Appendix C. Greenhouse Gas Reporting Program:
Recordkeeping Requirements (as of July 9, 2015)

Subpart
Recordkeeping Requirement
C  -  General Stationary Combustion
(§98.37)
    In addition to the requirements of §98.3(g), you must retain:

(a) The applicable records specified in §§98.34(f) and (g), 98.35(b), and 98.36(e).

(b) Verification software records. For each stationary fuel combustion source that elects to use the verification software specified in §98.5(b) rather than report data specified in paragraphs (b)(9)(iii), (c)(2)(ix), (e)(2)(i), (e)(2)(ii)(A), (e)(2)(ii)(C), (e)(2)(ii)(D), (e)(2)(iv)(A), (e)(2)(iv)(C), (e)(2)(iv)(F), and (e)(2)(ix)(D) through (F) of this section, you must keep a record of the file generated by the verification software for the applicable data specified in paragraphs (b)(1) through (36) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (b)(1) through (36) of this section.

(1) Mass of each solid fuel combusted (tons/year) (Equation C-1 of §98.33).

(2) Volume of each liquid fuel combusted (gallons/year) (Equation C-1).

(3) Volume of each gaseous fuel combusted (scf/year) (Equation C-1).

(4) Annual natural gas usage (therms/year) (Equation C-1a of §98.33).

(5) Annual natural gas usage (mmBtu/year) (Equation C-1b of §98.33).

(6) Mass of each solid fuel combusted (tons/year) (Equation C-2a of §98.33).

(7) Volume of each liquid fuel combusted (gallons/year) (Equation C-2a).

(8) Volume of each gaseous fuel combusted (scf/year) (Equation C-2a).

(9) Measured high heat value of each solid fuel, for month (which may be the arithmetic average of multiple determinations), or, if applicable, an appropriate substitute data value (mmBtu per ton) (Equation C-2b of §98.33).

(10) Measured high heat value of each liquid fuel, for month (which may be the arithmetic average of multiple determinations), or, if applicable, an appropriate substitute data value (mmBtu per gallons) (Equation C-2b).

(11) Measured high heat value of each gaseous fuel, for month (which may be the arithmetic average of multiple determinations), or, if applicable, an appropriate substitute data value (mmBtu per scf) (Equation C-2b).

(12) Mass of each solid fuel combusted during month (tons) (Equation C-2b).

(13) Volume of each liquid fuel combusted during month (gallons) (Equation C-2b).

(14) Volume of each gaseous fuel combusted during month (scf) (Equation C-2b).

(15) Total mass of steam generated by municipal solid waste or each solid fuel combustion during the reporting year (pounds steam) (Equation C-2c of §98.33).

(16) Ratio of the boiler's maximum rated heat input capacity to its design rated steam output capacity (MMBtu/pounds steam) (Equation C-2c).

(17) Annual mass of each solid fuel combusted (short tons/year) (Equation C-3 of §98.33).

(18) Annual average carbon content of each solid fuel (percent by weight, expressed as a decimal fraction) (Equation C-3).

(19) Annual volume of each liquid fuel combusted (gallons/year) (Equation C-4 of §98.33).

(20) Annual average carbon content of each liquid fuel (kg C per gallon of fuel) (Equation C-4).

(21) Annual volume of each gaseous fuel combusted (scf/year) (Equation C-5 of §98.33).

(22) Annual average carbon content of each gaseous fuel (kg C per kg of fuel) (Equation C-5).

(23) Annual average molecular weight of each gaseous fuel (kg/kg-mole) (Equation C-5).

(24) Molar volume conversion factor at standard conditions, as defined in §98.6 (scf per kg-mole) (Equation C-5).

(25) Identify for each fuel if you will use the default high heat value from Table C-1 of this subpart, or actual high heat value data (Equation C-8 of §98.33).

(26) High heat value of each solid fuel (mmBtu/tons) (Equation C-8).

(27) High heat value of each liquid fuel (mmBtu/gallon) (Equation C-8).

(28) High heat value of each gaseous fuel (mmBtu/scf) (Equation C-8).

(29) Cumulative annual heat input from combustion of each fuel (mmBtu) (Equation C-10 of §98.33).

(30) Total quantity of each solid fossil fuel combusted in the reporting year, as defined in §98.6 (pounds) (Equation C-13 of §98.33).

(31) Total quantity of each liquid fossil fuel combusted in the reporting year, as defined in §98.6 (gallons) (Equation C-13).

(32) Total quantity of each gaseous fossil fuel combusted in the reporting year, as defined in §98.6 (scf) (Equation C-13).

(33) High heat value of the each solid fossil fuel (Btu/lb) (Equation C-13).

(34) High heat value of the each liquid fossil fuel (Btu/gallons) (Equation C-13).

(35) High heat value of the each gaseous fossil fuel (Btu/scf) (Equation C-13).

(36) Fuel-specific carbon based F-factor per fuel (scf CO2/mmBtu) (Equation C-13).
D  -  Electricity Generation
(§98.47)
You shall comply with the recordkeeping requirements of §§98.3(g) and 98.37. Records retained under §75.57(h) of this chapter for missing data events satisfy the recordkeeping requirements of §98.3(g)(4) for those same events.

E  -  Adipic Acid Production
(§98.57)

    In addition to the information required by §98.3(g), you must retain the records specified in paragraphs (a) through (i) of this section at the facility level:
    (a) Annual adipic acid production capacity (tons).
    (b) Records of significant changes to process.
    (c) Number of facility and unit operating hours in calendar year.
    (d) Documentation of how accounting procedures were used to estimate production rate.
    (e) Documentation of how process knowledge was used to estimate abatement technology destruction efficiency.
    (f) Performance test reports.
    (g) Measurements, records and calculations used to determine reported parameters.
    (h) Documentation of the procedures used to ensure the accuracy of the measurements of all reported parameters, including but not limited to, calibration of weighing equipment, flow meters, and other measurement devices. The estimated accuracy of measurements made with these devices must also be recorded, and the technical basis for these estimates must be provided.
    (i) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (i)(1) through (3) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (i)(1) through (3) of this section.
    (1) Annual adipic acid production from each adipic acid production unit (tons) (Equations E-2, E-3a, E-3b, E-3c, and E-3d of §98.53).
    (2) Production rate per test run during the performance test for each production unit test run (tons adipic acid produced/hr) (Equation E-1 of §98.53).
    (3) Annual adipic acid production per N2O abatement technology during which N2O abatement technology was used (tons adipic acid produced) (Equation E-2).
F  -  Aluminum Production
(§98.67)

    In addition to the information required by §98.3(g), you must retain the following records:
    (a) Monthly aluminum production in metric tons.
    (b) Type of smelter technology used.
    (c) The following PFC-specific information on a monthly basis:
    (1) Perfluoromethane and perfluoroethane emissions from anode effects in prebake and Søderberg electolysis cells.
    (2) Anode effect minutes per cell-day (AE-mins/cell-day), anode effect frequency (AE/cell-day), anode effect duration (minutes). (Or anode effect overvoltage factor ((kg CF4/metric ton Al)/(mV/cell day)), potline overvoltage (mV/cell day), current efficiency (%).))
    (3) Smelter-specific slope coefficients and the last date when the smelter-specific-slope coefficients were measured.
    (d) Method used to measure the frequency and duration of anode effects (or to measure anode effect overvoltage and current efficiency).
    (e) The following CO2-specific information for prebake cells:
    (1) Annual anode consumption.
    (2) Annual CO2 emissions from the smelter.
    (f) The following CO2-specific information for Søderberg cells:
    (1) Annual paste consumption.
    (2) Annual CO2 emissions from the smelter.
    (g) Smelter-specific inputs to the CO2 process equations (e.g., levels of sulfur and ash) that were used in the calculation, on an annual basis.
    (h) Exact data elements required will vary depending on smelter technology (e.g., point-feed prebake or Søderberg) and process control technology (e.g., Pechiney or other).
    (i) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (i)(1) through (30) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (i)(1) through (30) of this section.
    (1) Slope coefficient per potline per month (kg CF4/metric ton Al)/(AE-Mins/cell-day)) (Equation F-2 of §98.63).
    (2) Anode effect minutes per cell-day per potline per month (AE-Mins/cell-day) (Equation F-2).
    (3) Anode effect frequency per potline per month (AE/cell-day) (Equation F-2).
    (4) Anode effect duration per potline per month (minutes) (Equation F-2).
    (5) Metal production of aluminum per potline per month (metric tons) (Equation F-2).
    (6) Overvoltage emission factor per potline per month (kg CF4/metric ton Al) (Equation F-3 of §98.63).
    (7) Metal production of aluminum per potline per month (metric tons) (Equation F-3).
    (8) Weight fraction of C2F6/CF4 per potline per month (kg C2F6/kg CF4) (Equation F-4 of §98.63).
    (9) Net annual prebaked anode consumption (metric tons C/metric tons Al) (Equation F-5 of §98.63).
    (10) Annual metal production of aluminum (metric tons) (Equation F-5).
    (11) Sulfur content in baked anode (weight percent) (Equation F-5).
    (12) Ash content in baked anode (weight percent) (Equation F-5).
    (13) Annual paste consumption (metric ton/metric ton Al) (Equation F-6 of §98.63).
    (14) Annual metal production of aluminum (metric tons) (Equation F-6).
    (15) Annual emissions of cyclohexane soluble matter (kg/metric ton Al) (Equation F-6).
    (16) Binder content of paste (weight percent) (Equation F-6).
    (17) Sulfur content of pitch (weight percent) (Equation F-6).
    (18) Ash content of pitch (weight percent) (Equation F-6).
    (19) Hydrogen content of pitch (weight percent) (Equation F-6).
    (20) Sulfur content in calcined coke (weight percent) (Equation F-6).
    (21) Ash content in calcined coke (weight percent) (Equation F-6).
    (22) Carbon in skimmed dust from Søderberg cells (metric ton C/metric ton Al) (Equation F-6).
    (23) Initial weight of green anodes (metric tons) (Equation F-7 of §98.63).
    (24) Annual hydrogen content in green anodes (metric tons) (Equation F-7).
    (25) Annual baked anode production (metric tons) (Equation F-7).
    (26) Annual waste tar collected (metric tons) (Equation F-7).
    (27) Annual packing coke consumption (metric tons/metric ton baked anode) (Equation F-8 of §98.63).
    (28) Annual baked anode production (metric tons) (Equation F-8).
    (29) Sulfur content in packing coke (weight percent) (Equation F-8).
    (30) Ash content in packing coke (weight percent) (Equation F-8).
G -  Ammonia Manufacturing
(§98.77)
    In addition to the records required by §98.3(g), you must retain the following records specified in paragraphs (a) through (c) of this section for each ammonia manufacturing unit.
    (a) If a CEMS is used to measure emissions, retain records of all feedstock purchases in addition to the requirements in §98.37 for the Tier 4 Calculation Methodology.
    (b) If a CEMS is not used to measure process CO2 emissions, you must also retain the records specified in paragraphs (b)(1) through (b)(2) of this section:
    (1) Records of all analyses and calculations conducted for reported data as listed in §98.76(b).
    (2) Monthly records of carbon content of feedstock from supplier and/or all analyses conducted of carbon content.
    (c) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (c)(1) through (7) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (c)(1) through (7) of this section.
    (1) Volume of each gaseous feedstock used in month (scf of feedstock) (in Equation G-1 of §98.73).
    (2) Carbon content of each gaseous feedstock, for month (kg C per kg of feedstock) (in Equation G-1).
    (3) Molecular weight of each gaseous feedstock per ammonia manufacturing unit with gaseous feedstock (kg/kg-mole) (Equation G-1).
    (4) Volume of each liquid feedstock used in month (gallons of feedstock) (Equation G-2 of §98.73).
    (5) Carbon content of each liquid feedstock, for month (kg C per gallon of feedstock) (Equation G-2).
    (6) Mass of each solid feedstock used in month (kg of feedstock) (Equation G-3 of §98.73).
    (7) Carbon content of each solid feedstock, for month (kg C per kg of feedstock) (Equation G-3).
H -  Cement Production
(§98.87)
    (a) If a CEMS is used to measure CO2 emissions, then in addition to the records required by §98.3(g), you must retain under this subpart the records required for the Tier 4 Calculation Methodology in §98.37.
    (b) If a CEMS is not used to measure CO2 emissions, then in addition to the records required by §98.3(g), you must retain the records specified in this paragraph (b) for each portland cement manufacturing facility.
    (1) Documentation of monthly calculated kiln-specific clinker CO2 emission factor.
    (2) Documentation of quarterly calculated kiln-specific CKD CO2 emission factor.
    (3) Measurements, records and calculations used to determine reported parameters.
    (c) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (c)(1) through (17) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (c)(1) through (17) of this section.
    (1) Identify per kiln per month if clinker is measured directly, or is calculated from raw feed (Equation H-2 of §98.83 and the method in §98.84(d)).
    (2) Quantity of raw kiln feed in month from kiln (tons) (Equation H-2 and the method in §98.84(d)).
    (3) Kiln-specific factor per kiln per month (ton clinker per ton raw feed) (Equation H-2 and the method in §98.84(d)).
    (4) Quantity of clinker produced in month from kiln (tons) (Equation H-2 and the method in §98.84(d)).
    (5) Cement kiln dust (CKD) not recycled to the kiln in quarter from kiln (tons) (Equation H-2 and the method in §98.84(d)).
    (6) Monthly total CaO content of clinker per kiln (weight fraction) (Equation H-3 of §98.83).
    (7) Monthly non-calcined CaO content of clinker per kiln (weight fraction) (Equation H-3).
    (8) Monthly total MgO content of clinker per kiln (weight fraction) (Equation H-3).
    (9) Monthly non-calcined MgO content of clinker per kiln (weight fraction) (Equation H-3).
    (10) Quarterly total CaO content of cement kiln dust not recycled to each kiln (weight fraction) (Equation H-4 of §98.83).
    (11) Quarterly non-calcined CaO content of cement kiln dust not recycled to each kiln (weight fraction) (Equation H-4).
    (12) Quarterly total MgO content of cement kiln dust not recycled to each kiln (weight fraction) (Equation H-4).
    (13) Quarterly non-calcined MgO content of cement kiln dust not recycled to each kiln (weight fraction) (Equation H-4).
    (14) The amount of each raw material consumed annually per kiln (tons/yr (dry basis)) (Equation H-5 of §98.83).
    (15) The amount of each raw kiln feed consumed annually per kiln (tons/yr (dry basis)) (Equation H-5).
    (16) Organic carbon content of each raw material per kiln, as determined in §98.84(c). Default value is 0.002 weight fraction (Equation H-5).
    (17) Organic carbon content of combined raw kiln feed per kiln, as determined in §98.84(c). Default value is 0.002 weight fraction (Equation H-5).

