Page 1 of 78

**Subpart C**

**— General Stationary Fuel Combustion Sources**  **§98.30 Definition of the source category.**  (a) Stationary

fuel combustion sources are devices that combust solid, liquid, or gaseous fuel, generall y for the purposes of producing electricity, generating steam, or providing useful heat or energy

for indus trial, commercial, or institutional use, or reducing the volume of waste b y removing combustible matter. Stationary fuel combustion sources include, but are not limited to, boilers, simple and combined

- cycle combustion turbines, engines, incinerators, and process heaters. (b) This source category does not include: (1) Portable equipment, as defined in §98.6. (2) Emergency

generators and emergency equipment, as defined in §98.6. (3) Irrigation pumps at agricultural operations. (4) Flares, unless otherwise re quired b y provisions of another subpart of this part to use methodologies in this subpart. (5) Electricity

generating units that are subject to subpart D of this part. (c) For a unit that combusts hazardous waste (as defined in §261.3 of this chapter), rep orting of GHG emissions is not required unless either of the following conditions apply : (1) Continuous emission monitors (CEMS) are used to quantify CO 2 mass emissions. (2) An y fuel listed in Table C

- 1 of this subpart is also combusted in the unit. In thi s case, report GHG emissions from combustion of all fuels listed in Table C

- 1 of this subpart. (d) You are not required to report GHG emissions from pilot lights. A pilot light is a small auxiliary

flame that ignites the burner of a combustion device when the control valve opens.Page 2 of 78

**§98.31 Reporting threshold.**  You must report GHG emissions under this subpart if your facility contains one or more stationary fuel combustion sources and the facility meets the applicability requirements of either §§98.2(a)(1), 98. 2(a)(2), or 98.2(a)(3). **§98.32 GHGs to report.**  You must report CO 2 , CH 4 , and N 2 O mass emissions from each stationary fuel combustion unit, except as otherwise indicated in this subpart. **§98.33 Calculating GHG emissions.**  You must calculate CO 2 emissions according to paragraph (a) of this section, and calculate CH 4 and N 2 O emissions according to paragraph (c) of this section. (a) CO2 emissions from fuel combustion. Calculate CO 2 mass emissions by using one of the four calculation methodologies in paragraphs (a)(1) through (a)(4) of this section, subject to the applicable conditions, requirements, and restrictions set forth in paragraph (b) of this section. Alternativel y, for units that meet the conditions of paragraph (a)(5) of this section, you may use CO 2 mass emissions calculation methods from part 75 of this chapter, as described in paragraph (a)(5) of this section. For units that combust both biomass and fossil fuels, you must calculate and report CO 2 emissions from the combustion of biomass separatel y using the methods in paragraph (e) of this section, except as otherwise provided in paragraphs (a)(5)(iv) and (e) of this section and in §98.36(d). (1) Tier 1 Calculation Methodology. Calculate the annual CO 2 mass emissions for each ty pe of fuel by

using Equation C

- 1, C
- 1a, or C
- 1b of this section (as applicable).Page 3 of 78

(i) Use Equation C

- 1 except when natural gas billing records are used to quantify fuel usage and gas consumption is expressed in units of therms or million Btu. In that case, use Equati on C
- 1a or C
- 1b, as applicable.

where: CO 2 = Annual CO 2 mass emissions for the specific fuel type (metric tons). Fuel = Mass or volume of fuel combusted per ye ar, from company records as defined in §98.6 (express mass in short tons for solid fuel, volume in standard cubic feet for gaseous fuel, and volume in gallons for liquid fuel). HHV = Default high heat value of the fuel, from Table C

- 1 of this subpart (mmBtu per mass or mmBtu per volume, as applicable). EF = Fuel

- specific default CO 2 emission factor, from Table C

- 1 of this subpart (kg CO 2 /mmBtu). 1 × 10 −3 = Conversion factor from kilograms to metric tons. (ii) If natural gas consumption is obtained from billing records and fuel usage is expressed in therms, use Equation C

- 1a.

where: CO 2 = Annual CO 2 mass emissions from natural gas combustion (metric tons). Gas = Annual natural gas usage, from billing records (therms). EF = Fuel

- specific default CO 2 emission factor for natural gas, from Table C

- 1 of this subpart (kg CO 2 /mmBtu). 0.1 = Conversion factor from therms to mmBtuPage 4 of 78

1 × 10 −3 = Conversion factor from kilograms to metric tons. (iii) If natural gas consumption is obtained from billing records and fuel usage is expressed in mmBtu, use Equation C

- 1b.

where: CO 2 = Annual CO 2 ma ss emissions from natural gas combustion (metric tons). Gas = Annual natural gas usage, from billing records (mmBtu). EF = Fuel

- specific default CO 2 emission factor for natural gas, from Table C

- 1 of this subpart (kg CO 2 /mmBtu). 1 × 10 −3 = Conversion facto r from kilograms to metric tons. (2) Tier 2 Calculation Methodology. Calculate the annual CO 2 mass emissions for each ty pe of fuel b y using either Equation C2a or C2c of this section, as appropriate. (i) Equation C

- 2a of this section applies to any typ e of fuel listed in Table C

- 1 of the subpart, except for municipal solid waste (MSW). For MSW combustion, use Equation C

- 2c of this section.

