volume.
n=Number of components in the sample.
x=Number of samples in the sample run.

(B) The total HAP concentration (C HAP ) shall be computed according to the equation in paragraph (l)(4)(ii)(A) of this section except that only HAP constituents shall be summed. t o the following equation:

C HAP = ∑ ∑ C ji n j = 1
x x

i = 1

where:

C HAP = Total concentration of HAP compounds listed in Table 1 of this subpart, dry basis, parts per million by volume.

C ij = Concentration of sample components j of sample i, dry basis, parts per million by volume.
n = Number of components in the sample.
x = Number of samples in the sample run.(iii) The measured TOC concentration or total HAP concentration shall be corrected to 3 percent

oxygen as follows:

(A) The emission rate correction factor or excess air, integrated sampling and analysis procedures of Method 3B of 40 CFR part 60, appendix A shall be used to determine the oxygen concentration (%O 2dry ). Alternatively, the owner or operator may use Method 3A of 40 CFR part 60, appendix A to determine the oxygen concentration. The samples shall be collected during the same time that the samples are collected for determining TOC concentration or total HAP concentration.
(B) The concentration corrected to 3 percent oxygen (C
c ) sha ll be computed using the following equation:

where:

C
c =TOC concentration or total HAP concentration corrected to 3 percent oxygen, dry basis, parts per million by volume.

C
m =Measured TOC concentration or total HAP concentration, dry basis, parts per mi llion by volume.

%O 2dry =Concentration of oxygen, dry basis, percent by volume.
(m) Determination of process vent stream flow rate and total HAP concentration.
(1) Method 1 or 1A of 40 CFR part 60, appendix A, as appropriate, must be used for selection of the sampling site.

(2) No traverse site selection method is needed for vents smaller than 0.10 meter in diameter. For vents smaller than 0.10 meter in diameter, sample at the center of the vent.
(3) Process vent stream gas volumetric flow rate must be dete rmined using Method 2, 2A, 2C, or 2D , 2F, or 2G of 40 CFR part 60, appendix A, as appropriate.
(4) Process vent stream total HAP concentration must be measured using the following procedures:
(i) Method 18 of 40 CFR part 60, appendix A, must be used to measure the total HAP concentration. Alternatively, any other method or data that has been validated according to the protocol in Method 301 of appendix A of this part may be used.(ii) Where Method 18 of 40 CFR part 60, appendix A, is used, the following procedures must be

used to calculate parts per million by volume concentration:
(A) The minimum sampling time for each run must be 1 hour in which either an integrated sample or four grab samples must be taken. If grab sampling is used, then the samples mu st be taken at approximately equal intervals in time, such as 15 minute intervals during the run.

(B) The total HAP concentration (C HAP ) must be computed according to the following equation:

Where:

C HAP = Total concentration of HAP compounds listed in Table 1 of this subpart, dry basis, parts per million by volume.

C ji = Concentration of sample component j of the sample i, dry basis, parts per million by volume.

n = Number of components in the sample.

x = Number of samples in the sample run. 

## §63.6 95 Inspection and monitoring requirements.

(a) The owner or operator must install, calibrate, maintain, and operate all monitoring system components according to §63.8 of this part
, § § 63.684(e), 63.693(d)(3), (e)(3), (f)(3), (g)(3), (h)(3) of this subpart
, and paragraph ( 5 ) of this section and perform the This section specifi es the inspection and monitoring procedures required to perform the following specified in paragraphs (a)(1) through (4) of this section. :
(1) To inspect tank fixed roofs and floating roofs for compliance with the Tank Level 2 controls standards specified in §63.685 of this subpart, the inspection procedures are specified in paragraph (b) of this section.
(2) To inspect and monitor closed

- vent systems for compliance with the st andards specified in §63.693 of this subpart, the inspection and monitoring procedures are specified in paragraph (c) of this section.
(3) To inspect and monitor transfer system covers for compliance with the standards specified in §63.689(c)(1) of this su bpart, the inspection and monitoring procedures are specified in paragraph (d) of this section.(4) To monitor and record off

- site material treatment processes for compliance with the standards specified in 63.684(e), the monitoring procedures are specifie d in paragraph (e) of this section.

( 5)(i ) Except for periods of monitoring system malfunctions, repairs associated with monitoring system malfunctions and required monitoring system quality assurance or quality control activities (including, as applicable , calibration checks and required zero and span adjustments), the owner or operator must operate the continuous monitoring system at all times the affected source is operating. A monitoring system malfunction is any sudden, infrequent, not reasonably preve ntable failure of the monitoring system to provide data. Monitoring system failures that are caused in part by poor maintenance or careless operation are not malfunctions. The owner or operator is required to complete monitoring system repairs in response to monitoring system malfunctions and to return them monitoring system to operation as expeditiously as practicable.

(ii ) The owner or operator may not use data recorded during monitoring system malfunctions, repairs associated with monitoring system malfu nctions, or required monitoring system quality assurance or control activities in calculations used to report emissions or operating levels. The owner or operator must use all the data collected during all other required data collection periods in assessin g the operation of the control device and associated control system. The owner or operator must report any periods for which the monitoring system failed to collect required data.
(b) Tank Level 2 fixed roof and floating roof inspection requirements.

(1) O wners and operators that use a tank equipped with an internal floating roof in accordance with the provisions of §63.685(e) of this subpart shall meet the following inspection requirements:
(i) The floating roof and its closure devices shall be visually in spected by the owner or operator to check for defects that could result in air emissions. Defects include, but are not limited to, the internal floating roof is not floating on the surface of the liquid inside the tank; liquid has accumulated on top of the internal floating roof; any portion of the roof seals have detached from the roof rim; holes, tears, or other openings are visible in the seal fabric; the gaskets no longer close off the waste surfaces from the atmosphere; or the slotted membrane has more than 10 percent open area.
(ii) The owner or operator shall inspect the internal floating roof components as follows except as provided for in paragraph (b)(1)(iii) of this section:
(A) Visually inspect the internal floating roof components through openin gs on the fixed

- roof (e.g., manholes and roof hatches) at least once every calendar year after initial fill, and
(B) Visually inspect the internal floating roof, primary seal, secondary seal (if one is in service), gaskets, slotted membranes, and sleeve se als (if any) each time the tank is emptied and degassed and at least every 10 years. Prior to each inspection, the owner or operator shall notify the Administrator in accordance with the reporting requirements specified in §63.697 of this subpart.(iii) As an alternative to performing the inspections specified in paragraph (b)(1)(ii) of this

section for an internal floating roof equipped with two continuous seals mounted one above the other, the owner or operator may visually inspect the internal floating r oof, primary and secondary seals, gaskets, slotted membranes, and sleeve seals (if any) each time the tank is emptied and degassed and at least every 5 years. Prior to each inspection, the owner or operator shall notify the Administrator in accordance with the reporting requirements specified in §63.697 of this subpart.
(iv) In the event that a defect is detected, the owner or operator shall repair the defect in accordance with the requirements of paragraph (b)(4) of this section.
(v) The owner or operator shall maintain a record of the inspection in accordance with the requirements specified in §63.696 of this subpart.
(2) Owners and operators that use a tank equipped with an external floating roof in accordance with the provisions of §63.685(f) of this sub part shall meet the following requirements:
(i) The owner or operator shall measure the external floating roof seal gaps in accordance with the following requirements:
(A) The owner or operator shall perform measurements of gaps between the tank wall and t he primary seal within 60 days after initial operation of the tank following installation of the floating roof and, thereafter, at least once every 5 years. Prior to each inspection, the owner or operator shall notify the Administrator in accordance with t he reporting requirements specified in §63.697 of this subpart.
(B) The owner or operator shall perform measurements of gaps between the tank wall and the secondary seal within 60 days after initial operation of the separator following installation of the floating roof and, thereafter, at least once every year. Prior to each inspection, the owner or operator shall notify the Administrator in accordance with the reporting requirements specified in §63.697 of this subpart.

