NR 664.1080(3)(3) For the owner and operator of a facility subject to this subchapter who received an operating license under s. 291.25, Stats., prior to June 1, 1998, the requirements of this subchapter shall be incorporated into the license when it is reissued according to s. NR 670.415 or reviewed according to s. NR 670.050 (4). Until the date when the license is reissued according to s. NR 670.415 or reviewed according to s. NR 670.050 (4), the owner and operator is subject to subch. CC of ch. NR 665. NR 664.1080(4)(4) The requirements of this subchapter, except for the recordkeeping requirements in s. NR 664.1089 (9), are administratively stayed for a tank or a container used to manage hazardous waste generated by organic peroxide manufacturing and its associated laboratory operations when the owner or operator of the unit meets all of the following conditions: NR 664.1080(4)(a)(a) The owner or operator identifies that the tank or container receives hazardous waste generated by an organic peroxide manufacturing process producing more than one functional family of organic peroxides or multiple organic peroxides within one functional family, that one or more of these organic peroxides could potentially undergo self-accelerating thermal decomposition at or below ambient temperatures and that organic peroxides are the predominant products manufactured by the process. For the purpose of meeting the conditions of this subsection, “organic peroxide” means an organic compound that contains the bivalent —O—O— structure and which may be considered to be a structural derivative of hydrogen peroxide where one or both of the hydrogen atoms has been replaced by an organic radical. NR 664.1080(4)(b)(b) The owner or operator prepares documentation, according to s. NR 664.1089 (9), explaining why an undue safety hazard would be created if air emission controls specified in ss. NR 664.1084 to 664.1087 are installed and operated on the tanks and containers used at the facility to manage the hazardous waste generated by the organic peroxide manufacturing process or processes meeting par. (a). NR 664.1080(4)(c)(c) The owner or operator notifies the department in writing that hazardous waste generated by an organic peroxide manufacturing process or processes meeting par. (a) are managed at the facility in tanks or containers meeting par. (b). The notification shall state the name and address of the facility and be signed and dated by an authorized representative of the facility owner or operator. NR 664.1080 HistoryHistory: CR 05-032: cr. Register July 2006 No. 607, eff. 8-1-06. NR 664.1081 HistoryHistory: CR 05-032: cr. Register July 2006 No. 607, eff. 8-1-06. NR 664.1082(1)(1) This section applies to the management of hazardous waste in tanks, surface impoundments and containers subject to this subchapter. NR 664.1082(2)(2) The owner or operator shall control air pollutant emissions from each hazardous waste management unit according to the standards in ss. NR 664.1084 to 664.1087, as applicable to the hazardous waste management unit, except as provided in sub. (3). NR 664.1082(3)(3) A tank, surface impoundment or container is exempt from the standards in ss. NR 664.1084 to 664.1087, as applicable, provided that the waste management unit is one of the following: NR 664.1082(3)(a)(a) A tank, surface impoundment or container for which all hazardous waste entering the unit has an average VO concentration at the point of waste origination of less than 500 parts per million by weight (ppmw). Determine the average VO concentration using the procedures in s. NR 664.1083 (1). Review and update, as necessary, this determination at least once every 12 months following the date of the initial determination for the hazardous waste streams entering the unit. NR 664.1082(3)(b)(b) A tank, surface impoundment or container for which the organic content of all the hazardous waste entering the waste management unit has been reduced by an organic destruction or removal process that achieves any one of the following conditions: NR 664.1082(3)(b)1.1. A process that removes or destroys the organics contained in the hazardous waste to a level such that the average VO concentration of the hazardous waste at the point of waste treatment is less than the exit concentration limit (Ct) established for the process. Determine the average VO concentration of the hazardous waste at the point of waste treatment and the exit concentration limit for the process using the procedures in s. NR 664.1083 (2). NR 664.1082(3)(b)2.2. A process that removes or destroys the organics contained in the hazardous waste to a level such that the organic reduction efficiency (R) for the process is equal to or greater than 95%, and the average VO concentration of the hazardous waste at the point of waste treatment is less than 100 ppmw. Determine the organic reduction efficiency for the process and the average VO concentration of the hazardous waste at the point of waste treatment using the procedures in s. NR 664.1083 (2). NR 664.1082(3)(b)3.3. A process that removes or destroys the organics contained in the hazardous waste to a level such that the actual organic mass removal rate (MR) for the process is equal to or greater than the required organic mass removal rate (RMR) established for the process. Determine the required organic mass removal rate and the actual organic mass removal rate for the process using the procedures in s. NR 664.1083 (2). NR 664.1082(3)(b)4.4. A biological process that destroys or degrades the organics contained in the hazardous waste, such that any of the following conditions is met: NR 664.1082(3)(b)4.a.a. The organic reduction efficiency (R) for the process is equal to or greater than 95%, and the organic biodegradation efficiency (Rbio) for the process is equal to or greater than 95%. Determine the organic reduction efficiency and the organic biodegradation efficiency for the process using the procedures in s. NR 664.1083 (2). NR 664.1082(3)(b)4.b.b. The total actual organic mass biodegradation rate (MRbio) for all hazardous waste treated by the process is equal to or greater than the required organic mass removal rate (RMR). Determine the required organic mass removal rate and the actual organic mass biodegradation rate for the process using the procedures in s. NR 664.1083 (2). NR 664.1082(3)(b)5.5. A process that removes or destroys the organics contained in the hazardous waste and meets all of the following conditions: NR 664.1082(3)(b)5.a.a. From the point of waste origination through the point where the hazardous waste enters the treatment process, the hazardous waste is managed continuously in waste management units which use air emission controls according to the standards in ss. NR 664.1084 to 664.1087, as applicable to the waste management unit. NR 664.1082(3)(b)5.b.b. From the point of waste origination through the point where the hazardous waste enters the treatment process, any transfer of the hazardous waste is accomplished through continuous hard-piping or other closed system transfer that does not allow exposure of the waste to the atmosphere. A drain system that meets 40 CFR part 63, subpart RR—National Emission Standards for Individual Drain Systems is a closed system. NR 664.1082(3)(b)5.c.c. The average VO concentration of the hazardous waste at the point of waste treatment is less than the lowest average VO concentration at the point of waste origination determined for each of the individual waste streams entering the process or 500 ppmw, whichever value is lower. Determine the average VO concentration of each individual waste stream at the point of waste origination using the procedures in s. NR 664.1083 (1). Determine the average VO concentration of the hazardous waste at the point of waste treatment using the procedures in s. NR 664.1083 (2). NR 664.1082(3)(b)6.6. A process that removes or destroys the organics contained in the hazardous waste to a level such that the organic reduction efficiency (R) for the process is equal to or greater than 95% and the owner or operator certifies that the average VO concentration at the point of waste origination for each of the individual waste streams entering the process is less than 10,000 ppmw. Determine the organic reduction efficiency for the process and the average VO concentration of the hazardous waste at the point of waste origination using the procedures in s. NR 664.1083 (2) and (1), respectively. NR 664.1082(3)(b)7.7. A hazardous waste incinerator for which any of the following conditions has been met: NR 664.1082(3)(b)8.8. A boiler or industrial furnace for which any of the following conditions has been met: