NR 440.74(4)(c)3.3. The coating mix preparation equipment is vented to a control device while preparation of the coating is taking place within the vessel; and NR 440.74(4)(c)4.4. The control device efficiency, E or Hsys as applicable, determined using Equation (1) or Equations (3) and (4), respectively and the test methods and procedures specified in sub. (6) (b) to (g) is equal to or greater than 0.95. NR 440.74(4)(d)(d) To demonstrate compliance with sub. (3) (c) 2., standard for coating mix preparation equipment servicing a coating operation that does not have concurrent construction of a control device but uses at least 130 Mg of VOC per year, or sub. (3) (c) 3., standard for coating mix preparation equipment servicing a coating operation that uses at least 95 Mg but less than 130 Mg of VOC per year, each owner or operator of affected coating mix preparation equipment shall demonstrate upon inspection that: NR 440.74(4)(d)1.1. Covers satisfying the specifications in par. (c) 1. a. to e. have been installed and are being properly operated and maintained; and NR 440.74(4)(d)2.2. Procedures detailing the proper use of covers, as specified in par. (c) 1. a., have been posted in all areas where affected coating mix preparation equipment is used. NR 440.74(4)(d)3.3. Owners or operators meeting the standard specified in sub. (3) (c) 2. b. or 3. b. shall also demonstrate that the coating mix preparation equipment is vented to a control device. NR 440.74(4)(e)(e) If a control device other than a carbon adsorber, condenser or incinerator is used to control emissions from an affected facility, the necessary operating specifications for that device shall be approved by the administrator. An example of such a device is a flare. NR 440.74(5)(a)(a) Each owner or operator of an affected facility shall install and calibrate all monitoring devices required under the provisions of this subsection according to the manufacturer’s specifications, prior to the initial performance test in locations such that representative values of the monitored parameters will be obtained. The parameters to be monitored shall be continuously measured and recorded during each performance test. NR 440.74(5)(b)(b) Each owner or operator of an affected facility that uses less that 95 Mg of VOC per year and each owner or operator of an affected facility subject to the provisions specified in sub. (3) (c) 3. shall: NR 440.74(5)(b)1.1. Make semiannual estimates of the projected annual amount of VOC to be used for the manufacture of polymeric coated substrate at the affected coating operation in that year; and NR 440.74(5)(c)(c) Each owner or operator of an affected facility controlled by a carbon adsorption system and demonstrating compliance by the procedures described in sub. (4) (a) 1., 2., (b) or (c), which include control device efficiency determinations, or sub. (4) (a) 4., short-term liquid material balance, shall carry out the monitoring provisions of subd. 1. or 2., as appropriate. NR 440.74(5)(c)1.1. For carbon adsorption systems with a common exhaust stack for all the individual adsorber vessels, install, calibrate, maintain and operate, according to the manufacturer’s specifications, a monitoring device that continuously indicates and records the concentration level of organic compounds in either the control device outlet gas stream or in both the control device inlet and outlet gas streams. The outlet gas stream shall be monitored if the percent increase in the concentration level of organic compounds is used as the basis for reporting, as described in sub. (8) (d) 1. a. The inlet and outlet gas streams shall be monitored if the percent control device efficiency is used as the basis for reporting, as described in sub. (8) (d) 2. a. NR 440.74(5)(c)2.2. For carbon adsorption systems with individual exhaust stacks for each adsorber vessel, install, calibrate, maintain and operate, according to the manufacturer’s specifications, a monitoring device that continuously indicates and records the concentration level of organic compounds in the outlet gas stream for a minimum of one complete adsorption cycle per day for each adsorber vessel. The owner or operator may also monitor and record the concentration level of organic compounds in the common carbon adsorption system inlet gas stream or in each individual carbon adsorber vessel inlet stream. The outlet gas streams shall be monitored if the percent increase in the concentration level of organic compounds is used as the basis for reporting, as described in sub. (8) (d) 1. b. In this case, the owner or operator shall compute daily a 3-day rolling average concentration level of organics in the outlet gas stream from each individual adsorber vessel. The inlet and outlet gas streams shall be monitored if the percent control device efficiency is used as the basis for reporting, as described in sub. (8) (d) 2. b. In this case, the owner or operator shall compute daily a 3-day rolling average efficiency for each individual adsorber vessel. NR 440.74(5)(d)(d) Each owner or operator of an affected facility controlled by a condensation system and demonstrating compliance by the test methods described in sub. (4) (a) 1., 2., (b) or (c), which include control device efficiency determinations, or sub. (4) (a) 4., short-term liquid