NR 440.59(3)(d)(d) Within 60 days after achieving the maximum production rate at which the affected facility will be operated, but not later than 180 days after initial startup of such facility, no owner or operator subject to the provisions of this section may cause to be discharged into the atmosphere from any mineral handling and storage facility emissions with opacity greater than one percent. NR 440.59(4)(a)(a) The owner or operator subject to the provisions of this section, and using either an electrostatic precipitator or a high velocity air filter to meet either the emission limit in sub. (3) (a) 1. or (b) 1., or both, shall continuously monitor and record the temperature of the gas at the inlet of the control device. The temperature monitoring instrument shall have an accuracy of ± 15°C (± 25°F) over its range. NR 440.59(4)(b)(b) The owner or operator subject to the provisions of this section and using an afterburner to meet either the emission limit in sub. (3) (a) 1. or (b) 1., or both, shall continuously monitor and record the temperature in the combustion zone of the afterburner. The monitoring instrument shall have an accuracy of ± 10°C (± 18°F) over its range. NR 440.59(4)(c)(c) An owner or operator subject to the provisions of this section and using a control device not mentioned in par. (a) or (b) shall provide to the department information describing the operation of the control device and the process parameter or parameters which would indicate proper operation and maintenance of the device. The department may require continuous monitoring and determine the process parameters to be monitored. NR 440.59(4)(d)(d) The industry is exempted from the quarterly reports required under s. NR 440.07 (3). The owner or operator is required to record and report the operating temperature of the control device during the performance test and, as required by s. NR 440.07 (5), maintain a file of the temperature monitoring results for at least 2 years. NR 440.59(5)(a)(a) For saturators, the owner or operator shall conduct performance tests required in s. NR 440.08 as follows: NR 440.59(5)(a)1.1. If the final product is shingle or mineral-surfaced roll roofing, the tests shall be conducted while 106.6-kg (235-lb) shingle is being produced. NR 440.59(5)(a)2.2. If the final product is saturated felt or smooth-surfaced roll roofing, the tests shall be conducted while 6.8-kg (15-lb) felt is being produced. NR 440.59(5)(a)3.3. If the final product is fiberglass shingle, the test shall be conducted while a nominal 100-kg (220-lb) shingle is being produced. NR 440.59(5)(b)(b) In conducting the performance tests required in s. NR 440.08, the owner or operator shall use as reference methods and procedures the test methods in Appendix A of 40 CFR part 60, incorporated by reference in s. NR 440.17, or other methods and procedures as specified in this subsection, except as provided in s. NR 440.08 (2). NR 440.59(5)(c)(c) The owner or operator shall determine compliance with the particulate matter standards in sub. (3) as follows: NR 440.59(5)(c)1.1. The emission rate (E) of particulate matter shall be computed for each run using the following equation: where:
E is the emission rate of particulate matter, kg/Mg (lb/ton)
cs is the concentration of particulate matter, g/dscm (gr/dscf)
Qsd is the volumetric flow rate of effluent gas, dscm/hr (dscf/hr)
P is the asphalt roofing production rate or asphalt charging rate, Mg/hr (ton/hr)
K is the conversion factor, 1000 g/kg (7000 gr/lb)
NR 440.59(5)(c)2.2. Method 5A shall be used to determine the particulate matter concentration (cs) and volumetric flow rate (Qsd) of the effluent gas. For a saturator, the sampling time and sample volume for each run shall be at least 120 minutes and 3.00 dscm (106 dscf), and for the blowing still, at least 90 minutes or the duration of the coating blow or non-coating blow, whichever is greater, and 2.25 dscm (79.4 dscf). NR 440.59(5)(c)3.3. For the saturator, the asphalt roofing production rate (P) for each run shall be determined as follows: The amount of asphalt roofing produced on the shingle or saturated felt process lines shall be obtained by direct measurement. The asphalt roofing production rate is the amount produced divided by the time taken for the run. NR 440.59(5)(c)4.4. For the blowing still, the asphalt charging rate (P) shall be computed for each run using the following equation: where:
P is the asphalt charging rate to blowing still, Mg/hr (ton/hr)
V is the volume of asphalt charged, m3 (ft3)
d is the density of asphalt, kg/m3 (lb/ft3)
K’ is the conversion factor, 1000 kg/Mg (2000 lb/ton)
θ here is the duration of test run, hr
