## 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 s ys tems. §63.690 Standards: Process vents. §63.691 Standards: Equipment leaks. §63.692 [Reserved] §63.693 Standards: Closed

- vent s ys tems and control devices. §63.694 Testing methods and procedures. §63.695 In spection 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

—Li st 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 b y 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 b y 40 CFR 63.685(b)(1) (ii) Table 5 to Subpart DD of Part 63

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

## §63.680 **Applicability and designation of affected sources.** (a) The provisions of this subpart appl y 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 b y s ection 502(3) and 502(4), respectivel y, 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 implementing 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 L iability

Act (CERCLA) authorities, or similar Federal or State authorities. (iv) Wast e containing HAP that is generated b y residential households (e.g., old paint, home garden pesticides) and subsequentl y is collected as a community service b y government agencies, businesses, or other organizations for the purpose of promoting the proper disposal of this waste. (v) Waste that is transferred from a chemical manufacturing plant or other facility for which the owner or operator of the facility from which the waste i s transferred has complied with the provisions of the air emission control standards for process wastewater specified b y another 40 CFR part 63 subpart. This exemption does not apply to a source which complies with another 40 CFR part 63 subpart by transferring its wastewater off

- site for control. (vi) Waste that is transferred from a chemical manufacturing plant, petroleum refinery , or coke b y- 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 facility 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 provisions 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 st ored for 10 day s or less at a transfer facility in compliance with the provisions of 40 CFR 263.12. (c) Affected 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 s ys tem 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 material 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 condenser, a bottoms receiver vessel, a surge control tank, a separator tank, and a hot well. (2) Process vents. For each operation specified in paragraph s (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 sec tion. (i) Distillation process used for the treatment, recycling, or recovery of off

- site material. Distillation 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 b y the redistribution of the components between the liquid and vapor phases as they approach equilibrium within the distillation unit. (ii) Fractionation proce ss used for the treatment, recycling, or recovery of off

- site material. Fractionation means a liquid mixture 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 use s a heating surface consisting of a large diameter tube that may be either straight or tapered, horizontal or vertical. L iquid 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 recovery 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 transfer 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 components of a liquid mixture occurs b y the introduction of steam directly into the process. (vi) Gas stripping process used for the treatment, recycling, or r ecovery 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 tow ers, and bubble

- cap, sieve, or valve

ty pe plate towers are examples of the process configurations used for 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 each 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 ap ply 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 sy stem, open
- ended valve or line, valve, connector, or instrumentation sy stem; (ii) The equipment component contains or contacts off

- site material having 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 o r more during a calendar year in off

- site material service, as defined in §63.681 of this subpart. (d) Facility

- wide exemption. The owner or operator of affected sources subject to this subpart is exempted from the requirements of §§63.682 through 63.699 o f 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 o wner 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 dete rmination is based on the total quantity of the HAP listed in Table 1 of this subpart as determined at the 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 d ocumentation to support the owner's or

operator's determination of the total annual HAP quantity in the off

- 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 specifie d in paragraph (e)(1)(i) , (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 provi sions of the subpart (except §§ 63. 685(b)(1) (ii) , 63.691(b) (2) , 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 ye ar s after the publication date of the final amendments on [DATE OF PUBLICATION OF THE FINAL RULE IN THE FEDERAL REGI STER] , the equipment leak requirements of § 63. 691(b) (2) of this subpart one ye ar after the publication date of the final amendments on [DATE OF PUBLICATION OF THE FINAL RULE INTHE FEDERALREGI STER] , 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 on [DATE OF PUBLICATION OF THE FINAL RULE IN THE FEDERAL REGI STER]

. (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 [DATE OF PUBLICATION OF THE FINAL RULE INTHE FEDERAL REGI STER] , 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 ) (2) , 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 on [DATE OF PUBLICATION OF THE FINAL RULE IN THE FEDERAL REGISTER] , the equipment leak requirements of §63. 691(b) (2) of this subpart one year after the publication date of the final amendments on [DATE OF PUBLICATION OF THE FINAL RULE IN THE FEDERAL REGI STER] , and the pressure relief device monitoring re quirements of § 63. 691 (c) ( 3)(i) and (ii) of this subpart three ye ars after the publication date of the final amendments on [DATE OF PUBLICATION OF THE FINAL RULE 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 [DATE OF PUBLICATION OF THE FINAL RULE IN THE FEDERAL REGISTER] , the owner or operator of the aff

ected source must achieve compliance with the provisions of this subpart (except §§ 63. 685 (b)(1) (ii) , 63.691(b) (2) , 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 affectedsources 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 [DATE OF PUBLICATION OF THE FINAL RULE IN THE FEDERAL REGI STER] , the equipment leak requirements of § 63. 691(b) (2) of this subpart one ye ar after the publication date of the final amendments on [ DATE OF PUBLICATION OF THE FINAL RULE IN THE FEDERAL REGI STER] , and the pressure relief device monitoring requirements of § 63. 691 (c) ( 3)(i) and (ii) of this subpart three ye ars after the publication date of the final amendments on [DATE OF PUBLICATION OF THE FINAL RULE IN THE FEDERALREGI STER]

. (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) (2) , 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 sources that commenced construction or reconstruction after October 13 , 199 4 , but on or before July 2, 2014 , 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) (2) of this subpart one after the publication date of the final amendments , and the pressure relief devi ce monitoring requirements of § 63. 691 (c) (3) (i) and (ii) of this subpart three ye ars after the effective date of the final amendments. New affected sources that commence construction or reconstruction after July 2, 2014 , shall be in compliance with the tank requirements of § 63. 685(b)(2 ) of this subpart , the equipment leak requirements of § 63. 691(b) (2) 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 thereof) resulting in cessation of the emissions to which this subpart applies. (2) The o wner 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 such 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 sy stem stream to the atmosphere such that it does not first pass thro ugh an emission control device.Closed

- vent system means a sy stem 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 convey s gas or vapor from an emission point to a control device. Closure device means a cap, hatch, lid, plug, seal, valve, or other typ e 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 th at are detachable from the cover (e.g., a sampling port cap), manually operated (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 boxes, 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 lea st once every 15 minutes and recorded at the frequency specified in this subpart. 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 destro yi ng organic vapors. Examples of such equipment include but are not limited to c arbon adsorbers, condensers, vapor incinerators, flares, boilers, and process heaters. Cover means a device or sy stem that provides a continuous barrier over the material managed in an off

- site material management unit to prevent or reduce air pollutant em issions to the atmosphere. 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 piec e of equipment which can be detached and removed from the unit or a cover may be formed by

structural features permanentl y integrated into the design of the unit. Emission point means an individual tank, surface impoundment, container, oil

- water or organic

water separator, transfer sy stem, 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 sy stem to a control device. External floating roof means a pontoon
- ty pe 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 fluctuation s in the level of the liquid 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 intern al floating cover which rests 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 by pa ss line. Hard

- piping means pipe or tubing that is manufactured and properl y installed in accordance with relevant standards and good engineering practices. Hazardous air pollutants or HAP means the specific organic chemical compounds, isomers, and mixture s 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

- site material service contains or contacts 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 s ervice. In light liquid service means that a piece of equipment in off

- site material service contains or contacts 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 compounds 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 ope rating conditions. N OT E : Vapor pressures may be determined b y 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 s ys tem used to convey

wastewater streams or residuals to a waste 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 bo xes (e.g., manholes, sumps, and lift stations) conveying wastewater streams or residuals. For the purpose of this subpart, an individual drain sy stem is not a drain and collection sy stem that is designed and operated for the sole purpose of collecting rain fall runoff (e.g., stormwater sewer sy stem) and is segregated from all other individual drain s ys tems. Internal floating roof means a cover that rests or floats on the liquid surface (but not necessaril y 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 kil opascals (kPa) at 20 °C; and the total concentration of the pure organic constituents 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 b y an off