(C) If a tank ceases to hold off

- sit e material for a period of 1 year or more, subsequent introduction of off

- site material into the tank shall be considered an initial operation for the purposes of paragraphs (b)(2)(i)(A) and (b)(2)(i)(B) of this section.

(D) The owner shall determine the t otal surface area of gaps in the primary seal and in the secondary seal individually using the following procedure.

( 1 ) The seal gap measurements shall be performed at one or more floating roof levels when the roof is floating off the roof supports.

( 2 ) Se al gaps, if any, shall be measured around the entire perimeter of the floating roof in each place where a 0.32

- centimeter (cm) ( 1 ⁄ 8 - inch) diameter uniform probe passes freely (without forcing or binding against the seal) between the seal and the wall of the tank and measure the circumferential distance of each such location.( 3 ) For a seal gap measured under paragraph (b)(2) of this section, the gap surface area shall be

determined by using probes of various widths to measure accurately the actual distance from the tank wall to the seal and multiplying each such width by its respective circumferential distance.

( 4 ) The total gap area shall be calculated by adding the gap surface areas determined for each identified gap location for the primary seal and the secondary seal individually, and then dividing the sum for each seal type by the nominal diameter of the tank. These total gap area s for the primary seal and secondary seal are then compared to the respective standards for the seal type as specified in §63.685(f)(1) of this subpart.
(E) In the event that the seal gap measurements do not conform to the specifications in §63.685(f)(1) o f this subpart, the owner or operator shall repair the defect in accordance with the requirements of paragraph (b)(4) of this section.
(F) The owner or operator shall maintain a record of the inspection in accordance with the requirements specified in §63. 696 of this subpart.
(ii) The owner or operator shall visually inspect the external floating roof in accordance with the following requirements:
(A) The floating roof and its closure devices shall be visually inspected by the owner or operator to check for defects that could result in air emissions. Defects include, but are not limited to: holes, tears, or other openings in the rim seal or seal fabric of the floating roof; a rim seal detached from the floating roof; all or a portion of the floating roof dec k being submerged below the surface of the liquid in the tank; broken, cracked, or otherwise damaged seals or gaskets on closure devices; and broken or missing hatches, access covers, caps, or other closure devices.
(B) The owner or operator shall perform the inspections following installation of the external floating roof and, thereafter, at least once every year.
(C) In the event that a defect is detected, the owner or operator shall repair the defect in accordance with the requirements of paragraph (b)(4 ) of this section.
(D) The owner or operator shall maintain a record of the inspection in accordance with the requirements specified in §63.696(d) of this subpart.
(3) Owners and operators that use a tank equipped with a fixed roof in accordance with the p rovisions of §63.685(g) of this subpart shall meet the following requirements:
(i) The fixed roof and its closure devices shall be visually inspected by the owner or operator to check for defects that could result in air emissions. Defects include, but are not limited to, visible cracks, holes, or gaps in the roof sections or between the roof and the separator wall; broken, cracked, or otherwise damaged seals or gaskets on closure devices; and broken or missing hatches, access covers, caps, or other closure devices. In the case when a tank is buried partially or entirely underground, inspection is required only for those portions of the cover that extend toor above the ground surface, and those connections that are on such portions of the cover (e.g.,

fill ports, access hatches, gauge wells, etc.) and can be opened to the atmosphere.
(ii) The owner or operator must perform an initial inspection following installation of the fixed roof. Thereafter, the owner or operator must perform the inspections at least o nce every calendar year except as provided for in paragraph (f) of this section.
(iii) In the event that a defect is detected, the owner or operator shall repair the defect in accordance with the requirements of paragraph (b)(4) of this section.

(iv) The o wner or operator shall maintain a record of the inspection in accordance with the requirements specified in §63.696(e) of this subpart.
(4) The owner or operator shall repair each defect detected during an inspection performed in accordance with the requir ements of paragraph (b)(1), (b)(2), or (b)(3) of this section in the following manner:
(i) The owner or operator shall within 45 calendar days of detecting the defect either repair the defect or empty the tank and remove it from service. If within this 45

- day period the defect cannot be repaired or the tank cannot be removed from service without disrupting operations at the plant site, the owner or operator is allowed two 30

- day extensions. In cases when an owner or operator elects to use a 30

- day extension , the owner or operator shall prepare and maintain documentation describing the defect, explaining why alternative storage capacity is not available, and specify a schedule of actions that will ensure that the control equipment will be repaired or the tank emptied as soon as possible.
(ii) When a defect is detected during an inspection of a tank that has been emptied and degassed, the owner or operator shall repair the defect before refilling the tank.
(c) Owners and operators that use a closed

- vent system in accordance with the provisions of §63.693 of this subpart shall meet the following inspection and monitoring requirements:

(1) Each closed

- vent system that is used to comply with §63.693(c)(1)(i) of this subpart shall be inspected and monitored in accor dance with the following requirements:
(i) At initial startup, the owner or operator shall monitor the closed

- vent system components and connections using the procedures specified in §63.694(k) of this subpart to demonstrate that the closed

- vent system operates with no detectable organic emissions.
(ii) After initial startup, the owner or operator shall inspect and monitor the closed

- vent system as follows:

(A) Closed

- vent system joints, seams, or other connections that are permanently or semi

permanentl y sealed (e.g., a welded joint between two sections of hard piping or a bolted and gasketed ducting flange) shall be visually inspected at least once per year to check for defects that could result in air emissions. The owner or operator shall monitor a co mponent orconnection using the procedures specified in §63.694(k) of this subpart to demonstrate that it

operates with no detectable organic emissions following any time the component is repaired or replaced (e.g., a section of damaged hard piping is repl aced with new hard piping) or the connection is unsealed (e.g., a flange is unbolted).

(B) Closed

- vent system components or connections other than those specified in paragraph (c)(1)(ii)(A) of this section, shall be monitored at least once per year using t he procedures specified in §63.694(k) of this subpart to demonstrate that components or connections operate with no detectable organic emissions.
(C) The continuous monitoring system required by §63.693(b)(4)(i) shall monitor and record either an instantan eous data value at least once every 15 minutes or an average value for intervals of 15 minutes or less.
(D) The owner or operator shall visually inspect the seal or closure mechanism required by §63.693(c)(2)(ii) at least once every month to verify that th e bypass mechanism is maintained in the closed position.
(iii) In the event that a defect or leak is detected, the owner or operator shall repair the defect or leak in accordance with the requirements of paragraph (c)(3) of this section.

(iv) The owner or operator shall maintain a record of the inspection and monitoring in accordance with the requirements specified in §63.696 of this subpart.

(2) Each closed

- vent system that is used to comply with §63.693(c)(1)(ii) of this subpart shall be inspected and mo nitored in accordance with the following requirements:

(i) The closed

- vent system shall be visually inspected by the owner or operator to check for defects that could result in air emissions. Defects include, but are not limited to, visible cracks, holes, or gaps in ductwork or piping; loose connections; or broken or missing caps or other closure devices.
(ii) The owner or operator must perform an initial inspection following installation of the closed

vent system. Thereafter, the owner or operator must per form the inspections at least once every calendar year except as provided for in paragraph (f) of this section.
(iii) In the event that a defect is detected, the owner or operator shall repair the defect in accordance with the requirements of paragraph (c) (3) of this section.
(iv) The owner or operator shall maintain a record of the inspection in accordance with the requirements specified in §63.696 of this subpart.
(3) The owner or operator shall repair all detected defects as follows:(i) The owner or ope rator shall make first efforts at repair of the defect no later than 5 calendar

days after detection and repair shall be completed as soon as possible but no later than 45 calendar days after detection.
(ii) Repair of a defect may be delayed beyond 45 cale ndar days if either of the conditions specified in paragraph (c)(3)(ii)(A) or (c)(3)(ii)(B) occurs. In this case, the owner or operator must repair the defect the next time the process or unit that vents to the closed

- vent system is shutdown. Repair of the defect must be completed before the process or unit resumes operation.
(A) Completion of the repair is technically infeasible without the shutdown of the process or unit that vents to the closed

- vent system.
(B) The owner or operator determines that the a ir emissions resulting from the repair of the defect within the specified period would be greater than the fugitive emissions likely to result by delaying the repair until the next time the process or unit that vents to the closed

- vent system is shutdown.
(iii) The owner or operator shall maintain a record of the defect repair in accordance with the requirements specified in §63.696 of this subpart.
(d) Owners and operators that use a transfer system equipped with a cover in accordance with the provisions o f §63.689(c)(1) of this subpart shall meet the following inspection requirements:
(1) The cover and its closure devices shall be visually inspected by the owner or operator to check for defects that could result in air emissions. Defects include, but are n ot limited to, visible cracks, holes, or gaps in the cover sections or between the cover and its mounting; broken, cracked, or otherwise damaged seals or gaskets on closure devices; and broken or missing hatches, access covers, caps, or other closure devic es. In the case when a transfer system is buried partially or entirely underground, inspection is required only for those portions of the cover that extend to or above the ground surface, and those connections that are on such portions of the cover (e.g., access hatches, etc.) and can be opened to the atmosphere.
(2) The owner or operator must perform an initial inspection following installation of the cover. Thereafter, the owner or operator must perform the inspections at least once every calendar year

ex cept as provided for in paragraph (f) of this section.
(3) In the event that a defect is detected, the owner or operator shall repair the defect in accordance with the requirements of paragraph (d)(5) of this section.
(4) The owner or operator shall mainta in a record of the inspection in accordance with the requirements specified in §63.696 of this subpart.
(5) The owner or operator shall repair all detected defects as follows:(i) The owner or operator shall make first efforts at repair of the defect no la ter than 5 calendar

days after detection and repair shall be completed as soon as possible but no later than 45 calendar days after detection except as provided in paragraph (d)(5)(ii) of this section.
(ii) Repair of a defect may be delayed beyond 45 calen dar days if the owner or operator determines that repair of the defect requires emptying or temporary removal from service of the transfer system and no alternative transfer system is available at the site to accept the material normally handled by the sys tem. In this case, the owner or operator shall repair the defect the next time the process or unit that is generating the material handled by the transfer system stops operation. Repair of the defect must be completed before the process or unit resumes ope ration.
(iii) The owner or operator shall maintain a record of the defect repair in accordance with the requirements specified in §63.696 of this subpart.

(e) Control device monitoring requirements. For each control device required under §63.693 of this subpart to be monitored in accordance with the provisions of this paragraph (e), the owner or operator must ensure that each control device operates properly by monitoring the control device in accord ance with the requirements specified in paragraphs (e)(1) through (e)(7) of this section.
(1) A continuous parameter monitoring system must be used to measure the operating parameter or parameters specified for the control device in §63.693(d) through §63. 693(g) of this subpart as applicable to the type and design of the control device. The continuous parameter monitoring system must meet the following specifications and requirements:
(i) The continuous parameter monitoring system must measure either an ins tantaneous value at least once every 15 minutes or an average value for intervals of 15 minutes or less and continuously record either:

(A) Each measured data value; or
(B) Each block average value for each 1

- hour period or shorter periods calculated from all measured data values during each period. If values are measured more frequently than once per minute, a single value for each minute may be used to calculate the hourly (or shorter period) block average instead of all measured values.

(ii) The monitori ng system must be installed, calibrated, operated, and maintained in accordance with the manufacturer's specifications or other written procedures that provide reasonable assurance that the monitoring equipment is operating properly.
(2) Using the data rec orded by the monitoring system, the owner or operator must calculate the daily average value for each monitored operating parameter for each operating day. If operation of the control device is continuous, the operating day is a 24

- hour period. If control device operation is not continuous, the operating day is the total number of hours of control device operation per 24

- hour period. Valid data points must be available for 75 percent of the operating hours in an operating day to compute the daily average.( 3) For each monitored operating parameter, the owner or operator must establish a minimum

operating parameter value or a maximum operating parameter value, as appropriate, to define the range of conditions at which the control device must be operated to co ntinuously achieve the applicable performance requirements specified in §63.693(b)(2) of this subpart. Each minimum or maximum operating parameter value must be established in accordance with the requirements in paragraphs (e)(3)(i) and (e)(3)(ii) of this section.
(i) If the owner or operator conducts a performance test to demonstrate control device performance, then the minimum or maximum operating parameter value must be established based on values measured during the performance test and supplemented, as necessary, by the control device design specifications, manufacturer recommendations, or other applicable information.
(ii) If the owner or operator uses a control device design analysis to demonstrate control device performance, then the minimum or maxim um operating parameter value must be established based on the control device design analysis and supplemented, as necessary, by the control device manufacturer recommendations or other applicable information.

(4) A n excursion deviation for a given control d evice is determined to have occurred when the monitoring data or lack of monitoring data result in any one of the criteria specified in paragraphs (e)(4)(i) through (e)(4)(iii) of this section being met. When multiple operating parameters are monitored for the same control device and during the same operating day more than one of these operating parameters meets a n excursion deviation criterion specified in paragraphs (e)(4)(i) through (e)(4)(iii) of this section, then a single excursion deviation is determined to have occurred for the control device for that operating day.

(i) A n excursion deviation occurs when the daily average value of a monitored operating parameter is less than the minimum operating parameter limit (or, if applicable, greater than the maximum operating parameter limit) established for the operating parameter in accordance with the requirements of paragraph (e)(3) of this section.

(ii) A n excursion deviation occurs when the period of control device operation is 4 hours or greater in a n operating day and the monitoring data are insufficient to constitute a valid hour of data for at least 75 percent of the operating hours. Monitoring data are insufficient to constitute a valid hour of data if measured values are unavailable for any of th e 15

- minute periods within the hour.

(iii) A n excursion deviation occurs when the period of control device operation is less than 4 hours in an operating day and more than 1 of the hours during the period does not constitute a valid hour of data due to insu fficient monitoring data. Monitoring data are insufficient to constitute a valid hour of data if measured values are unavailable for any of the 15

- minute periods within the hour.

(5) For each excursion deviation , except when the deviation occurs during peri ods of non

operation of the unit or the process that is vented to the control device (resulting in cessation of HAP emissions to which the monitoring applies) as provided for in paragraph (e)(6) of thissection , the owner or operator shall be deemed to have failed to have applied control in a manner

that achieves the required operating parameter limits. Failure to achieve the required operating parameter limits is a violation of this standard.

(6) An excursion is not a violation of this standard under any one of the conditions specified in paragraphs (e)(6)(i) and (e)(6)(ii) of this section.