Where: CO 2 = Annual CO 2 mass emissions for a specific fuel ty pe (metric tons). Fuel = Mass or volume of the fuel comb usted during the ye ar, from company records as defined in §98.6 (express mass in short tons for solid fuel, volume in standard cubic feet for gaseous fuel, and volume in gallons for liquid fuel).Page 5 of 78

HHV = Annual average high heat value of the fuel (mmBtu per mass or volume). The average HHV shall be calculated according to the requirements of paragraph (a)(2)(ii) of this section.EF = Fuel

- specific default CO 2 emission factor, from Table C

- 1 of this subpart (kg CO 2 /mmBtu). 1 × 10 −3 = Conversion factor from kil ograms to metric tons. (ii) The minimum required sampling frequency for determining the annual average HHV ( e.g., monthly , quarterl y, semi

- annuall y, or b y lot) is specified in §98.34. The method for computing the annual average HHV is a function of unit si ze and how frequently you perform or receive from the fuel supplier the results of fuel sampling for HHV. The method is specified in paragraph (a)(2)(ii)(A) or (a)(2)(ii)(B) of this section, as applicable. (A) If the results of fuel sampling are received m onthly or more frequently , then for each unit with a maximum rated heat input capacity greater than or equal to 100 mmBtu/hr (or for a group of units that includes at least one unit of that size), the annual average HHV shall be calculated using Equation C

- 2b of this section. If multiple HHV determinations are made in any month, average the values for the month arithmetically
.

Where: (HHV) annual = Weighted annual average high heat value of the fuel (mmBtu per mass or volume).Page 6 of 78

(HHV) I = Measured high heat value of the fuel, for sample period “i” (which may be the arithmetic average of multiple determinations), or, if applicable, an appropriate substitute data value (mmBtu per mass or volume). (Fuel) I = Mass or volume of the fuel combusted during the sample period “i, ” (e.g., monthly , quart erly , semi

- annually , or by lot) from company

records (express mass in short tons for solid fuel, volume in standard cubic feet (e.g., for gaseous fuel, and vol ume in gallons for liquid fuel). n = Number of sample periods in the year . (B) If the results of fuel sampling are received less frequentl y than monthl y, or, for a unit with a maximum rated heat input capacity le ss than 100 mmBtu/hr (or a group of such units) regardless of the HHV sampling frequency , the annual average HHV shall either be computed according to paragraph (a)(2)(ii)(A) of this section or as the arithmetic average HHV for all values for the ye ar (inc luding valid samples and substitute data values under §98.35). (iii) For units that combust municipal solid waste (MSW) and that produce steam, use Equation C

- 2c of this section. Equation C

- 2c of this section may also be used for any

other solid fuel liste d in Table C

- 1 of this subpart provided that steam is generated b y the unit.

Where: CO 2 = Annual CO 2 mass emissions from MSW or solid fuel combustion (metric tons). Steam = Total mass of steam generated b y MSW or solid fuel combustion during the reporting year (lb steam). B = Ratio of the boiler's maximum rated heat input capacity to its design rated steam output capacity (mmBtu/lb steam).Page 7 of 78

EF = Fuel

- specific default CO 2 emission factor, from Table C

- 1 of this subpart (kg CO 2 /mmBtu). 1 × 10 −3 = Conversion factor from kilograms to metric tons. (3) Tier 3 Calculation Methodology. Calculate the annual CO 2 mass emissions for each fuel by using either Equation C3, C4, or C5 of this section, as appropriate. (i) For a solid fuel, use Equation C

- 3 of this s ection.

Where: CO 2 = Annual CO 2 mass emissions from the combustion of the specific solid fuel (metric tons). Fuel = Annual mass of the solid fuel combusted, from company records as defined in §98.6 (short tons). CC = Annual average carbon content of the solid fuel (percent by weight, expressed as a decimal fraction, e.g., 95% = 0.95). The annual average carbon content shall be determined using the same procedures as specified for HHV in paragraph (a)(2)(ii) of this section. 44/12 = Ratio of molecular weights, CO 2 to carbon. 0.91 = Conversion factor from short tons to metric tons. (ii) For a liquid fuel, use Equation C

- 4 of this section.

Where: CO 2 = Annual CO 2 mass emissions from the combustion of the specific liquid fuel (metric tons).Page 8 of 78

Fuel = Annual volume of the liquid fuel combusted (gallons). The volume of fuel combusted must be measured directly , using fuel flow meters calibrated according to §98.3(i). Fuel billing meters may

be used for this purpose. Tank drop measurements may also be used. CC = Annual average carbon content of the liquid fuel (kg C per gallon of fuel). The annual average carbon content shall be determined using the same procedures as specified for HHV in paragraph (a)(2)(ii) of this section. 44/12 = Ratio of molecular weights, CO 2 t o carbon. 0.001 = Conversion factor from kg to metric tons. (iii) For a gaseous fuel, use Equation C

- 5 of this section.

