NR 440.675(6)(b)1.1. Where an owner or operator subject to this section seeks to demonstrate compliance with sub. (3) (a) through use of either a thermal or catalytic incinerator: NR 440.675(6)(b)1.a.a. The average firebox temperature of the incinerator, or the average temperature upstream and downstream of the catalyst bed for a catalytic incinerator, measured at least every 15 minutes and averaged over the same time period of the performance testing, and NR 440.675(6)(b)1.b.b. The percent reduction of TOC determined as specified in sub. (5) (b) achieved by the incinerator or the concentration of TOC (ppmv, by compound) determined as specified in sub. (5) (b) at the outlet of the control device on a dry basis corrected to 3% oxygen. NR 440.675(6)(b)2.2. Where an owner or operator subject to the provisions of this section seeks to demonstrate compliance with sub. (3) (a) through use of a boiler or process heater: NR 440.675(6)(b)2.a.a. A description of the location at which the vent stream is introduced into the boiler or process heater, and NR 440.675(6)(b)2.b.b. The average combustion temperature of the boiler or process heater with a design heat input capacity of less than 44 MW (150 million Btu/hr) measured at least every 15 minutes and averaged over the same time period of the performance testing. NR 440.675(6)(b)3.3. Where an owner or operator subject to the provisions of this section seeks to comply with sub. (3) (b) through the use of a smokeless flare, flare design, that is, steam-assisted, air-assisted or nonassisted, all visible emission readings, heat content determinations, flow rate measurements and exit velocity determinations made during the performance test, continuous records of the flare pilot flame monitoring and records of all periods of operations during which the pilot flame is absent. NR 440.675(6)(b)4.a.a. Where an absorber is the final recovery device in a recovery system, the exit specific gravity, or alternative parameter which is a measure of the degree of absorbing liquid saturation, if approved by the department, and average exit temperature of the absorbing liquid, measured at least every 15 minutes and averaged over the same time period of the performance testing, both measured while the vent stream is normally routed and constituted; or NR 440.675(6)(b)4.b.b. Where a condenser is the final recovery device in a recovery system, the average exit, that is, product side, temperature, measured at least every 15 minutes and average over the same time period of the performance testing while the vent stream is normally routed and constituted. NR 440.675(6)(b)4.c.c. Where a carbon adsorber is the final recovery device in a recovery system, the total steam mass flow measured at least every 15 minutes and averaged over the same time period of the performance test, that is, full carbon bed cycle, temperature of the carbon bed after regeneration, and within 15 minutes of completion of any cooling cycle, and duration of the carbon bed steaming cycle, all measured while the vent stream is normally routed and constituted; or NR 440.675(6)(b)4.d.d. As an alternative to subd. 4. a., b. or c., the concentration level or reading indicated by the organic monitoring device at the outlet of the absorber, condenser or carbon adsorber measured at least every 15 minutes and averaged over the same time period of the performance testing while the vent stream is normally routed and constituted. NR 440.675(6)(b)4.e.e. All measurements and calculations performed to determine the TRE index value of the vent stream. NR 440.675(6)(c)(c) Each owner or operator subject to the provisions of this section shall keep up-to-date, readily accessible continuous records of the equipment operating parameters specified to be monitored under sub. (4) (a) and (c) as well as up-to-date, readily accessible records of periods of operation during which the parameter boundaries established during the most recent performance test are exceeded. The department may at any time require a report of these data. Where a combustion device is used by an owner or operator seeking to demonstrate compliance with sub. (3) (a) or (c), periods of operation during which the parameter boundaries established during the most recent performance tests are exceeded are defined as follows: NR 440.675(6)(c)1.1. For thermal incinerators, all 3-hour periods of operation during which the average combustion temperature was more than 28°C (50°F) below the average temperature of the vent stream during the most recent performance test at which compliance with sub. (3) (a) was determined. NR 440.675(6)(c)2.2. For catalytic incinerators, all 3-hour periods of operation during which the average temperature of the vent stream immediately before the catalyst bed is more than 28°C (50°F) below the average temperature of the vent stream during the most recent