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

- site material is stored 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 ambie nt temperature or when the off

- site material is stored or treated at temperatures 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. Metalli c shoe seal means a continuous seal that is constructed of metal sheets which are held verticall y against the wall of the tank by springs, weighted levers, or other mechanisms and is connected to the floating roof b y braces or other means. A flexible coate d fabric (envelope) spans the annular space between the metal sheet and the 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 paragraph §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 impoun dment, oil

- water separator, organic

- water separator, or transfer s ys tem used to manage off

- site material.Off

-site material service means an y time when a pump, compressor, agitator, pressure relief device, sampling connection sy stem, open
- ended valve or l ine, valve, connector, or instrumentation sy stem 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 comprisi ng the stream remain consistent. An off

- site material stream may be delivered, 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 multiple 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 b y itself or in combination with one or more other operating parameter values, determines that an owner or operator has complied with an applicable 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 und er common control including properties 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 contiguous 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 poi nt at the boundary or within the plant site where the owner or operator first accepts custody , takes possession, or assumes responsibility for the management of an off

- site material stream managed in a waste management operation or recovery operation speci fied in §63.680 (a)(2)(i) through (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 treated 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 relea sed to the atmosphere. For the purpose of appl yi ng 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, co mpressors, valves, connectors, instrumentation sy stems, or pressure relief devices

.Pressure release means the emission of materials resulting from the sy stem pressure being

greater than the set pressure of the pressure relief device. This re lease can be one release or a series of releases 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 pressure relief valve. Devices that are actuated either by a pressure of less than or equal to 2.5 pounds per square inch gauge or b y 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 (vi) of this s ubpart . For the purpose of this subpart, a process vent is none of the following: a pressure relief device ; 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 of f

- 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 ph ys ical and chemical impurities of concern.

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

- plate interceptor, 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 that is a natural topographical depression, man

- made excavation, or diked area formed primaril y of earthen materials (although it may be l ined with man - made materials), which is designed to hold an accumulation of liquids. Examples of surface impoundments include 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 designed to hold an accumulation of liquids or other materials. Transfer system means a stationary s ys tem for which the predominant functi on is to convey liquids or solid materials from one point to another point within a waste management operation or recovery

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

- prop elled vehicle (e.g., a front

- end loader) is not a transfer s ys tem. Examples of a transfer s ys tem include but are not limited to a pipeline, an individual drain sy stem, 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 phy sicall y, chemicall y, thermall y, or biologicall y 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 sy stem). A treatment process can be used to treat one or more off

- site material streams at the same time. Used oil means an y oil refined from crude oil or any s ynthetic oil that has been used and as a result of such use is contaminated b y ph ys ical or chemical impurities. 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 h ydrocarbons that has been used as a solvent and as a result of such use is contaminated by phy sical 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 b y 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 alternative 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 list ed in Table 1 of this subpart to determine a VOHAP concentration. 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 phy sicall y, chemicall y, thermally, or biologically treated 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

- delivery 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 an y ph ys ical 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, Phy sical/Chemical Methods,” EPA Publication No. SW

- 846, Third Edition, September 1986, as amended b y 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 mixing the wast e with binders or other materials and curing the resulting waste and binder mixture. Other sy nony mous terms used to refer to this process are “waste fixation” or “waste solidification.” A waste stabilization process does not include the adding 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 appl y 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)(i i), 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 accordance with the appli cable standards specified in §§63.685 through 63.689 of this subpart. (ii) The owner or operator removes or destro ys HAP in the off

- site material before placing the material in the off

- site material management unit by treating the material in accordance wi th 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 than 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 andupdate, as necessary , 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 the owner or operat or 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 mat erial 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 provisions 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 o perator 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 manageme nt units selected to be exempted under this paragraph (b)(2)(ii) b y preparing a new designation for the exempt

- units as required b y paragraph (b)(2)(ii)(A) of this section and performing a new determination as required by paragraph (b)(2)(ii)(B) of this se ction. (A) The owner or operator must designate each of the off

- site material management units selected b y the owner or operator to be exempt under paragraph (b)(2)(ii) of this section by either submitting to the Administrator a written notification identi fying the exempt

- units or permanentl y marking the exempt

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

- units. I f 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 readil y identified as an exempt

- unit from the other off

- site material management uni ts 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 based on the total q uantity 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 quantity or compositio n 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 determination 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 section 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 biod egradation 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) The total actual HAP mass removal rate (MR bio ) for the off

- site material treated b y 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 bio ) must be determ ined 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 unit is exempted fro m 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 hazardous waste meets th e 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 hazardous constituents in the hazardous waste have been treated b y the treatment technology

established by

the EPA for the hazardous waste in 40 CFR 268.42(a), or have been removed or destroyed b y an equivalent method of treatment approved by the EPA under 40 CFR 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 Benzene Waste Operation s for a facility at which the total annual benzene quantity

from the facility

waste is equal to or greater than 10 megagrams per ye ar; (B) The enclosure and control device serving the tank were installed and began operation prior to July 1, 1996; and (C) T he 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 theenclosure b y conveyor, vehicles, or other mechanical or electrical equipment; or to direct air

flow into the enclosure. The owner or operator 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 affected 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 from 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 500 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 before an y 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

- site material s tream. (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 from the proce ss 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 determines that the p rocess 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 sub part. Documentation must be prepared b y 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 under this paragr aph 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 b y the owner or operator and maintained at the plant site tosupport the determination of the process vent stream flow rate and total HAP concentration. This

documentation must include identificati on 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 r ate 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 exceed 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 measures 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 emissions. The general duty to minimize emissions does not require the owner operator to make any further efforts to reduce emissions if levels required b y the applicable standard have been achieved. Determinatio n of whether a source is operating in compliance 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 records, 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 (6) of this section. (1) An y 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 b y this subpart, including, but not limited to, any

emission limit, operating limit or work practice standard. (2) When a performance test indicates 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 operatin g 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 directl y into 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 by pass, as defined in § 63.681 of this subpart

.(5) An y 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) An y term or condition that is adopted to implement an applicable requirement in this subpart. (ii) Any term or condition relating to compliance with this subpart that is included in the operating permit for an affected source to obtain such a permit. (6) An y failure to collect required data, except for periods of monitoring s ystem malfunctions, repairs ass ociated with monitoring s ys tem malfunctions, and required monitoring s ys tem 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 treatment 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 destro y the HAP contained in off

- site material streams to be managed in the off

- site material management unit in accordance with §63.683(b)(1)(ii) of this subpart using a treatment process that continuously achieves, under normal operations, one o r 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 le vel 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 average 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 conc entration 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 performanc e level such that the total quantity

of HAP actually

removed from 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 determined using the procedures specified in §63.694(f) of this subpart. (3) HAP reduction efficiency. For an y treatment process except a treatment process that uses biological degradation and is performed in an open tank or surface impoundment, the treatment 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

- sit e 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 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

- delivery shall be determined using the procedure specified in §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 p oint

- 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 b y 95 percent or more, and the average VOHAP concentration of the off

- site material at the point

- o f

- 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 mat erial stream at the point

- of

- treatment shall be determined using 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 perfo rmed in an open tank or surface impoundment must achieve the performance 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 (Rbio ) for the treatment process 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 actuall y removed from the off