Where: CO 2 = Annual CO 2 mass emissions from combustion of the specific gaseous fuel (metric tons). Fuel = Annual volume of the gaseous fuel combusted (scf). The volume of fuel combusted must be measured directly , using fuel flow meters calibrated according to §98.3(i). Fuel billing meters may

be used for this purpose. CC = Annual average carbon content of the gaseous fuel (kg C per kg of fuel). The annual average carbon content shall be determined using the same procedures as specified for HHV in paragraph (a)(2)(ii) of this section. MW = Annual average molecular weight of the gaseous fuel (kg/kg

- mole). The annual average molecular weight shall be determined using the same procedures as specified for HHV in paragraph (a)(2)(ii) of this section.Page 9 of 78

MVC = Molar volume conversion factor at standard conditions, as defined in §98.6. Use 849.5 scf per kg mole if you select 68 °F as standard temperature and 836.6 scf per kg mole if yo u select 60 °F as standard temperature. 44/12 = Ratio of molecular weights, CO 2 to carbon. 0.001 = Conversion factor from kg to metric tons. (iv) Fuel flow meters that measure mass flow rates may be used for liquid or gaseous fuels, provided that the fuel density is used to convert the readings to volumetric flow rates. The density shall be measured at the same frequency as the carbon content. You must measure the density using one of the following appropriate methods. You may use a method published by a
consensus - based standards organization, if such a method exists, or you may use industry standard practice. Consensus

- based standards organizations include, but are not limited to, the following: ASTM International (100 Barr Harbor Drive, P.O. Box CB700, West Conshohocken, Pennsylvania 19428

- B2959, (800) 262

- 1373, http://www.astm.org), the American National Standards Institute (ANSI, 1819 L Street, NW., 6 th floor, Washington, DC 20036, (202) 293

- 8020, http://www.ansi.org), the American Gas Association (AGA), 400 North Capitol Street, NW., 4th Floor, Washington, DC 20001, (202) 824

- 7000, http://www.aga.org), the American Society of Mechanical Engineers (ASM E, Three Park Avenue, New York, NY 10016

- 5990, (800) 843

- 2763, http://www.asme.org), the American Petroleum Institute (API , 1220 L Street, NW., Washington, DC 20005

- 4070, (202) 682

- 8000, http://www.api.org), and the North American Energy

Standards Board (NAESB, 801 Travis Street, Suite 1675, Houston, TX 77002, (713) 356

- 0060, http://www.api.org). The method(s) used shall be documented in the GHG Monitoring Plan required under §98.3(g)(5).Page 10 of 78

(v) The following default density values may

be used for fuel oil, in lieu of using the methods in paragraph (a)(3)(iv) of this section: 6.8 lb/gal for No. 1 oil; 7.2 lb/gal for No. 2 oil; 8.1 lb/gal for No. 6 oil. (4) Tier 4 Calculation Methodology. Calculate the annual CO 2 mass emissions from all fuels combusted in a unit , by using quality

- assured data from continuous emission monitoring sy stems (CEMS). (i) This methodology

requires a CO 2 concentration monitor and a stack gas volumetric flow rate monitor, except as otherwise provided in paragraph (a)(4)(iv) of this section . Hourly measurements of CO 2 concentration and stack gas flow rate are converted to CO 2 mass emission rates in metric tons per hour. (ii) When the CO 2 concentration is measured on a wet basis, Equation C

- 6 of this section is used to calculate the hourly CO 2 emission rates:

Where: CO 2 = CO 2 mass emission rate (metric tons/hr). C CO2 = Hourly

average CO 2 concentration (% CO 2 ). Q = Hourl y average stack gas volumetric flow rate (scfh). 5.18 × 10 −7 = Conversion factor (metric tons/scf/% CO 2 ). (iii) If the CO 2 c oncentration is measured on a dry basis, a correction for the stack gas moisture content is required. You shall either continuously monitor the stack gas moisture content using a method described in §75.11(b)(2) of this chapter or use an appropriate default moisture percentage. For coal, wood, and natural gas combustion, you may use the default moisture values specified in §75.11(b)(1) of this chapter. Alternativel y, for any typ e of fuel, youPage 11 of 78

may determine an appropriate site

- specific default moisture value (or values), using measurements made with EPA Method 4

—Determination Of Moisture Content In Stack Gases, in appendix A

- 3 to part 60 of this chapter. Moisture data from the relative accuracy test audit (RATA) of a CEMS may be used for this purpose. If this option is selected, the site

- specific moisture default value(s) must represent the fuel(s) or fuel blends that are combusted in the unit during normal, stable operation, and must account for any distinct difference(s) in the stack gas moisture content ass ociated with different process operating conditions. For each site

- specific default moisture percentage, at least nine Method 4 runs are required, except where the option to use moisture data from a RATA is selected, and the applicable regulation allows a single moisture determination to represent two or more RATA runs. In that case, you may base the site

specific moisture percentage on the number of moisture runs allowed b y the RATA regulation. Calculate each site

- specific default moisture value by taking the arithmetic average of the Method 4 runs. Each site

- specific moisture default value shall be updated whenever the owner or operator believes the current value is non

- representative, due to changes in unit or process operation, but in any event no less f requentl y than annually. Use the updated moisture value in the subsequent CO 2 emissions calculations. For each unit operating hour, a moisture correction must be applied to Equation C

- 6 of this section as follows:

where: CO 2 * = Hourly

CO 2 mass emission rate, corrected for moisture (metric tons/hr). CO 2 = Hourly

CO 2 mass emission rate from Equation C

- 6 of this section, uncorrected (metric tons/hr).Page 12 of 78

%H 2 O = Hourl y moisture percentage in the stack gas (measured or default value, as appropriate). (iv) An ox yge n (O 2 ) concentration monitor may be used in lieu of a CO 2 concentration monitor to determine the hourly CO 2 concentrations, in accordance with Equation F