performance test at which compliance with sub. (3) (a) was determined. The owner or operator also shall record all 3-hour periods of operation during which the average temperature difference across the catalyst bed is less than 80% of the average temperature difference of the device during the most recent performance test at which compliance with sub. (3) (a) was determined. NR 440.675(6)(c)3.3. All 3-hour periods of operation during which the average combustion temperature was more than 28°C (50°F) below the average combustion temperature during the most recent performance test at which compliance with sub. (3) (a) was determined for boilers or process heaters with a design heat input capacity of less than 44 MW (150 million Btu/hr). NR 440.675(6)(c)4.4. For boilers or process heaters, whenever there is a change in the location at which the vent stream is introduced into the flame zone as required under sub. (3) (a). NR 440.675(6)(d)(d) Each owner or operator subject to the provisions of this section shall keep up-to-date, readily accessible continuous records of the flow indication specified under sub. (4) (a) 2., (b) 2. and (c) 1. as well as up-to-date, readily accessible records of all periods when the vent stream is diverted from the control device or has no flow rate. NR 440.675(6)(e)(e) Each owner or operator subject to the provisions of this section who uses a boiler or process heater with a design heat input capacity of 44 MW (150 million Btu/hour) or greater to comply with sub. (3) (a) shall keep an up-to-date, readily accessible record of all periods of operation of the boiler or process heater. NR 440.675 NoteNote: Examples of such records could include records of steam use, fuel use or monitoring data collected pursuant to other state or federal regulatory requirements.
NR 440.675(6)(f)(f) Each owner or operator subject to the provisions of this section shall keep up-to-date, readily accessible continuous records of the flare pilot flame monitoring specified in sub. (4) (b), as well as up-to-date, readily accessible records of all periods of operations in which the pilot flame is absent. NR 440.675(6)(g)(g) Each owner or operator subject to the provisions of this section shall keep up-to-date, readily accessible continuous records of the equipment operating parameters specified to be monitored under sub. (4) (e) as well as up-to-date, readily accessible records of periods of operation during which the parameter boundaries established during the most recent performance test are exceeded. The department may at any time require a report of these data. Where the owner or operator seeks to demonstrate compliance with sub. (3) (c), periods of operation during which the parameter boundaries established during the most recent performance tests are exceeded are defined as follows: NR 440.675(6)(g)1.1. Where an absorber is the final recovery device in a recovery system and where an organic monitoring device is not used: NR 440.675(6)(g)1.a.a. All 3-hour periods of operation during which the average absorbing liquid temperature was more than 11°C (20°F) above the average absorbing liquid temperature during the most recent performance test or NR 440.675(6)(g)1.b.b. All 3-hour periods of operation during which the average absorbing liquid specific gravity was more than 0.1 unit above or more than 0.1 unit below, the average absorbing liquid specific gravity during the most recent performance test, unless monitoring of an alternative parameter, which is a measure of the degree of absorbing liquid saturation, is approved by the department, in which case the department will define appropriate parameter boundaries and periods of operation during which they are exceeded. NR 440.675(6)(g)2.2. When a condenser is the final recovery device in a recovery system and where an organic monitoring device is not used, all 3-hour periods of operation during which the average exit or product side condenser operating temperature was more than 6°C (11°F) above the average exit (product side) operating temperature during the most recent performance test. NR 440.675(6)(g)3.3. Where a carbon adsorber is the final recovery device in a recovery system and where an organic monitoring device is not used: NR 440.675(6)(g)3.a.a. All carbon bed regeneration cycles during which the total mass steam flow was more than 10% below the total mass steam flow during the most recent performance test; or NR 440.675(6)(g)3.b.b. All carbon bed regeneration cycles during which the temperature of the carbon bed after regeneration, and after completion of any cooling cycle, was more than 10% greater than the carbon bed temperature, in degrees Celsius, during the most recent performance test. NR 440.675(6)(g)4.4. Where an absorber, condenser or carbon adsorber is the final recovery device in the recovery system and an organic monitoring device