- site material stream by

biological degradation (MR bio ) shall be equal to or greater than the require d mass removal (RMR) established for the off

- site material stream 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 contained in the off

- site material stream using one of the combustion devices specified in paragraphs (b)(5)(i) through (b)(5)(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 incinerator is designed and operated in accordance with the requirements of 40 CFR part 264, subpart O

—In cinerators, or (ii) An incinerator for which the owner or operator has certified complian ce with the interim status requirements of 40 CFR part 265, subpart O

—In cinerators. (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 o f 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 H AP to the atmosphere, to the extent practical. Examples of HAP emission 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, th e 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 day s after first time an owner or operator begins using the treatment process to manage off

- site material streams in accordancewith the requirements of either §63.683(b)(1)(ii) or §63.683(b)(2)(ii) of this subpart as applicable

to th e affected off

- site material management unit or process equipment. Thereafter, the owner or operator shall review and update, as necessary , this demonstration at least once every calendar ye ar following the date of the initial demonstration. (e) When the o wner 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 require ments by continuousl y monitoring the operation of the process when 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 s y stem shall be installed and operated for each treatment that measures operating parameters appropriate for the treatment process technology . This s ys tem shall include a continuous recorder that records the measured values of the selected operating paramete rs. 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 v alue at least once every 15 minutes or an average value for intervals 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 the range of conditions at which the treatment 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 monitoring s ys tem 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 l ess 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 esta blish and implement a written procedure to monitor the appropriate 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 o perating parameters that will be monitored and state the frequency

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 requirement. (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 the requirements of §63.697(a) of this subpart.(h) The Administrator may at any time conduct or require that the owner or operator conduct testing necessary

to demonstrate that a treatm ent 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 testin g 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) through (iii) of this subpart , the 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

. (1) (i) 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 b y 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 b y 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 b y 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 b y 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 b y 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 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 b y Table 5 of this subp art 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 b y Table 5 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 b y Table 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 stabilizatio n 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. (c) Owners and operators controlling air emissions from a tank using Tank Level 1 controls sh all 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 , Table 4 or Table 5 of this subpart, as applicable 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 controls air emis sions from the tank in accordance with the provisions specified in subpart OO of 40 CFR part 63

— National Emission Standards for Tanks

—Level 1 , except that 40 CFR 63.902(c)(2) and (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. (iii) 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 control 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 dump tr ucks, 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 6 3 , subpart OO

— National Emission Standards for Tanks

— Level 1 , with the exceptions specified in paragraphs (c)(2)(iii)( B ) ( 1 ) and ( 2 ) of this section

. ( 1 ) Where 40 CFR 63.902(c)( 2 ) provides an exception for a spring

- loaded pressure

- vacuum relief valve, conservation vent, or similar ty pe of pressure relief device which vents to theatmosphere , onl y a conservation vent shall be eligible for the exception for the purposes of this

subpart

. ( 2 ) 40 CFR 63.902(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 in 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 sy stem 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 sy stem 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 accordance 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 s hall be equipped with a continuous seal 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 §63.6 81 of this subpart; or (B) Two continuous 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 ex cept for automatic bleeder vents

(vacuum 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 sl eeves, automatic bleeder vents, rim space 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 th e opening. (D) Each automatic bleeder 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 ro of that allows for passage of a column 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 ro of is resting on the leg supports, the process of filling, emptyi ng, 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 being 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 open 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 accordan ce 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 sup ports.(ii) The floating roof shall be 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

- mounted 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 these 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 tank and the other end extends a vertical distance of at least 61 centimeters (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 secondary

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 fo llowing specifications: (A) Except for 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, ri m 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 with a slotted membrane fabric cover that co vers 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 equipped 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, emptyi ng, or

refilling shall be continuous and shall 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 o n 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 recommended 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 shall 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 the 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 emissions by venting to a control device shall m eet the requirements specified in paragraphs (g)(1) through (g)(3) of this section. (1) The tank shall be covered b y a fixed roof and vented directl y through a closed

- vent s ys tem 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 closu re devices shall be 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 cover opening and the closure d evice. If the pressure in the vapor headspace underneath the fixedroof 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. F actors 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 the tank on which the fixed roof is installed. (iv) The closed

- vent s ys tem and control device shall be designed and operated in accordance with the requirements of §63.693 of this su bpart. (2) Whenever an off

- site material is in the tank, the fixed roof shall 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 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: ( i ) To provide access to the tank for performing routine inspection, maintenance, or other activities needed fo r 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 worker 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. ( ii ) To remove accumulated sludge or other residues from the bottom of the tank. (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 s ys tem 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 sy stem 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 control air emissions by using an enclosure vented through a closed

- vent sy stem to an enclosed combustion control device shall meet the requirements specified in paragraphs (i)(1) through ( 3 ) of this section. (1) The tank shall be l ocated inside an enclosure. 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 enclosure may have permanent or temporary openings to allow worker access; passage of material into or out of the enclosure b y conve yo r, 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 installed and, thereafter, annually

. (2) The enclosure shall be vented through a closed

- vent sy stem to an enclosed combustion control device that is designed and operated in accordance with the standards for either a vapor incinerator, b oiler, or process heater specified in §63.693 of this subpart.

( 3 ) The owner or operator shall inspect and monitor the closed

- vent sy stem 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 operator shall control air emissions from each separator subject to this section by using one of the followi ng: (1) A floating roof in accordance with all applicable provisions 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 . 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 compl y with the requirements specified in paragraph (b )(2) of this section. (2) A fixed

- roof that is vented through a closed

- vent sy stem to a control device in accordance with all applicable provisions 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 em issions 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 , except that §§ 63.942(c)(2) and (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 subp art QQ

— National Emission Standards for Surface Impoundments , except that §§ 63.942(c)(2) and (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 air 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 from the container in accordance with the standards for Container Level 1 controls as specified in 40 CFR part 63, subpart PP

— National Emission Standards for Containers , except that §§ 63.922(d)(4) and (5) and 63.923(d)(4) and (5) shall not apply

for the p urposes 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 co ntrols or Container Level 3 controls as specified insubpart PP of this part 63

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

. (2) For a container 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 paragr aph (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 the c ontainer 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 (5) and 63.923(d)(4) and (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 from 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 Standards for Containers. 

## §63.689 **Standards: Transfer systems.** (a) The provisions of this section apply to the control of air emissions from transfer s ys tems for which §63.683(b)(1)(i) of this subpart references the use of this section for such air emission control. (b) For each transfer s ys tem that is subject to this section and is an individual drain s ys tem, the owner or operator shall control air emissions in accordance with the standards specified in 40 CFR part 63, subpart RR

— National Emission Standards for Indi vidual Drain Systems. (c) For each transfer s ys tem that is subject to this section but is not an individual drain sy stem, the owner or operator shall control air emissions by using one of the transfer sy stems specified in paragraphs (c)(1) through (c)(3) o f this section. (1) A transfer s ys tem that uses covers in accordance with the requirements specified in paragraph (d) of this section.(2) A transfer s ys tem 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 s ys tem that is enclosed and vented through a closed

- vent s ys tem to a control device in accordance with the requirements specified in paragraphs (c)(3)(i) and (c)(3)(ii) of this section. (i) The transfer s ys tem 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 when 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 s ys tem using c overs 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 sy stem except for the openings at the inlet and outlet to the transfer s ys tem through which the off

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

- site material through the transfer s ys tem 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 betw een 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 s ys tem through which the off

- site material passes, each opening in the cover shall be equipped with a closur e 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 c over 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 cover and closure devices shall include: organic vapor permeability ; the effects of any contact with the material or its vapors conveyed in the transfer s ys tem; the effects of outdoor exp osure to wind, moisture, and sunlight; and the operating practices used for the transfer s ys tem on which the cover is installed. (5) Whenever an off

- site material is in the transfer sy stem, the cover shall be installed with each closure device secured in the closed position , except the o pening of closure devices or removal of the cover is allowed to provide access to the transfer s ys tem 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 insid e the sy stem. 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.