- 14a or F
14b (as applicable) in appendix F to part 75 of this chapter, if the effluent gas stream moni tored by the CEMS consists solely of combustion products ( i.e., no process CO 2 emissions or CO 2 emissions from sorbent are mixed with the combustion products) and if only fuels that are listed in Table 1 in section 3.3.5 of appendix F to part 75 of this ch apter are combusted in the unit. I f the O 2 monitoring option is selected, the F

- factors used in Equations F

- 14a and F

- 14b shall be determined according to section 3.3.5 or section 3.3.6 of appendix F to part 75 of this chapter, as applicable. If Equation F

- 14b is used, the hourl y moisture percentage in the stack gas shall be determined in accordance with paragraph (a)(4)(iii) of this section. (v) Each hourl y CO 2 mass emission rate from Equation C

- 6 or C
- 7 of this section is multiplied by

the operating time to convert it from metric tons per hour to metric tons. The operating time is the fraction of the hour during which fuel is combusted (e.g., the unit operating time is 1.0 if the unit operates for the whole hour and is 0.5 if the unit operates for 30 minut es in the hour). For common stack configurations, the operating time is the fraction of the hour during which effluent gases flow through the common stack. (vi) The hourl y CO 2 mass emissions are then summed over each calendar quarter and the quarterl y totals are summed to determine the annual CO 2 mass emissions. (vii) If both biomass and fossil fuel are combusted during the ye ar, determine and report the biogenic CO 2 mass emiss ions separately, as described in paragraph (e) of this section.Page 13 of 78

(viii) If a portion of the flue gases generated b y a unit subject to Tier 4 ( e.g., a slip stream) is continuously

diverted from the main flue gas exhaust sy stem for the purpose of heat recovery or some other similar process, and then exhausts through a stack that is not equipped with the continuous emission monitors to measure CO 2 mass emissions, CO 2 emissions shall be determined as follows: (A) At least once a ye ar, use EPA Methods 2 and 3A, and (if necessary) Method 4 in appendices A

- 2 and A

- 3 to part 60 of this chapter to perform emissions testing at a set point that best represents n ormal, stable process operating conditions. A minimum of three one

- hour Method 3A tests are required, to determine the CO 2 concentration. A Method 2 test shall be performed during each Method 3A run, to determine the stack gas volumetric flow rate. If mois ture correction is necessary, a Method 4 run shall also be performed during each Method 3A run. Important parametric information related to the stack gas flow rate ( e.g., damper positions, fan settings, etc. ) shall also be recorded during the test. (B) Cal culate a CO 2 mass emission rate (in metric tons/hr) from the stack test data, using a version of Equation C

- 6 in paragraph (a)(4)(ii) of this section, modified as follows. In the Equation C

- 6 nomenclature, replace the words “Hourly average” in the definiti ons of “C CO2 ” and “Q” with the words “3

- run average”. Substitute the arithmetic average values of CO 2 concentration and stack gas flow rate from the emission testing into modified Equation C

- 6. If CO 2 is measured on a dry basis, a moisture correction of th e calculated CO 2 mass emission rate is required. Use Equation C

- 7 in paragraph (a)(4)(ii) of this section to make this correction; replace the word “Hourl y” with the words “3

- run average” in the equation nomenclature. (C) The results of each annual stack t est shall be used in the GHG emissions calculations for the ye ar of the test.Page 14 of 78

(D) If, for the majority

of the operating hours during the ye ar, the diverted stream is withdrawn at a steady rate at or near the tested set point (as evidenced b y fan and damper settings and/or other parameters), you may use the calculated CO 2 mass emission rate from paragraph (a)(4)(viii)(B) of this section to estimate the CO 2 mass emissions for all operating hours in which flue gas is diverted from the main exhaust system. Othe rwise, you must account for the variation in the flow rate of the diverted stream, as described in paragraph (c)(4)(viii)(E) of this section. (E) If the flow rate of the diverted stream varies significantly throughout the year, except as provided below, repeat the stack test and emission rate calculation procedures described in paragraphs (c)(4)(viii)(A) and (c)(4)(viii)(B) of this section at a minimum of two more set points across the range of ty

pical operating conditions to develop a correlation between C O 2 mass emission rate and the parametric data. If additional testing is not feasible, use the following approach to develop the necessary correlation. Assume that the average CO 2 concentration obtained in the annual stack test is the same at all operating set points. Then, beginning with the measured flow rate from the stack test and the associated parametric data, perform an engineering anal ys is to estimate the stack gas flow rate at two or more additional set points. Calculate the CO 2 mass emission rate at each set point. (F) Calculate the annual CO 2 mass emissions for the diverted stream as follows. For a steady

- state process, multiply the number of hours in which flue gas was diverted from the main exhaust system by

the CO 2 mass emission rate from the st ack test. Otherwise, using the best available information and engineering judgment, apply the most representative CO 2 mass emission rate from the correlation in paragraph (c)(4)(viii)(E) of this section to determine the CO 2 mass emissions for each hour in which flue gas was diverted, and sum the results. To simplify the calculations, you may count partial operating hours as full hours.Page 15 of 78

