NR 664.1064(5)
(5) Record design documentation and monitoring, operating and inspection information for each closed-vent system and control device required to comply with s.
NR 664.1060 and keep them up-to-date in the facility operating record as specified in s.
NR 664.1035 (3). Design documentation is specified in s.
NR 664.1035 (3) (a) and
(b) and monitoring, operating and inspection information in s.
NR 664.1035 (3) (c) to
(h).
NR 664.1064(6)
(6) For a control device other than a thermal vapor incinerator, catalytic vapor incinerator, flare, boiler, process heater, condenser or carbon adsorption system, the department shall specify the appropriate recordkeeping requirements.
NR 664.1064(7)
(7) Record all of the following information pertaining to all equipment subject to ss.
NR 664.1052 to
664.1060 in a log that is kept in the facility operating record:
NR 664.1064(7)(a)
(a) A list of identification numbers for equipment (except welded fittings) subject to this subchapter.
NR 664.1064(7)(d)3.
3. The maximum instrument reading measured at the equipment during each compliance test.
NR 664.1064(7)(e)
(e) A list of identification numbers for equipment in vacuum service.
NR 664.1064(7)(f)
(f) Identification, either by list or location (area or group) of equipment that contains or contacts hazardous waste with an organic concentration of at least 10% by weight for less than 300 hours per calendar year.
NR 664.1064(8)
(8) Record all of the following information pertaining to all valves subject to s.
NR 664.1057 (7) and
(8) in a log that is kept in the facility operating record:
NR 664.1064(8)(a)
(a) A list of identification numbers for valves that are designated as unsafe to monitor, an explanation for each valve stating why the valve is unsafe to monitor and the plan for monitoring each valve.
NR 664.1064(8)(b)
(b) A list of identification numbers for valves that are designated as difficult to monitor, an explanation for each valve stating why the valve is difficult to monitor and the planned schedule for monitoring each valve.
NR 664.1064(9)
(9) Record all of the following information in the facility operating record for valves complying with s.
NR 664.1062:
NR 664.1064(9)(b)
(b) The percent of valves found leaking during each monitoring period.
NR 664.1064(10)
(10) Record all of the following information in a log that is kept in the facility operating record:
NR 664.1064(11)
(11) Record all of the following information in a log that is kept in the facility operating record for use in determining exemptions in the applicability section of this subchapter and other specific subchapters:
NR 664.1064(11)(a)
(a) An analysis determining the design capacity of the hazardous waste management unit.
NR 664.1064(11)(b)
(b) A statement listing the hazardous waste influent to and effluent from each hazardous waste management unit subject to ss.
NR 664.1052 to
664.1060 and an analysis determining whether these hazardous wastes are heavy liquids.
NR 664.1064(11)(c)
(c) An up-to-date analysis and the supporting information and data used to determine whether or not equipment is subject to ss.
NR 664.1052 to
664.1060. The record shall include supporting documentation as required by s.
NR 664.1063 (4) (c) when application of the knowledge of the nature of the hazardous waste stream or the process by which it was produced is used. If the owner or operator takes any action (e.g., changing the process that produced the waste) that could result in an increase in the total organic content of the waste contained in or contacted by equipment determined not to be subject to ss.
NR 664.1052 to
664.1060, then a new determination is required.
NR 664.1064(12)
(12) Keep records of the equipment leak information required by sub.
(4) and the operating information required by sub.
(5) for at least 3 years.
NR 664.1064(13)
(13) The owner or operator of a facility with equipment that is subject to this subchapter and to
40 CFR part 60,
61 or
63, or to corresponding provisions of ch.
NR 440, subch.
III of ch. NR 446 and chs.
NR 447 to
469, may elect to determine compliance with this subchapter either by documentation pursuant to this section, or by documentation of compliance with
40 CFR part 60,
61 or
63, or with corresponding provisions of ch.
NR 440, subch.
III of ch. NR 446 and chs.
NR 447 to
469, pursuant to the relevant provisions of
40 CFR part 60,
61 or
63, or the corresponding provisions of ch.
NR 440, subch.
III of ch. NR 446 and chs.
NR 447 to
469. The owner or operator shall keep documentation of compliance required by
40 CFR part 60,
61 or
63, or corresponding provisions of ch.
NR 440, subch.
III of ch. NR 446 and chs.
NR 447 to
469, or make readily available with the facility operating record.
NR 664.1064 History
History: CR 05-032: cr.
Register July 2006 No. 607, eff. 8-1-06;
CR 19-082: am. (13)
Register August 2020 No 776, eff. 9-1-20.