approved by the department is used, all 3-hour periods of operation during which the average concentration level or reading of organic compounds in the exhaust gases is more than 20% greater than the exhaust gas organic compound concentration level or reading measured by the monitoring device during the most recent performance test. NR 440.675(6)(h)(h) Each owner or operator subject to the provisions of this section and seeking to demonstrate compliance with sub. (3) (c) shall keep up-to-date, readily accessible records of: NR 440.675(6)(h)1.1. Any changes in production capacity, feedstock type or of any replacement, removal or addition of recovery equipment or air oxidation reactors; NR 440.675(6)(h)3.3. The results of any performance test performed pursuant to the methods and procedures required by sub. (5) (d). NR 440.675(6)(i)(i) Each owner and operator subject to the provisions of this section is exempt from the quarterly reporting requirements contained in s. NR 440.07 (3). NR 440.675(6)(j)(j) Each owner or operator that seeks to comply with the requirements of this section by complying with the requirements of sub. (3) shall submit to the department semiannual reports of the following information. The initial report shall be submitted within 6 months after the initial startup date. NR 440.675(6)(j)2.2. All periods recorded under par. (d) when the vent stream is diverted from the control device or has no flow rate. NR 440.675(6)(j)3.3. All periods recorded under par. (e) when the boiler or process heater was not operating. NR 440.675(6)(j)4.4. All periods recorded under par. (f) in which the pilot flame of the flare was absent. NR 440.675 NoteNote: The requirements of par. (j) remain in force until and unless EPA, in delegating enforcement authority to a state under section 111 (c) of the act, approves reporting requirements or an alternative means of compliance surveillance adopted by such state. In that event, affected sources within the state will be relieved of the obligation to comply with par. (j), provided that they comply with the requirements established by the state.
NR 440.675(6)(L)(L) The department will specify appropriate reporting and recordkeeping requirements where the owner or operator of an affected facility seeks to demonstrate compliance with the standards specified under sub. (3) other than as provided under sub. (4) (a) to (d). NR 440.675(7)(a)(a) For purposes of this section “fixed capital cost of the new components”, as used in s. NR 440.15, includes the fixed capital cost of all depreciable components which are or will be replaced pursuant to all continuous programs of components which are commenced within any 2-year period following October 21, 1983. For purposes of this paragraph,“commenced” means that an owner or operator has undertaken a continuous program of component replacement or that an owner or operator has entered into a contractual obligation to undertake and complete, within a reasonable time, a continuous program of component replacement. *CAS numbers refer to the Chemical Abstracts Service Registry numbers assigned to specific isomers or mixtures of chemicals. Some isomers or mixtures that are covered by the standards do not have CAS numbers assigned to them. The standards apply to all of the chemicals listed, whether CAS numbers have been assigned or not.
NR 440.675 HistoryHistory: Cr. Register, July, 1993, No. 451, eff. 8-1-93; am. (4) (a) 1. (intro.), (d) 1. a., 3. a., (5) (e) 1. a., Register, December, 1995, No. 480, eff. 1-1-96; renum. (2) (a) (intro.) and 1. to 18. to be (2) (intro.) and (a) to (r), am. (2) (p), Register, November, 1999, No. 527, eff. eff. 12-1-99; CR 06-109: cr. (1) (d), renum. (4) (c) 3. to be (4) (d) and am., renum. (4) (d) and (e) to be (4) (e) and (f), renum. (5) (b) 5., (c), (d), (e) and (f) to be (5) (c), (d), (e), (f) and (g) and am. (5) (e) 1., 3. b., 5. and 6. and (f) 1. a. and b., am. (5) (b) 4. b. and c., (6) (e) and (g) (intro.) and (8) Register May 2008 No. 629, eff. 6-1-08; corrections in (1) (d) 2. and (2) (p) made under s. 13.92 (4) (b) 7., Stats., Register May 2008 No. 629. NR 440.68(1)(1) Applicability and designation of affected facility. NR 440.68(1)(a)(a) The provisions of this section are applicable to the following affected facilities located at a petroleum dry cleaning plant with a total manufacturer’s rated dryer capacity equal to or greater than 38 kilograms (84 pounds): Petroleum solvent dry cleaning dryers, washers, filters, stills and settling tanks. NR 440.68(1)(a)1.1. When the affected facility is installed in an existing plant that is not expanding the manufacturer’s rated capacity of its petroleum solvent dryer(s) the total manufacturer’s rated dryer capacity is the summation of the manufacturer’s rated capacity for each existing petroleum solvent dryer. NR 440.68(1)(a)2.2. When the affected facility