I -- Electronics Manufacturing
(§98.97)

    In addition to the information required by §98.3(g), you must retain the following records:
    (a) All data used and copies of calculations made as part of estimating gas consumption and emissions, including all spreadsheets.
    (b) [Reserved]
    (c) Documentation for the fab-specific engineering model used to apportion fluorinated GHG and N2O consumption. This documentation must be part of your site GHG Monitoring Plan as required under §98.3(g)(5). At a minimum, you must retain the following:
    (1) A clear, detailed description of the fab-specific model, including how it was developed; the quantifiable metric used in the model; all sources of information, equations, and formulas, each with clear definitions of terms and variables; all apportioning factors used to apportion fluorinated GHG and N2O; and a clear record of any changes made to the model while it was used to apportion fluorinated GHG and N2O consumption across process sub-types, process types, tools with and without abatement systems, stack systems, and/or fabs.
    (2) Sample calculations used for developing the gas apportioning factors (fij) for the two fluorinated GHGs used at your facility in the largest quantities, on a mass basis, during the reporting year.
    (3) If you develop apportioning factors through the use of direct measurement according to §98.94(c)(3), calculations and data used to develop each gas apportioning factor.
    (4) Calculations and data used to determine and document that the fab was operating at representative operating levels, as defined in §98.98, during the apportioning model verification specified in §98.94(c).
    (d) For all abatement systems through which fluorinated GHGs or N2O flow at your facility, and for which you are reporting controlled emissions, the following in paragraphs (d)(1) to (9) of this section:
    (1) Records of the information in paragraphs (d)(1)(i) though (iv) of this section:
    (i) Documentation to certify that each abatement system or group of abatement systems is installed, maintained, and operated in accordance with the site maintenance plan for abatement systems that is specified in paragraph (d)(9) of this section.
    (ii) Documentation from the abatement system supplier describing the abatement system's designed purpose and emission control capabilities for fluorinated GHG and N2O for which the systems or group of systems is certified to abate, where available.
    (iii) If you use default destruction or removal efficiency values in your emissions calculations under §98.93(a), (b), and/or (i), certification that the abatement systems for which emissions are being reported were specifically designed for fluorinated GHG and N2O abatement, as required under §98.94(f)(3), and certification that the site maintenance plan includes manufacturer's recommendations and specifications for installation, operation, and maintenance for all applicable abatement systems.
    (iv) Certification that you have included and accounted for all abatement systems and any respective downtime in your emissions calculations under §98.93(i)(3), as required under §98.94(f)(3).
    (2) Abatement system calibration and maintenance records.
    (3) Where the default destruction or removal efficiency value is used, documentation from the abatement system supplier describing the equipment's designed purpose and emission control capabilities for fluorinated GHG and N2O.
    (4) Where properly measured site-specific destruction or removal efficiencies are used to report emissions, the information in paragraphs (d)(4)(i) though (vi) of this section:
    (i) Dated certification by the technician who made the measurement that the destruction or removal efficiency is calculated in accordance with methods in EPA 430-R-10-003 (incorporated by reference, see §98.7) and, if applicable Appendix A of this subpart, or an alternative method approved by the Administrator as specified in §98.94(k), complete documentation of the results of any initial and subsequent tests, the final report as specified in EPA 430-R-10-003 (incorporated by reference, see §98.7) and, if applicable, the records and documentation specified in Appendix A of this subpart including the information required in paragraph (b)(7) of Appendix A of this subpart, or a final report as specified in an alternative method approved by the Administrator as specified in §98.94(k).
    (ii) The average destruction or removal efficiency of the abatement systems operating during the reporting year for each process type and gas combination.
    (iii) A description of the calculation used to determine the average destruction or removal efficiency for each process type and gas combination, including all inputs to the calculation.
    (iv) The records of destruction or removal efficiency measurements for abatement systems for all tests that have been used to determine the site-specific destruction or removal efficiencies currently being used.
    (v) A description of the method used for randomly selecting abatement systems for testing.
    (vi) The total number of systems for which destruction or removal efficiency was properly measured for each process type and gas combination for the reporting year.
    (5) In addition to the inventory specified in §98.96(p), the information in paragraphs (d)(5)(i) though (iii) of this section:
    (i) The number of abatement systems of each manufacturer, and model numbers, and the manufacturer's claimed fluorinated GHG and N2O destruction or removal efficiency, if any.
    (ii) Records of destruction or removal efficiency measurements over the in-use life of each abatement system.
    (iii) A description of the tool, with the process type or sub-type, for which the abatement system treats exhaust.
    (6) Records of all inputs and results of calculations made accounting for the uptime of abatement systems used during the reporting year, in accordance with Equations I-15 or I-23 of this subpart, as applicable. The inputs should include an indication of whether each value for destruction or removal efficiency is a default value or a measured site-specific value.
    (7) Records of all inputs and results of calculations made to determine the average weighted fraction of each gas destroyed or removed in the abatement systems for each stack system using Equation I-24 of this subpart, if applicable. The inputs should include an indication of whether each value for destruction or removal efficiency is a default value or a measured site-specific value.
    (8) Records of all inputs and the results of the calculation of the facility-wide emission destruction or removal efficiency factor calculated according to Equations I-26, I-27, and I-28 of this subpart.
    (9) A site maintenance plan for abatement systems, which must be maintained on-site at the facility as part of the facility's GHG Monitoring Plan as described in §98.3(g)(5), and be developed and implemented according to paragraphs (d)(9)(i) through (iii) of this section.
    (i) The site maintenance plan for abatement systems must be based on the abatement system manufacturer's recommendations and specifications for installation, operation, and maintenance if you use default destruction and removal efficiency values in your emissions calculations under §98.93(a), (b), and/or (i). If the manufacturer's recommendations and specifications for installation, operation, and maintenance are not available, you cannot use default destruction and removal efficiency values in your emissions calculations under §98.93(a), (b), and/or (i). If you use an average of properly measured destruction or removal efficiencies determined in accordance with the procedures in §98.94(f)(4)(i) through (vi), the site maintenance plan for abatement systems must be based on the abatement system manufacturer's recommendations and specifications for installation, operation, and maintenance, where available. If you deviate from the manufacturer's recommendations and specifications, you must include documentation that demonstrates how the deviations do not negatively affect the performance or destruction or removal efficiency of the abatement systems.
    (ii) The site maintenance plan for abatement systems must include a defined preventative maintenance process and checklist.
    (iii) The site maintenance plan for abatement systems must include a corrective action process that you must follow whenever an abatement system is found to be not operating properly.
    (e) Purchase records for gas purchased.
    (f) Invoices for gas purchases and sales.
    (g) Documents and records used to monitor and calculate abatement system uptime.
    (h) GHG Monitoring Plans, as described in §98.3(g)(5), must be completed by April 1, 2011. You must update your GHG Monitoring Plan to comply with §98.94(c) consistent with the requirements in §98.3(g)(5)(iii).
    (i) Retain the following records for each fab for which you elect to calculate fab-level emissions of fluorinated GHG using the procedures specified in §98.93(i)(3) or (4).
    (1) Document all stack systems with emissions of fluorinated GHG that are less than 10,000 metric tons of CO2e per year and all stack systems with emissions of 10,000 metric tons CO2e per year or more. Include the data and calculation used to develop the preliminary estimate of emissions for each stack system.
    (2) For each stack system, identify the method used to calculate annual emissions; either §98.93(i)(3) or (4).
    (3) The identity and total annual consumption of each gas identified as an intermittent low use fluorinated GHG as specified in §98.93(i)(4)(i) and defined in §98.98.
    (4) The emissions test data and reports (see §98.94(j)(4)) and the calculations used to determine the fab-specific emission factor, including the actual fab-specific emission factor, the average hourly emission rate of each fluorinated GHG from the stack system during the test and the stack system activity rate during the test. The report must also contain any changes in the stack system configuration during or between tests in a reporting year.
    (5) The fab-specific emission factor and the calculations and data used to determine the fab-specific emission factor for each fluorinated GHG and by-product, as calculated using Equations I-19 and I-20 of §98.93(i)(3).
    (6) Calculations and data used to determine annual emissions of each fluorinated GHG for each fab.
    (7) Calculations and data used to determine and document that the fab was operating at representative operating levels, as defined in §98.98, during the stack testing period.
    (8) A copy of the certification that no significant changes in stack system flow configuration occurred between tests conducted for any particular fab in a reporting year, as required by §98.94(j)(1)(iv) and any calculations and data supporting the certification.
    (9) The number of tools vented to each stack system in the fab.
    (j) If you report the approximate percentage of total GHG emissions from research and development activities under §98.96(x), documentation for the determination of the percentage of total emissions of each fluorinated GHG and/or N2O attributable to research and development activities, as defined in §98.6.
    (k) Annual gas consumption for each fluorinated GHG and N2O as calculated in Equation I-11 of this subpart, including where your fab used less than 50 kg of a particular fluorinated GHG or N2O used at your facility for which you have not calculated emissions using Equations I-6, I-7, I-8, I-9, I-10, I-21, or I-22 of this subpart, the chemical name of the GHG used, the annual consumption of the gas, and a brief description of its use.
    (l) All inputs used to calculate gas consumption in Equation I-11 of this subpart, for each fluorinated GHG and N2O used.
    (m) Annual amount of each fluorinated GHG consumed for process sub-type, process type, stack system, or fab, as appropriate, and the annual amount of N2O consumed for the aggregate of all chemical vapor deposition processes and for the aggregate of all other electronics manufacturing production processes, as calculated using Equation I-13 of this subpart.
    (n) Disbursements for each fluorinated GHG and N2O during the reporting year, as calculated using Equation I-12 of this subpart and all inputs used to calculate disbursements for each fluorinated GHG and N2O used in Equation I-12 of this subpart, including all fab-wide gas-specific heel factors used for each fluorinated GHG and N2O. If your fab used less than 50 kg of a particular fluorinated GHG during the reporting year, fab-wide gas-specific heel factors do not need to be reported for those gases.
    (o) Fraction of each fluorinated GHG or N2O fed into a process sub-type, process type, stack system, or fab that is fed into tools connected to abatement systems.
    (p) Fraction of each fluorinated GHG or N2O destroyed or removed in abatement systems connected to process tools where process sub-type, process type j is used, or to process tools vented to stack system j or fab f.
    (q) All inputs and results of calculations made accounting for the uptime of abatement systems used during the reporting year, or during an emissions sampling period, in accordance with Equations I-15 and/or I-23 of this subpart, as applicable.
    (r) For fluorinated heat transfer fluid emissions, inputs to the fluorinated heat transfer fluid mass balance equation, Equation I-16 of this subpart, for each fluorinated heat transfer fluid used.
    (s) Where missing data procedures were used to estimate inputs into the fluorinated heat transfer fluid mass balance equation under §98.95(b), the estimates of those data.
Subpart K  -  Ferroalloy Production
(§98.117)