. (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: Proces s 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 s ys tem to a control device that meets the standards specified in §63.693 of this subpart. For the purpose of complying with this paragraph (b), a primary condenser is not a control device; howeve r, a second condenser or other organic recovery device that is operated downstream of the primary condenser 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) through (iii) of this subpart , the 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 1 through 61.247 in 40 CFR part 61, subpart V

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

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

. (iii) On or after [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) or the requirements of 40 CFR 63.167(a)(2) , the open end is sealed wheninstrument mon itoring 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 [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) or the requirements of 40 CFR 63.167(d) , o pen - ended valves or lines in an emergency

shutdown s ys tem which are designed to open automaticall y in the event of a process upset and that are exempt from the requirements in 40 CFR 61.242

- 6(a), (b) , and (c) or 40 CFR 63.167(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 b y 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 b y M ethod 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 [DATE OF PUBLICATION OF THE FINAL RULE IN THE **FEDERAL REGISTER** ], for the purpose of compl yi ng 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 [DATE OF PUBLICATION OF THE FINAL RULE IN THE **FEDERAL REGISTER** ], for the pur pose of compl yi ng with the requirements of 40 CFR 6 3

. 167 (d), o pen ended valves or lines in an emergency shutdown sy stem 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, the pressure relief device requirements of § 63.691(c) of this subpart rather than those of 40 CFR 63.165 or of 40 CFR 61.242

- 4, as applicable, shall appl y. The pressure relief device requirements of § 63.691(c)(3) and (4) of this subpart appl y in addition to the requirements of 40 CFR 63.169 or of 40 CFR 61.242

- 8, as applicable , for pressure relief devices i n liquid service

. (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 gas /vapor service with an instrument reading of less than 500 ppm above background as detected b y M ethod 21 of 40 CFR part 60, a ppendix A. (2) Pressure release requirements

. For pressure relief devices in gas /vapor s ervice, the owner or operator must compl y 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 b y Method 21 of 40 CFR part 60, appendix A, no later than 5 calendar day s after the pressure rel ease device returns to off

- site material service following 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 day s 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 directl y 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) through (iii) of this subpart , the owner or operator must compl y 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 must equip each pressure relief device in off

- site material service with a device(s) or use a monitoring s ys tem . The device or monitoring s ys tem may be either specific to the pressure release device itself or may be associated with the process sy stem or piping, sufficient to indicate a pressure release to the atmo sphere. Examples of these ty pes of devices 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 sy stem
. The devices or monito ring s ystems must be capable of meeting the requirements specified in paragraphs (c)(3)(i)(A) through (C) of this section. (A) I dentifying the pressure release; (B ) R ecording the time and duration of each pressure release ; and (C ) N otifying operators immediately that a pressure release is occurring. (ii) If an y pressure relief device in off

- site material service releases directl y 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 pressure release event and report this quantity as required i n § 63.697(b)(5) of this subpart . Calculations may be based on data fromthe pressure relief device monitoring alone or in combination with process parameter monitoring

data and process knowledge. (4) Pressure relief devices routed to a drain s ys tem, fuel gas s ys tem, 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 sy stem to a control device or to a drain sy stem, fuel gas s ys tem, process or control device , paragraphs (c)(1), (2), and (3) of this section do not apply

. T he fuel gas s y s tem or closed vent sy stem and the process or control device (if applicable) must meet the requirements of § 63. 693 of this subpart . The drain sy stem (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 sy stems 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 sy stem 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 sy stem th at 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 and design of the contro l device selected b y the owner or operator to comply with the provisions of this section. (3) Whenever gases or vapors containing HAP are routed from a tank through a closed

- vent sy stem connected to a control device used to comply with the requirements of § 63.6 8 5(b ) (1), (2) or (3) of this subpart , the control device must be operating except as provided for in paragraph s (b)(3)(i) and (b)(3)(ii) of this section. (i) T he control device may onl y be by passed for the purpose of performing planned routine maintenance of the closed

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

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

- vent s ys tem or control device is b ypassed to perform routine maintenance shall not exceed 240 hours per each calendar year. (4) The owner or operator mu st inspect and monitor each closed

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

- vent sy stem in accordance with the

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

- vent sy stem 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 operat ion of each control device in accordance with the requirements specified in paragraphs (d) through (h) of this section as applicable to the type and design of the control device selected b y the owner or operator to comply with the provisions of this sectio n. (6) The owner or operator shall maintain records for each control device in accordance with the requirements of §63.696 of this subpart. (7) The 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 anal ys is to demonstrate compliance of a control device with the applicable performance requirements specified in this section as provided for in paragraphs (d) through (g) of this section, the Administrator may require that the design analy sis be revised or amended by the owner or operator to correct any deficiencies identified b y the Administrator. If the owner or operator and the Administrator do not agree on the acceptability of using the design analy sis (including any changes required by

the Administrator) to demonstrate that the control device achieves the applicable performance requirements, then the disagreement must be resolved using the results of a performance test conducted b y the owner or operator in accordance with the requirements of §63.694(l) of this subpart. The Administrator 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 anal ys is, then the results of the performance test will be used to establish compliance with this subpart. (c) Closed

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

- vent sy stems: (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 close d

- vent sy stem that is designed to operate at a pressure below atmospheric pressure.

The sy stem shall be equipped with at least one pressure ga u ge or other pressure measurement device that can be read from a readil y accessible location to verify that negati ve pressure is being maintained in the closed

- vent sy stem when the control device is operating. (2) In situations when the closed

- vent s ys tem includes by pass devices that could be used to divert a vent stream from the closed

- vent s ys tem to the atmosphere at a point upstream of the control device inlet, each by pass 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 , 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 b yp ass line used to divert the vent stream from the closed

- vent sy stem 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 reco rds of all periods when flow is detected or the flow indicator is not operating. (ii) 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 b ypass 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

- key configuration valve. (iii) Equipment needed for safety reasons, including l ow leg drains, open - ended valves and lines not in emergency

shutdown sy stems , 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 sy stem 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 total HAP listed in Table 1 of this subpart contained in the vent stream entering the carbon adsorption sy stem. (2) The owner or operator must demonstrate that the carbon adsorption s ys tem achieves the performance requirements in paragraph (d)(1) of this section by either performing a performance test as specified in paragraph (d)(2)(i) of this section or a design analy sis as specified in paragraph (d)(2)(ii) of this section. (i) An owner or operator choosing to use a performance tes t 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 anal ys is to demonstrate compliance must

include as part of this design analy sis the info rmation specified in either paragraph (d)(2)(ii)(A) or (d)(2)(ii)(B) of this section as applicable to the carbon adsorption sy stem design. (A) For a regenerable carbon adsorption sy stem, the design anal ys is shall address the vent stream composition, consti tuent 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, design 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 adsorption sy stem (e.g., a carbon canister), the design anal ys is 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, carbon bed capacity , activated carbon ty pe 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 the operation of the carbon adsorption sy stem in accordance with the requirements of §63.695(e) using one of the continuous monitoring sy stems specified in paragraphs (d)(3)(i) through (iii) of this section. Monitoring the operatio n of a nonregenerable carbon adsorption sy stem ( e.g., a carbon canister) using a continuous monitoring sy stem 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 section. (i) For a regenerat ive