(G) Finally , add the CO 2 mass emissions from paragraph(c)(4)(viii)(F) of this section to the annual CO 2 mass emissions meas ured b y the CEMS at the main stack. Report this sum as the total annual CO 2 mass emissions for the unit. (H) The exact method and procedures used to estimate the CO 2 mass emissions for the diverted portion of the flue gas exhaust stream shall be documented in the Monitoring Plan required under §98.3(g)(5). (5) Alternative methods for certain units subject to Part 75 of this chapter. Certain units that are not subject to subpart D of this part and that report data to EPA according to part 75 of this chapter may

qualify to use the alternative methods in this paragraph (a)(5), in lieu of using any of the four calculation methodology tiers. (i) For a unit that combusts only natural gas and/or fuel oil, is not subject to subpart D of this part, monitors and reports heat input data ye ar - round according to appendix D to part 75 of this chapter, but is not required by the applicable part 75 program to report CO 2 mass emissions data, calculate the annual CO 2 mass emissions for the purposes of this part as follows: (A) Use the hourl y heat input data from appendix D to part 75 of this chapter, together with Equation G

- 4 in appendix G to part 75 of this chapter to determine the hourly CO 2 mass emission rates, in units of tons/hr; (B) Use Equations F

- 12 and F

- 13 in appendi x F to part 75 of this chapter to calculate the quarterl y and cumulative annual CO 2 mass emissions, respectivel y, in units of short tons; and (C) Divide the cumulative annual CO 2 mass emissions value by 1.1023 to convert it to metric tons. (ii) For a un it that combusts only natural gas and/or fuel oil, is not subject to subpart D of this part, monitors and reports heat input data ye ar - round according to §75.19 of this chapter butPage 16 of 78

is not required b y the applicable part 75 program to report CO 2 mass emissi ons data, calculate the annual CO 2 mass emissions for the purposes of this part as follows: (A) Calculate the hourl y CO 2 mass emissions, in units of short tons, using Equation LM
11 in §75.19(c)(4)(iii) of this chapter. (B) Sum the hourl y CO 2 mass emission s values over the entire reporting year to obtain the cumulative annual CO 2 mass emissions, in units of short tons. (C) Divide the cumulative annual CO 2 mass emissions value by 1.1023 to convert it to metric tons. (iii) For a unit that is not subject to subpart D of this part, uses flow rate and CO 2 (or O 2 ) CEMS to report heat input data year - round according to part 75 of this chapter, but is not required b y the applicable part 75 program to report CO 2 mass emissions data, calculate the annual CO 2 mass emissions as follows: (A) Use Equation F

- 11 or F
- 2 (as applicable) in appendix F to part 75 of this chapter to calculate the hourl y CO 2 mass emission rates from the CEMS data. If an O 2 monitor is used, convert the hourl y average O 2 readings to CO 2 us ing Equation F

- 14a or F
- 14b in appendix F to part 75 of this chapter (as applicable), before appl ying Equation F

- 11 or F
- 2. (B) Use Equations F

- 12 and F

- 13 in appendix F to part 75 of this chapter to calculate the quarterl y and cumulative annual CO 2 mass e missions, respectivel y, in units of short tons. (C) Divide the cumulative annual CO 2 mass emissions value by 1.1023 to convert it to metric tons. (iv) For units that qualify to use the alternative CO 2 emissions calculation methods in paragraphs (a)(5)(i ) through (a)(5)(iii) of this section, if both biomass and fossil fuel are combusted during the ye ar, separate calculation and reporting of the biogenic CO 2 massPage 17 of 78

emissions (as described in paragraph (e) of this section) is optional, only for the 2010 reporting ye ar, as provided in §98.3(c)(12). (b) Use of the four tiers. Use of the four tiers of CO 2 emissions calculation methodologies described in paragraph (a) of this section is subject to the following conditions, requirements, and restrictions: (1) The Tier 1 Calculation Methodology : (i) May be used for any fuel listed in Table C

- 1 of this subpart that is combusted in a unit with a maximum rated heat input capacity of 250 mmBtu/hr or less. (ii) May be used for MSW in a unit of any size that does not produce steam, if the use of Tier 4 is not required. (iii) May be used for solid, gaseous, or liquid biomass fuels in a unit of any size provided that the fuel is listed in Table C

- 1 of this subpart. (iv) May not be used if you routinely perform fuel sampling and anal ys is for the fuel high heat value (HHV) or routinely receive the results of HHV sampling and analy sis from the fuel supplier at the minimum frequency specified in §98.34(a), or at a greater frequency . In such cases, Tier 2 shall be used. This restriction does not apply to paragraphs (b)(1)(ii), (b)(1)(v), (b)(1)(vi), and (b)(1)(vii) of this section. (v) May be used for natural gas combustion in a unit of any size, in cases where the annual natural gas consumption is obtained from fuel billing record s in units of therms or mmBtu. (vi) May be used for MSW combustion in a small, batch incinerator that burns no more than 1,000 tons per year of MSW.Page 18 of 78

(vii) May be used for the combustion of MSW and/or tires in a unit, provided that no more than 10 percent o f the unit's annual heat input is derived from those fuels, combined. Notwithstanding this requirement, if a unit combusts both MSW and tires and the reporter elects not to separatel y calculate and report biogenic CO 2 emissions from the combustion of tires , Tier 1 may be used for the MSW combustion, provided that no more than 10 percent of the unit's annual heat input is derived from MSW. (viii) May

be used for the combustion of a fuel listed in Table C

- 1 if the fuel is combusted in a unit with a maximum rated heat input capacity greater than 250 mmBtu/hr (or, pursuant to §98.36(c)(3), in a group of units served by a common supply

pipe, having at least one unit with a maximum rated heat input capacity greater than 250 mmBtu/hr), provided that both of the fol lowing conditions apply : (A) The use of Tier 4 is not required. (B) The fuel provides less than 10 percent of the annual heat input to the unit, or if §98.36(c)(3) applies, to the group of units served by a common supply

pipe. (2) The Tier 2 Calculation Me thodology : (i) May be used for the combustion of any type of fuel in a unit with a maximum rated heat input capacity

of 250 mmBtu/hr or less provided that the fuel is listed in Table C

- 1 of this subpart. (ii) May be used in a unit with a maximum rated heat input capacity greater than 250 mmBtu/hr for the combustion of natural gas and/or distillate fuel oil. (iii) May be used for MSW in a unit of any size that produces steam, if the use of Tier 4 is not required. (3) The Tier 3 Calculation Methodology :Page 19 of 78

(i) M ay be used for a unit of any

size that combusts any

typ e of fuel listed in Table C

- 1 of this subpart (except for MSW), unless the use of Tier 4 is required. (ii) Shall be used for a unit with a maximum rated heat input capacity greater than 250 mmBtu/hr th at combusts any typ e of fuel listed in Table C

- 1 of this subpart (except MSW), unless either of the following conditions appl y: (A) The use of Tier 1 or 2 is permitted, as described in paragraphs (b)(1)(iii), (b)(1)(v), (b)(1)(viii), and (b)(2)(ii) of this section. (B) The use of Tier 4 is required. (iii) Shall be used for a fuel not listed in Table C

- 1 of this subpart if the fuel is combusted in a unit with a maximum rated heat input capacity greater than 250 mmBtu/hr (or, pursuant to §98.36(c)(3), in a group of units served by a common supply

pipe, having at least one unit with a maximum rated heat input capacity greater than 250 mmBtu/hr), provided that both of the following conditions apply : (A) The use of Tier 4 is not required. (B) The fuel provides 10 % or more of the annual heat input to the unit or, if §98.36(c)(3) applies, to the group of units served b y a common supply pipe. (iv) Shall be used when specified in another applicable subpart of this part, regardless of unit size. (4) The Tier 4 Calculation Methodology : (i) May be used for a unit of any

size, combusting any

typ e of fuel. Tier 4 may

also be used for any group of stationary fuel combustion units, process units, or manufacturing units that share a common stack or duct.Page 20 of 78

(ii) Shall be used if the unit meets all six of the conditions specified in paragraphs (b)(4)(ii)(A) through (b)(4)(ii)(F) of this section: (A) The unit has a maximum rated heat input capacity greater than 250 mmBtu/hr, or if the unit combusts municipal solid waste and has a maximum rated input capacity greater than 600 tons per day

of MSW. (B) The unit combusts solid fossil fuel or MSW as the primary fuel. (C) The unit has operated for more than 1,000 hours in any calendar year since 2005. (D) The unit has installed CEMS that are required either b y an applicable Federal or State regulation or the unit's operating permit. (E) The installed CEMS include a gas monitor of any kind or a stack gas volumetric flow rate monitor, or both and the monitors have been certified, either in ac cordance with the requirements of part 75 of this chapter, part 60 of this chapter, or an applicable State continuous monitoring program. (F) The installed gas or stack gas volumetric flow rate monitors are required, either b y an applicable Federal or Stat e regulation or b y the unit's operating permit, to undergo periodic quality assurance testing in accordance with either appendix B to part 75 of this chapter, appendix F to part 60 of this chapter, or an applicable State continuous monitoring program. (iii ) Shall be used for a unit with a maximum rated heat input capacity of 250 mmBtu/hr or less and for a unit that combusts municipal solid waste with a maximum rated input capacity of 600 tons of MSW per day or less, if the unit meets all of the following three conditions: (A) The unit has both a stack gas volumetric flow rate monitor and a CO 2 concentration monitor.Page 21 of 78

(B) The unit meets the conditions specified in paragraphs (b)(4)(ii)(B) through (b)(4)(ii)(D) of this section. (C) The CO 2 and stack gas volumetric flow rate monitors meet the conditions specified in paragraphs (b)(4)(ii)(E) and (b)(4)(ii)(F) of this section. (iv) May appl y to common stack or duct configurations where: (A) The combined effluent gas streams from two or more stationary fuel combusti on units are vented through a monitored common stack or duct. In this case, Tier 4 shall be used if all of the conditions in paragraph (b)(4)(iv)(A)(1) of this section or if the conditions in paragraph (b)(4)(iv)(A)(2) of this section are met. ( 1 ) At least one of the units meets the requirements of paragraphs (b)(4)(ii)(A) through (b)(4)(ii)(C) of this section, and the CEMS installed at the common stack (or duct) meet the requirements of paragraphs (b)(4)(ii)(D) through (b)(4)(ii)(F) of this section. ( 2 ) At least one of the units and the monitors installed at the common stack or duct meet the requirements of paragraph (b)(4)(iii) of this section. (B) The combined effluent gas streams from a process or manufacturing unit and a stationary fuel combustion unit are vented through a monitored common stack or duct. In this case, Tier 4 shall be used if the combustion unit and the monitors installed at the common stack or duct meet the applicability criteria specified in paragraph (b)(4)(iv)(A)( 1 ), or (b)(4)(iv)(A)( 2 ) of this section. (C) The combined effluent gas streams from two or more manufacturing or process units are vented through a common stack or duct. In this case, if any of the units is required b y an applicable subpart of this part to use Tier 4, the CO 2 mass emissions may be monitored at each individual unit, or the combined CO 2 mass emissions may be monitored at the common stack orPage 22 of 78

duct. However, if it is not feasible to monitor the individual units, the combined CO 2 mass emissions shall be monitored at the common stack or duct. (5) The Tier 4 Calculation Methodology shall be used: (i) Starting on January