In addition to the records required by §98.3(g), you must retain the records specified in paragraphs (a) through (e) of this section for each EAF, as applicable.
(a) If a CEMS is used to measure CO2 emissions according to the requirements in §98.113(a), then you must retain under this subpart the records required for the Tier 4 Calculation Methodology in §98.37 and the information specified in paragraphs (a)(1) through (a)(3) of this section.
(1) Monthly EAF production quantity for each ferroalloy product (tons).
(2) Number of EAF operating hours each month.
(3) Number of EAF operating hours in a calendar year.
(b) If the carbon mass balance procedure is used to determine CO2 emissions according to the requirements in §98.113(b)(2), then you must retain records for the information specified in paragraphs (b)(1) through (b)(5) of this section.
(1) Monthly EAF production quantity for each ferroalloy product (tons).
(2) Number of EAF operating hours each month.
(3) Number of EAF operating hours in a calendar year.
(4) Monthly material quantity consumed, used, or produced for each material included for the calculations of annual process CO2 emissions (tons).
(5) Average carbon content determined and records of the supplier provided information or analyses used for the determination for each material included for the calculations of annual process CO2 emissions.
(c) You must keep records that include a detailed explanation of how company records of measurements are used to estimate the carbon input and output to each EAF, including documentation of specific input or output materials excluded from Equation K-1 of this subpart that contribute less than 1 percent of the total carbon into or out of the process. You also must document the procedures used to ensure the accuracy of the measurements of materials fed, charged, or placed in an EAF including, but not limited to, calibration of weighing equipment and other measurement devices. The estimated accuracy of measurements made with these devices must also be recorded, and the technical basis for these estimates must be provided.
(d) If you are required to calculate CH4 emissions for the EAF as specified in §98.113(d), you must maintain records of the total amount of each alloy product produced for the specified reporting period, and the appropriate alloy-product specific emission factor used to calculate the CH4 emissions.
(e) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (e)(1) through (13) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (e)(1) through (13) of this section.
(1) Carbon content in reducing agent (percent by weight, expressed as a decimal fraction) (Equation K-1 of §98.113).
(2) Annual mass of reducing agent fed, charged, or otherwise introduced into the EAF (tons) (Equation K-1).
(3) Carbon content of carbon electrode (percent by weight, expressed as a decimal fraction) (Equation K-1).
(4) Annual mass of carbon electrode consumed in the EAF (tons) (Equation K-1).
(5) Carbon content in ore (percent by weight, expressed as a decimal fraction) (Equation K-1).
(6) Annual mass of ore charged to the EAF (tons) (Equation K-1).
(7) Carbon content in flux material (percent by weight, expressed as a decimal fraction) (Equation K-1).
(8) Annual mass of flux material fed, charged, or otherwise introduced into the EAF to facilitate slag formation (tons) (Equation K-1).
(9) Carbon content in alloy product (percent by weight, expressed as a decimal fraction) (Equation K-1).
(10) Annual mass of alloy product produced/tapped in the EAF (tons) (Equation K-1).
(11) Carbon content in non-product outgoing material (percent by weight, expressed as a decimal fraction) (Equation K-1).
(12) Annual mass of non-product outgoing material removed from EAF (tons) (Equation K-1).
(13) CH4 emission factor selected from Table K-1 of this subpart for each product (kg of CH4 emissions/metric ton of alloy product) (Equation K-3 of §98.113).

Subpart L  -  Fluorinated Gas Production
(§98.127)

    In addition to the records required by §98.3(g), you must retain the dated records specified in paragraphs (a) through (l) of this section, as applicable.
    (a) Process information records. (1) Identify all products and processes subject to this subpart. Include the unit identification as appropriate, the generic process identification reported for the process under §98.126(a)(2)(i) through (iii), and the product with which the process is associated.
    (2) Monthly and annual records, as applicable, of all analyses and calculations conducted as required under §98.123, including the data monitored under §98.124, and all information reported as required under §98.126.
    (3) Identify all fluorinated GHGs with emissions of 1,000 metric tons CO2e or more from production and transformation processes, summed across the facility as a whole, and identify all fluorinated GHGs with total emissions less than 1,000 metric tons CO2e from production and transformation processes, summed across the facility as a whole.
    (4) Calculations used to determine the total GWP-weighted emissions of fluorinated GHGs by fluorinated GHG group for each process, in metric tons CO2e.
    (b) Scoping speciation. Retain records documenting the information collected under §98.124(a).
    (c) Mass balance method. Retain the following records for each process for which the mass balance method was used to estimate emissions in reporting years 2011, 2012, 2013, or 2014. If you used an element other than fluorine in the mass balance equation pursuant to the former §98.123(b)(3) as included in paragraph 1 of Appendix A of this subpart for the former mass balance method, substitute that element for fluorine in the recordkeeping requirements of this paragraph.
    (1) The data and calculations used to estimate the absolute and relative errors associated with use of the mass-balance approach.
    (2) The data and calculations used to estimate the mass of fluorine emitted from the process.
    (3) The data and calculations used to determine the fractions of the mass emitted consisting of each reactant (FERd), product (FEP), and by-product (FEBk), including the preliminary calculations in the former §98.123(b)(8)(i).
    (d) Emission factor and emission calculation factor method. Retain the following records for each process for which the emission factor or emission calculation factor method was used to estimate emissions.
    (1) Identify all continuous process vents with emissions of fluorinated GHGs that are less than 10,000 metric tons CO2e per year and all continuous process vents with emissions of 10,000 metric tons CO2e per year or more. Include the data and calculation used to develop the preliminary estimate of emissions for each process vent.
    (2) Identify all batch process vents.
    (3) For each vent, identify the method used to develop the factor (i.e., emission factor by emissions test or emission calculation factor).
    (4) The emissions test data and reports (see §98.124(c)(5)) and the calculations used to determine the process-vent-specific emission factor, including the actual process-vent-specific emission factor, the average hourly emission rate of each fluorinated GHG from the process vent during the test and the process feed rate, process production rate, or other process activity rate during the test.
    (5) The process-vent-specific emission calculation factor and the calculations used to determine the process-vent-specific emission calculation factor.
    (6) The annual process production quantity or other process activity information in the appropriate units, along with the dates and time period during which the process was operating and dates and time periods the process vents are vented to the destruction device. As an alternative to date and time periods when process vents are vented to the destruction device, a facility may track dates and time periods that process vents by-pass the destruction device.
    (7) Calculations used to determine annual emissions of each fluorinated GHG for each process and the total fluorinated GHG emissions for all processes, i.e., total for facility.
    (e) Destruction efficiency testing. A fluorinated GHG production facility that destroys fluorinated GHGs and reflects this destruction in §98.123 must retain the emissions performance testing reports (including revised reports) for each destruction device. The emissions performance testing report must contain all information and data used to derive the destruction efficiency for each fluorinated GHG whose destruction the facility reflects in §98.123, as well as the key process and device conditions during the test. This information includes the following:
    (1) Destruction efficiency (DE) determined for each fluorinated GHG whose destruction the facility reflects in §98.123, in accordance with §98.124(g)(1)(i) through (iv).
    (2) Chemical identity of the fluorinated GHG(s) used in the performance test conducted to determine destruction efficiency, including surrogates, and information on why the surrogate is sufficient to demonstrate destruction efficiency for each fluorinated GHG, consistent with requirements in §98.124(g)(1)(i) through (iv), vented to the destruction device.
    (3) Mass flow rate of the stream containing the fluorinated GHG(s) or surrogate into the device during the test.
    (4) Concentration (mass fraction) of each fluorinated GHG or surrogate in the stream flowing into the device during the test.
    (5) Concentration (mass fraction) of each fluorinated GHG or surrogate at the outlet of the destruction device during the test.
    (6) Mass flow rate at the outlet of the destruction device during the test.
    (7) Test methods and analytical methods used to determine the mass flow rates and fluorinated GHG (or surrogate) concentrations of the streams flowing into and out of the destruction device during the test.
    (8) Destruction device conditions that are normally monitored for device control, such as temperature, total mass flow rates into the device, and CO or O2 levels.
    (9) Name of all applicable Federal or State regulations that may apply to the destruction process.
    (f) Equipment leak records. If you are subject to §98.123(d) of this subpart, you must maintain information on the number of each type of equipment; the service of each piece of equipment (gas, light liquid, heavy liquid); the concentration of each fluorinated GHG in the stream; each piece of equipment excluded from monitoring requirement; the time period each piece of equipment was in service, and the emission calculations for each fluorinated GHG for all processes. Depending on which equipment leak monitoring approach you follow, you must maintain information for equipment on the associated screening data concentrations for greater than or equal to 10,000 ppmv and associated screening data concentrations for less than 10,000 ppmv; associated actual screening data concentrations; and associated screening data and leak rate data (i.e., bagging) used to develop a unit-specific correlation. If you developed and follow a site-specific leak detection approach, provide the records for monitoring events and the emissions estimation calculations, as appropriate, consistent with the approach for equipment leak emission estimation in your GHG Monitoring Plan.
    (g) Container heel records. If you vent residual fluorinated GHGs from containers, maintain the following records of the measurements and calculations used to estimate emissions of residual fluorinated GHGs from containers.
    (i) If you measure the contents of each container, maintain records of these measurements and the calculations used to estimate emissions of each fluorinated GHG from each container size and type.
    (ii) If you develop and apply container heel factors to estimate emissions, maintain records of the measurements and calculations used to develop the heel factor for each fluorinated GHG and each container size and type and of the number of containers of each fluorinated GHG and of each container size and type returned to your facility.
    (h) Missing data records. Where missing data have been estimated pursuant to §98.125, you must record the reason the data were missing, the length of time the data were missing, the method used to estimate the missing data, and the estimates of those data.
    (i) All facilities. Dated records documenting the initial and periodic calibration of all analytical equipment used to determine the concentration of fluorinated GHGs, including but not limited to gas chromatographs, gas chromatography-mass spectrometry (GC/MS), gas chromatograph-electron capture detector (GC/ECD), fourier transform infrared (FTIR), and nuclear magnetic resonance (NMR) devices, and all mass measurement equipment such as weigh scales, flowmeters, and volumetric and density measures used to measure the quantities reported under this subpart, including the industry standards or manufacturer directions used for calibration pursuant to §98.124(e), (f), (g), (m), and (n).
    (j) GHG Monitoring Plans, as described in §98.3(g)(5), must be completed by April 1, 2011.
    (k) For fluorinated GHGs whose GWPs are not listed in Table A-1 to subpart A of this part, maintain records of the GWPs used to calculate facility-wide CO2e emissions under §98.127(j). Where you used your best estimate of the GWP, maintain records of the data and analysis used to develop that GWP, including the data elements at §98.123(c)(1)(vi)(A)(1)through (3). If you have used QSARs to estimate the GWP, include information documenting the level of accuracy of the QSAR-derived GWP, including information on how the structure of the "target" fluorinated GHG is similar to the structures of the fluorinated GHGs used to model the radiative forcing and/or reaction rate of the "target" fluorinated GHG, the quality and quantity of the measurements of the radiative forcings and/or reaction rates of the fluorinated GHGs used to model these parameters for the "target" fluorinated GHG, any estimated uncertainties of the modeled forcings and/or reaction rates, and descriptions and results of any efforts to validate the QSAR model(s).
    (l) Verification software records. For reporting year 2015 and thereafter, you must enter into verification software specified in §98.5(b) the data specified in paragraphs (l)(1) through (15) of this section. The data specified in paragraphs (l)(1) through (11) must be entered for each process and each process vent, as applicable. The data specified in paragraphs (l)(1) through (15) must be entered for each fluorinated GHG, as applicable. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (l)(1) through (15) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (l)(1) through (15) of this section.
    (1) The identity of the process vent (e.g., name or number assigned by the facility).
    (2) The equation used to estimate emissions from the process vent (Equations L-21, L-22, L-26, or L-27).
    (3) The type of process activity used to estimate emissions from the process vent (e.g., product of process or reactant consumed by process) (Activity, ActivityC, or ActivityU) (Equations L-21, L-22, L-26, L-27, L-35).
    (4) The quantities of the process activity used to estimate controlled and uncontrolled emissions, respectively, for the process vent, Activity, ActivityU, or ActivityC, (e.g. kg product) (Equations L-21, L-22, L-26, L-27, L-35).
    (5) The site-specific, process-vent-specific emission factor, EFPV-C, for the process vent, measured after the destruction device (kg fluorinated GHG emitted per kg activity) (Equation L-21).
    (6) The site-specific, process-vent-specific emission calculation factor, ECFPV-U, for the process vent, for periods not vented to destruction device (kg fluorinated GHG emitted per kg activity) (Equations L-21, L-35).
    (7) The site-specific, process-vent-specific emission factor(s), EFPV-U, for the process vent, measured before the destruction device (kg fluorinated GHG emitted per kg activity) (Equations L-22, L-35).
    (8) The site-specific, process-vent-specific emission calculation factor for the process vent, ECFPV (kg fluorinated GHG emitted per kg of activity) (Equations L-26, L-27, L-35).
    (9) Destruction efficiency, DE, of each destruction device for each fluorinated GHG whose destruction the facility reflects in §98.123, in accordance with §98.124(g)(1)(i) through (iv) (weight fraction) (Equations L-22, L-27, L-31).
    (10) Emissions of each fluorinated GHG for equipment pieces for the process, EELf (metric ton/yr) (98.123(d)(3)).
    (11) The mass of the fluorinated GHG previously produced and fed into the destruction device, RED, (metric tons) (Equation L-31).
    (12) If applicable, the heel factor, hfj, calculated for each container size and type (decimal fraction) (Equation L-34).
    (13) If applicable, the number of containers of size and type j returned to the fluorinated gas production facility, Nfj, (Equation L-34).
    (14) If applicable, the full capacity of containers of size and type j containing fluorinated GHG f, Ffj, (metric tons) (Equation L-34).
    (15) For fluorinated GHGs that do not have a chemical-specific GWP on Table A-1 of subpart A of this part, the fluorinated GHG group of which the fluorinated GHG is a member, as applicable (to permit look-up of global warming potential, GWPf, or GWPi, for that fluorinated GHG in Table A-1 of subpart A of this part (Equation A-1 of subpart A of this part, Equation L-35)).