- ty

pe carbon adsorption s ys tem: (A) A continuous parameter monitoring s ys tem to measure and record the average total regeneration stream mass flow or volumetric flow during each carbon bed regeneration cycle. The integrating regenerating stream flow mon itoring device must have an accuracy of ±10 percent; and (B) A continuous parameter monitoring s ys tem to measure and record the average carbon bed temperature for the duration of the carbon bed steaming cycle and to measure the actual 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 is greater. (ii) A continuo us monitoring s ys tem to measure and record the dail y average concentration level of organic compounds in the exhaust gas stream from the control device. The organic monitoring sy stem must comply

either with Performance Specification 8 or 9 in 40 CFR part 6 0, appendix B. The relative accuracy

provision of Performance Specification 8, Sections 2.4 and 3 need not be conducted.(iii) A continuous monitoring s ys tem that measures other alternative operating parameters upon

approval of the Administrator as specifi ed 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 sy stem, as follows: (i) Following the initial startup of the control device, all carbon in the control device shall be rep laced with fresh carbon on a regular, predetermined time interval that is no longer than the carbon service life established for the carbon adsorption sy stem. The provisions of this paragraph (d)(4)(i) do not appl y to a nonregenerable carbon adsorption sys tem ( 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 from the carbon adsorption sy stem 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 owner or operator has been i ssued 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) Reg enerated 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 operat or 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 permit 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 sy stem may choose toreplace on a regular basis the carbon canister or the carbon in the c ontrol 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 sy stem means a carbon adsorption sy stem 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 sy stem 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 sy stem on a regular schedule, and when carbon breakthrough is indicated, immediately

replace either the existing carbon canister with a new carbon cani ster 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 for the composition of organic constituents in the vent stream and is routinel y 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 the time required to consum e 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 carbon in the control devic e 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 requirements. (1) The condenser mus t 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 the vent stream entering th e 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 condenser achieves the perform ance requirements in paragraph (e)(1) of this section b y either performing a performance test as specified in paragraph (e)(2)(i) of this section or a design anal ys is as specified in paragraph (e)(2)(ii) of this section. (i) An owner or operator choosing t o 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 anal ys is to demonstrate compliance must include as part of this design analy sis the following information: description of the vent stream composition, constituent concentrations, flow rate, relative humidity , and temperature; andspecification of the design outlet organic compound concentration level, design average

te mperature 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 with the requirements of §63.695 (e) of this subpart using one of the continuous monitoring s ys tems specified in paragraphs (e)(3)(i) through (e)(3)(iii) of this section. (i) A continuous parameter monitoring s ys tem to measure and record the daily average temperature 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 s ys tem to measure and record the daily average concentration level of organic compounds in the exhaust gas stream from the control device. The organic monitoring sy stem 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 s ys tem 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) Destro y the total organic compounds (TOC), less meth ane 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 p pmv on a dry basis corrected to 3 percent oxygen. (ii) Destro y 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 i ncinerator 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 ox ygen. (iii) Maintain the conditions in the vapor incinerator combustion chamber 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 conducting either a performance tes t as specified in paragraph (f)(2)(i) of this section or a design anal ys is as specified in paragraph (f)(2)(ii) of this section , except as provided for in paragraph (f)(2)(iii) 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 anal ys is to demonstrate compliance must include as part of this design analy sis the informat ion 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 analy sis shall address the vent stream composition, constituent concentrations, and flow rate and shall establish the design minimum and average temperatures in the combustion chamber and the combustion chamber residence time. (B) For a cataly

tic vapor incinerator, the design analy sis shall address the vent stream composition, constituent concentrations, and flow rate and shall establish the design minimum and average temperatures across the catal ys t bed inlet and outlet, and the design service life of the catal ys t. (iii) An owner or operator is not required to conduct a performance te st or design anal ys is if the incinerator has been issued a final permit under 40 CFR part 270 and complies with the requirements of 40 CFR part 264, subpart O, or has certified compliance with the interim status requirements of 40 CFR part 265, subpart O. (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 sy stems specified in paragraphs (f)(3)(i) through (f)(3)(iv) of this section as applicable to the ty pe of vapor incinerator used. (i) For a thermal vapor incinerator, a continuous parameter monitoring s ys tem to measure and record the dail y 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 catal yt ic 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 nearest feasible point to the cataly st bed inlet and a second temperature sensor shall be installed in the vent stream at the nearest fe asible point to the cataly st bed outlet. (iii) For either ty

pe of vapor incinerator, a continuous monitoring sy stem to measure and record the daily average concentration of organic compounds in the exhaust vent stream from the control device. The organic m onitoring s ys tem must comply either with PerformanceSpecification 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. (iv) For either type of vapor incinerator, a continuous monitoring sy stem 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) Destro y the total organic compounds (TOC), less methane and ethane, contained in the vent stream introduced into the flame zone of the boiler 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) Destro y 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 ox ygen. (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 ; or has certified compliance with the interim status requirements of 40 CFR part 266, subpart H ; 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 d emonstrate 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 applicable method specified in paragraph (g)(2)(i) or (g)(2)(ii) of this section. (i) If an o wner or operator chooses to compl y 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 demonstrate compliance with the applicable performance specifications by conducting either a performance test as specified in paragraph (g)(2)(i)(A) of this section or a design anal ys is as specified in paragraph (g)(2)(i)(B) of this section , except as provided for in paragraph (g)(2)(i)(C) of this section

. (A) 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. (B) An owner or operator choosing to use a design anal ys is to demonstrate compliance must include as part of this design analy sis 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 residence time; and d escription of the method and location b y which the vent stream is introduced into the flame zone. (C) An owner or operator is not required to conduct a performance test or design anal ys is if the boiler or process heater has been issued a final permit under 40 CFR part 270 and complies with the requirements of 40 CFR part 266, subpart H; or has certified compliance with the interim status requirements of 40 CFR part 266, subpart H. (ii) If an owner or operator chooses to compl y with the performance specifications in either paragraph (g)(1)(iv) or (g)(1)(v) of this section, the owner or operator must demonstrate compliance b y maintaining the records that document that the boiler or process heater is designed and operated in accordance with the applicable requi rements of this section. (3) For a boiler or process heater complying 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) of this subpart using one of the continuous monitoring s ys tems specified in paragraphs (g)(3)(i) through (g)(3)(iii) of this section. (i) A continuous parameter monitoring s ys tem 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 s ys tem to measure and rec ord the dail y average concentration of organic compounds in the exhaust vent stream from the control device. The organic monitoring sy stem must comply

either with Performance Specification 8 or 9 in 40 CFR part 60, appendix B. The relative accuracy

provisi on of Performance Specification 8, Sections 2.4 and 3 need not be conducted.(iii) A continuous monitoring s ys tem that measures alternative operating parameters other than

those specified in paragraph (g)(3)(i) or (g)(3)(ii) of this section upon approval o f 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 speci fied 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 perf

orms all of the procedures specified in paragraphs (h)(2)(i)(A) through (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 owne r or operator determines the net heating value of the gas being combusted 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 requirement s applicable to the flare design as specified in 40 CFR 63.11(b)(7) or 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 flare 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 spe cified 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 monito r 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 e ach 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 tes ting 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 specified §63.683 of this subpart, the te sting 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 specified §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 ar e 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 specified in paragraph (e) of this sec tion. (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 process required HAP biodegradation effi ciency (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 mass removal rate (MR bio ) for compl iance 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 tanks 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 specified in paragraph (k) of this sectio n.(11) To determine closed