(i) An excursion is not a violation nor does it count toward the number of excused excursions allowed under paragraph (e)(6)(ii) of this section when the excursion occ urs during any one of the following periods:
(A) During a period of startup, shutdown, or malfunction when the affected facility is operated during such period in accordance with §63.6(e)(1); or
(B) During periods of non

- operation of the unit or the proces s that is vented to the control device (resulting in cessation of HAP emissions to which the monitoring applies).
(ii) For each control device, one excused excursion is allowed per semiannual period for any reason. The initial semiannual period is the 6

- mo nth reporting period addressed by the first semiannual report submitted by the owner or operator in accordance with §63.697(b)(4) of this subpart.

( 7 ) Nothing in paragraphs (e)(1) through (e)( 6 ) of this section shall be construed to allow or excuse a monitoring parameter excursion caused by any activity that violates other applicable provisions of this subpart.

(f) Alternative inspection and monitoring interval. Following the initial inspection and monitoring of a piece of air pollution control equipment in accordance with the applicable provisions of this section, subsequent inspection and monitoring of the equipment may be performed at intervals longer than 1 year when an owner or operator dete rmines that performing the required inspection or monitoring procedures would expose a worker to dangerous, hazardous, or otherwise unsafe conditions and the owner or operator complies with the requirements specified in paragraphs (f)(1) and (f)(2) of this section.
(1) The owner or operator must prepare and maintain at the plant site written documentation identifying the specific air pollution control equipment designated as “unsafe to inspect and monitor.” The documentation must include for each piece of a ir pollution control equipment designated as such a written explanation of the reasons why the equipment is unsafe to inspect or monitor using the applicable procedures under this section.
(2) The owner or operator must develop and implement a written plan and schedule to inspect and monitor the air pollution control equipment using the applicable procedures specified in this section during times when a worker can safely access the air pollution control equipment. The required inspections and monitoring mus t be performed as frequently as practicable but do notneed to be performed more frequently than the periodic schedule that would be otherwise

applicable to the air pollution control equipment under the provisions of this section. A copy of the written pla n and schedule must be maintained at the plant site. 

## §63.696 Recordkeeping requirements.

(a) The owner or operator subject to this subpart shall comply with the recordkeeping requirements in §63.10 under 40 CFR 63 subpart A

— General Provisions that are applicable to this subpart as specified in Table 2 of this subpart.
(b) The owner or operato r of a control device subject to this subpart shall maintain the records in accordance with the requirements of 40 CFR 63.10 of this part.

(c) [Reserved]
(d) Each owner or operator using an internal floating roof to comply with the tank control requireme nts specified in §63.685(e) of this subpart or using an external floating roof to comply with the tank control requirements specified in §63.685(f) of this subpart shall prepare and maintain the following records:
(1) Documentation describing the floating roof design and the dimensions of the tank.
(2) A record for each inspection required by §63.695(b) of this subpart, as applicable to the tank, that includes the following information: a tank identification number (or other unique identification descript ion as selected by the owner or operator) and the date of inspection.
(3) The owner or operator shall record for each defect detected during inspections required by §63.695(b) of this subpart the following information: the location of the defect, a descri ption of the defect, the date of detection, and corrective action taken to repair the defect. In the event that repair of the defect is delayed in accordance with the provisions of §63.695(b)(4) of this section, the owner or operator shall also record the reason for the delay and the date that completion of repair of the defect is expected.
(4) Owners and operators that use a tank equipped with an external floating roof in accordance with the provisions of §63.685(f) of this subpart shall prepare and maint ain records for each seal gap inspection required by §63.695(b) describing the results of the seal gap measurements. The records shall include the date of that the measurements are performed, the raw data obtained for the measurements, and the calculations of the total gap surface area. In the event that the seal gap measurements do not conform to the specifications in §63.695(b) of this subpart, the records shall include a description of the repairs that were made, the date the repairs were made, and the d ate the separator was emptied, if necessary.
(e) Each owner or operator using a fixed roof to comply with the tank control requirements specified in §63.685(g) of this subpart shall prepare and maintain the following records:(1) A record for each inspec tion required by §63.695(b) of this subpart, as applicable to the tank,

that includes the following information: a tank identification number (or other unique identification description as selected by the owner or operator) and the date of inspection.

(2) The owner or operator shall record for each defect detected during inspections required by §63.695(b) of this subpart the following information: the location of the defect, a description of the defect, the date of detection, and corrective action taken to repair the defect. In the event that repair of the defect is delayed in accordance with the provisions of §63.695(b)(4) of this section, the owner or operator shall also record the reason for the delay and the date that completion of repair of the defect is expected.
(f) Each owner or operator using an enclosure to comply with the tank control requirements specified in §63.685(i) of this subpart shall prepare and maintain records for the most recent set of calculations and measurements performed by the ow ner or operator to verify that the enclosure meets the criteria of a permanent total enclosure as specified in “Procedure T

— Criteria for and Verification of a Permanent or Temporary Total Enclosure” under 40 CFR 52.741, appendix B.
(g) An owner or operato r shall record, on a semiannual basis, the information specified in paragraphs (g)(1) and (g)(2) of this section for those planned routine maintenance operations that would require the control device not to meet the requirements of §63.693(d) through (h) o f this subpart, as applicable.
(1) A description of the planned routine maintenance that is anticipated to be performed for the control device during the next 6 months. This description shall include the type of maintenance necessary, planned frequency of maintenance, and lengths of maintenance periods.
(2) A description of the planned routine maintenance that was performed for the control device during the previous 6 months. This description shall include the type of maintenance performed and the total n umber of hours during these 6 months that the control device did not meet the requirement of §63.693 (d) through (h) of this subpart, as applicable, due to planned routine maintenance.
(h) An owner or operator shall record the malfunction information specified in paragraphs (h)(1) through (h)(3) of this section

. for those unexpected control device system malfunctions that would require the control device not to meet the requirements of §63.693 (d) through (h) of this subpart, as applicable.

(1) In the event that an affected unit fails to meet an applicable standard, record the number of failures. For each failure record the date, time and duration of the failure.
(2) For each failure to meet an applicable standard, record and retain a list of the affec ted sources or equipment, an estimate of the volume of each regulated pollutant emitted over any emission limit and a description of the method used to estimate the emissions.(3) Record actions taken to minimize emissions in accordance with § 63.683(e) of this subpart

and any corrective actions taken to return the affected unit to its normal or usual manner of operation.
(1) The occurrence and duration of each malfunction of the control device system.
(2) The duration of each period during a malfunctio n when gases, vapors, or fumes are vented from the waste management unit through the closed

- vent system to the control device while the control device is not properly functioning.
(3) Actions taken during periods of malfunction to restore a malfunctioning control device to its normal or usual manner of operation.

( i ) F or pressure relief devices in off

- site material service, keep records of the inform ation specified in paragraphs ( i )(1) through (5) of this section, as applicable.
(1) A list of identification numbers for pressure relief devices that the owner or operator elects to route emissions t hrough a closed

- vent system to a control device, process or drain system unde r the provisions in § 63. 691(c) (4) of this subpart

. (2) A list of identification numbers for pressure relief devices that do not consist of or include a rupture disk, subject to the provisions in § 63.691(c) (2 ) (i) of this subpart

. (3) A list of identification numbers for pressure relief devices equipped with rupture disks, subject to the provisions in § 63.691(c) ( 2 ) (ii) of this subpart

. (4) The dates and results of the Method 21 of 40 CFR part 60, appendix A
, monitoring following

a pressure release for each pressure relief device subject t o the provisions in § 63.691(c) (2) (i) of this subpart . The results of each monitoring event shall include:

(i) The measured background level.
(ii) The maximum instrument reading measured at each pressure relief device

. (5) For pressure relief devices in off

- site material service subject to § 63.691(c)( 3 ) of this subpart
, keep records of each pressure release to the atmosphere, including the following information:

(i) The source, nature, and cause of the pressure release.
(ii) The date, time, and duration of the pressure release.