Subpart N  -  Glass Production
(§98.147)

    In addition to the information required by §98.3(g), you must retain the records listed in paragraphs (a) through (d) of this section.
    (a) If a CEMS is used to measure emissions, then you must retain the records required under §98.37 for the Tier 4 Calculation Methodology and the following information specified in paragraphs (a)(1) and (a)(2) of this section:
    (1) Monthly glass production rate for each continuous glass melting furnace (tons).
    (2) Monthly amount of each carbonate-based raw material charged to each continuous glass melting furnace (tons).
    (b) If process CO2 emissions are calculated according to the procedures specified in §98.143(b), you must retain the records in paragraphs (b)(1) through (b)(5) of this section.
    (1) Monthly glass production rate for each continuous glass melting furnace (metric tons).
    (2) Monthly amount of each carbonate-based raw material charged to each continuous glass melting furnace (metric tons).
    (3) Data on carbonate-based mineral mass fractions provided by the raw material supplier for all raw materials consumed annually and included in calculating process emissions in Equation N-1 of this subpart.
    (4) Results of all tests used to verify the carbonate-based mineral mass fraction for each carbonate-based raw material charged to a continuous glass melting furnace, including the data specified in paragraphs (b)(4)(i) through (b)(4)(v) of this section.
    (i) Date of test.
    (ii) Method(s), and any variations of the methods, used in the analyses.
    (iii) Mass fraction of each sample analyzed.
    (iv) Relevant calibration data for the instrument(s) used in the analyses.
    (v) Name and address of laboratory that conducted the tests.
    (5) The decimal fraction of calcination achieved for each carbonate-based raw material, if a value other than 1.0 is used to calculate process mass emissions of CO2.
    (c) All other documentation used to support the reported GHG emissions.
    (d) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (d)(1) through (3) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (d)(1) through (3) of this section.
    (1) Annual average decimal mass fraction of carbonate-based mineral in each carbonate-based raw material for each continuous glass melting furnace (specify the default value, if used, or the value determined according to §98.144) (percentage, expressed as a decimal) (Equation N-1 of §98.143).
    (2) Annual amount of each carbonate-based raw material charged to each continuous glass melting furnace (tons) (Equation N-1).
    (3) Decimal fraction of each calcination achieved for carbonate-based raw material for each continuous glass melting furnace (specify the default value, if used, or the value determined according to §98.144) (percentage, expressed as a decimal) (Equation N-1).

Subpart O  -  HCFC-22 Production and HFC-23 Destruction
(§98.157)

    (a) In addition to the data required by §98.3(g), HCFC-22 production facilities shall retain the following records:
    (1) The data used to estimate HFC-23 emissions.
    (2) Records documenting the initial and periodic calibration of the gas chromatographs, weigh scales, volumetric and density measurements, and flowmeters used to measure the quantities reported under this rule, including the industry standards or manufacturer directions used for calibration pursuant to §98.154(p) and (q).
    (b) In addition to the data required by §98.3(g), the HFC-23 destruction facilities shall retain the following records:
    (1) Records documenting their one-time and annual reports in §98.156(b) through (e).
    (2) Records documenting the initial and periodic calibration of the gas chromatographs, weigh scales, volumetric and density measurements, and flowmeters used to measure the quantities reported under this subpart, including the industry standard practice or manufacturer directions used for calibration pursuant to §98.154(p) and (q).
    (c) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (c)(1) through (16) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (c)(1) through (16) of this section.
    (1) Factor to account for the loss of HCFC-22 upstream of the measurement over the period, determined pursuant to §98.154(e) (Equation O-3 of §98.153).
    (2) Mass of HCFC-22 that is measured coming out of the production process over the period. A period can be one year (kg) (Equation O-3).
    (3) Mass of used HCFC-22 that is added to the production process upstream of the output measurement over the period. A period can be one year (kg) (Equation O-3).
    (4) Mass of HFC-23 generated annually per HCFC-22 production process (metric tons) (Equation O-4 of §98.153).
    (5) Mass of HFC-23 sent off site for sale annually per HCFC-22 production process (metric tons) (Equation O-4).
    (6) Mass of HFC-23 sent off site for destruction annually per HCFC-22 production process (metric tons) (Equation O-4).
    (7) Mass of HFC-23 destroyed on site per HCFC-22 production process (metric tons) (Equation O-4).
    (8) HFC-23 in storage at end of year per HCFC-22 production process (metric tons) (Equation O-4).
    (9) HFC-23 in storage at beginning of year per HCFC-22 production process (metric tons) (Equation O-4).
    (10) Mass of HFC-23 fed into each destruction device annually per HCFC-22 production process (metric tons) (Equation O-9 of §98.153 and the calculation method in either §98.154(l)(1) or (2)).
    (11) Identify if each destruction efficiency for each HCFC-22 production process is entered directly, or is calculated using §98.154(l)(1), or is calculated using §98.154(l)(2) (Equation O-9 and the calculation method in either §98.154(l)(1) or (2)).
    (12) Destruction efficiency of each destruction device for each HCFC-22 production process (decimal fraction) (Equation O-9 and the calculation method in either §98.154(l)(1) or (2)).
    (13) Volumetric flow rate at the inlet of each destruction device for each HCFC-22 production process from previous test (kg/hr) (Equation O-9 and the calculation method in either §98.154(l)(1) or (2)).
    (14) Volumetric flow rate at the inlet of destruction device during test for each HCFC-22 production process (kg/hr) (Equation O-9 and the calculation method in either §98.154(l)(1) or (2)).
    (15) Concentration of HFC-23 at the inlet of destruction device for each HCFC-22 production process from previous test (weight fraction) (Equation O-9 and the calculation method in either §98.154(l)(1) or (2)).
    (16) Concentration of HFC-23 at the inlet of destruction device for each HCFC-22 production process during test (weight fraction) (Equation O-9 and the calculation method in either §98.154(l)(1) or (2)).

Subpart P  -  Hydrogen Production
(§98.167)

    In addition to the information required by §98.3(g), you must retain the records specified in paragraphs (a) through (e) of this section for each hydrogen production facility.
    (a) If a CEMS is used to measure CO2 emissions, then you must retain under this subpart the records required for the Tier 4 Calculation Methodology in §98.37.
    (b) If a CEMS is not used to measure CO2 emissions, then you must retain records of all analyses and calculations conducted as listed in §§98.166(b), (c), and (d).
    (c) For units using the calculation methodologies described in §98.163(b), the records required under §98.3(g) must include both the company records and a detailed explanation of how company records are used to estimate the following:
    (1) Fuel and feedstock consumption, when solid fuel and feedstock is combusted and a CEMS is not used to measure GHG emissions.
    (2) Fossil fuel consumption, when, pursuant to §98.33(e), the owner or operator of a unit that uses CEMS to quantify CO2 emissions and that combusts both fossil and biogenic fuels separately reports the biogenic portion of the total annual CO2 emissions.
    (3) Sorbent usage, if the methodology in §98.33(d) is used to calculate CO2 emissions from sorbent.
    (d) The owner or operator must document the procedures used to ensure the accuracy of the estimates of fuel and feedstock usage and sorbent usage (as applicable) in §98.163(b), including, but not limited to, calibration of weighing equipment, fuel and feedstock flow meters, and other measurement devices. The estimated accuracy of measurements made with these devices must also be recorded, and the technical basis for these estimates must be provided.
    (e) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (e)(1) through (12) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (e)(1) through (12) of this section.
    (1) Indicate whether the monthly consumption of each gaseous fuel or feedstock is measured as mass or volume (Equation P-1 of §98.163).
    (2) Monthly volume of the gaseous fuel or feedstock (scf at standard conditions of 68 °F and atmospheric pressure) (Equation P-1).
    (3) Monthly mass of the gaseous fuel or feedstock (kg of fuel or feedstock) (Equation P-1).
    (4) Average monthly carbon content of the gaseous fuel or feedstock (kg C per kg of fuel or feedstock) (Equation P-1).
    (5) Average monthly molecular weight of the gaseous fuel or feedstock (kg/kg-mole) (Equation P-1).
    (6) Indicate whether the monthly consumption of each liquid fuel or feedstock is measured as mass or volume (Equation P-2 of §98.163).
    (7) Monthly volume of the liquid fuel or feedstock (gallons of fuel or feedstock) (Equation P-2).
    (8) Monthly mass of the liquid fuel or feedstock (kg of fuel or feedstock) (Equation P-2).
    (9) Average monthly carbon content of the liquid fuel or feedstock (kg C per gallon of fuel or feedstock) (Equation P-2).
    (10) Average monthly carbon content of the liquid fuel or feedstock (kg C per kg of fuel or feedstock) (Equation P-2).
    (11) Monthly mass of solid fuel or feedstock (kg of fuel and feedstock) (Equation P-3 of §98.163).
    (12) Average monthly carbon content of the solid fuel or feedstock (kg C per kg of fuel and feedstock) (Equation P-3).

Subpart Q  -  Iron and Steel Production
(§98.177)