- vent sy stem 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 section. (12) To determine process ve nt 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 determi ne 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 measurement 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 the container, pipeline, or other de vice 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 adequatel y representative sample is collected and maintained for anal ys is by the selected metho d. (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 an y time interval that the owner or o perator 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 th at 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 normal variations are seasonal variations i n 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 sampling plan. This plan shall describe th e procedure b y 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 b y which sample integrity is maintained. A cop y of the written s ampling 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 f or Evaluating Solid Waste, Phy sical/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 anal yz ed 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 method is used to anal yz e 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 an y more re cent, updated version of Method 8260 approved b y 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 mu st 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 anal ys is. ( 3 ) Measurement of the average accuracy 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 anal yt es. (H) Method 8270 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 an y more recent, updated version of Method 8270 approved b y the EPA. For the purp ose 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 volati le 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 a ssurance procedures followed during sampling, sample preparation, sample introduction, and anal ys is. ( 3 ) Measurement of the average accuracy 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 anal yt es. (I) An y other anal ys is 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 is required under section 6.3.3 of Meth od 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 basis shall be calculated b y using the re sults 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 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 mu ltiplied 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 b y 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 determine 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 bas is 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 off

- site mate rial 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 are 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 anal yt ical variability

are accounted for in the determination of the average VOHAP concentration. 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 material sample s 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 concentration u sing 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 that the owner or operator perform this determi nation 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 adequatel y representative sample is collected and maintained for anal ys is by the selected method. (i) The averaging period to be used for determining the average VOHAP concentrati on for the off

- site material stream on a mass

- weighted average basis shall be designated and recorded. The averaging period can represent an y 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 period due t o 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 b y 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 b y which sample integrity is maintained. A cop y 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, Phy sical/Chemical Methods,” EPA Publication No. SW

- 846 or Method 25D in 40 CFR part 60, appen dix 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 purpose of m easuring the HAP listed in Table 1 of this subpart. (3) Calculations. The average VOHAP concentration (C ̅ ) a mass - weighted basis shall be calculated b y using the results for all samples analyzed in accordance with paragraph (c)(2) of this section and the f

ollowing 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 be en 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.

Where: C̅ = Average VOHAP concentration of the off

- 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 b y 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. (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 concentration of eac h 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 b y using the results determined for each individual off

- sit e 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= In dividual off

- site material stream “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 treat ed b y process. Q x=Total mass quantity

of off

- site material stream “x”, kg/yr. Q y=Total mass quantity

of off

- site material stream “y”, kg/yr. C̅ 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 secti on 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 poi nt
- of

- delivery , the average volumetric 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 b y using the average VOHAP concentration, averag e volumetric flow rate, and density determined 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

- delivery as determined in §63.694(b). n = Total number of “y” streams treated by process. Vy = Average volumetric flow rate of stream “y” at the point

- of

- delivery , m 3 /hr. k y = Density

of stream “y”, kg/m 3

. C̅ 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 conse cutive runs. The sampling time for each 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 determined 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 treatment 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 process shall be identified. The owner or operator shall prepare a sampling plan for measuring the identified streams that accuratel y reflects the retention time of the material in the process. (3) For each run, inf

ormation shall be determined for each stream 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) o f 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 determ ined 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 exitin g the process (E a ) shall be calculated using 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 = Mass 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 i n 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 biode graded 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 consecutive runs. The sampling tim e 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 HAP 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 paragraphs (i)(2) and (i)(3), res pectivel y, 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 HAP 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 of the off

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

- site material is collected such that a minimum loss of organics occurs throughout the sample collection and handling process and b y which sample integrity is maintained. A cop y 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, Phy sical/Chemical Methods,” EPA Publication No. SW

- 846 or Method 25D in 40 CFR part 60, appendix A.(ii) Anal ys is. 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 a ppendix 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) An y other method approved b y 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 knowledge that the maximum HAP vapor pressure of the off

- site material is less than the maximum vapor pressure limit listed in Table 3 , 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 the 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 compl yi ng with this subpart. (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 cover and 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 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 m ethane 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 trav ersing 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 accessibl e portions of the interface shall be sampled. In the case when the configuration of the closure device prevents any s ampling at the interface and the device is equipped with an enclosed extension or horn (e.g., some pressure relief devices), the instrument 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 paragrap h (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 b y the detection instrument 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 level , 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 sectio n.(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 paragrap h (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 based on representative performance (i.e., performance based on normal operating conditions) and shall exclude periods or startup and shutdown unless spec ified b y the Administrator

. The owner or operator may

not conduct performance tests during periods of malfunction. The owner or operator must record the process information that is necessary to document operating conditions during the test and include in s uch record an explanation to support that such conditions represent normal operation. Upon request, the owner or operator shall make available to the Administrator such records as may be necessary

to determine the conditions of performance tests. (1) Metho d 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 location 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 o utlet of the device. (2) The gas volumetric flow rate shall be determined using Method 2, 2A, 2C, 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 to measure the HAP in Table 1 of this subpart or Method 25A of 40 CFR 60, appendix A 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 lternatively , any other method or data that has been validated according to the applicable procedures in Method 301 in 40 CFR part 63, appendix A may be used. The following procedures shall be used to calculate percent reduction efficiency :(i) A minimum of three sample runs must be performed. The minimum sampling time for each

run shall be 1 hour

. For Method 18, 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 ,respectivel y) 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, respectivel y, 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 average concentration reading (minus methane and ethane) measured b y Method 25A of 40 CFR part 60, appendix A shall be used in 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:

Rcd=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 b y comparing the TOC (minus methane and ethane) or total 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 measured concentration may

be subtracted from the Method 25A measurement. Alternativel y, an y other method or data that has been validated according to Method 301 in appendix A of this part, may be used. T he following procedures shall be used to calculate parts per million by volume concentration, corrected to 3 percent ox ygen: (i) A minimum of three sample runs must be performed. The minimum sampling time for each run shall be 1 hour . For Method 18, 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 o r 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 average concentration readings provided by Method 25 A of 40 CFR part 60, appendix A, minus the concentration of methane and ethane. (B) The total HAP concentration (C HAP ) shall 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 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 anal ys is procedures of Method 3B of 40 CFR part 60, appendix A shall be used to determine the ox ygen concentration (%O 2dry). Alternatively , the owner or operator may use Method 3A of 40 CFR part 60, appendix A to determine the ox ygen concentration. The samples s hall 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 ox yg en (C c ) shall 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 million by volume. %O 2dr y=Concentration of oxygen, dry bas is, 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 determined using Method 2, 2A, 2C, 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 mil lion 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 must be taken at approximately

equal intervals in ti me, 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 mill ion by

volume. Cji = 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. 