material balance, shall install, calibrate, maintain and operate, according to the manufacturer’s specifications, a monitoring device that continuously indicates and records the temperature of the condenser exhaust stream. NR 440.74(5)(e)(e) Each owner or operator of an affected facility controlled by a thermal incinerator and demonstrating compliance by the test methods described in sub. (4) (a) 1., 2., (b) or (c), which include control device efficiency determinations, shall install, calibrate maintain and operate, according to the manufacturer’s specifications, a monitoring device that continuously indicates and records the combustion temperature of the incinerator. The monitoring device shall have an accuracy within ± 1% of the temperature being measured in Celsius degrees. NR 440.74(5)(f)(f) Each owner or operator of an affected facility controlled by a catalytic incinerator and demonstrating compliance by the test methods described in sub. (4) (a) 1., 2., (b) or (c), which include control device efficiency determinations, shall install, calibrate maintain and operate, according to the manufacturer’s specifications, a monitoring device that continuously indicates and records the gas temperature both upstream and downstream of the catalyst bed. The monitoring device shall have an accuracy within ± 1% of the temperature being measured in Celsius degrees. NR 440.74(5)(g)(g) Each owner or operator of an affected facility who demonstrates compliance by the test methods described in sub. (4) (a) 1. or 2., which include vapor capture system efficiency determinations, or sub. (4) (a) 4., short-term liquid material balance, shall submit a monitoring plan for the vapor capture system to the department for approval. This plan shall identify the parameter to be monitored as an indicator of vapor capture system performance, for example, the amperage to the exhaust fans or duct flow rates, and the method for monitoring the chosen parameter. The owner or operator shall install, calibrate, maintain and operate, according to the manufacturer’s specifications, a monitoring device that continuously indicates and records the value of the chosen parameter. NR 440.74(5)(h)(h) Each owner or operator of an affected facility who demonstrates compliance as described in sub. (4) (b) shall follow the procedures described in par. (g) to establish a monitoring system for the total enclosure. NR 440.74(5)(i)(i) Each owner or operator of an affected facility shall record time periods of mixing or coating operations when the emission control device is malfunctioning or not in use. NR 440.74(5)(j)(j) Each owner or operator of an affected facility shall record time periods of mixing or coating operations when each monitoring device is malfunctioning or not in use. NR 440.74(5)(k)(k) Records of the measurements and calculations required in subs. (4) and (5) shall be retained for at least 2 years following the date of the measurements and calculations. NR 440.74(6)(a)(a) Method 24 is used to determine the VOC content in coatings. If it is demonstrated to the satisfaction of the administrator that coating formulation data are equivalent to Method 24 results, formulation data may be used. In the event of any inconsistency between a Method 24 test and a facility’s formulation data, the Method 24 test will govern. For Method 24, the coating sample shall be a 1-liter sample collected in a 1-liter container at a point in the process where the sample will be representative of the coating applied to the substrate, that is, the sample shall include any dilution solvent or other VOC added during the manufacturing process. The container shall be tightly sealed immediately after the sample is collected. Any solvent or other VOC added after the sample is taken shall be measured and accounted for in the calculations that use Method 24 results. NR 440.74(6)(b)(b) Method 25 shall be used to determine VOC concentrations from incinerator gas streams. Alternative Methods (18 or 25A), may be used as explained in the applicability section of Method 25 in cases where use of Method 25 is demonstrated to be technically infeasible. The owner or operator shall submit notice of the intended test method to the department for approval along with the notification of the performance test required under s. NR 440.08 (4). Except as indicated in subds. 1. and 2., the test shall consist of 3 separate runs, each lasting a minimum of 30 minutes. NR 440.74(6)(b)1.1. When the method is to be used in the determination of the efficiency of a fixed-bed carbon adsorption system with a common exhaust stack for all the individual adsorber vessels pursuant to sub. (4) (a) 1., (b) or (c), the test shall consist of 3 separate runs, each coinciding with one or more complete system rotations through the adsorption cycles of all the individual adsorber vessels. NR 440.74(6)(b)2.2. When the method is to be used in the determination of the efficiency of a fixed-bed carbon adsorption system with individual exhaust stacks for each adsorber vessel pursuant to sub. (4) (a) 2., (b) or (c), each adsorber vessel shall be tested individually. Each test shall consist of 3 separate runs, each coinciding with one or more complete adsorption cycles. NR 440.74(6)(c)(c) Method 1 or 1A is used for sample and velocity traverses;