    In addition to the records required by §98.3(g), you must retain the records specified in paragraphs (a) through (f) of this section, as applicable. Facilities that use CEMS to measure emissions must also retain records of the verification data required for the Tier 4 Calculating Methodology in §98.36(e).
    (a) Records of all analyses and calculations conducted, including all information reported as required under §98.176.
    (b) When the carbon mass balance method is used to estimate emissions for a process, the monthly mass of each process input and output that are used to determine the annual mass, except that no determination of the mass of steel output from decarburization vessels is required.
    (c) Production capacity (in metric tons per year) for the production of taconite pellets, coke, sinter, iron, and raw steel.
    (d) Annual operating hours for each taconite indurating furnace, basic oxygen furnace, non-recovery coke oven battery, sinter process, electric arc furnace, decarburization vessel, and direct reduction furnace.
    (e) Facilities must keep records that include a detailed explanation of how company records or measurements are used to determine all sources of carbon input and output and the metric tons of coal charged to the coke ovens (e.g., weigh belts, a combination of measuring volume and bulk density). You also must document the procedures used to ensure the accuracy of the measurements of fuel usage including, but not limited to, calibration of weighing equipment, fuel flow meters, coal usage including, but not limited to, calibration of weighing equipment and other measurement devices. The estimated accuracy of measurements made with these devices must also be recorded, and the technical basis for these estimates must be provided.
    (f) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (f)(1) through (9) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (f)(1) through (9) of this section.
    (1) The data in paragraphs (f)(1)(i) through (xxv) of this section for each applicable taconite indurating furnace for which the carbon mass balance method of reporting is used.
    (i) Annual mass of each solid fuel (metric tons) (Equation Q-1 of §98.173).
    (ii) Carbon content of each solid fuel, from the fuel analysis (expressed as a decimal fraction) (Equation Q-1).
    (iii) Annual volume of each gaseous fuel (scf) (Equation Q-1).
    (iv) Average carbon content of each gaseous fuel, from the fuel analysis results (kg C per kg of fuel) (Equation Q-1).
    (v) Molecular weight of each gaseous fuel (kg/kg-mole) (Equation Q-1).
    (vi) Annual volume of each liquid fuel (gallons) (Equation Q-1).
    (vii) Carbon content of each liquid fuel, from the fuel analysis results (kg C per gallon of fuel) (Equation Q-1).
    (viii) Annual mass of the greenball (taconite) pellets fed to the furnace (metric tons) (Equation Q-1).
    (ix) Carbon content of the greenball (taconite) pellets, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-1).
    (x) Annual mass of fired pellets produced by the furnace (metric tons) (Equation Q-1).
    (xi) Carbon content of the fired pellets, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-1).
    (xii) Annual mass of air pollution control residue collected (metric tons) (Equation Q-1).
    (xiii) Carbon content of the air pollution control residue, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-1).
    (xiv) Annual mass of each other solid input containing carbon fed to each furnace (metric tons) (Equation Q-1).
    (xv) Carbon content of each other solid input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-1).
    (xvi) Annual mass of each other solid output containing carbon produced by each furnace (metric tons) (Equation Q-1).
    (xvii) Carbon content of each other solid output containing carbon (expressed as a decimal fraction) (Equation Q-1).
    (xviii) Annual mass of each other gaseous input containing carbon fed to each furnace (metric tons) (Equation Q-1).
    (xix) Carbon content of each other gaseous input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-1).
    (xx) Annual mass of each other gaseous output containing carbon produced by each furnace (metric tons) (Equation Q-1).
    (xxi) Carbon content of each other gaseous output containing carbon produced by each furnace (expressed as a decimal fraction) (Equation Q-1).
    (xxii) Annual mass of each other liquid input containing carbon fed to each furnace (metric tons) (Equation Q-1).
    (xxiii) Carbon content of each other liquid input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-1).
    (xxiv) Annual mass of each other liquid output containing carbon produced by each furnace (metric tons) (Equation Q-1).
    (xxv) Carbon content of each other liquid output containing carbon produced by each furnace (expressed as a decimal fraction) (Equation Q-1).
    (2) The data in paragraphs (f)(2)(i) through (xxvi) of this section for each applicable basic oxygen process furnace for which the carbon mass balance method of reporting is used.
    (i) Annual mass of molten iron charged to the furnace (metric tons) (Equation Q-2 of §98.173).
    (ii) Carbon content of the molten iron charged to the furnace, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-2).
    (iii) Annual mass of ferrous scrap charged to the furnace (metric tons) (Equation Q-2).
    (iv) Carbon content of the ferrous scrap charged to the furnace, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-2).
    (v) Annual mass of the flux materials (e.g., limestone, dolomite) charged to the furnace (metric tons) (Equation Q-2).
    (vi) Carbon content of the flux materials charged to the furnace, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-2).
    (vii) Annual mass of the carbonaceous materials (e.g., coal, coke) charged to the furnace (metric tons) (Equation Q-2).
    (viii) Carbon content of the carbonaceous materials charged to the furnace, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-2).
    (ix) Annual mass of molten raw steel produced by the furnace (metric tons) (Equation Q-2).
    (x) Carbon content of the steel produced by the furnace, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-2).
    (xi) Annual mass of slag produced by the furnace (metric tons) (Equation Q-2).
    (xii) Carbon content of the slag produced by the furnace, from the carbon analysis (expressed as a decimal fraction) (Equation Q-2).
    (xiii) Annual mass of air pollution control residue collected for the furnace (metric tons) (Equation Q-2).
    (xiv) Carbon content of the air pollution control residue collected for the furnace, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-2).
    (xv) Annual mass of each other solid input containing carbon fed to each furnace (metric tons) (Equation Q-2).
    (xvi) Carbon content of each other solid input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-2).
    (xvii) Annual mass of each other solid output containing carbon produced by each furnace (metric tons) (Equation Q-2).
    (xviii) Carbon content of each other solid output containing carbon (expressed as a decimal fraction) (Equation Q-2).
    (xix) Annual mass of each other gaseous input containing carbon fed to each furnace (metric tons) (Equation Q-2).
    (xx) Carbon content of each other gaseous input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-2).
    (xxi) Annual mass of each other gaseous output containing carbon produced by each furnace (metric tons) (Equation Q-2).
    (xxii) Carbon content of each other gaseous output containing carbon produced by each furnace (expressed as a decimal fraction) (Equation Q-2).
    (xxiii) Annual mass of each other liquid input containing carbon fed to each furnace (metric tons) (Equation Q-2).
    (xxiv) Carbon content of each other liquid input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-2).
    (xxv) Annual mass of each other liquid output containing carbon produced by each furnace (metric tons) (Equation Q-2).
    (xxvi) Carbon content of each other liquid output containing carbon produced by each furnace (expressed as a decimal fraction) (Equation Q-2).
    (3) The data in paragraphs (f)(3)(i) through (xviii) of this section for each applicable non-recovery coke oven battery for which the carbon mass balance method of reporting is used.
    (i) Annual mass of coal charged to the battery (metric tons) (Equation Q-3 of §98.173).
    (ii) Carbon content of the coal, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-3).
    (iii) Annual mass of coke produced by the battery (metric tons) (Equation Q-3).
    (iv) Carbon content of the coke, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-3).
    (v) Annual mass of air pollution control residue collected (metric tons) (Equation Q-3).
    (vi) Carbon content of the air pollution control residue, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-3).
    (vii) Annual mass of each other solid input containing carbon fed to each battery (metric tons) (Equation Q-3).
    (viii) Carbon content of each other solid input containing carbon fed to each battery (expressed as a decimal fraction) (Equation Q-3).
    (ix) Annual mass of each other solid output containing carbon produced by each battery (metric tons) (Equation Q-3).
    (x) Carbon content of each other solid output containing carbon (expressed as a decimal fraction) (Equation Q-3).
    (xi) Annual mass of each other gaseous input containing carbon fed to each battery (metric tons) (Equation Q-3).
    (xii) Carbon content of each other gaseous input containing carbon fed to each battery (expressed as a decimal fraction) (Equation Q-3).
    (xiii) Annual mass of each other gaseous output containing carbon produced by each battery (metric tons) (Equation Q-3).
    (xiv) Carbon content of each other gaseous output containing carbon produced by each battery (expressed as a decimal fraction) (Equation Q-3).
    (xv) Annual mass of each other liquid input containing carbon fed to each battery (metric tons) (Equation Q-3).
    (xvi) Carbon content of each other liquid input containing carbon fed to each battery (expressed as a decimal fraction) (Equation Q-3).
    (xvii) Annual mass of each other liquid output containing carbon produced by each battery (metric tons) (Equation Q-3).
    (xviii) Carbon content of each other liquid output containing carbon produced by each battery (expressed as a decimal fraction) (Equation Q-3).
    (4) The data in paragraphs (f)(4)(i) through (xxi) of this section for each applicable sinter process for which the carbon mass balance method of reporting is used.
    (i) Annual volume of the gaseous fuel (scf) (Equation Q-4 of §98.173).
    (ii) Carbon content of the gaseous fuel, from the fuel analysis results (kg C per kg of fuel) (Equation Q-4).
    (iii) Molecular weight of the gaseous fuel (kg/kg-mole) (Equation Q-4).
    (iv) Annual mass of sinter feed material (metric tons) (Equation Q-4).
    (v) Carbon content of the mixed sinter feed materials that form the bed entering the sintering machine, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-4).
    (vi) Annual mass of sinter produced (metric tons) (Equation Q-4).
    (vii) Carbon content of the sinter pellets, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-4).
    (viii) Annual mass of air pollution control residue collected (metric tons) (Equation Q-4).
    (ix) Carbon content of the air pollution control residue, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-4).
    (x) Annual mass of each other solid input containing carbon fed to each sinter process (metric tons) (Equation Q-4).
    (xi) Carbon content of each other solid input containing carbon fed to each sinter process (expressed as a decimal fraction) (Equation Q-4).
    (xii) Annual mass of each other solid output containing carbon produced by each sinter process (metric tons) (Equation Q-4).
    (xiii) Carbon content of each other solid output containing carbon (expressed as a decimal fraction) (Equation Q-4).
    (xiv) Annual mass of each other gaseous input containing carbon fed to each sinter process (metric tons) (Equation Q-4).
    (xv) Carbon content of each other gaseous input containing carbon fed to each sinter process (expressed as a decimal fraction) (Equation Q-4).
    (xvi) Annual mass of each other gaseous output containing carbon produced by each sinter process (metric tons) (Equation Q-4).
    (xvii) Carbon content of each other gaseous output containing carbon produced by each sinter process (expressed as a decimal fraction) (Equation Q-4).
    (xviii) Annual mass of each other liquid input containing carbon fed to each sinter process (metric tons) (Equation Q-4).
    (xix) Carbon content of each other liquid input containing carbon fed to each sinter process (expressed as a decimal fraction) (Equation Q-4).
    (xx) Annual mass of each other liquid output containing carbon produced by each sinter process (metric tons) (Equation Q-4).
    (xxi) Carbon content of each other liquid output containing carbon produced by each sinter process (expressed as a decimal fraction) (Equation Q-4).
    (5) The data in paragraphs (f)(5)(i) through (xxxi) of this section for each applicable electric arc furnace for which the carbon mass balance method of reporting is used.
    (i) Annual mass of direct reduced iron (if any) charged to the furnace (metric tons) (Equation Q-5 of §98.173).
    (ii) Carbon content of the direct reduced iron, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-5)
    (iii) Annual mass of ferrous scrap charged to the furnace (metric tons) (Equation Q-5).
    (iv) Carbon content of the ferrous scrap, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-5).
    (v) Annual mass of flux materials (e.g., limestone, dolomite) charged to the furnace (metric tons) (EquationQ-5).
    (vi) Carbon content of the flux materials, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-5).
    (vii) Annual mass of carbon electrode consumed (metric tons) (Equation Q-5).
    (viii) Carbon content of the carbon electrode, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-5).
    (ix) Annual mass of carbonaceous materials (e.g., coal, coke) charged to the furnace (metric tons) (Equation Q-5).
    (x) Carbon content of the carbonaceous materials, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-5).
    (xi) Annual mass of molten raw steel produced by the furnace (metric tons) (Equation Q-5).
    (xii) Carbon content of the steel, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-5).
    (xiii) Annual volume of the gaseous fuel (scf at 60F and 1 atm) (Equation Q-5).
    (xiv) Average carbon content of the gaseous fuel, from the fuel analysis results (kg C per kg of fuel) (Equation Q-5).
    (xv) Molecular weight of the gaseous fuel (kg/kg-mole) (Equation Q-5).
    (xvi) Annual mass of slag produced by the furnace (metric tons) (Equation Q-5).
    (xvii) Carbon content of the slag, from the carbon analysis (expressed as a decimal fraction) (Equation Q-5).
    (xviii) Annual mass of air pollution control residue collected (metric tons) (Equation Q-5).
    (xix) Carbon content of the air pollution control residue, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-5).
    (xx) Annual mass of each other solid input containing carbon fed to each furnace (metric tons) (Equation Q-5).
    (xxi) Carbon content of each other solid input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-5).
    (xxii) Annual mass of each other solid output containing carbon produced by each furnace (metric tons) (Equation   Q-5).
    (xxiii) Carbon content of each other solid output containing carbon (expressed as a decimal fraction) (Equation Q-5).
    (xxiv) Annual mass of each other gaseous input containing carbon fed to each furnace (metric tons) (Equation Q-5).
    (xxv) Carbon content of each other gaseous input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-5).
    (xxvi) Annual mass of each other gaseous output containing carbon produced by each furnace (metric tons) (Equation Q-5).
    (xxvii) Carbon content of each other gaseous output containing carbon produced by each furnace (expressed as a decimal fraction) (Equation Q-5).
    (xxviii) Annual mass of each other liquid input containing carbon fed to each furnace (metric tons) (Equation Q-5).
    (xxix) Carbon content of each other liquid input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-5).
    (xxx) Annual mass of each other liquid output containing carbon produced by each furnace (metric tons) (Equation Q-5).
    (xxxi) Carbon content of each other liquid output containing carbon produced by each furnace (expressed as a decimal fraction) (Equation Q-5).
    (6) The data in paragraphs (f)(6)(i) through (xvii) of this section for each applicable decarburization vessel for which the carbon mass balance method of reporting is used.
    (i) Annual mass of molten steel charged to the vessel (metric tons) (Equation Q-6 of §98.173).
    (ii) Carbon content of the molten steel before decarburization, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-6).
    (iii) Carbon content of the molten steel after decarburization, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-6).
    (iv) Annual mass of air pollution control residue collected (metric tons) (Equation Q-6).
    (v) Carbon content of the air pollution control residue, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-6).
    (vi) Annual mass of each other solid input containing carbon fed to each decarburization vessel (metric tons) (Equation Q-6).
    (vii) Carbon content of each other solid input containing carbon fed to each decarburization vessel (expressed as a decimal fraction) (Equation Q-6).
    (viii) Annual mass of each other solid output containing carbon produced by each decarburization vessel (metric tons) (Equation Q-6).
    (ix) Carbon content of each other solid output containing carbon (expressed as a decimal fraction) (Equation Q-6).
    (x) Annual mass of each other gaseous input containing carbon fed to each decarburization vessel (metric tons) (Equation Q-6).
    (xi) Carbon content of each other gaseous input containing carbon fed to each decarburization vessel (expressed as a decimal fraction) (Equation Q-6).
    (xii) Annual mass of each other gaseous output containing carbon produced by each decarburization vessel (metric tons) (Equation Q-6).
    (xiii) Carbon content of each other gaseous output containing carbon produced by each decarburization vessel (expressed as a decimal fraction) (Equation Q-6).
    (xiv) Annual mass of each other liquid input containing carbon fed to each decarburization vessel (metric tons) (Equation Q-6).
    (xv) Carbon content of each other liquid input containing carbon fed to each decarburization vessel (expressed as a decimal fraction) (Equation Q-6).
    (xvi) Annual mass of each other liquid output containing carbon produced by each decarburization vessel (metric tons) (Equation Q-6).
    (xvii) Carbon content of each other liquid output containing carbon produced by each decarburization vessel (expressed as a decimal fraction) (Equation Q-6).
    (7) The data in paragraphs (f)(7)(i) through (xxvii) of this section for each applicable direct reduction furnace for which the carbon mass balance method of reporting is used.
    (i) Annual volume of the gaseous fuel (scf at 68F and 1 atm) (Equation Q-7 of §98.173).
    (ii) Average carbon content of the gaseous fuel, from the fuel analysis results (kg C per kg of fuel) (Equation Q-7).
    (iii) Molecular weight of the gaseous fuel (kg/kg-mole) (Equation Q-7).
    (iv) Annual mass of iron ore or iron pellets fed to the furnace (metric tons) (Equation Q-7).
    (v) Carbon content of the iron ore or iron pellets, from the carbon analysis (expressed as a decimal fraction) (Equation Q-7).
    (vi) Annual mass of carbonaceous materials (e.g., coal, coke) charged to the furnace (metric tons) (Equation Q-7).
    (vii) Carbon content of the carbonaceous materials, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-7).
    (viii) Annual mass of each other material charged to the furnace (metric tons) (Equation Q-7).
    (ix) Average carbon content of each other material charged to the furnace, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-7).
    (x) Annual mass of iron produced (metric tons) (Equation Q-7).
    (xi) Carbon content of the iron produced, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-7).
    (xii) Annual mass of non-metallic materials produced by the furnace (metric tons) (Equation Q-7).
    (xiii) Carbon content of the non-metallic materials produced, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-7).
    (xiv) Annual mass of air pollution control residue collected (metric tons) (Equation Q-7).
    (xv) Carbon content of the air pollution control residue collected, from the carbon analysis results (expressed as a decimal fraction) (Equation Q-7).
    (xvi) Annual mass of each other solid input containing carbon fed to each furnace (metric tons) (Equation Q-7).
    (xvii) Carbon content of each other solid input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-7).
    (xviii) Annual mass of each other solid output containing carbon produced by each furnace (metric tons) (Equation Q-7).
    (xix) Carbon content of each other solid output containing carbon (expressed as a decimal fraction) (Equation Q-7).
    (xx) Annual mass of each other gaseous input containing carbon fed to each furnace (metric tons) (Equation Q-7).
    (xxi) Carbon content of each other gaseous input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-7).
    (xxii) Annual mass of each other gaseous output containing carbon produced by each furnace (metric tons) (Equation Q-7).
    (xxiii) Carbon content of each other gaseous output containing carbon produced by each furnace (expressed as a decimal fraction) (Equation Q-7).
    (xxiv) Annual mass of each other liquid input containing carbon fed to each furnace (metric tons) (Equation Q-7).
    (xxv) Carbon content of each other liquid input containing carbon fed to each furnace (expressed as a decimal fraction) (Equation Q-7).
    (xxvi) Annual mass of each other liquid output containing carbon produced by each furnace (metric tons) (Equation Q-7).
    (xxvii) Carbon content of each other liquid output containing carbon produced by each furnace (expressed as a decimal fraction) (Equation Q-7).
    (8) The data in paragraphs (f)(8)(i) and (ii) of this section for each process unit for which the site-specific emission factor method was used.
    (i) Average hourly feed or production rate, as applicable, during the test (metric tons/hour) (as used in §98.173(b)(2)(iii)).
    (ii) Annual total feed or production, as applicable (metric tons) (as used in §98.173(b)(2)(iv)).
    (9) Total coal charged to the coke ovens for each process (metric tons/year)(as used in §98.173(c)).
Subpart R  -  Lead Production
(§98.187)