NR 440.59(5)(c)4.a.a. The volume (V) of asphalt charged shall be measured by any means accurate to within 10%. NR 440.59(5)(c)4.b.b. The density (d) of the asphalt shall be computed using the following equation: where:
d is the density of the asphalt, kg/m3 (lb/ft3)
K1 is 1056.1 kg/m3 for metric units and 64.70 lb/ft3 for English units
K2 is 0.6176 kg/(m3 °C) for metric units and 0.0694 lb/(ft3 °F) for English units
Ti is the temperature at the start of the blow, °C (°F)
NR 440.59(5)(d)(d) The department shall determine compliance with the standards in sub. (3) (a) 3. by using Method 22, modified so that readings are recorded every 15 seconds for a period of consecutive observations during representative conditions, in accordance with s. NR 440.08 (3), totaling 60 minutes. A performance test shall consist of one run. NR 440.59(5)(e)(e) The owner or operator shall use the monitoring device in sub. (4) (a) or (b) to monitor and record continuously the temperature during the particulate matter run and shall report the results to the department with the performance test results. NR 440.59(5)(f)(f) If at a later date the owner or operator believes that the emission limits in sub. (3) (a) and (b) are being met even though one of the conditions in subd. 1. or 2. exists, the owner or operator may submit a written request to the department to repeat the performance test and procedure outlined in par. (c). NR 440.59(5)(f)1.1. The temperature measured in accordance with sub. (4) (a) is exceeding that measured during the performance test. NR 440.59(5)(f)2.2. The temperature measured in accordance with sub. (4) (b) is lower than that measured during the performance test. NR 440.59 NoteNote: Under 40 CFR 60.474 (g), if fuel oil is to be used to fire an afterburner used to control emissions from a blowing still, the owner or operator may petition the administrator in accordance with 40 CFR 60.11 (e), to establish an opacity standard for the blowing still that will be the opacity standard when fuel oil is used to fire the afterburner. To obtain this opacity standard, the owner or operator must request the administrator to determine opacity during an initial, or subsequent, performance test when fuel oil is used to fire the afterburner. Upon receipt of the results of the performance test, the administrator will made a finding concerning compliance with the mass standard for the blowing still. If the administrator finds that the facility was in compliance with the mass standard during the performance test but failed to meet the zero opacity standard, the administrator will establish and promulgate in the Federal Register an opacity standard for the blowing still that will be the opacity standard when fuel oil is used to fire the afterburner. When the afterburner is fired with natural gas, the zero percent opacity remains the applicable opacity standard. NR 440.59 HistoryHistory: Cr. Register, January, 1984, No. 337, eff. 2-1-84; am. (2) (intro.), (3) (a) 1. a. and b. and (5) (k), Register, September, 1990, No. 417, eff. 10-1-90; am. (4) (d), r. and recr. (5), Register, July, 1993, No. 451, eff. 7-1-93; CR 06-109: am. (3) (a) 1., (b), (4) (a) to (c) and (5) (c) 1., r. and recr. (5) (c) 4. b., renum. (5) (f) to be (5) (f) (intro.) and am., cr. (5) (f) 1. and 2. Register May 2008 No. 629, eff. 6-1-08. NR 440.62NR 440.62 Equipment leaks of VOC in the synthetic organic chemicals manufacturing industry. NR 440.62(1)(1) Applicability and designation of affected facility. NR 440.62(1)(a)1.1. The provisions of this section apply to affected facilities in the synthetic organic chemicals manufacturing industry. NR 440.62(1)(a)2.2. The group of all equipment (defined in sub. (2)) within a process unit is an affected facility. NR 440.62(1)(b)(b) Any affected facility under par. (a) that commences construction or modification after January 5, 1981, shall be subject to the requirements of this section. NR 440.62(1)(c)(c) Addition or replacement of equipment for the purpose of process improvement which is accomplished without a capital expenditure is not by itself considered a modification under this section. NR 440.62(1)(d)1.1. If an owner or operator applies for one of the exemptions in this paragraph the owner or operator shall maintain records as required in sub. (7) (i). NR 440.62(1)(d)2.2. Any affected facility that has the design capacity to produce less than 1,000 Mg/yr (1,102 ton/yr) is exempt from sub. (3). NR 440.62(1)(d)3.3. If an affected facility produces heavy liquid chemicals only from heavy liquid feed or raw materials it is exempt from sub. (3). NR 440.62(1)(d)5.5. Any affected facility that has no equipment in