NR 664.1065(1)(1)
Owners and operators subject to this subchapter shall submit a semiannual report to the department by dates specified by the department. The report shall include all of the following information:
NR 664.1065(1)(a)
(a) The EPA identification number, name and address of the facility.
NR 664.1065(1)(c)
(c) Dates of hazardous waste management unit shutdowns that occurred within the semiannual reporting period.
NR 664.1065(1)(d)
(d) For each month during the semiannual reporting period, dates when the control device installed as required by s.
NR 664.1052,
664.1053,
664.1054 or
664.1055 exceeded or operated outside of the design specifications as defined in s.
NR 664.1064 (5) and as indicated by the control device monitoring required by s.
NR 664.1060 and was not corrected within 24 hours, the duration and cause of each exceedance and any corrective measures taken.
NR 664.1065(2)
(2) If, during the semiannual reporting period, leaks from valves, pumps and compressors are repaired as required in ss.
NR 664.1057 (4),
664.1052 (3) and
(4) (f), and
664.1053 (7), respectively, and the control device does not exceed or operate outside of the design specifications as defined in s.
NR 664.1064 (5) for more than 24 hours, a report to the department is not required.
NR 664.1065 History
History: CR 05-032: cr.
Register July 2006 No. 607, eff. 8-1-06.
NR 664.1080(1)(1)
This subchapter applies to owners and operators of all facilities that treat, store or dispose of hazardous waste in containers, tanks or surface impoundments subject to subch.
I,
J or
K except as s.
NR 664.0001 and sub.
(2) provide otherwise.
NR 664.1080(2)
(2) This subchapter does not apply to the following waste management units at the facility:
NR 664.1080(2)(a)
(a) A waste management unit that holds hazardous waste placed in the unit before June 1, 1998, and in which no hazardous waste is added to the unit on or after June 1, 1998.
NR 664.1080(2)(b)
(b) A container that has a design capacity less than or equal to 0.1 m
3.
NR 664.1080(2)(c)
(c) A tank in which an owner or operator has stopped adding hazardous waste and the owner or operator has begun implementing or completed closure pursuant to an approved closure plan.
NR 664.1080(2)(d)
(d) A surface impoundment in which an owner or operator has stopped adding hazardous waste (except to implement an approved closure plan) and the owner or operator has begun implementing or completed closure pursuant to an approved closure plan.
NR 664.1080(2)(e)
(e) A waste management unit that is used solely for on-site treatment or storage of hazardous waste that is placed in the unit as a result of implementing remedial activities required under the corrective action authorities of
42 USC 6924(u) or (v),
6928(h) or
9601 to
9675, similar federal authorities or s.
291.37 or
292.11, Stats.
NR 664.1080(2)(f)
(f) A waste management unit that is used solely for the management of radioactive mixed waste according to all applicable regulations under the authority of
42 USC 2011 to
2297 and
10101 to
10270.
NR 664.1080 Note
Note: The U.S. code (USC) cites in this paragraph are also known as the federal atomic energy act and the federal nuclear waste policy act, respectively.
NR 664.1080(2)(g)
(g) A hazardous waste management unit that the owner or operator certifies is equipped with and operating air emission controls according to
40 CFR part 60,
61 or
63, or to corresponding provisions of ch.
NR 440, subch.
III of ch.
NR 446 and chs.
NR 447 to
469. For the purpose of complying with this paragraph, a tank for which the air emission control includes an enclosure, as opposed to a cover, shall be in compliance with the enclosure and control device requirements of s.
NR 664.1084 (9), except as provided in s.
NR 664.1082 (3) (e).
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 History
History: CR 05-032: cr.
Register July 2006 No. 607, eff. 8-1-06.
NR 664.1081 History
History: 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 (C
t) 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 (R
bio) 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 (MR
bio) 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:
NR 664.1082(3)(b)9.
9. For the purpose of determining the performance of an organic destruction or removal process according to subds.
1. to
6., the owner or operator shall account for VO concentrations determined to be below the limit of detection of the analytical method using the following VO concentration:
NR 664.1082(3)(b)9.a.
a. If Method 25D in appendix A of
40 CFR part 60, incorporated by reference in s.
NR 660.11, is used for the analysis, one-half the blank value determined in the method at section 4.4, or a value of 25 ppmw, whichever is less.
NR 664.1082(3)(b)9.b.
b. If any other analytical method is used, one-half the sum of the limits of detection established for each organic constituent in the waste that has a Henry's law constant value at least 0.1 mole-fraction-in-the-gas-phase/mole-fraction-in-the-liquid-phase (0.1 Y/X) [which can also be expressed as 1.8 x 10
-6 atmospheres/gram-mole/m
3] at 25
°C.