    In addition to the records required by §98.3(g), you must retain the records of the information specified in paragraphs (a) through (d) of this section, as applicable to the smelting furnaces at your facility.
    (a) If a CEMS is used to measure combined process and combustion CO2 emissions according to the requirements in §98.183(a) or (b)(1), then you must retain the records required for the Tier 4 Calculation Methodology in §98.37 and the information specified in paragraphs (a)(1) through (a)(3) of this section.
    (1) Monthly smelting furnace production quantity for each lead product (tons).
    (2) Number of smelting furnace operating hours each month.
    (3) Number of smelting furnace operating hours in calendar year.
    (b) If the carbon mass balance procedure is used to determine process CO2 emissions according to the requirements in §98.183(b)(2)(i) and (b)(2)(ii), then you must retain under this subpart the records specified in paragraphs (b)(1) through (b)(5) of this section.
    (1) Monthly smelting furnace production quantity for each lead product (tons).
    (2) Number of smelting furnace operating hours each month.
    (3) Number of smelting furnace operating hours in calendar year.
    (4) Monthly material quantity consumed, used, or produced for each material included for the calculations of annual process CO2 emissions using Equation R-1 of this subpart (tons).
    (5) Average carbon content determined and records of the supplier provided information or analyses used for the determination for each material included for the calculations of annual process CO2 emissions using Equation R-1 of this subpart.
    (c) You must keep records that include a detailed explanation of how company records of measurements are used to estimate the carbon input to each smelting furnace, including documentation of any materials excluded from Equation R-1 of this subpart that contribute less than 1 percent of the total carbon into or out of the process. You also must document the procedures used to ensure the accuracy of the measurements of materials fed, charged, or placed in an smelting furnace including, but not limited to, calibration of weighing equipment and other measurement devices. The estimated accuracy of measurements made with these devices must also be recorded, and the technical basis for these estimates must be provided.
    (d) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (d)(1) through (10) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (d)(1) through (10) of this section.
    (1) Annual mass of lead ore charged to each smelting furnace (tons) (Equation R-1 of §98.183).
    (2) Carbon content of the lead ore per furnace, from the carbon analysis results (percent by weight, expressed as a decimal fraction) (Equation R-1).
    (3) Annual mass of lead scrap charged to each smelting furnace (tons) (Equation R-1).
    (4) Carbon content of the lead scrap per furnace, from the carbon analysis (percent by weight, expressed as a decimal fraction) (Equation R-1).
    (5) Annual mass of flux materials (e.g., limestone, dolomite) charged to each smelting furnace (tons) (Equation R-1).
    (6) Carbon content of the flux materials per furnace, from the carbon analysis (percent by weight, expressed as a decimal fraction) (Equation R-1).
    (7) Annual mass of carbonaceous materials (e.g., coal, coke) charged to each smelting furnace (tons) (Equation R-1).
    (8) Carbon content of the carbonaceous materials per furnace, from the carbon analysis (percent by weight, expressed as a decimal fraction) (Equation R-1).
    (9) Annual mass of each other material containing carbon, other than fuel, fed, charged, or otherwise introduced into the smelting furnace (tons) (Equation R-1).
    (10) Carbon content of each other material, from the carbon analysis results per furnace (percent by weight, expressed as a decimal fraction) (Equation R-1).

Subpart S  -  Lime Production
(§98.197)

    In addition to the records required by §98.3(g), you must retain the records specified in paragraphs (a) through (c) of this section.
    (a) Annual operating hours in calendar year.
    (b) Records of all analyses (e.g. chemical composition of lime products, by type) and calculations conducted.
    (c) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (c)(1) through (9) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (c)(1) through (9) of this section.
    (1) Monthly calcium oxide content for each lime type, determined according to §98.194(c) (metric tons CaO/metric ton lime) (Equation S-1 of §98.193).
    (2) Monthly magnesium oxide content for each lime type, determined according to §98.194(c) (metric tons MgO/metric ton lime) (Equation S-1).
    (3) Monthly calcium oxide content for each calcined lime byproduct or waste type sold (metric tons CaO/metric ton lime) (Equation S-2 of §98.193).
    (4) Monthly magnesium oxide content for each calcined lime byproduct or waste type sold (metric tons MgO/metric ton lime) (Equation S-2).
    (5) Calcium oxide content for each calcined lime byproduct or waste type that is not sold (metric tons CaO/metric ton lime) (Equation S-3 of §98.193).
    (6) Magnesium oxide content for each calcined lime byproduct or waste type that is not sold (metric tons MgO/metric ton lime) (Equation S-3).
    (7) Annual weight or mass of calcined byproducts or wastes for lime type that is not sold (tons) (Equation S-3).
    (8) Monthly weight or mass of each lime type produced (tons) (Equation S-4 of §98.193).
    (9) Monthly weight or mass of each calcined byproducts or wastes sold (tons) (Equation S-4).
Subpart T  -  Magnesium Production
(§98.207)

    In addition to the records specified in §98.3(g), you must retain the following information at the facility level:
    (a) Check-out and weigh-in sheets and procedures for gas cylinders.
    (b) Accuracy certifications and calibration records for scales including the method or manufacturer's specification used for calibration.
    (c) Residual gas amounts (heel) in cylinders sent back to suppliers.
    (d) Records, including invoices, for gas purchases, sales, and disbursements for all GHGs.
Subpart U  -  Miscellaneous Uses of Carbonate
(§98.217)
    In addition to the records required by §98.3(g), you must retain the records specified in paragraphs (a) through (e) of this section:
    (a) Monthly carbonate consumption (by carbonate type in tons).
    (b) You must document the procedures used to ensure the accuracy of the monthly measurements of carbonate consumption, carbonate input or carbonate output including, but not limited to, calibration of weighing equipment and other measurement devices.
    (c) Records of all analyses conducted to meet the requirements of this rule.
    (d) Records of all calculations conducted.
    (e) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (e)(1) through (4) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (e)(1) through (4) of this section.
    (1) Fraction calcination achieved for each particular carbonate type. As an alternative to measuring the calcination fraction, a value of 1.0 can be used (decimal fraction) (Equation U-1 of §98.213).
    (2) Annual mass of each carbonate type consumed (tons) (Equation U-1).
    (3) Annual mass of each input carbonate type (tons) (Equation U-2 of §98.213).
    (4) Annual mass of each output carbonate type (tons) (Equation U-2).
Subpart V  -  Nitric Acid Production
(§98.227)
    In addition to the information required by §98.3(g), you must retain the records specified in paragraphs (a) through (h) of this section for each nitric acid production facility:
    (a) Records of significant changes to process.
    (b) Documentation of how process knowledge was used to estimate abatement technology destruction efficiency (if applicable).
    (c) Performance test reports.
    (d) Number of operating hours in the calendar year for each nitric acid train (hours).
    (e) Annual nitric acid permitted production capacity (tons).
    (f) Measurements, records, and calculations used to determine reported parameters.
    (g) Documentation of the procedures used to ensure the accuracy of the measurements of all reported parameters, including but not limited to, calibration of weighing equipment, flow meters, and other measurement devices. The estimated accuracy of measurements made with these devices must also be recorded, and the technical basis for these estimates must be provided.
    (h) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (h)(1) through (10) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (h)(1) through (10) of this section.
    (1) Annual nitric acid produced from each nitric acid train (tons nitric acid produced, 100% acid basis).
    (2) Indicate which equation was used to calculate emissions for each nitric acid train.
    (3) N2O concentration per test run during the performance test (ppm N2O) (Equation V-1 of §98.223).
    (4) Volumetric flow rate of effluent gas per test run during the performance test (dscf/hr) (Equation V-1).
    (5) Production rate per test run during the performance test (tons nitric acid produced per hour, 100 percent acid basis) (Equation V-1).
    (6) Annual nitric acid production from each nitric acid train during which each N2O abatement technology was operational (tons nitric acid produced, 100 percent acid basis) (Equation V-2 of §98.223).
    (7) Destruction efficiency of N2O abatement technology that is used on each nitric acid train (decimal fraction of N2O removed from vent stream) (Equation V-3a of §98.223).
    (8) Destruction efficiency of each N2O abatement technology that is used on each nitric acid train (decimal fraction of N2O removed from vent stream) (Equation V-3b of §98.223).
    (9) Destruction efficiency of each N2O abatement technology that is used on each nitric acid train (decimal fraction of N2O removed from vent stream) (Equation V-3c of §98.223).
    (10) Fraction control factor of each N2O abatement technology that is used on each nitric acid train (decimal fraction of total emissions from nitric acid train "t" that are sent to abatement technology "n") (Equation V-3c).
Subpart W  -  Petroleum and Natural Gas Systems
(§98.237)
    Monitoring Plans, as described in §98.3(g)(5), must be completed by April 1, 2011. In addition to the information required by §98.3(g), you must retain the following records:
    (a) Dates on which measurements were conducted.
    (b) Results of all emissions detected and measurements.
    (c) Calibration reports for detection and measurement instruments used.
    (d) Inputs and outputs of calculations or emissions computer model runs used for engineering estimation of emissions.
    (e) The records required under §98.3(g)(2)(i) shall include an explanation of how company records, engineering estimation, or best available information are used to calculate each applicable parameter under this subpart.
    (f) For each time a missing data procedure was used, keep a record listing the emission source type, a description of the circumstance that resulted in the need to use missing data procedures, the missing data provisions in §98.235 that apply, the calculation or analysis used to develop the substitute value, and the substitute value.