is installed in a plant that is expanding the manufacturer’s rated capacity of its petroleum solvent dryers the total manufacturer’s rated dryer capacity is the summation of the manufacturer’s rated dryer capacity for each existing and proposed new petroleum solvent dryer. NR 440.68(1)(a)3.3. When the affected facility is installed in a new plant the total manufacturer’s rated dryer capacity is the summation of the manufacturer’s rated dryer capacity for each proposed new petroleum solvent dryer. NR 440.68(1)(a)4.4. The petroleum solvent dryers considered in the determination of the total manufacturer’s rated dryer capacity are those new and existing dryers in the plant that will be in service at any time after the proposed new source or modification commences operation. NR 440.68(1)(b)(b) Any facility under par. (a) that commences construction or modification after December 14, 1982, is subject to the requirements of this section, except that a dryer installed between December 14, 1982 and September 21, 1984, in a plant with an annual solvent consumption level of less than 17,791 liters (4,700 gallons), is exempt from the requirements of this section. NR 440.68(2)(2) Definitions. As used in this section, terms not defined in this subsection have the meanings given in s. NR 440.02. NR 440.68(2)(a)(a) “Cartridge filter” means a discrete filter unit containing both filter paper and activated carbon that traps and removes contaminants from petroleum solvent together with the piping and ductwork used in the installation of this device. NR 440.68(2)(b)(b) “Dryer” means a machine used to remove petroleum solvent from articles of clothing or other textile or leather goods, after washing and removing of excess petroleum solvent, together with the piping and ductwork used in the installation of this device. NR 440.68(2)(c)(c) “Manufacturer’s rated dryer capacity” means the dryer’s rated capacity of articles, in pounds or kilograms of clothing articles per load, dry basis, that is typically found on each dryer on the manufacturer’s name-plate or in the manufacturer’s equipment specifications. NR 440.68(2)(d)(d) “Perceptible leaks” means any petroleum solvent vapor or liquid leaks that are conspicuous from visual observation or that bubble after application of a soap solution such as pools or droplets of liquid, open containers or solvent, or solvent laden waste standing open to the atmosphere. NR 440.68(2)(e)(e) “Petroleum dry cleaner” means a dry cleaning facility that uses petroleum solvent in a combination of washers, dryers, filters, stills and settling tanks. NR 440.68(2)(f)(f) “Settling tank” means a container that gravimetrically separates oils, grease and dirt from petroleum solvent together with the piping and ductwork used in the installation of this device. NR 440.68(2)(g)(g) “Solvent filter” means a discrete solvent filter unit containing a porous medium that traps and removes contaminants from petroleum solvent together with the piping and ductwork used in the installation of this device. NR 440.68(2)(h)(h) “Solvent recovery dryer” means a class of dry cleaning dryers that employs a condenser to condense and recover solvent vapors evaporated in a closed-loop stream of heated air together with the piping and ductwork used in the installation of this device. NR 440.68(2)(i)(i) “Still” means a device used to volatilize, separate and recover petroleum solvent from contaminated solvent together with the piping and ductwork used in the installation of this device. NR 440.68(2)(j)(j) “Washer” means a machine which agitates fabric articles in a petroleum solvent bath and spins the articles to remove the solvent together with the piping and ductwork used in the installation of this device. NR 440.68(3)(a)(a) Each affected petroleum solvent dry cleaning dryer that is installed at a petroleum dry cleaning plant shall be a solvent recovery dryer. The solvent recovery dryers shall be properly installed, operated and maintained. NR 440.68(3)(b)(b) Each affected petroleum solvent filter that is installed at a petroleum dry cleaning plant shall be a cartridge filter. Cartridge filters shall be drained in their sealed housings for at least 8 hours prior to their removal. NR 440.68(3)(c)(c) Each manufacturer of an affected petroleum solvent dryer shall include leak inspection and leak repair cycle information in the operating manual and on a clearly visible label posted on each affected facility. Such information should state: To protect against fire hazards, loss of valuable solvents and emissions of solvent to the atmosphere, periodic inspection of this equipment for evidence of leaks and prompt repair of any leaks is recommended. The Wisconsin Department of Natural Resources recommends that the equipment be inspected every 15 days and all vapor or liquid leaks be repaired within the subsequent 15 day period.
NR 440.68 NoteNote: The administrator may approve the use of equipment of procedures that have been demonstrated to be equivalent, in terms of reducing VOC emissions, to those prescribed for compliance in this section, under 40 CFR 60.623. NR 440.68(5)(5) Test methods and procedures. Each owner or operator of an affected facility subject to the provisions of sub. (3) (a) shall perform an initial test to verify that the flow rate of recovered solvent from the solvent recovery dryer at the termination of the recovery cycle is no greater than 0.05 liters per minute. This test shall be conducted for a duration of no less than 2 weeks during which no less than 50% of the dryer loads shall be monitored for their final recovered solvent flow rate. The suggested point for measuring the flow rate of recovered solvent is the outlet of the solvent-water separator. Near the end of the recovery cycle the entire flow of recovered solvent should be diverted to a graduated cylinder. As the recovered solvent collects in the graduated cylinder the elapsed time is monitored and recorded in periods of greater than or equal to one minute. At the same time the volume of solvent in the graduated cylinder is monitored and recorded to determine the volume of recovered solvent that is collected during each time period. The recovered solvent flow rate is calculated by dividing the volume of solvent collected per period by the length of time elapsed during the period and converting the result with appropriate factors into units of liters per minute. The recovery cycle and the monitoring procedure should continue until the flow rate of solvent is less than or equal to 0.05 liter per minute. The type of articles cleaned and the total length of the cycle should then be recorded. NR 440.68(6)(6) Recordkeeping requirements. Each owner or operator of an affected facility subject to the provisions of this section shall maintain a record of the performance test required under sub. (5). NR 440.68 HistoryHistory: Cr. Register, September, 1986, No. 369, eff. 10-1-86; am. (2) Intro.), r. (4), Register, September, 1990, No. 417, eff. 10-1-90; CR 06-109: am. (1) (b) and (5) Register May 2008 No. 629, eff. 6-1-08. NR 440.682NR 440.682 Equipment leaks of VOC from onshore natural gas processing plants. NR 440.682(1)(1) Applicability and designation of affected facility: NR 440.682(1)(a)1.1. The provisions of this section apply to affected facilities in onshore natural gas processing plants. NR 440.682(1)(a)2.2. A compressor in VOC service or in wet gas service is an affected facility. NR 440.682(1)(a)3.3. The group of all equipment except compressors, as defined in sub. (2), within a process unit is an affected facility. NR 440.682(1)(b)(b) Any affected facility under par. (a) that commences construction, reconstruction or modification after January 20, 1984 is subject to the requirements of this section. NR 440.682(1)(c)(c) Addition or replacement of equipment, as defined in sub. (2), for the purpose of process improvement that is accomplished without a capital expenditure may not by itself be considered a modification under this section. NR 440.682(1)(e)(e) A compressor station, dehydration unit, sweetening unit, underground storage tank, field gas gathering system, or liquified natural gas unit is covered by this section if it is located at an onshore natural gas processing plant. If the unit is not located at the plant site, then it is exempt from the provisions of this section. NR 440.682(2)(2) Definitions. As used in this section, terms not defined in this subsection have the meanings given in s. NR 440.02 or 440.62.
