NR 661.1034(5)(b)(b) Annually for continuously generated material, or whenever there is a change in the material being managed or a change in the process that generates or treats the material. NR 661.1034(6)(6) When a remanufacturer or other person that stores or treats the hazardous secondary material 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 secondary material with organic concentrations of at least 10 ppmw based on knowledge of the material, the dispute may be resolved by using direct measurement as specified in sub. (4) (a). NR 661.1034 HistoryHistory: CR 19-082: cr. Register August 2020 No. 776, eff. 9-1-20; correction in (1), (2) (a), (4) (a) 3. made under s. 35.17, Stats., Register August 2020 No. 776. NR 661.1035(1)(a)(a) A remanufacturer or other person that stores or treats the hazardous secondary material subject to the provisions of this subchapter shall comply with the recordkeeping requirements of this section. NR 661.1035(1)(b)(b) A remanufacturer or other person that stores or treats the hazardous secondary material of more than one hazardous secondary material management unit subject to the provisions of this subchapter may comply with the recordkeeping requirements for these hazardous secondary material management units in one recordkeeping system if the system identifies each record by each hazardous secondary material management unit. NR 661.1035(2)(2) A remanufacturer or other person that stores or treats the hazardous secondary material shall keep all of the following records on-site: NR 661.1035(2)(a)(a) For facilities that comply with the provisions specified in s. NR 661.1033 (1), 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 kept on-site at the facility by the effective date that the facility becomes subject to the provisions of this subchapter. NR 661.1035(2)(b)(b) Up-to-date documentation of compliance with the process vent standards specified in s. NR 661.1032, including all of the following: NR 661.1035(2)(b)1.1. Information and data identifying all affected process vents, annual throughput and operating hours of each affected unit, estimated emission rates for each affected vent and for the overall facility, and the approximate location within the facility of each affected unit, such as identifying the hazardous secondary material management units on a facility plot plan. NR 661.1035(2)(b)2.2. Information and data supporting determinations of vent emissions and emission reductions achieved by add-on control devices based on engineering calculations or source tests. For the purpose of determining compliance, determinations of vent emissions and emission reductions shall be made using operating parameter values, such as temperatures, flow rates, or vent stream organic compounds and concentrations, that represent the conditions that result in maximum organic emissions, such as when the hazardous secondary material management unit is operating at the highest load or capacity level reasonably expected to occur. If the remanufacturer or other person that stores or treats the hazardous secondary material takes any action, such as managing a material of different composition or increasing operating hours of affected hazardous secondary material management units, that would result in an increase in total organic emissions from affected process vents at the facility, then a new determination is required. NR 661.1035(2)(c)(c) When a remanufacturer or other person that stores or treats the hazardous secondary material chooses to use test data to determine the organic removal efficiency or total organic compound concentration achieved by the control device, a performance test plan shall be developed and include all of the following: NR 661.1035(2)(c)1.1. A description of how it is determined that the planned test is going to be conducted when the hazardous secondary material management unit is operating at the highest load or capacity level reasonably expected to occur. This shall include the estimated or design flow rate and organic content of each vent stream and define the acceptable operating ranges of key process and control device parameters during the test program. NR 661.1035(2)(c)2.2. A detailed engineering description of the closed-vent system and control device including all of the following: NR 661.1035(2)(c)3.3. A detailed description of sampling and monitoring procedures, including sampling and monitoring locations in the system, the equipment to be used, sampling and monitoring frequency, and planned analytical procedures for sample analysis. NR 661.1035(2)(d)1.1. A list of all information references and sources used in preparing the documentation. NR 661.1035(2)(d)3.3. If engineering calculations are used, a design analysis, specifications, drawings, schematics, and piping and instrumentation diagrams based on the appropriate sections of “APTI Course 415: Control of Gaseous Emissions,” incorporated by reference in s. NR 660.11, or other engineering texts acceptable to the department that present basic control device design information. Documentation provided by the control device manufacturer or vendor that describes the control device design in accordance with this subdivision may be used to comply with this requirement. The design analysis shall address the vent stream characteristics and control device operation parameters as follows: NR 661.1035(2)(d)3.a.a. For a thermal vapor incinerator, the design analysis shall consider the vent stream composition, constituent concentrations, and flow rate. The design analysis shall also establish the design minimum and average temperature in the combustion zone and the combustion zone residence time. NR 661.1035(2)(d)3.b.b. For a catalytic vapor incinerator, the design analysis shall consider the vent stream composition, constituent concentrations, and flow rate. The design analysis shall also establish the design minimum and average temperatures across the catalyst bed inlet and outlet. NR 661.1035(2)(d)3.c.c. For a boiler or process heater, the design analysis shall consider the vent stream composition, constituent concentrations, and flow rate. The design analysis shall also establish the design minimum and average flame zone temperatures, combustion zone residence time, and description of method and location where the vent stream is introduced into the combustion zone. NR 661.1035(2)(d)3.d.d. For a flare, the design analysis shall consider the vent stream composition, constituent concentrations, and flow rate. The design analysis shall also consider the requirements specified in s. NR 661.1033 (4).