Subpart X  -  Petrochemical Production
(§98.247)

    In addition to the recordkeeping requirements in §98.3(g), you must retain the records specified in paragraphs (a) through (d) of this section, as applicable.
    (a) If you comply with the CEMS measurement methodology in §98.243(b), then you must retain under this subpart the records required for the Tier 4 Calculation Methodology in §98.37, records of the procedures used to develop estimates of the fraction of total emissions attributable to combustion of petrochemical process off-gas as required in §98.246(b), and records of any annual average HHV calculations.
    (b) If you comply with the mass balance methodology in §98.243(c), then you must retain records of the information listed in paragraphs (b)(1) through (4) of this section.
    (1) Results of feedstock or product composition determinations conducted in accordance with §98.243(c)(4).
    (2) Start and end times for time periods when off-specification product is produced, if you comply with the alternative methodology in §98.243(c)(4) for determining carbon content of product.
    (3) As part of the monitoring plan required under §98.3(g)(5), record the estimated accuracy of measurement devices and the technical basis for these estimates.
    (4) The dates and results (e.g., percent calibration error) of the calibrations of each measurement device.
    (c) If you comply with the combustion methodology in §98.243(d), then you must retain under this subpart the records required for the applicable Tier Calculation Methodologies in §98.37. If you comply with §98.243(d)(2), you must also keep records of the annual average flow calculations.
    (d) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (d)(1) through (30) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (d)(1) through (30) of this section.
    (1) Indicate whether the feedstock is measured as mass or volume (Equation X-1 of §98.243).
    (2) Indicate whether you used the alternative to sampling and analysis specified in §98.243(c)(4) (Equation X-1).
    (3) Volume of gaseous feedstock introduced per month (scf) (Equation X-1).
    (4) Mass of gaseous feedstock introduced per month (kg) (Equation X-1).
    (5) Average carbon content of the gaseous feedstock per month (kg C per kg of feedstock) (Equation X-1).
    (6) Molecular weight of gaseous feedstock per month (kg per kg-mole) (Equation X-1).
    (7) Indicate whether the gaseous product is measured as mass or volume (Equation X-1).
    (8) Volume of gaseous product produced per month (scf) (Equation X-1).
    (9) Mass of gaseous product produced per month (kg) (Equation X-1).
    (10) Average carbon content of gaseous product (including streams containing CO2 recovered for sale or use in another process) per month (kg C per kg of product) (Equation X-1).
    (11) Molecular weight of gaseous product per month (kg per kg-mole) (Equation X-1).
    (12) Molar volume conversion factor of product (scf per kg-mole) (Equation X-1).
    (13) Indicate whether feedstock is measured as mass or volume (Equation X-2 of §98.243).
    (14) Indicate whether you used the alternative to sampling and analysis specified in §98.243(c)(4) (Equation X-2).
    (15) Volume of liquid feedstock introduced per month (gallons) (Equation X-2).
    (16) Mass of liquid feedstock introduced per month (kg) (Equation X-2).
    (17) Average carbon content of liquid feedstock per month (kg C per gallon) (Equation X-2).
    (18) Average carbon content of liquid feedstock per month (kg C per kg of feedstock) (Equation X-2).
    (19) Indicate whether product is measured as mass or volume per month (Equation X-2).
    (20) Volume of liquid product produced per month (gallons) (Equation X-2).
    (21) Mass of liquid product produced per month (kg) (Equation X-2).
    (22) Average carbon content of liquid product per month, including organic liquid wastes (kg C per gallon) (Equation X-2).
    (23) Average carbon content of liquid product, including organic liquid wastes (kg C per kg of product) (Equation X-2).
    (24) Indicate whether you used the alternative to sampling and analysis specified in §98.243(c)(4) (Equation X-3 of §98.243).
    (25) Mass of solid feedstock introduced per month (kg) (Equation X-3).
    (26) Average carbon content of solid feedstock per month (kg C per kg of feedstock) (Equation X-3).
    (27) Mass of solid product produced per month (kg) (Equation X-3).
    (28) Average carbon content of solid product per month (kg C per kg of product) (Equation X-3).
    (29) Records required in §98.257(b)(1) through (8) of this section for each flare that burns ethylene process off-gas.
    (30) Records required in §98.37 for each stationary fuel combustion unit (or group of stationary sources with a common pipe) that burns ethylene process off-gas, except flares.
Subpart Y  -  Petroleum Refineries
(§98.257)
    In addition to the records required by §98.3(g), you must retain the records specified in paragraphs (a) and (b) of this section.
    (a) The records of all parameters monitored under §98.255. If you comply with the combustion methodology in §98.252(a), then you must retain under this subpart the records required for the Tier 3 and/or Tier 4 Calculation Methodologies in §98.37 and you must keep records of the annual average flow calculations.
    (b) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (b)(1) through (67) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (b)(1) through (67) of this section.
    (1) Volume of flare gas combusted during measurement period (scf) (Equation Y-1b of §98.253).
    (2) Mole percent CO2 concentration in the flare gas stream during the measurement period (mole percent) (Equation Y-1b).
    (3) Mole percent concentration of compound "x" in the flare gas stream during the measurement period (mole percent) (Equation Y-1b).
    (4) Carbon mole number of compound "x" in the flare gas stream during the measurement period (mole carbon atoms per mole compound) (Equation Y-1b).
    (5) Molar volume conversion factor (scf per kg-mole) (Equation Y-1b).
    (6) Annual volume of flare gas combusted for each flare during normal operations from company records (million (MM) standard cubic feet per year, MMscf/year) (Equation Y-3 of §98.253).
    (7) Higher heating value for fuel gas or flare gas for each flare from company records (British thermal units per scf, Btu/scf = MMBtu/MMscf) (Equation Y-3).
    (8) Volume of flare gas combusted during indexed start-up, shutdown, or malfunction event from engineering calculations (scf) (Equation Y-3).
    (9) Average molecular weight of the flare gas, from the analysis results or engineering calculations for the event (kg/kg-mole) (Equation Y-3).
    (10) Molar volume conversion factor (scf per kg-mole) (Equation Y-3).
    (11) Average carbon content of the flare gas, from analysis results or engineering calculations for the event (kg C per kg flare gas) (Equation Y-3).
    (12) Weight fraction of carbon in the flare gas prior to combustion in each flare that is contributed by methane from measurement values or engineering calculations (kg C in methane in flare gas/kg C in flare gas) (Equation Y-4 of §98.253).
    (13) Annual throughput of unit from company records for each catalytic cracking unit or fluid coking unit (barrels/year) (Equation Y-8 of §98.253).
    (14) Coke burn-off factor from engineering calculations (default for catalytic cracking units = 7.3; default for fluid coking units = 11) (kg coke per barrel of feed) (Equation Y-8).
    (15) Carbon content of coke based on measurement or engineering estimate (kg C per kg coke) (Equation Y-8).
    (16) Value of unit-specific CH4 emission factor, including the units of measure, for each catalytic cracking unit, traditional fluid coking unit, catalytic reforming unit, and coke calcining unit (calculation method in §98.253(c)(4)).
    (17) Annual activity data (e.g., input or product rate), including the units of measure, in units of measure consistent with the emission factor, for each catalytic cracking unit, traditional fluid coking unit, catalytic reforming unit, and coke calcining unit (calculation method in §98.253(c)(4)).
    (18) Value of unit-specific N2O emission factor, including the units of measure, for each catalytic cracking unit, traditional fluid coking unit, catalytic reforming unit, and coke calcining unit (calculation method in §98.253(c)(5)).
    (19) Annual activity data (e.g., input or product rate), including the units of measure, in units of measure consistent with the emission factor, for each catalytic cracking unit, traditional fluid coking unit, catalytic reforming unit, and coke calcining unit (calculation method in §98.253(c)(5)).
    (20) Carbon content of coke based on measurement or engineering estimate (default = 0.94) (kg C per kg coke) (Equation Y-11 of §98.253).
    (21) Volumetric flow rate of sour gas (including sour water stripper gas) feed sent off site for sulfur recovery in the year (scf/year) (Equation Y-12 of §98.253).
    (22) Mole fraction of carbon in the sour gas feed sent off site for sulfur recovery (kg-mole C/kg-mole gas) (Equation Y-12).
    (23) Molar volume conversion factor for sour gas sent off site (scf per kg-mole) (Equation Y-12).
    (24) Volumetric flow rate of sour gas (including sour water stripper gas) fed to the onsite sulfur recovery plant (scf/year) (Equation Y-12).
    (25) Mole fraction of carbon in the sour gas fed to the onsite sulfur recovery plant (kg-mole C/kg-mole gas) (Equation Y-12).
    (26) Molar volume conversion factor for onsite sulfur recovery plant (scf per kg-mole) (Equation Y-12).
    (27) Annual mass of green coke fed to the coke calcining unit from facility records (metric tons/year) (Equation Y-13 of §98.253).
    (28) Annual mass of marketable petroleum coke produced by the coke calcining unit from facility records (metric tons/year) (Equation Y-13).
    (29) Annual mass of petroleum coke dust removed from the process through the dust collection system of the coke calcining unit from facility records. For coke calcining units that recycle the collected dust, the mass of coke dust removed from the process is the mass of coke dust collected less the mass of coke dust recycled to the process (metric tons/year) (Equation Y-13).
    (30) Average mass fraction carbon content of green coke from facility measurement data (metric tons C per metric ton green coke) (Equation Y-13).
    (31) Average mass fraction carbon content of marketable petroleum coke produced by the coke calcining unit from facility measurement data (metric tons C per metric ton petroleum coke (Equation Y-13).
    (32) Quantity of asphalt blown for each asphalt blowing unit (million barrels per year (MMbbl/year)) (Equation Y-14 of §98.253).
    (33) Emission factor for CO2 from uncontrolled asphalt blowing from facility-specific test data for each asphalt blowing unit (metric tons CO2/MMbbl asphalt blown) (Equation Y-14).
    (34) Emission factor for CH4 from uncontrolled asphalt blowing from facility-specific test data for each asphalt blowing unit (metric tons CH4/MMbbl asphalt blown) (Equation Y-15 of §98.253).
    (35) Quantity of asphalt blown (million barrels/year (MMbbl/year)) (Equation Y-16a of §98.253).
    (36) Carbon emission factor from asphalt blowing from facility-specific test data (metric tons C/MMbbl asphalt blown) (Equation Y-16a).
    (37) Quantity of asphalt blown for each asphalt blowing unit (million barrels per year (MMbbl/year)) (Equation Y-16b of §98.253).
    (38) Emission factor for CO2 from uncontrolled asphalt blowing from facility-specific test data for each asphalt blowing unit (metric tons CO2/MMbbl asphalt blown) (Equation Y-16b).
    (39) Carbon emission factor from asphalt blowing from facility-specific test data for each asphalt blowing unit (metric tons C/MMbbl asphalt blown) (Equation Y-16b).
    (40) Emission factor for CH4 from uncontrolled asphalt blowing from facility-specific test data for each asphalt blowing unit (metric tons CH4/MMbbl asphalt blown) (Equation Y-17 of §98.253).
    (41) Cumulative number of vessel openings for all delayed coking unit vessels of the same dimensions during the year (Equation Y-18 of §98.253).
    (42) Height of coking unit vessel for each set of coke drums or vessels of the same size (feet) (Equation Y-18).
    (43) Gauge pressure of the coking vessel when opened to the atmosphere prior to coke cutting or, if the alternative method provided in §98.253(i)(2) is used, gauge pressure of the coking vessel when depressurization gases are first routed to the atmosphere for each set of coke drums or vessels of the same size (pounds per square inch gauge (psig)) (Equation Y-18).
    (44) Volumetric void fraction of coking vessel prior to steaming for each set of coke drums or vessels of the same size (cf gas/cf of vessel) (Equation Y-18).
    (45) Diameter of coking unit vessel for each set of coke drums or vessels of the same size (feet) (Equation Y-18).
    (46) Molar volume conversion factor for each set of coke drums or vessels of the same size (scf per kg-mole) (Equation Y-18).
    (47) Average volumetric flow rate of process gas during the event from measurement data, process knowledge, or engineering estimates for each set of coke drums or vessels of the same size (scf per hour) (Equation Y-19 of §98.253).
    (48) Mole fraction of methane in process vent during the event from measurement data, process knowledge, or engineering estimates for each set of coke drums or vessels of the same size (kg-mole CH4/kg-mole gas) (Equation Y-19).
    (49) Venting time for the event for each set of coke drums or vessels of the same size (hours) (Equation Y-19).
    (50) Molar volume conversion factor for each set of coke drums or vessels of the same size (scf per kg-mole) (Equation Y-19).
    (51) Quantity of crude oil plus the quantity of intermediate products received from off site that are processed at the facility (MMbbl/year) (Equation Y-20 of §98.253).
    (52) Molar volume conversion factor (scf per kg-mole) (Equation Y-20).
    (53) Methane emission factor for uncontrolled blown systems (scf CH4/MMbbl) (Equation Y-20).
    (54) Quantity of crude oil plus the quantity of intermediate products received from off site that are processed at the facility (MMbbl/year) (Equation Y-22 of §98.253).
    (55) Quantity of unstabilized crude oil received at the facility (MMbbl/year) (Equation Y-23 of §98.253).
    (56) Pressure differential from the previous storage pressure to atmospheric pressure (psi) (Equation Y-23).
    (57) Average mole fraction of CH4 in vent gas from the unstabilized crude oil storage tanks from facility measurements (kg-mole CH4/kg-mole gas) (Equation Y-23).
    (58) Molar volume conversion factor (scf per kg-mole) (Equation Y-23).
    (59) Specify whether the calculated or default loading factor L specified in §98.253(n) is entered, for each liquid loaded to each (methods specified in §98.253(n)).
    (60) Saturation factor specified in §98.253(n), for each liquid loaded to each vessel (methods specified in §98.253(n)).
    (61) True vapor pressure of liquid loaded, for each liquid loaded to each vessel (psia) (methods specified in §98.253(n)).
    (62) Molecular weight of vapors (lb per lb-mole), for each liquid loaded to each vessel (methods specified in §98.253(n)).
    (63) Temperature of bulk liquid loaded, for each liquid loaded to each vessel (°R, degrees Rankine) (methods specified in §98.253(n)).
    (64) Total loading loss (without efficiency correction), for each liquid loaded to each vessel (pounds per 1000 gallons loaded) (methods specified in §98.253(n)).
    (65) Overall emission control system reduction efficiency, including the vapor collection system efficiency and the vapor recovery or destruction efficiency (enter zero if no emission controls), for each liquid loaded to each vessel (percent) (methods specified §98.253(n)).
    (66) Vapor phase concentration of methane in liquid loaded, for each liquid loaded to each vessel (percent by volume) (methods specified in §98.253(n)).
    (67) Quantity of material loaded, for each liquid loaded to each vessel (thousand gallon per year) (methods specified in §98.253(n)).