(iii) An estimate of the quantity of HAP listed in Table 1 of this subpart emitted during the pressure release and the calculations used for determining this quantity.

(iv) The actions taken to prevent this pressure release.(v) The measures adopted to prevent future such pressure releases.

(j) (1) For pressure tank closure devices
, as specified in §63.685(h)(2) of this subpart
, keep records of each release to the atmosphere, including the information specifi ed in paragraphs (j)(3) though ( 7 ) of this section.

( 2 ) For each closed vent system that includes bypass devices that could divert a stream away from the control device and into the atmosphere, as specified in §63.693(c)(2) of this subpart
, and each open

- ended valve or line in an emergency shutdown system which is designed to open automatically in the event of a process upse t, as specified in 40 CFR 63.167(d) or 40 CFR 61.242

- 6(d), keep records of each releas e to the atmosphere, including the information specified in paragraphs (j)(3) though (9) of this section.

( 3 ) The source, nature, and cause of the release.

( 4 ) The date, time, and duration of the release.

( 5 ) An estimate of the quantity of HAP listed in Table 1 of this subpart emitted during the release and the calculations used for determining this quantity.

( 6 ) The actions taken to prevent this release.

( 7 ) The measures adopted to prevent future such release.

( 8 ) Hourly records of whether the bypass flow indicator specified under § 63.693(c)( 2 ) of this subpart was operating and whether a diversion was detected at any time during the hour , as well as records of the times of all periods when the vent stream is diverted from the control device or the flow indicator is not operating

. ( 9 ) Where a seal mechanism is used to comply with § 63.693(c)(2) of this subpart, hourly records of flow are not required. In such cases, the owner or operator shall record that the monthly visual inspection of the seals or closure mechanism has been done, and shall record the duration of all periods when the seal mechanism is broken, the bypass line valve position has changed, or the key for a lock

- and

- key type lock has been checked out, and records of any car

- seal that has broken. 

## §63.697 Reporting requirements.

(a) Each owner or operator of an affected source subject to this subpart must comply with the notification requirements specified in paragraph (a)(1) of this section and the reporting requirements specified in paragraph (a)(2) and (a)(3) of this section.
(1) The owner or operator of an affected source must submit notices to the Administrator in accordance with the applicable notification requirements in 40 CFR 63.9 as specified in Table 2 of this subpart. For the purpose of this subpart, an owner or operat or subject to the initialnotification requirements under 40 CFR 63.9(b)(2) must submit the required notification on or

before October 19, 1999.
(i) For pressure relief devices in off

- site material service subject to the requirements of §63.691(c) of this subpart , the owner or operator must submit the information listed in paragraph (a)(1)(ii) of this section in the notification of compliance status required under §63.9(h) of this part within 150 days after the first applicable compliance date for pressure relief device monitoring.

(ii ) For pressure relief devices in off

- site material service, a description of the device or monitoring system to be implemented, including the pressure relief devices and process parameters to be monitored (if applicable), a de scription of the alarms or other methods by which operators will be notified of a pressure release, and a description of how the owner or operator will determine the information to be recorded under § 63.6 96(i) (5) ( ii )

- ( iii ) of this subpart (i.e., the duration of the pressure release and the methodology and calculations for determining the quantity of HAP listed in Table 1 of this subpart emitted during the pressure release )

. (2) The owner or operator of an affected source must submit report s to the Administrator in accordance with the applicable reporting requirements in 40 CFR 63.10 as specified in Table 2 of this subpart.

(3) Electronic reporting. Within 60 days after the date of completing each performance test (as defined in §63.2 of this part ) required by this subpart , the owner or operator must submit the results of the performance test according to the manner specified by either paragraph (a)( 3 )(i) or (ii) of this section.
(i) For data collected using test methods supported by t he EPA ’s Electronic Reporting Tool (ERT) as listed on the EPA’s ERT website (http://www.epa.gov/ttn/chief/ert/index.html) , the owner or operator must submit the results of the performance test to the EPA via the Compliance and Emissions Data Reporting Interface (CEDRI) accessed through the EPA’s Central Data Exchange (CDX) (http://cdx.epa.gov/epa_home.asp)

. Performance test data must be submitted in a file format generated through the use of the EPA’s ERT. Owners or operators who claim that some of the performance test information being submitted is confidential business information (CBI) must submit a complete file generated through the us e of the EPA ’s ERT, includ ing information claimed to be CBI
, on a compact disc, flash drive, or other commonly used electronic storage media to the EPA. The electronic media must be clearly marked as CBI and mailed to U.S. EPA/OAPQS/CORE CBI Office, Attention: WebFIRE Administrator, MD C404

- 02, 4930 Old Page Rd., Durham, NC 27703. The same ERT file with the CBI omitted must be submitted to the EPA via the EPA ’s CDX as described earlier in this paragraph

. (ii) For data collected using test methods that are not supported by the EPA ’s ERT as listed on the EPA’s ERT website , the owner or operator must submit the results of the performance test to the Administrator at the appropriate address listed in 40 CFR 60.4.
(b) The owner or operator of a control device used to meet the requirements of §63.693 of this subpart shall submit the following notifications and reports to the A dministrator:(1) A Notification of Performance Tests specified in §63.7 and §63.9(g) of this part,

(2) Performance test reports specified in §63.10(d)(2) of this part, and

(3) Reports of malfunctions. If a source fails to meet an applicable standard, report such events in the Periodic Report. Report the number of failures to meet an applicable standard. For each instance, report the date, time and duration of each failure. For each failure the report must include a list of the affected sour ces or equipment, an estimate of the volume of each regulated pollutant emitted over any emission limit, and a description of the method used to estimate the emissions

. (3) Startup, shutdown, and malfunction reports specified in §63.10(d)(5) of this part

. (i) If actions taken by an owner or operator during a startup, shutdown, or malfunction of an affected source (including actions taken to correct a malfunction) are not completely consistent with the procedures specified in the source's startup, shutdown, and malfunction plan specified in §63.6(e)(3) of this part, the owner or operator shall state such information in the report. The startup, shutdown, or malfunction report shall consist of a letter, containing the name, title, and signature of the responsible official who is certifying its accuracy, that shall be submitted to the Administrator, and
(ii) Separate startup, shutdown, or malfunction reports are not required if the information is included in the summary report specified in paragraph (b)(4) of this section.
(4) A summary report specified in §63.10(e)(3) of this part shall be submitted on a semiannual basis (i.e., once every 6

- month period). The summary report must include a description of all excursions deviations as defined in §63.695( e) of this subpart that have occurred during the 6

- month reporting period. For each deviation excursion caused when the daily average value of a monitored operating parameter is less than the minimum operating parameter limit (or, if applicable, greater tha n the maximum operating parameter limit), the report must include the daily average values of the monitored parameter, the applicable operating parameter limit, and the date and duration of the period that the deviation exceedance occurred. For each excursion deviation caused by lack of monitoring data, the report must include the date and duration of period when the monitoring data were not collected and the reason why the data were not collected.
(5) For pressure relief devices in off

- site material s ervice subject to § 63.691(c) of this subpart
, Periodic Reports must include the information specified in paragraphs (b)(5)(i) through (b)(5)( i ii) of this section.
(i) For pressure relief devices in off

- site material service subject to § 63.691(c) of this su bpart
, report the results of all monitoring conducted within the reporting period.
(ii) For pressure relief devices in off

- site material service subject to § 63.691(c)(2) (i) of this subpart , report any instrument reading of 500 ppm above background or greater, if detected more than 5 days after the pressure release.(iii) For pressure relief devices in off

- site material service subject to § 63.691(c)(3) of this

subpart , report each pressure release to the atmosphere, including the following information:
(A) The source, nature, and cause of the pressure release.
(B) The date, time, and duration of the pressure release.

