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40 C.F.R. §§ 60.692-1–60.692-5

5 sections in range

§60.692-1. Standards: General.

40 C.F.R. § 60.692-1

(a)
Each owner or operator subject to the provisions of this subpart shall comply with the requirements of §§ 60.692-1 to 60.692-5 and with §§ 60.693-1 and 60.693-2, except during periods of startup, shutdown, or malfunction.
(b)
Compliance with §§ 60.692-1 to 60.692-5 and with §§ 60.693-1 and 60.693-2 will be determined by review of records and reports, review of performance test results, and inspection using the methods and procedures specified in § 60.696.
(c)
Permission to use alternative means of emission limitation to meet the requirements of §§ 60.692-2 through 60.692-4 may be granted as provided in § 60.694.
(d)
(1)
Stormwater sewer systems are not subject to the requirements of this subpart.
(2)
Ancillary equipment, which is physically separate from the wastewater system and does not come in contact with or store oily wastewater, is not subject to the requirements of this subpart.
(3)
Non-contact cooling water systems are not subject to the requirements of this subpart.
(4)
An owner or operator shall demonstrate compliance with the exclusions in paragraphs (d)(1), (2), and (3) of this section as provided in § 60.697 (h), (i), and (j).
Notes, amendments, and revision history

Source

Source: 53 FR 47623, Nov. 23, 1988, unless otherwise noted.

Authority

Authority: 42 U.S.C. 7401 et seq.

Source

Source: 36 FR 24877, Dec. 23, 1971, unless otherwise noted.

§60.692-2. Standards: Individual drain systems.

40 C.F.R. § 60.692-2

(a)
(1)
Each drain shall be equipped with water seal controls.
(2)
Each drain in active service shall be checked by visual or physical inspection initially and monthly thereafter for indications of low water levels or other conditions that would reduce the effectiveness of the water seal controls.
(3)
Except as provided in paragraph (a)(4) of this section, each drain out of active service shall be checked by visual or physical inspection initially and weekly thereafter for indications of low water levels or other problems that could result in VOC emissions.
(4)
As an alternative to the requirements in paragraph (a)(3) of this section, if an owner or operator elects to install a tightly sealed cap or plug over a drain that is out of service, inspections shall be conducted initially and semiannually to ensure caps or plugs are in place and properly installed.
(5)
Whenever low water levels or missing or improperly installed caps or plugs are identified, water shall be added or first efforts at repair shall be made as soon as practicable, but not later than 24 hours after detection, except as provided in § 60.692-6.
(b)
(1)
Junction boxes shall be equipped with a cover and may have an open vent pipe. The vent pipe shall be at least 90 cm (3 ft) in length and shall not exceed 10.2 cm (4 in) in diameter.
(2)
Junction box covers shall have a tight seal around the edge and shall be kept in place at all times, except during inspection and maintenance.
(3)
Junction boxes shall be visually inspected initially and semiannually thereafter to ensure that the cover is in place and to ensure that the cover has a tight seal around the edge.
(4)
If a broken seal or gap is identified, first effort at repair shall be made as soon as practicable, but not later than 15 calendar days after the broken seal or gap is identified, except as provided in § 60.692-6.
(c)
(1)
Sewer lines shall not be open to the atmosphere and shall be covered or enclosed in a manner so as to have no visual gaps or cracks in joints, seals, or other emission interfaces.
(2)
The portion of each unburied sewer line shall be visually inspected initially and semiannually thereafter for indication of cracks, gaps, or other problems that could result in VOC emissions.
(3)
Whenever cracks, gaps, or other problems are detected, repairs shall be made as soon as practicable, but not later than 15 calendar days after identification, except as provided in § 60.692-6.
(d)
Except as provided in paragraph (e) of this section, each modified or reconstructed individual drain system that has a catch basin in the existing configuration prior to May 4, 1987 shall be exempt from the provisions of this section.
(e)
Refinery wastewater routed through new process drains and a new first common downstream junction box, either as part of a new individual drain system or an existing individual drain system, shall not be routed through a downstream catch basin.
Notes, amendments, and revision history

Source

Source: 53 FR 47623, Nov. 23, 1988, unless otherwise noted.

Authority

Authority: 42 U.S.C. 7401 et seq.

Source

Source: 36 FR 24877, Dec. 23, 1971, unless otherwise noted.

§60.692-3. Standards: Oil-water separators.