Subpart Z  -  Phosphoric Acid Production
(§98.267)
    In addition to the records required by §98.3(g), you must retain the records specified in paragraphs (a) through (d) of this section for each wet-process phosphoric acid production facility.
    (a) Monthly mass of phosphate rock consumed by origin (tons).
    (b) Records of all phosphate rock purchases and/or deliveries (if vertically integrated with a mine).
    (c) Documentation of the procedures used to ensure the accuracy of monthly phosphate rock consumption by origin.
    (d) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (d)(1) through (4) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (d)(1) through (4) of this section.
    (1) Inorganic carbon content of a grab sample batch of phosphate rock by origin obtained during month by wet-process phosphoric acid process line, from the carbon analysis results (percent by weight, expressed as a decimal fraction) (Equation Z-1a of §98.263).
    (2) Mass of phosphate rock by origin consumed in month by wet-process phosphoric acid process line (tons) (Equation Z-1a).
    (3) Carbon dioxide content of a grab sample batch of phosphate rock by origin obtained during month by wet-process phosphoric acid process line (percent by weight, expressed as a decimal fraction) (Equation Z-1b of §98.263).
    (4) Mass of phosphate rock by origin consumed in month by wet-process phosphoric acid process line (tons) (Equation Z-1b).
Subpart AA  -  Pulp and Paper Manufacturing
(§98.277)
    In addition to the information required by §98.3(g), you must retain the records in paragraphs (a) through (g) of this section.
    (a) GHG emission estimates (including separate estimates of biogenic CO2) for each emissions source listed under §98.270(b).
    (b) Annual analyses of spent pulping liquor HHV for each chemical recovery furnace at kraft and soda facilities.
    (c) Annual analyses of spent pulping liquor carbon content for each chemical recovery combustion unit at a sulfite or semichemical pulp facility.
    (d) Annual quantity of spent liquor solids combusted in each chemical recovery furnace and chemical recovery combustion unit, and the basis for detemining the annual quantity of the spent liquor solids combusted (whether based on T650 om-05 Solids Content of Black Liquor, TAPPI (incorporated by reference, see §98.7) or an online measurement system). If an online measurement system is used, you must retain records of the calculations used to determine the annual quantity of spent liquor solids combusted from the continuous measurements.
    (e) Annual steam purchases.
    (f) Annual quantities of makeup chemicals used.
    (g) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (g)(1) through (27) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (g)(1) through (27) of this section.
    (1) Mass of the solid fuel combusted (tons/year) (Equation C-1 of §98.33).
    (2) Volume of the liquid fuel combusted (gallons/year) (Equation C-1).
    (3) Volume of the gaseous fuel combusted (scf/year) (Equation C-1).
    (4) Annual natural gas usage (therms/year) (Equation C-1a of §98.33).
    (5) Annual natural gas usage (mmBtu/year) (Equation C-1b of §98.33).
    (6) Mass of the solid fuel combusted (tons/year) (Equation C-2a of §98.33).
    (7) Volume of the liquid fuel combusted (gallons/year) (Equation C-2a).
    (8) Volume of the gaseous fuel combusted (scf/year) (Equation C-2a).
    (9) Annual mass of the solid fuel combusted (short tons/year) (Equation C-3 of §98.33).
    (10) Annual average carbon content of the solid fuel (percent by weight, expressed as a decimal fraction) (Equation C-3).
    (11) Annual volume of the liquid fuel combusted (gallons/year) (Equation C-4 of §98.33).
    (12) Annual average carbon content of the liquid fuel (kg C per gallon of fuel) (Equation C-4).
    (13) Annual volume of the gaseous fuel combusted (scf/year) (Equation C-5 of §98.33).
    (14) Annual average carbon content of the gaseous fuel (kg C per kg of fuel) (Equation C-5).
    (15) Annual average molecular weight of the gaseous fuel (kg/kg-mole) (Equation C-5).
    (16) Molar volume conversion factor at standard conditions, as defined in §98.6 (scf per kg-mole) (Equation C-5).
    (17) Identify if you will use the default high heat value from Table C-1 of subpart C of this part, or actual HHV data (Equation C-8 of §98.33).
    (18) High heat value of the fuel (mmBTU/tons) (Equation C-8).
    (19) High heat value of the fuel (mmBTU/gallons) (Equation C-8).
    (20) High heat value of the fuel (mmBTU/scf) (Equation C-8).
    (21) Mass of spent liquor solids combusted from each chemical recovery furnace located at a kraft or soda facility, in short tons in year, determined according to §98.274(b) (tons/year) (Equation AA-1 of §98.273).
    (22) Annual high heat value of the spent liquor solids from each chemical recovery furnace located at a kraft or soda facility determined according to §98.274(b) (mmBtu per kilogram) (Equation AA-1).
    (23) Annual high heat value of the spent liquor solids from each chemical recovery combustion unit located at a sulfite or stand-alone semichemical facility, determined according to §98.274(b) (mmBtu per kilogram) (Equation AA-1).
    (24) Mass of the spent liquor solids combusted in short tons per year determined according to §98.274(b) (tons/year) (Equation AA-2 of §98.273).
    (25) Annual carbon content of the spent liquor solids, determined according to §98.274(b) (percent by weight, expressed as a decimal fraction (e.g., 95% = 0.95)) (Equation AA-2).
    (26) Make-up quantity of CaCO3 used for the reporting year (metric tons/year) (Equation AA-3 of §98.273).
    (27) Make-up quantity of Na2CO3 used for the reporting year metric tons/year) (Equation AA-3).
Subpart BB  -  Silicon Carbide Production
(§98.287)
    In addition to the records required by §98.3(g), you must retain the records specified in paragraphs (a) through (c) of this section for each silicon carbide production facility.
    (a) If a CEMS is used to measure CO2 emissions, you must retain under this subpart the records required for the Tier 4 Calculation Methodology in §98.37 and the information listed in this paragraph (a):
    (1) Records of all petroleum coke purchases.
    (2) Annual operating hours.
    (b) If a CEMS is not used to measure emissions, you must retain records for the information listed in this paragraph (b):
    (1) Records of all analyses and calculations conducted for reported data listed in §98.286(b).
    (2) Records of all petroleum coke purchases.
    (3) Annual operating hours.
    (c) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (c)(1) and (2) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (c)(1) and (2) of this section.
    (1) Carbon content factor for petroleum coke consumed in month from the supplier or as measured by the applicable method (percent by weight expressed as a decimal fraction) (Equation BB-1 of §98.283).
    (2) Petroleum coke consumption in month (tons) (Equation BB-2 of §98.283).
Subpart CC  -  Soda Ash Manufacturing
(§98.297)
    In addition to the records required by §98.3(g), you must retain the records specified in paragraphs (a) through (c) of this section for each soda ash manufacturing line.
    (a) If a CEMS is used to measure CO2 emissions, then you must retain under this subpart the records required for the Tier 4 Calculation Methodology specified in subpart C of this part and the information listed in this paragraph (a):
    (1) Monthly production of soda ash (tons)
    (2) Monthly consumption of trona or liquid alkaline feedstock (tons)
    (3) Annual operating hours (hours).
    (b) If a CEMS is not used to measure emissions, then you must retain records for the information listed in this paragraph (b):
    (1) Records of all analyses and calculations conducted for determining all reported data as listed in §98.296(b).
    (2) If using Equation CC-1 or CC-2 of this subpart, weekly inorganic carbon content factor of trona or soda ash, depending on method chosen, as measured by the applicable method in §98.294(b) (percent by weight expressed as a decimal fraction).
    (3) Annual operating hours for each manufacturing line used to produce soda ash (hours).
    (4) You must document the procedures used to ensure the accuracy of the monthly trona consumption or soda ash production measurements including, but not limited to, calibration of weighing equipment and other measurement devices. The estimated accuracy of measurements made with these devices must also be recorded, and the technical basis for these estimates must be provided.
    (5) If you produce soda ash using the liquid alkaline feedstock process and use the site-specific emission factor method to estimate emissions (§98.293(b)(3)) then you must also retain the following relevant information:
    (i) Records of performance test results.
    (ii) You must document the procedures used to ensure the accuracy of the annual average vent flow measurements including, but not limited to, calibration of flow rate meters and other measurement devices. The estimated accuracy of measurements made with these devices must also be recorded, and the technical basis for these estimates must be provided.
    (c) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (c)(1) through (4) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (c)(1) through (4) of this section
    (1) Inorganic carbon content in trona input, from the carbon analysis results for month (percent by weight, expressed as a decimal fraction) (Equation CC-1 of §98.293).
    (2) Mass of trona input in month (tons) (Equation CC-1).
    (3) Inorganic carbon content in soda ash output, from the carbon analysis results for month (percent by weight, expressed as a decimal fraction) (Equation CC-2 of §98.293).
    (4) Mass of soda ash output in month (tons) (Equation CC-2).

Subpart DD- Electrical Transmission and Distribution Equipment Use
(§98.307)
In addition to the information required by §98.3(g), you must retain records of the information reported and listed in §98.306.
Subpart EE  -  Titanium Dioxide Production
(§98.317)
    In addition to the records required by §98.3(g), you must retain the records specified in paragraphs (a) through (c) of this section for each titanium dioxide production facility.
    (a) If a CEMS is used to measure CO2 emissions, then you must retain under this subpart required for the Tier 4 Calculation Methodology in §98.37 and the information listed in this paragraph (a):
    (1) Records of all calcined petroleum coke purchases.
    (2) Annual operating hours for each titanium dioxide process line.
    (b) If a CEMS is not used to measure CO2 emissions, then you must retain records for the information listed in this paraghraph:
    (1) Records of all calcined petroleum coke purchases (tons).
    (2) Records of all analyses and calculations conducted for all reported data as listed in §98.316(b).
    (3) Sampling analysis results for carbon content of consumed calcined petroleum coke (percent by weight expressed as a decimal fraction).
    (4) Sampling analysis results for the carbon content of carbon containing waste (percent by weight expressed as a decimal fraction), if applicable.
    (5) Monthly production of carbon-containing waste (tons).
    (6) You must document the procedures used to ensure the accuracy of the monthly petroleum coke consumption and quantity of carbon-containing waste measurement including, but not limited to, calibration of weighing equipment and other measurement devices. The estimated accuracy of measurements made with these devices must also be recorded, and the technical basis for these estimates must be provided.
    (7) Annual operating hours for each titanium dioxide process line (hours).
    (c) Verification software records. You must keep a record of the file generated by the verification software specified in §98.5(b) for the applicable data specified in paragraphs (c)(1) and (2) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (c)(1) and (2) of this section.
    (1) Carbon content factor for petroleum coke consumed in month from the supplier or as measured by the applicable method incorporated by reference in §98.7 according to §98.314(c) (percent by weight, expressed as a decimal fraction) (Equation EE-2 of §98.313).
    (2) Calcined petroleum coke consumption for process line in month (tons) (Equation EE-2).
Subpart FF  -  Underground Coal Mines
(§98.327)
    In addition to the information required by §98.3(g), you must retain the following records:
    (a) Calibration records for all monitoring equipment, including the method or manufacturer's specification used for calibration.
    (b) Records of gas sales.
    (c) Logbooks of parameter measurements.
    (d) Laboratory analyses of samples.
Subpart GG  -  Zinc Production
(§98.337)
    In addition to the records required by §98.3(g), you must retain the records specified in paragraphs (a) through (c) of this section for each zinc production facility.
    (a) If a CEMS is used to measure emissions, then you must retain under this subpart the records required for the Tier 4 Calculation Methodology in §98.37 and the information listed in this paragraph (a):
    (1) Monthly facility production quantity for each zinc product (tons).
    (2) Annual operating hours for all Waelz kilns and electrothermic furnaces used in zinc production.
    (b) If a CEMS is not used to measure emissions, you must also retain the records specified in paragraphs (b)(1) through (b)(7) of this section.
    (1) Records of all analyses and calculations conducted for data reported as listed in §98.336(b).
    (2) Annual operating hours for Waelz kilns and electrothermic furnaces used in zinc production.
    (3) Monthly production quantity for each zinc product (tons).
    (4) Monthly mass of zinc bearing materials, flux materials (e.g., limestone, dolomite), and carbonaceous materials (e.g., coal, coke) charged to the kiln or furnace (tons).
    (5) Sampling and analysis records for carbon content of zinc bearing materials, flux materials (e.g., limestone, dolomite), carbonaceous materials (e.g., coal, coke), charged to the kiln or furnace (percent by weight, expressed as a decimal fraction).
    (6) Monthly mass of carbon electrode consumed in for each electrothermic furnace (tons).
    (7) Sampling and analysis records for carbon content of electrode materials.
    (8) You must keep records that include a detailed explanation of how company records of measurements are used to estimate the carbon input to each Waelz kiln or electrothermic furnace, as applicable to your facility, including documentation of any materials excluded from Equation GG-1 of this subpart that contribute less than 1 percent of the total carbon inputs to the process. You also must document the procedures used to ensure the accuracy of the measurements of materials fed, charged, or placed in an affected unit including, but not limited to, calibration of weighing equipment and other measurement devices. The estimated accuracy of measurements made with these devices must also be recorded, and the technical basis for these estimates must be provided.