(C) An estimate of t he quantity of HAP listed in Table 1 of this subpart emitted during the pressure release and the method us ed for determining this quantity.
(D) The actions taken to prevent this pressure release.
(E) The measures adopted to prevent future such pressure releases.

(6) Pressure tank closure device or bypass deviation report. The owner or operator must submit to the Administrator the information specified in paragraph (b)(6) (i v ) of this section when any of the condition s in paragraph s (b)(6) (i) through ( i ii) of this section are met.

(i ) Any pressure tank closure device, as specified in §63.685(h)(2) of this subpart, has released to the atmosphere.

(ii ) Any closed vent system that includes bypass devices that could divert a vent a stream away from the control device and into the atmosphere , as specified in §63.693(c)(2) of this subpart , has released directly to the atmosphere.
(iii) Any open

- ended valve or line in an emergency shutdown system which is designed to open automatically in the event of a process upse t, as specified in 40 CFR 63.167(d) or 40 CFR 61.242

- 6(d), has released directly to the atmosphere.

(i v ) The p ressure tank closure device or bypass deviation report must include the information specified in paragraphs (b)(6)(i ii )(A) through (E) of this section

. (A) The source, nature and cause of the release.

( B ) The date, time and duration of the discharge.

(C ) An estimate of the quantity of HAP listed in Table 1 of this subpart emitted during the release and the method used for determining this quantity.

(D ) The actions taken to prevent this release.

(E ) The measures adopted to prevent future such releases.
(c) Each owner or operator using an internal floating roof or external floating roof to comply with the Tank Level 2 control requirements specified in §63.685(d) of this subpart shall notify the Administra tor in advance of each inspection required under §63.695(b) of this subpart toprovide the Administrator with the opportunity to have an observer present during the inspection.

The owner or operator shall notify the Administrator of the date and location o f the inspection as follows:
(1) Prior to each inspection to measure external floating roof seal gaps as required under §63.695(b) of this subpart, written notification shall be prepared and sent by the owner or operator so that it is received by the Admi nistrator at least 30 calendar days before the date the measurements are scheduled to be performed.
(2) Prior to each visual inspection of an internal floating roof or external floating roof in a tank that has been emptied and degassed, written notificati on shall be prepared and sent by the owner or operator so that it is received by the Administrator at least 30 calendar days before refilling the tank except when an inspection is not planned as provided for in paragraph (c)(3) of this section.

(3) When a visual inspection is not planned and the owner or operator could not have known about the inspection 30 calendar days before refilling the tank, the owner or operator shall notify the Administrator as soon as possible, but no later than 7 calendar days be fore refilling of the tank. This notification may be made by telephone and immediately followed by a written explanation for why the inspection is unplanned. Alternatively, written notification, including the explanation for the unplanned inspection, may b e sent so that it is received by the Administrator at least 7 calendar days before refilling the tank. 

## §63.698 Implementation and enforcement.

(a) This subpart can be implemented and enforced by the U.S. EPA, or a delegated authority such as the applica ble State, local, or Tribal agency. If the U.S. EPA Administrator has delegated authority to a State, local, or Tribal agency, then that agency, in addition to the U.S. EPA, has the authority to implement and enforce this subpart. Contact the applicable U. S. EPA Regional Office to find out if this subpart is delegated to a State, local, or Tribal agency.
(b) In delegating implementation and enforcement authority of this subpart to a State, local, or Tribal agency under subpart E of this part, the authoritie s contained in paragraph (c) of this section are retained by the Administrator of U.S. EPA and cannot be transferred to the State, local, or Tribal agency.
(c) The authorities that cannot be delegated to State, local, or Tribal agencies are as specified in paragraphs (c)(1) through ( 4 5 ) of this section.
(1) Approval of alternatives to the requirements in §§63.680, 63.683 through 63.691, and 63.693. Where these standards reference another subpart, the cited provisions will be delegated according to the delegation provisions of the referenced subpart.
(2) Approval of major alternatives to test methods under §63.7(e)(2)(ii) and (f), as defined in §63.90, and as required in this subpart.(3) Approval of major alternatives to monitoring under §63.8(f), as de fined in §63.90, and as

required in this subpart.
(4) Approval of major alternatives to recordkeeping and reporting under §63.10(f), as defined in §63.90, and as required in this subpart.
(5) Approval of alternative s to the electronic reporting requirement s in § 63.697(a)(3)

. 

## Table 1 to Subpart DD of Part 63

— List of Hazardous Air Pollutants (HAP) for Subpart DD

CAS No. a Chemical name f m 305

75

- 07

- 0 Acetaldehyde 1.000 75

- 05

- 8 Acetonitrile 0.989 98

- 86

- 2 Acetophenone 0.314 107

- 02

- 8 Acrolein 1.000

107

- 13

- 1 Acrylonitrile 0.999

107

- 05

- 1 Allyl chloride 1.000

71

- 43

- 2 Benzene (includes benzene in gasoline) 1.000 98

- 07

- 7 Benzotrichloride (isomers and mixture) 0.958 100

- 44

- 7 Benzyl chloride 1.000

92

- 52

- 4 Biphenyl 0.864 542

- 88

- 1 Bis(chloromethyl)ether b 0.999

75

- 25

- 2 Bromoform 0.998 106

- 99

- 0 1,3

- Butadiene 1.000

75

- 15

- 0 Carbon disulfide 1.000 56

- 23

- 5 Carbon tetrachloride 1.000 43

- 58

- 1 Carbonyl sulfide 1.000 133

- 90

- 4 Chloramben 0.633

108

- 90

- 7 Chlorobenzene 1.000

67

- 66

- 3 Chloroform 1.000107

- 30

-

2 Chloromethyl methyl ether b 1.000

126

- 99

- 8 Chloroprene 1.000

98

- 82

- 8 Cumene 1.000 94

- 75

- 7 2,4

- D, salts and esters 0.167 334

- 88

- 3 Diazomethane c 0.999

132

- 64

- 9 Dibenzofurans 0.967

96

- 12

- 8 1,2

- Dibromo

- 3

- chloropropane 1.000 106

- 46

- 7 1,4

- Dichlorobenzene(p) 1.000

107

- 06

- 2 Dichloroethane (Ethylene dichloride) 1.000

111

- 44

- 4 Dichloroethyl ether (Bis(2

- chloroethyl ether) 0.757

542

- 75

- 6 1,3

- Dichloropropene 1.000

79

- 44

- 7 Dimethyl carbamoyl chloride c 0.150 64

- 67

- 5 Diethyl sulfate 0.0025 77

- 78

- 1 Dimethyl sulfate 0.086 121

- 69

- 7 N,N

- Dimethylaniline 0.0008

51

- 28

- 5 2,4

- Dinitrophenol 0.0077 121

- 14

- 2 2,4

- Dinitrotoluene 0.0848

123

- 91

- 1 1,4

- Dioxane (1,4

- Diethyleneoxide) 0.869

106

- 89

- 8 Epichlorohydrin (1

- Chloro

- 2,3

- epoxypropane) 0.939

106

- 88

- 7 1,2

- Epoxybutane 1.000

140

- 88

- 5 Ethyl acrylate 1.000

100

- 41

- 4 Ethyl benzene 1.000

75

- 00

- 3 Ethyl chloride (Chloroethane) 1.000 106

- 93

- 4 Ethylene dibromide (Dibromoethane) 0.999107

- 06

-

2 Ethylene dichloride (1,2

- Dichloroethane) 1.000

151

- 56

- 4 Ethylene imine (Aziridine) 0.867

75

- 21

- 8 Ethylene oxide 1.000 75

- 34

- 3 Ethylidene dichloride (1,1

- Dichloroethane) 1.000 Glycol ethers d that have a Henry's Law constant value equal to or greater than 0.1 Y/X (1.8×10 −6 atm/gm