1, 2010, for a unit that is required to report CO 2 mass emissions beginning on that date, if all of the monitors needed to measure CO 2 mass emissions have been installed and certified b y that date. (ii) No later than January 1, 2011, for a unit that is required to report CO 2 mass emissions beginning on January

1, 2010, if all of the monitors needed to measure CO 2 mass emissions have not been installed and certified by January 1, 2010. In this case, you may use Tier 2 or Tier 3 to report GHG emissions for 2010. However, if the required CEMS are certified some time in 2010, yo u need not wait until January 1, 2011 to begin using Tier 4. Rather, you may switch from Tier 2 or Tier 3 to Tier 4 as soon as CEMS certification testing is successfully completed. If this reporting option is chosen, you must document the change in CO 2 calculation methodology in the Monitoring Plan required under §98.3(g)(5) and in the GHG emissions report under §98.3(c). Data recorded b y the CEMS during a certification test period in 2010 may be used for reporting under this part, provided that the following two conditions are met: (A) The certification tests are passed in sequence, with no test failures. (B) No unscheduled maintenance or repair of the CEMS is performed during the certification test period. (iii) No later than 180 days following the date on which a change is made that triggers Tier 4 applicability

under paragraph (b)(4)(i i) or (b)(4)(iii) of this section ( e.g., a change in the primary fuel, manner of unit operation, or installed continuous monitoring equipment).Page 23 of 78

(6) You may

elect to use any

applicable higher tier for one or more of the fuels combusted in a unit. For exampl e, if a 100 mmBtu/hr unit combusts natural gas and distillate fuel oil, you may

elect to use Tier 1 for natural gas and Tier 3 for the fuel oil, even though Tier 1 could have been used for both fuels. However, for units that use either the Tier 4 or the al ternative calculation methodology specified in paragraph (a)(5)(iii) of this section, CO 2 emissions from the combustion of all fuels shall be based solel y on CEMS measurements. (c) Calculation of CH 4 and N

2 O emissions from stationary combustion sources. Yo u must calculate annual CH 4 and N 2 O mass emissions only for units that are required to report CO 2 emissions using the calculation methodologies of this subpart and for onl y those fuels that are listed in Table C

- 2 of this subpart. (1) Use Equation C

- 8 of this section to estimate CH 4 and N 2 O emissions for any fuels for which you use the Tier 1 or Tier 3 calculation methodologies for CO 2 , except when natural gas usage in units of therms or mmBtu is obtained from gas billing records. In that case, use Equation C

- 8a in paragraph (c)(1)(i) of this section or Equation C

- 8b in paragraph (c)(1)(ii) of this section (as applicable). For Equation C

- 8, use the same values for fuel consumption that you use for the Tier 1 or Tier 3 calculation.

Where: CH 4 or N 2 O = Annual CH 4 or N 2 O emissions from the combustion of a particular type of fuel (metric tons). Fuel = Mass or volume of the fuel combusted, either from company records or directl y measured by

a fuel flow meter, as applicable (mass or volume per ye ar).Page 24 of 78

HHV = Default high heat value of the fuel from Table C

- 1 of this subpart; alternativel y, for Tier 3, if actual HHV data are available for the reporting year, you may average these data using th e procedures specified in paragraph (a)(2)(ii) of this section, and use the average value in Equation C

- 8 (mmBtu per mass or volume). EF = Fuel

- specific default emission factor for CH 4 or N 2 O, from Table C

- 2 of this subpart (kg CH 4 or N 2 O per mmBtu). 1 × 1 0 −3 = Conversion factor from kilograms to metric tons. (i) Use Equation C

- 8a to calculate CH 4 and N 2 O emissions when natural gas usage is obtained from gas billing records in units of therms.

where: CH 4 or N 2 O = Annual CH 4 or N 2 O emissions from the combu stion of natural gas (metric tons). Fuel = Annual natural gas usage, from gas billing records (therms). EF = Fuel

- specific default emission factor for CH 4 or N 2 O, from Table C

- 2 of this subpart (kg CH 4 or N 2 O per mmBtu). 0.1 = Conversion factor from therms to mmBtu 1 × 10 −3 = Conversion factor from kilograms to metric tons. (ii) Use Equation C

- 8b to calculate CH 4 and N 2 O emissions when natural gas usage is obtained from gas billing records in units of mmBtu. CH 4 or N 2 O = 1 × 10 −3 * Fuel * EF (Eq. C

- 8b) where:Page 25 of 78

CH 4 or N 2 O = Annual CH 4 or N 2 O emissions from the combustion of natural gas (metric tons). Fuel = Annual natural gas usage, from gas billing records (mmBtu). EF = Fuel

- specific default emission factor for CH 4 or N 2 O, from Table C

- 2 of this subpart (kg CH 4 or N 2 O per mmBtu). 1 × 10 −3 = Conversion factor from kilograms to metric tons. (2) Use Equation C

- 9a of this section to estimate CH 4 and N 2 O emissions for an y fuels for which you use the Tier 2 Equation C

- 2a of this section to estimate CO 2 emissions. Use the same values for fuel consumption and HHV that you use for the Tier 2 calculation.

