NR 664.1033(12)(c)3.3. Delay of repair of a closed-vent system for which leaks have been detected is allowed if the repair is technically infeasible without a process unit shutdown, or if the owner or operator determines that emissions resulting from immediate repair would be greater than the fugitive emissions likely to result from delay of repair. Complete repair of the equipment by the end of the next process unit shutdown. NR 664.1033(13)(13) Operate closed-vent systems and control devices used to comply with this subchapter at all times when emissions may be vented to them. NR 664.1033(14)(14) The owner or operator using a carbon adsorption system to control air pollutant emissions shall document that all carbon that is a hazardous waste and that is removed from the control device is managed in one of the following manners, regardless of the average volatile organic concentration of the carbon: NR 664.1033(14)(a)(a) Regenerated or reactivated in a thermal treatment unit that meets one of the following: NR 664.1033(14)(a)1.1. The owner or operator of the unit has been issued an operating license under ch. NR 670 which implements the requirements of subch. X. NR 664.1033(14)(b)(b) Incinerated in a hazardous waste incinerator for which any of the following conditions has been met: NR 664.1033(14)(b)1.1. The owner or operator has been issued an operating license under ch. NR 670 which implements the requirements of subch. O. NR 664.1033(14)(c)(c) Burned in a boiler or industrial furnace for which any of the following conditions has been met: NR 664.1033(14)(c)2.2. The owner or operator has designed and operates the boiler or industrial furnace according to the interim license requirements of subch. H of ch. NR 666. NR 664.1033(15)(a)(a) Determines that the components of the closed-vent system are unsafe to monitor because monitoring personnel would be exposed to an immediate danger as a consequence of complying with sub. (12) (a) 2. b. NR 664.1033(15)(b)(b) Adheres to a written plan that requires monitoring the closed-vent system components using the procedure in sub. (12) (a) 2. b. as frequently as practicable during safe-to-monitor times. NR 664.1033 HistoryHistory: CR 05-032: cr. Register July 2006 No. 607, eff. 8-1-06; correction in (14) (a) 2. made under s. 13.92 (4) (b) 7., Stats., Register March 2013 No. 687. NR 664.1034(1)(1) Each owner or operator subject to this subchapter shall comply with the test methods and procedures requirements in this section. NR 664.1034(2)(2) When a closed-vent system is tested for compliance with no detectable emissions, as required in s. NR 664.1033 (12), the test shall comply with all of the following requirements: NR 664.1034(2)(d)2.2. A mixture of methane or n-hexane and air at a concentration of approximately, but less than, 10,000 ppm methane or n-hexane. NR 664.1034(2)(f)(f) Traverse the instrument probe around all potential leak interfaces as close to the interface as possible as described in Method 21 in appendix A of 40 CFR part 60, incorporated by reference in s. NR 660.11. NR 664.1034(2)(g)(g) Compare the arithmetic difference between the maximum concentration indicated by the instrument and the background level with 500 ppm for determining compliance. NR 664.1034(3)(a)(a) Conduct performance tests to determine total organic compound concentrations and mass flow rates entering and exiting control devices and reduce data according to all of the following methods and calculation procedures: NR 664.1034(3)(a)2.2. Method 18 or Method 25A in Appendix A of 40 CFR part 60, incorporated by reference in s. NR 660.11, for organic content. If Method 25A is used, the organic HAP used as the calibration gas shall be the single organic HAP representing the largest percent by volume of the emissions. The use of Method 25A is acceptable if the response from the high-level calibration gas is at least 20 times the standard deviation of the response from the zero calibration gas when the instrument is zeroed on the most sensitive scale. NR 664.1034(3)(a)3.3. Each performance test shall consist of 3 separate runs; conduct each run for at least one hour under the conditions that exist when the hazardous waste management unit is operating at the highest load or capacity level reasonably expected to occur. For the purpose of determining total organic compound concentrations and mass flow rates, average the results of all runs. Compute the average on a time-weighted basis. where:
Eh = Total organic mass flow rate, kg/h
Q2sd = Volumetric flow rate of gases entering or exiting control device, determined by Method 2, dscm/h
n = Number of organic compounds in the vent gas
Ci = Organic concentration in ppm, dry basis, of compound i in the vent gas, determined by Method 18
MWi = Molecular weight of organic compound i in the vent gas, kg/kg-mol
0.0416 = Conversion factor for molar volume, kg-mol/m3 (at 293 K and 760 mm Hg)
10-6 = Conversion from ppm
Eh = (Q)(C)(MW)(0.0416)(10-6)
where:
Eh = Total organic mass flow rate, kg/h
Q = Volumetric flow rate of gases entering or exiting control device, as determined by Method 2, dscm/h;
C = Organic concentration in ppm, dry basis, as determined by Method 25A
MW = Molecular weight of propane, 44
0.0416 = Conversion factor for molar volume, kg-mol/m3 (at 293 K and 760 mm Hg)
10 -6 = Conversion from ppm.