- mole/m 3 ) at 25°C (e)

118

- 74

- 1 Hexachlorobenzene 0.97

87

- 68

- 3 Hexachlorobutadiene 0.88 67

- 72

- 1 Hexachloroethane 0.499 110

- 54

- 3 Hexane 1.000

78

- 59

- 1 Isophorone 0.506 58

- 89

- 9 Lindane (all isomers) 1.000 67

- 56

- 1 Methanol 0.855 74

- 83

- 9 Methyl bromide (Bromomethane) 1.000 74

- 87

- 3 Methyl chloride (Choromethane) 1.000 71

- 55

- 6 Methyl chloroform (1,1,1

- Trichloroethane) 1.000 78

- 93

- 3 Methyl ethyl ketone (2

- Butanone) 0.990 74

- 88

- 4 Methyl iodide (Iodomethane) 1.0001 108

- 10

- 1 Methyl isobutyl ketone (Hexone) 0.9796

624

- 83

- 9 Methyl isocyanate 1.000

80

- 62

- 6 Methyl methacrylate 0.916 1634

- 04

- 4 Methyl tert butyl ether 1.000

75

- 09

- 2 Methylene chloride (Dichloromethane) 1.000 91

- 20

- 3 Naphthalene 0.994 98

- 95

- 3 Nitrobenzene 0.394 79

- 46

- 9 2

- Nitropropane 0.989 82

- 68

- 8 Pentachloronitrobenzene (Quintobenzene) 0.839 87

- 86

- 5 Pentachlorophenol 0.0898 75

- 44

- 5 Phosgene c 1.000 123

- 38

- 6 Propionaldehyde 0.999

78

- 87

- 5 Propylene dichloride (1,2

- Dichloropropane) 1.00075

- 56

- 9 Propylene oxide 1.000

75

- 55

- 8 1,2

- Propylenimine (2

- Methyl aziridine) 0.945 100

- 42

- 5 Styrene 1.000

96

- 09

- 3 Styrene oxide 0.830 79

- 34

- 5 1,1,2,2

- Tetrachloroethane 0.999 127

- 18

- 4 Tetrachloroethylene (Perchloroethylene) 1.000

108

- 88

- 3 Toluene 1.000

95

- 53

- 4 o

- Toluidine 0.152 120

- 82

- 1 1,2,4

- Trichlorobenzene 1.000

71

- 55

- 6 1,1,1

- Trichloroethane (Methyl chlorform) 1.000 79

- 00

- 5 1,1,2

- Trichloroethane (Vinyl trichloride) 1.000 79

- 01

- 6 Trichloroethylene 1.000 95

- 95

- 4 2,4,5

- Trichlorophenol 0.108 88

- 06

- 2 2,4,6

- Trichlorophenol 0.132 121

- 44

- 8 Triethylamine 1.000

540

- 84

- 1 2,2,4

- Trimethylpentane 1.000

108

- 05

- 4 Vinyl acetate 1.000

593

- 60

- 2 Vinyl bromide 1.000

75

- 01

- 4 Vinyl chloride 1.000 75

- 35

- 4 Vinylidene chloride (1,1

- Dichloroethylene) 1.000 1330

- 20

- 7 Xylenes (isomers and mixture) 1.000

95

- 47

- 6 o

- Xylenes 1.000 108

- 38

- 3 m

- Xylenes 1.000

106

- 42

- 3 p

- Xylenes 1.000

Notes:

f m 305 = Method 305 fraction measure factor.a. CAS numbers refer to the Chemical Abstracts Services registry number assigned to specific

compounds, isomers, or mixtures of compounds.
b. Denotes a HAP that hydrolyzes quickly in water, but the hydrolysis products are also HAP chemicals.
c. Denotes a HAP that may react violently with water, exercise caustic is an expected analyte.
d. Denotes a HAP that hydrolyzes sl owly in water.

e. The f

m 305 factors for some of the more common glycol ethers can be obtained by contacting the Waste and Chemical Processes Group, Office of Air Quality Planning and Standards, Research Triangle Park, NC 27711. 

## Table 2 to Subpart DD of Pa rt 63

—Applicability of Paragraphs in Subpart A of This Part 63

— General Provisions to Subpart DD

Subpart A reference Applies to

Subpart DD Explanation

63.1(a)(1) Yes 63.1(a)(2) Yes 63.1(a)(3) Yes
63.1(a)(4) No Subpart DD (this table) specifies applicability of each paragraph in subpart A to subpart DD. 63.1(a)(5)

- 63.1(a)(9) No
63.1(a)(10) Yes 63.1(a)(11) Yes 63.1(a)(12) Yes 63.1(a)(13) Yes 63.1(a)(14) Yes 63.1(b)(1) No Subpart DD specifies its own applicability. 63.1(b)(2) Yes No Reserved 63.1(b)(3) No 63.1(c)(1) No Subpart DD explicitly specifies requirements that apply. 63.1(c)(2) No Area sources are not subject to subpart DD. 63.1(c)(3) No Reserved 63.1(c)(4) No Yes Reserved63.1(c)(5) Yes Except that sources are not required to submit notifications overridden by this table. 63.1(d) No 63.1(e) No

63.2 Yes §63.681 of subpart DD specifies that if the same term is defined in subparts A and DD, it shall have the meaning given in subpart DD. 63.3 Yes 63.4(a)(1)

- 63.4(a) ( 3 2 ) Yes
63.4(a)(3) No Reserved 63.4(a)(4) No Reserved. 63.4(a)(5) Yes No Reserved 63.4(b) Yes 63.4(c) Yes
63.5(a)(1) Yes Except replace term “source” and “stationary source” in §63.5(a)(1) of subpart A with “affected source.” 63.5(a)(2) Yes 63.5(b)(1) Yes 63.5(b)(2) No Reserved. 63.5(b)(3) Yes

63.5(b)(4) Yes Except the cross

- reference to §63.9(b) is changed to §63.9(b)(4) and (5). Subpart DD overrides §63.9(b)(2) and (b)(3). 63.5(b)(5) Yes No Reserved 63.5(b)(6) Yes 63.5(c) No Reserved. 63.5(d)(1)(i) Yes 63.5(d)(1)(ii) Yes 63.5(d)(1)(iii) Yes 63.5(d)(2) No 63.5(d)(3) Yes 63.5(d)(4) Yes 63.5(e) Yes 63.5(f)(1) Yes 63.5(f)(2) Yes 63.6(a) Yes
63.6(b)(1) No Subpart DD specifies compliance dates for sources subject to subpart DD.63.6(b)(2) No

63.6(b)(3) Yes No
63.6(b)(4) No May apply when standards are proposed under section 112(f) of the Clean Air Act. 63.6(b)(5) No §63.697 of subpart DD includes notification requirements. 63.6(b)(6) No 63.6(b)(7) No 63.6(c)(1) No §63.680 of subpart DD specifies the compliance date. 63.6(c)(2)