## §63.695 **Inspection and monitoring requirements.** (a) The owner or operator must install, calibrate, maintain, and operate all monitoring sy stem components according to § § 63.8 of this part , 63.684(e), 63.693(d)(3), (e)(3), (f)(3), (g)(3), and (h)(3) of this subpart , and paragraph ( 5 ) of this section and perf orm the inspection and monitoring procedures 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 s ys tems for compliance with the standards specified in §63.693 of this subpart, the in spection and monitoring procedures are specified in paragraph (c) of this section. (3) To inspect and monitor transfer s ys tem covers for compliance with the standards specified in §63.689(c)(1) of this subpart, 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 specified in paragraph (e) of this section. ( 5)(i ) Except for periods of monitoring s ys tem malfunctions, repairs associated with monitoring sy stem malfunctions and required monitoring s ys tem quality assurance or quality

control activities (including, as applicable, calibration checks and required zero and span ad justments), the owner or operator must operate the continuous monitoring sy stem at all times the affected source is operating. A monitoring s ys tem malfunction is any sudden, infrequent, not reasonabl y preventable failure of the monitoring sy stem 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 s ys tem repairs in response to monitoring sy stem malfunctions and to return th e monitoring s ys tem to operation as expeditiously as practicable. (ii ) The owner or operator may not use data recorded during monitoring s ys tem malfunctions, repairs associated with monitoring s ys tem malfunctions, or required monitoring s ys tem quality ass urance 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 assessing the operation of the control device and associat ed control s ys tem. The owner or operator must report an y periods for which the monitoring s ys tem failed to collect required data. (b) Tank Level 2 fixed roof and floating roof inspection requirements. (1) Owners 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 inspected by

the owner or operator to check for defe cts 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 s eals 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) Visuall y inspect the internal floating roof components through openings 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 seals (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 visuall y inspect the internal floating roof, primary and secondary seals, gaskets, slo tted 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 §63.6 97 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 subpart 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 the primary seal within 60 day s after initial o peration 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 the 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 day s 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

- site material for a period of 1 ye ar or more, sub sequent 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 total 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 ) Seal gaps, if an y, 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 distan ce of each such location. ( 3 ) For a seal gap measured under paragraph (b)(2) of this section, the gap surface area shall be determined b y using probes of various widths to measure accuratel y the actual distance from the tank wall to the seal and multiplyin g each such width by its respective circumferential distance. ( 4 ) The total gap area shall be calculated b y 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 typ e by the nominal diameter of the tank. These total gap areas for the primary seal and secondary

seal are then compared to the respective standards for the seal ty pe 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) of 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 deck 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, ac cess 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 op erator 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) Own ers and operators that use a tank equipped with a fixed roof in accordance with the

provisions of §63.685(g) of this subpart shall meet the following requirements: (i) The fixed roof and its closure devices shall be visually inspected b y 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 entirel y 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., 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 once every calendar ye ar 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 defec t in accordance with the requirements of paragraph (b)(4) of this section. (iv) The owner 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 requirements 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 day s of detecting the defect e ither 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 tw o 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 sche dule 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 d efect 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 sy stem that is used t o comply with §63.693(c)(1)(i) of this subpart shall be inspected and monitored in accordance with the following requirements:(i) At initial startup, the owner or operator shall monitor the closed

- vent s ystem components and

connections using the procedure s specified in §63.694(k) of this subpart to demonstrate that the closed

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

- vent s ys tem as follows: (A) Closed

- ve nt s ys tem 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 component or connection 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 replaced 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 the procedures specified in §63.694(k) of this subpart to demonstrate that components or connections operate with no detectable organic emissions. (C) The continuous monito ring s ys tem required by §63.693(b)(4)(i) shall monitor and record either an instantaneous 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 the b yp ass 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 ac cordance 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 sy stem th at is used to comply with §63.693(c)(1)(ii) of this subpart shall be inspected and monitored in accordance with the following requirements: (i) The closed

- vent s ys tem shall be visually inspected by

the owner or operator to check for defects that could resu lt 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 followi ng installation of the closed

vent sy stem. Thereafter, the owner or operator must perform 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 operator shall make first efforts at repair of the defect no later than 5 calendar day s after detection and repair shall be completed as soon as possible but no later than 45 calendar day s after detection. (ii) Repair of a defect may be delayed beyond 45 calendar day s 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 tim e the process or unit that vents to the closed

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

- vent sy stem. (B) The owner or operator determines that the air 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 s ys tem 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 s ys tem equipped with a cover in accordance with the provisions of §63.689(c)(1) of this subpart shall meet the following inspection requirements: (1) The cover and its closure devices shall be visually inspected b y the owner or operato r to check for defects that could result in air emissions. Defects include, but are not 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 devices. In the case when a transfer s ys tem is buried partiall y or entirely underground, inspection is required onl y 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, th e owner or operator must perform the inspections at least once every calendar year except 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 req

uirements of paragraph (d)(5) of this section.(4) The owner or operator shall maintain 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 later than 5 calendar day s after detection and repair shall be completed as soon as possible but no later than 45 calendar day s after detection except as provided in paragraph (d)(5)(ii) of this section. (ii) Repair of a defect may be delayed beyond 45 calendar day s if the owner or operator determines that repair of the defect requires emptying or temporary removal from service of the transfer s ys tem and no alternative transfer s ys tem is available at the site to accept the material normally handled by

the sy stem. In this case, the owner or operator shall repair the defect the next time the process or unit that is generating the material handled b y the transfer s ys tem stops operation. Repair of the defect must be completed before the process or unit resumes operation. (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 properl y b y monitoring the control device in accordance with the requirements specified in paragraphs (e)(1) through (e)( 5 ) of this section. (1) A continuous parameter monitoring s ys tem must be used to measure the operating parameter or parameters specified for the c ontrol 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 sy stem must meet the following specifications and requirements: (i) The continuous parameter moni toring s ys tem must measure either an instantaneous 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 pe riod 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 o f all measured values. (ii) The monitoring s ys tem 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 op erating properl y. (2) Using the data recorded by the monitoring s ys tem, the owner or operator must calculate the daily average value for each monitored operating parameter for each operating day . If operationof 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 continuously 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 para graphs (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 anal ys is to demonstrate control devic e performance, then the minimum or maximum operating parameter value must be established based on the control device design analy sis and supplemented, as necessary, by the control device manufacturer recommendations or other applicable information. (4) A deviation for a given control device 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 multipl e operating parameters are monitored for the same control device and during the same operating day more than one of these operating parameters meets a deviation criterion specified in paragraphs (e)(4)(i) through (e)(4)(iii) of this section, then a single deviation is determined to have occurred for the control device for that operating day

. (i) A deviation occurs when the dail y 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 deviation occurs when the period of control device operation is 4 hours or greater in an 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 the 15

- minute periods within the hour. (iii) A 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 insufficient 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 deviation , except when the deviation occurs during periods 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) , 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.

(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 ye ar when an owner or operator determines 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 air 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 safel y access the air pollution control equipment. The required inspections and monitoring mus t be performed as frequentl y as practicable but do not need to be performed more frequentl y than the periodic schedule that would be otherwise applicable to the air pollution control equipment under the provisions of this section. A cop y of the written plan 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 ap plicable to this subpart as specified in Table 2 of this subpart. (b) The owner or operator 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 requirements specified in §63.685(e) of this subpart or using an external floating roof to complywith the tank control requirements specified in §63.685(f) of this subpart s hall 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 b y §63.695(b) of this subpart, as applicable to the tank, that includes the f

ollowing information: a tank identification number (or other unique identification description as selected b y the owner or operator) and the date of inspection. (3) The owner or operator shall record for each defect detected during inspections required b y §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 th e 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 maintain 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 m easurements 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 inc lude a description of the repairs that were made, the date the repairs were made, and the date 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 inspection required b y §63.695(b) of this subpart, as applicable to the tank, that includes the following information: a tank identification number (or other unique identi fication description as selected b y the owner or operator) and the date of inspection. (2) The owner or operator shall record for each defect detected during inspections required b y §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 b y the owner 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 Perman ent or Temporary Total Enclosure” under 40 CFR 52.741, appendix B.(g) An owner or operator 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) of 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 ty pe of maintenance performed and the total number 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