NR 664.1034(3)(a)5.5. Determine the annual total organic emission rate by the following equation: where:
EA = Total organic mass emission rate, kg/y
Eh = Total organic mass flow rate for the process vent, kg/h
H = Total annual hours of operations for the affected unit, h
NR 664.1034(3)(a)6.6. Determine total organic emissions from all affected process vents at the facility by summing the hourly total organic mass emission rates (Eh, determined in subd. 4.) and by summing the annual total organic mass emission rates (EA, determined in subd. 5.) for all affected process vents at the facility. NR 664.1034(3)(b)(b) Record the process information as may be necessary to determine the conditions of the performance tests. Operations during periods of startup, shutdown and malfunction may not constitute representative conditions for the purpose of a performance test. NR 664.1034(3)(c)(c) For an affected facility, provide, or cause to be provided, all of the following performance testing facilities: NR 664.1034(3)(d)(d) For the purpose of making compliance determinations, use the time-weighted average of the results of the 3 runs. In the event that a sample is accidentally lost or conditions occur in which one of the 3 runs must be discontinued because of forced shutdown, failure of an irreplaceable portion of the sample train, extreme meteorological conditions or other circumstances beyond the owner or operator’s control, compliance may, upon the department’s approval, be determined using the average of the results of the 2 other runs. NR 664.1034(4)(4) To show that a process vent associated with a hazardous waste distillation, fractionation, thin-film evaporation, solvent extraction or air or steam stripping operation is not subject to this subchapter, the owner or operator shall make an initial determination that the time-weighted, annual average total organic concentration of the waste managed by the waste management unit is less than 10 ppmw using one of the following 2 methods: NR 664.1034(4)(a)(a) Direct measurement of the organic concentration of the waste. This method requires all of the following: NR 664.1034(4)(a)1.1. Take a minimum of 4 grab samples of waste for each waste stream managed in the affected unit under process conditions expected to cause the maximum waste organic concentration. NR 664.1034(4)(a)2.2. For waste generated onsite, collect the grab samples at a point before the waste is exposed to the atmosphere such as in an enclosed pipe or other closed system that is used to transfer the waste after generation to the first affected distillation, fractionation, thin-film evaporation, solvent extraction or air or steam stripping operation. For waste generated off-site, collect the grab samples at the inlet to the first waste management unit that receives the waste provided the waste has been transferred to the facility in a closed system such as a tank truck and the waste is not diluted or mixed with other waste. NR 664.1034(4)(a)3.3. Analyze each sample and compute the total organic concentration of the sample using Method 9060A of EPA SW-846, incorporated by reference in s. NR 660.11, or analyze for its individual organic constituents. NR 664.1034(4)(a)4.4. Use the arithmetic mean of the results of the analyses of the 4 samples for each waste stream managed in the unit in determining the time-weighted, annual average total organic concentration of the waste. Calculate the time-weighted average using the annual quantity of each waste stream processed and the mean organic concentration of each waste stream managed in the unit. NR 664.1034(4)(b)(b) Using knowledge of the waste to determine that its total organic concentration is less than 10 ppmw. This method requires documentation of the waste determination. Examples of documentation that shall be used to support a determination under this paragraph include production process information documenting that no organic compounds are used, information that the waste is generated by a process that is identical to a process at the same or another facility that has previously been demonstrated by direct measurement to generate a waste stream having a total organic content less than 10 ppmw, or prior speciation analysis results on the same waste stream where it can also be documented that no process changes have occurred since that analysis that could affect the waste total organic concentration. NR 664.1034(5)(5) Make the determination that distillation, fractionation, thin-film evaporation, solvent extraction or air or steam stripping operations manage hazardous wastes with time-weighted, annual average total organic concentrations less than 10 ppmw according to pars. (a) and (b) or (c): NR 664.1034(5)(a)(a) By the effective date that the facility becomes subject to this subchapter or by the date when the waste is first managed in a waste management unit, whichever is later. NR 664.1034(5)(c)(c) Whenever there is a change in the waste being managed or a change in the process that generates or treats the waste. NR 664.1034(6)(6) When an owner or operator and the department do not agree on whether a distillation, fractionation, thin-film evaporation, solvent extraction or air or steam stripping operation manages a hazardous waste with organic concentrations of at least 10 ppmw based on knowledge of the waste, the dispute may be resolved by using direct measurement as specified in sub. (4) (a). NR 664.1034 HistoryHistory: CR 05-032: cr. Register July 2006 No. 607, eff. 8-1-06; CR 16-007: am. (3) (a) 2., 4., (4) (a) 3., (6) Register July 2017 No. 739, eff. 8-1-17. NR 664.1035(1)(a)(a) Each owner or operator subject to this subchapter shall comply with this section. NR 664.1035(1)(b)(b) An owner or operator of more than one hazardous waste management unit subject to this subchapter may comply with the recordkeeping requirements for these hazardous waste management units in one recordkeeping system if the system identifies each record by each hazardous waste management unit. NR 664.1035(2)(2) Record all of the following information in the facility operating record: NR 664.1035(2)(a)(a) For facilities that comply with s. NR 664.1033 (1) (b), an implementation schedule that includes dates by which the closed-vent system and control device will be installed and in operation. The schedule shall also include a rationale of why the installation cannot be completed at an earlier date. The implementation schedule shall be in the facility operating record by the effective date that the facility becomes subject to this subchapter.