- 63.6(c)(4) No
63.6(c)(5) Yes 63.6(d) No 63.6(e) (1)(i) No See § 63.683( e ) of this subpart for general duty requirement. 63.6(e)(1)(ii) No 63.6(e)(1)(iii) Yes 63.6(e)(2) 63.6(e) No Yes Reserved. 63.6(e)(3) No 63.6(f)(1) No Yes 63.6(f)(2)(i) Yes
63.6(f)(2)(ii) Yes Subpart DD specifies the use of monitoring data in determining compliance with subpart DD. 63.6(f)(2)(iii) (A), (B), and (C) Yes
63.6(f)(2)(iii) (D) No 63.6(f)(2)(iv) Yes 63.6(f)(2)(v) Yes 63.6(f)(3) Yes 63.6(g) Yes
63.6(h) No Subpart DD does not require opacity and visible emission standards. 63.6(i) Yes Except for §63.6(i)(15), which is reserved. 63.6(j) Yes
63.7(a)(1) No Subpart DD specifies required testing and compliance demonstration procedures. 63.7(a)(2) Yes 63.7(a)(3) Yes 63.7(a)(4 ) Yes 63.7(b) No63.7(c) No

63.7(d) Yes 63.7(e)(1) No Yes See 63.694(l) of this subpart

. 63.7(e)(2) Yes 63.7(e)(3) No Subpart DD specifies test methods and procedures. 63.7(e)(4) Yes
63.7(f) Yes No Subpart DD specifies applicable methods and provides alternatives. 63.7(g) Yes 63.7(h)(1) Yes 63.7(h)(2) Yes 63.7(h)(3) Yes 63.7(h)(4) No 63.7(h)(5) Yes 63.8(a) No 63.8(b)(1) Yes 63.8(b)(2) No Subpart DD specifies locations to conduct monitoring. 63.8(b)(3) Yes 63.8(c)(1)(i) Yes 63.8(c)(1)(ii) Yes 63.8(c)(1)(iii) No Yes 63.8(c)(2) Yes 63.8(c)(3) Yes 63.8(c)(4) No Subpart DD specifies monitoring frequency 63.8(c)(5)

- 63.8(c)(8) No
63.8(d) No 63.8(e) No 63.8(f)(1) Yes 63.8(f)(2) Yes 63.8(f)(3) Yes 63.8(f)(4)(i) Yes 63.8(f)(4)(ii) Yes 63.8(f)(4)(iii) No 63.8(f)(5)(i) Yes 63.8(f)(5)(ii) No 63.8(f)(5)(iii) Yes 63.8(f)(6) Yes63.8(g) Yes

63.9(a) Yes 63.9(b)(1)(i) Yes 63.9(b)(1)(ii) No 63.9(b)(2) Yes 63.9(b)(3) No 63.9(b)(4) Yes 63.9(b)(5) Yes 63.9(c) Yes 63.9(d) Yes 63.9(e) No 63.9(f) No 63.9(g) Yes No 63.9(h) Yes 63.9(i) Yes 63.9(j) No 63.10(a) Yes 63.10(b)(1) Yes 63.10(b)(2)(i) No Yes

63.10(b)(2)(ii) No Yes See § 63.696(h) of this subpart for recordkeeping of (1) date, time and duration; (2) listing of affected source or equipment, and an estimate of the volume of each regulated pollutant emitted over the standard; and (3) actions to minimize emissions and correct the failure. 63.10(b)(2) (iii) No Yes 63.10(b)(2)(iv) No Yes 63.10(b)(2)(v) No Yes 63.10(b)(2)(vi)

- (ix) Yes 63.10(b)(2)(x)

- (xi) Yes 63.10(b)(2) (xii)

- (xiv) No
63.10(b)(3) Yes 63.10(c) (1)

- (6) No 63.10(c)(7)

- (8) Yes 63.10(c)(9)

- (15) No 63.10(d)(1) No 63.10(d)(2) Yes 63.10(d)(3) No63.10(d)(4) Yes

63.10(d)(5) (i) No Yes See § 63.697(b)(3) of this subpart for reporting of malfunctions. 63.10(d)(5)(ii) Yes 63.10(e) (1)

- (2) No 63.10(e)(3) Yes 63.10(e)(4) No 63.10(f) Yes 63.11

- 63.15 Yes 63.16 No

a Wherever subpart A specifies “postmark” dates, submittals may be sent by methods other than the U.S. Mail (e.g., by fax or courier). Submittals shall be sent by the specified dates, but a postmark is not required. 

## Table 3 to Subpart DD of Part 63

— Tank Cont rol Levels for Tanks at Existing Affected Sources as Required by 40 CFR 63.685( b )(1) (i)

Tank design capacity (cubic meters) Maximum HAP vapor

pressure of off

- site material managed in tank (kilopascals) Tank control level

Design capacity less than 75 m 3 Maximum HAP vapor

pressure less than 76.6 kPa Level 1.

Design capacity less than 75 m 3 Maximum HAP vapor

pressure equal to or greater tha n 76.6 kPa Level 2
, e xcept that fixed roof tanks equipped with an internal floating roof and tanks equipped with an external floating roof as provided for in § 63.685(d)( 1) and (2) of this subpart shall not be used

. Design capacity equal to or greater than 75 m 3 and less than 151 m 3 Maximum HAP vapor

pressure less than 27.6 kPa Level 1.

Maximum HAP vapor pressure equal to or greater than 27.6 kPa Level 2.

Design capacity equal to or greater than 151 m 3 Maximum HAP vapor

pressure s less than 5.2 kPa Level 1.Maximum HAP vapor pressure equal to or greater than 5.2 kPa Level 2.



## Table 4 to Subpart DD of Part 63

— Tank Control Levels for Tanks at Existing Affected Sources as Required by 40 CFR 63.685( b )(1) (ii)

Tank design capacity (cubic meters) Maximum HAP vapor

pressure of off

- site material managed in tank (kilopascals) Tank control level

Design capacity less than 75 m 3 Maximum HAP vapor

pressure less than 76.6 kPa Level 1.

Design capacity less than 75 m 3 Maximum HAP vapor

pressure equal to or greater tha n 76.6 kPa Level 2
, e xcept that fixed roof tanks equipped with an internal floating roof and tanks equipped with an external floating roof as provided for in § 63.685(d)(1) and (2) of this subpart shall not be used

. Design capacity equal to or greater than 75 m 3 and less than 151 m 3 Maximum HAP vapor

pressure less than 13.1 kPa Level 1.

Maximum HAP vapor pressure equal to or greater than 13.1 kPa Level 2.

Design capacity equal to or greater than 151 m 3 Maximum HAP vapor

pressure less than 5.2 kPa Level 1.

Maximum HAP vapor pressure equal to or greater than 5.2 kPa Level 2.



## Table 5 4 to Subpart DD of Part 63

— Tank Control Levels for Tanks at New Affected Sources as Required by 40 CFR 63.685( b )(2)Tank design

capacity (cubic meters) Maximum HAP vapor

pressure of off

- site material managed in tank (kilopascals) Tank control level

Design capacity less than 38 m 3 Maximum HAP vapor

pressure less than 76.6 kPa Level 1.

Design capacity less than 38 m 3 Maximum HAP vapor

pressure equal to or greater than 76.6 kPa Level 2
, e xcept that fixed roof tanks equipped with an internal floating roof and tanks equipped with an external floating roof as provided for in § 63.685(d)(1) and (2) of this subpart shall not be used

. Design capacity equal to or greater than 38 m 3 and less than 151 m 3 Maximum HAP vapor

pressure less than 13.1 kPa Level 1.

Maximum HAP vapor pressure equal to or greater than 13.1 kPa Level 2.

Design capacity equal to or greater than 151 m 3 Maximum HAP vapor

pressure less than 0.7 kPa Level 1.

Maximum HAP vapor pressure equal to or greater than 0.7 kPa Level 2.