40 C.F.R. § 60.692-3

(a)
Each oil-water separator tank, slop oil tank, storage vessel, or other auxiliary equipment subject to the requirements of this subpart shall be equipped and operated with a fixed roof, which meets the following specifications, except as provided in paragraph (d) of this section or in § 60.693-2.
(1)
The fixed roof shall be installed to completely cover the separator tank, slop oil tank, storage vessel, or other auxiliary equipment with no separation between the roof and the wall.
(2)
The vapor space under a fixed roof shall not be purged unless the vapor is directed to a control device.
(3)
If the roof has access doors or openings, such doors or openings shall be gasketed, latched, and kept closed at all times during operation of the separator system, except during inspection and maintenance.
(4)
Roof seals, access doors, and other openings shall be checked by visual inspection initially and semiannually thereafter to ensure that no cracks or gaps occur between the roof and wall and that access doors and other openings are closed and gasketed properly.
(5)
When a broken seal or gasket or other problem is identified, first efforts at repair shall be made as soon as practicable, but not later than 15 calendar days after it is identified, except as provided in § 60.692-6.
(b)
Each oil-water separator tank or auxiliary equipment with a design capacity to treat more than 16 liters per second (250 gallons per minute (gpm)) of refinery wastewater shall, in addition to the requirements in paragraph (a) of this section, be equipped and operated with a closed vent system and control device, which meet the requirements of § 60.692-5, except as provided in paragraph (c) of this section or in § 60.693-2.
(c)
(1)
Each modified or reconstructed oil-water separator tank with a maximum design capacity to treat less than 38 liters per second (600 gpm) of refinery wastewater which was equipped and operated with a fixed roof covering the entire separator tank or a portion of the separator tank prior to May 4, 1987 shall be exempt from the requirements of paragraph (b) of this section, but shall meet the requirements of paragraph (a) of this section, or may elect to comply with paragraph (c)(2) of this section.
(2)
The owner or operator may elect to comply with the requirements of paragraph (a) of this section for the existing fixed roof covering a portion of the separator tank and comply with the requirements for floating roofs in § 60.693-2 for the remainder of the separator tank.
(d)
Storage vessels, including slop oil tanks and other auxiliary tanks that are subject to the standards in §§ 60.112, 60.112a, and 60.112b and associated requirements, 40 CFR part 60, subparts K, Ka, or Kb are not subject to the requirements of this section.
(e)
Slop oil from an oil-water separator tank and oily wastewater from slop oil handling equipment shall be collected, stored, transported, recycled, reused, or disposed of in an enclosed system. Once slop oil is returned to the process unit or is disposed of, it is no longer within the scope of this subpart. Equipment used in handling slop oil shall be equipped with a fixed roof meeting the requirements of paragraph (a) of this section.
(f)
Each oil-water separator tank, slop oil tank, storage vessel, or other auxiliary equipment that is required to comply with paragraph (a) of this section, and not paragraph (b) of this section, may be equipped with a pressure control valve as necessary for proper system operation. The pressure control valve shall be set at the maximum pressure necessary for proper system operation, but such that the value will not vent continuously.
Notes, amendments, and revision history

Amendments

[53 FR 47623, Nov. 23, 1988, as amended at 60 FR 43259, Aug. 18, 1995; 65 FR 61778, Oct. 17, 2000]

Source

Source: 53 FR 47623, Nov. 23, 1988, unless otherwise noted.

Authority

Authority: 42 U.S.C. 7401 et seq.

Source

Source: 36 FR 24877, Dec. 23, 1971, unless otherwise noted.

Amendments

[53 FR 47623, Nov. 23, 1988, as amended at 60 FR 43259, Aug. 18, 1995; 65 FR 61778, Oct. 17, 2000]

§60.692-4. Standards: Aggregate facility.

40 C.F.R. § 60.692-4

A new, modified, or reconstructed aggregate facility shall comply with the requirements of §§ 60.692-2 and 60.692-3.
Notes, amendments, and revision history

Source

Source: 53 FR 47623, Nov. 23, 1988, unless otherwise noted.

Authority

Authority: 42 U.S.C. 7401 et seq.

Source

Source: 36 FR 24877, Dec. 23, 1971, unless otherwise noted.

§60.692-5. Standards: Closed vent systems and control devices.

40 C.F.R. § 60.692-5

(a)
Enclosed combustion devices shall be designed and operated to reduce the VOC emissions vented to them with an efficiency of 95 percent or greater or to provide a minimum residence time of 0.75 seconds at a minimum temperature of 816 °C (1,500 °F).
(b)
Vapor recovery systems (for example, condensers and adsorbers) shall be designed and operated to recover the VOC emissions vented to them with an efficiency of 95 percent or greater.
(c)
Flares used to comply with this subpart shall comply with the requirements of 40 CFR 60.18.
(d)
Closed vent systems and control devices used to comply with provisions of this subpart shall be operated at all times when emissions may be vented to them.
(e)
(1)
Closed vent systems shall be designed and operated with no detectable emissions, as indicated by an instrument reading of less than 500 ppm above background, as determined during the initial and semiannual inspections by the methods specified in § 60.696.
(2)
Closed vent systems shall be purged to direct vapor to the control device.
(3)
A flow indicator shall be installed on a vent stream to a control device to ensure that the vapors are being routed to the device.
(4)
All gauging and sampling devices shall be gas-tight except when gauging or sampling is taking place.
(5)
When emissions from a closed system are detected, first efforts at repair to eliminate the emissions shall be made as soon as practicable, but not later than 30 calendar days from the date the emissions are detected, except as provided in § 60.692-6.
Notes, amendments, and revision history

Source

Source: 53 FR 47623, Nov. 23, 1988, unless otherwise noted.

Authority

Authority: 42 U.S.C. 7401 et seq.

Source

Source: 36 FR 24877, Dec. 23, 1971, unless otherwise noted.