VOC service is exempt from sub. (3). NR 440.62(1)(e)2.2. Owners or operators who choose to comply with 40 CFR part 65, subpart F, as in effect on December 14, 2000, shall also comply with ss. NR 440.01, 440.02, 440.05, 440.06, 440.07 (1) (a) and (d), 440.14 and 440.15 for that equipment. Any section or subsection from ss. NR 440.01 to 440.19 not specified in this subdivision does not apply to owners or operators of equipment subject to this section complying with 40 CFR part 65, subpart F, except that provisions required to be met prior to implementing 40 CFR part 65 still apply. Owners and operators who choose to comply with 40 CFR part 65, subpart F, shall comply with 40 CFR part 65, subpart A, as in effect on December 14, 2000. NR 440.62(2)(2) Definitions. As used in this section, terms not defined in this subsection have the meanings given in s. NR 440.02. NR 440.62(2)(a)(a) “Capital expenditure” means, in addition to the definition in s. NR 440.02 (6), an expenditure for a physical or operational change to an existing facility that: NR 440.62(2)(a)1.1. Exceeds P, the product of the facility’s replacement cost, R, and an adjusted annual asset guideline repair allowance, A, as reflected by the following equation: P = R × A,
where
NR 440.62(2)(a)1.a.a. The adjusted annual asset guideline repair allowance, A, is the product of the percent of the replacement cost, Y, and the applicable basic annual asset guideline repair allowance, B, divided by 100 as reflected by the following equation: A = Y × (B ⁄ 100);
Y = 1.0 - 0.575 log X,
where X is 1982 minus the year of construction; and
NR 440.62(2)(a)1.c.c. The applicable basic annual asset guideline repair allowance, B, is selected from the following table consistent with the applicable section: Table for Determining Applicable Value of B
NR 440.62(2)(b)(b) “Closed vent system” means a system that is not open to the atmosphere and that is composed of hard-piping, ductwork, connections and, if necessary, flow inducing devices that transport gas or vapor from a piece or pieces of equipment to a control device or back to a process. NR 440.62(2)(c)(c) “Connector” means flanged, screwed, welded, or other joined fittings used to connect two pipe lines or a pipe line and a piece of process equipment. NR 440.62(2)(d)(d) “Control device” means an enclosed combustion device, vapor recovery system, or flare. NR 440.62(2)(e)(e) “Distance piece” means an open or enclosed casing through which the piston rod travels, separating the compressor cylinder from the crankcase. NR 440.62(2)(f)(f) “Double block and bleed system” means two blocks valves connected in series with a bleed valve or line that can vent the line between the two block valves. NR 440.62(2)(fm)(fm) “Ductwork” means a conveyance system such as those commonly used for heating and ventilation systems. It is often made of sheet metal and often has sections connected by screws or crimping. Hard-piping is not ductwork. NR 440.62(2)(g)(g) “Equipment” means each pump, compressor, pressure relief device, sampling connection system, open-ended valve or line, valve and flange or other connection in VOC service and any devices or systems required by this section. NR 440.62(2)(h)(h) “First attempt at repair” means to take rapid action for the purpose of stopping or reducing leakage of organic material to atmosphere using best practices. NR 440.62(2)(he)(he) “Fuel gas” means gases that are combusted to derive useful work or heat. NR 440.62(2)(hm)(hm) “Fuel gas system” means the offsite and onsite piping and flow and pressure control system that gathers gaseous streams generated by onsite operations, may blend them with other sources of gas, and transports the gaseous stream for use as fuel gas in combustion devices or in-process combustion equipment, such as furnaces and gas turbines, either singly or in combination. NR 440.62(2)(hs)(hs) “Hard-piping” means pipe or tubing that is manufactured and properly installed using good engineering judgment and standards such as ASME B31.3, Process Piping (available from the American Society of Mechanical Engineers, PO Box 2900, Fairfield, NJ 07007-2900). NR 440.62(2)(i)(i) “In gas/vapor service” means that the piece of equipment contains process fluid that is in the gaseous state at operating conditions. NR 440.62(2)(j)(j) “In heavy liquid service” means that the piece of equipment is not in gas vapor service or in light liquid service. NR 440.62(2)(k)(k) “In light liquid service” means that the piece of equipment contains a liquid that meets the conditions specified in sub. (6) (e). NR 440.62(2)(ke)(ke) “In-situ sampling systems” means nonextractive samplers or in-line samplers.