. (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 affected sources or equipment, an estimate of the volume of each regulated pollutant emitted over an y 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 an y corrective actions taken to return the affected unit 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 through a closed

- vent sy stem to a control device, process or drain s ys tem 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 sy stem that includes b yp ass 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 sy stem 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 release 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 ) Hourl y records of whether the by pass 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, hourl y 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 by pass 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 specifie d in paragraph (a)(2) and (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 operator subject to the initial notification 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 day s 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 sy stem to be implemented, including the pressure relief devices and process parameters to be monitored (if applicable), a description 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 ) through ( 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 b y 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 the EPA ’s Electronic Reporting Tool (ERT) as listed on the EPA’s ERT W eb site (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 ina 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, including 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 clearl y marked as CBI and mailed to U.S. EPA/OAPQS/CORE CBIOffice, Attention: Group L eader, Measurement Policy Group, MD C404

- 02, 4930 Old Page Roa d, 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 (a)(3)(i)

. (ii) For data collected using test methods that are not supported by the EPA ’s ERT as listed on the EPA’s ERT W eb site , 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 subm it the following notifications and reports to the Administrator: (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 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

. (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 de viations as defined in § 63.6 83(f) and § 63.695(e) of this subpart that have occurred during the 6

- month reporting period. For each deviation caused 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), the report must include the daily average values of the moni tored parameter, the applicable operating parameter limit, and the date and duration of the period that the deviation occurred. For each deviation caused b y lack of monitoring data, the report must include the date and duration of perio d 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 service subject to § 63.691(c) of this subpart , Periodic Reports must include the information specified in paragraphs (b)(5)(i) through ( i ii) of this section. (i) For pressure relief devices in off

- site material service subject to § 63.691(c) of this subpart , report the results of all monitoring condu cted 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 an y instrument reading of 500 ppm above background or greater, if detected more than 5 day s 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 the quantity of HAP listed in Table 1 of this subpart emitted during the pressure release and the method used 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 b yp ass deviation report. The owner or operator must submit to the Administrator the information specified in paragraph (b)(6) (i v ) of this section when an y of the condition s in paragraph s (b)(6) (i) through ( i ii) of this section are met. (i ) An y pressure tank closure device, as s pecified in § 63.685(h)(2) of this subpart, has released to the atmosphere. (ii ) Any closed vent s ys tem that includes by pass 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 sy stem 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 b ypass 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 meas ures 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 Administrator in advance of each inspection required under §6 3.695(b) of this subpart to provide 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 of the inspection as follows: (1) Prior to each ins pection 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 Administrator at least 30 calendar day s 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 notification shall be prepared and sent by the owner or operator so that it is received by the Administrator at least 30 calendar day s 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 day s before refilling the tank, the owner or operator shall notify the Administrator as soon as possible, but no later than 7 calendar day s before refilling of the tank. This notification may b e made b y t elephone and immediately followed by

a written explanation for why

the inspection is unplanned. Alternativel y, written notification, including the explanation for the unplanned inspection, may be sent so that it is received by the Administrator at least 7 calendar day s 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 applicable State, local, or Tribal agency . I f the U.S. EPA Administrator has delegated authority to a State, local, or Tribal agency , then that agency , in addition to the U.S. EPA, has the authority to implement and enforce this subpart. Contact the applicable U.S. EPA Regional Office to find out if this subpart is delegated to a State, local, or Tribal agency

. (b) In delegating implementation and enforcement authority of this subpart to a State, local, or Tribal agency

under subpart E of this part, the authorities contained in paragraph (c) of this section are re tained b y 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 ( 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) App roval 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 defined in §63.90, and as required in this subpart. (4) Ap proval 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 requirements 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 Acetaldeh yd e 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 Biphen yl 0.864 542

- 88

- 1 Bis(chlorometh yl )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

- Chlorobenzene 1.0007

67

- 66

- 3 Chloroform 1.000 107

- 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 (Eth yl ene dichloride) 1.000 111

- 44

- 4 Dichloroeth ylether (Bis(2

- chloroeth ylether) 0.757 542

- 75

- 6 1,3

- Dichloropropene 1.000 79

- 44

- 7 Dimethyl carbamo ylchloride 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

- Dieth yl eneoxide) 0.869 106

- 89

- 8 Epichlorohydrin (1

- Chloro

- 2,3

- epox yp ropane) 0.939 106

- 88

- 7 1,2

- Epox yb utane 1.000 140

- 88

- 5 Ethyl acrylate 1.000 100

- 41

- 4 Ethyl benzene 1.000 75

- 00

- 3 Ethyl chloride (Chloroethane) 1.000106

- 93

-

4 Ethylene dibromide (Dibromoethane) 0.999 107

- 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 butylether 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

- Propionaldehyde 0.9996

78

- 87

- 5 Propylene dichloride (1,2

- Dichloropropane) 1.000 75

- 56

- 9 Propylene oxide 1.000 75

- 55

- 8 1,2

- Propylenimine (2

- Methyl aziridine) 0.945 100

- 42

- 5 Sty

rene 1.000 96

- 09

- 3 Sty

rene oxide 0.830 79

- 34

- 5 1,1,2,2

- Tetrachloroethane 0.999 127

- 18

- 4 Tetrachloroeth yl ene (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 Trichloroeth yl ene 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

- Dichloroeth yl ene) 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 hydroly zes quickl y in water, but the hydrol ys is products are also HAP chemicals. c. Denotes a HAP that may react violently

with water, exercise caustic is an expected anal yt e. d. Denotes a HAP that hydroly zes slowl y in water. e. The f

m 305 factors for some of the more common gl ycol 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 Part 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(b)(1) No Subpart DD specifies its own applicability

. 63.1(b)(2) 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 Reserved 63.1(c)(5) Yes Except that sources are not required to submit notificationsoverridden b y 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)

- ( 2 ) Yes 63.4(a)(3) No Reserved 63.4(a)(4) No Reserved. 63.4(a)(5) No Reserved 63.4(b) Yes 63.4(c) Yes 63.5(a)(1) Yes 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) 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) No 63.6(b)(4) No63.6(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) No Reserved. 63.6(e)(3) No 63.6(f)(1) No 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) Yes 63.7(c) Yes 63.7(d) Yes 63.7(e)(1) No See § 63.694(l) of this subpart

. 63.7(e)(2) Yes63.7(e)(3) No Subpart DD specifies test methods and procedures.

63.7(e)(4) Yes 63.7(f) Yes 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 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) Yes 63.8(g) Yes 63.9(a) Yes 63.9(b)(1)(i) Yes 63.9(b)(1)(ii) No 63.9(b)(2) Yes63.9(b)(3) No

63.9(b)(4) Yes 63.9(b)(5) Yes 63.9(c) Yes 63.9(d) Yes 63.9(e) Yes 63.9(f) No 63.9(g) Yes 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
63.10(b)(2)(ii) No 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) Yes 63.10(b)(2)(iv) No 63.10(b)(2)(v) No 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) No 63.10(d)(4) Yes 63.10(d)(5) No See § 63.697(b)(3) of this subpart for reporting of malfunctions. 63.10(e) (1)

- (2) No 63.10(e)(3) Yes 63.10(e)(4) No63.10(f) Yes

63.11

- 63.15 Yes 63.16 No

aWherever subpart A specifies “postmark” dates, submittals may be sent by methods other than the U.S. Mail (e.g., b y 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**  **ma terial 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 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 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 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**  **ma terial 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 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 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 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**  **ma terial 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.