Where: CH 4 or N 2 O = Annual CH 4 or N 2 O emissions from the combustion of a particular type of fuel (metric tons). Fuel = Mass or volume of the fuel combus ted during the reporting year. HHV = High heat value of the fuel, averaged for all valid measurements for the reporting ye ar (mmBtu per mass or volume). EF = Fuel

- specific default emission factor for CH 4 or N 2 O, from Table C

- 2 of this subpart (kg CH 4 or N 2 O per mmBtu). 1 × 10 −3 = Conversion factor from kilograms to metric tons. (3) Use Equation C

- 9b of this section to estimate CH 4 and N 2 O emissions for an y fuels for which you use Equation C

- 2c of this section to calculate the CO 2 emissions. Use the same values for steam generation and the ratio “B” that you use for Equation C

- 2c.Page 26 of 78

Where: CH 4 or N 2 O = Annual CH 4 or N 2 O emissions from the combustion of a solid fuel (metric tons). Steam = Total mass of steam generated b y solid fuel combustion during the reporting ye ar (lb steam). B = Ratio of the boiler's maximum rated heat input capacity to its design rated steam output (mmBtu/lb steam). EF = Fuel

- specific emission factor for CH 4 or N 2 O, from Table C

- 2 of this subpart (kg CH 4 or N 2 O per mmBtu). 1 × 10 −3 = Conversion factor from kilograms to metric tons. (4) Use Equation C

- 10 of this section for: units subject to subpart D of this part; units that qualify for and elect to use the alternative CO 2 mass emissions calculation methodologies described in paragra

ph (a)(5) of this section; and units that use the Tier 4 Calculation Methodology
.

Where: CH 4 or N 2 O = Annual CH 4 or N 2 O emissions from the combustion of a particular type of fuel (metric tons). (HI) A = Cumulative annual heat input from combustion of the fuel (mmBtu). EF = Fuel

- specific emission factor for CH 4 or N 2 O, from Table C

- 2 of this section (kg CH 4 or N 2 O per mmBtu). 0.001 = Conversion factor from kg to metric tons.Page 27 of 78

(i) If onl y one type of fuel listed in Table C

- 2 of this subpart is combusted during the reporting year, substitute the cumulative annual heat input from combustion of the fuel into Equation C

- 10 of this section to calculate the annual CH 4 or N 2 O emissions. For units in the Acid Rain Program and units that report heat input data to EPA year - round according to part 75 of this chapter, obtain the cumulative annual heat input directl y from the electronic data reports required under §75.64 of this chapter. For Tier 4 units, use the best available information, as described in paragraph (c)(4)(ii)(C) of this section, to estimate the cumulative annual heat input (HI) A . (ii) If more than one type of fuel listed in Table C

- 2 of this subpart is combusted during the reporting ye ar, use Equation C

- 10 of this section separately for each type of fuel, except as provided in paragraph (c)(4)(ii)(B) of this section. Determine the appropriate values of (HI) A as follows: (A) For units in the Acid Rain Program and other units that report heat input data to EPA ye ar - round according to part 75 of this chapter, obtain (HI) A for each type of fuel from the electronic data reports required under §75.64 of this chapter, except as otherwise provided in paragraphs (c)(4)(ii)(B) and (c)(4)(ii)(D) of this section. (B) For a unit that uses CEMS to monitor hourly heat input according to part 75 of this chapter, the value of (HI) A obtained from the electronic data reports under §75.64 of this chapter may be attributed exclusively to the fuel with the highest F

- factor, whe n the reporting option in 3.3.6.5 of appendix F to part 75 of this chapter is selected and implemented. (C) For Tier 4 units, use the best available information ( e.g., fuel feed rate measurements, fuel heating values, engineering analy sis) to estimate the value of (HI) A for each typ e of fuel. Instrumentation used to make these estimates is not subject to the calibration requirements of §98.3(i) or to the QA requirements of §98.34.Page 28 of 78

(D) Units in the Acid Rain Program and other units that report heat input dat a to EPA ye ar - round according to part 75 of this chapter may use the best available information described in paragraph (c)(4)(ii)(C) of this section, to estimate (HI) A for each fuel typ e, whenever fuel

specific heat input values cannot be directly obtained from the electronic data reports under §75.64 of this chapter. (5) When multiple fuels are combusted during the reporting year, sum the fuel

- specific results from Equations C

- 8, C
- 8a, C
- 8b, C

- 9a, C
- 9b, or C

- 10 of this section (as applicable) to obtain the total annual CH 4 and N 2 O emissions, in metric tons. (6) Calculate the annual CH 4 and N 2 O mass emissions from the combustion of blended fuels as follows: (i) If the mass or volume of each component fuel in the blend is measured before the fuels are mixed and combusted, calculate and report CH 4 and N 2 O emissions separatel y for each component fuel, using the applicable procedures in this paragraph (c). (ii) If the mass or volume of each component fuel in the blend is not measured before the fuels are mixed and combusted, a reasonable estimate of the percentage composition of the blend, based on best available information, is required. Perform the following calculations for each component fuel “i” that is listed in Table C

- 2: (A) Multiply

(% Fuel) i , the estimated mass or volume percentage (decimal fraction) of component fuel “i”, b y the total annual mass or volume of the blended fuel combusted during the reporting year, to obtain an estimate of the annual consumption of component “i”; (B) Multiply

the result fr om paragraph (c)(6)(ii)(A) of this section b y the HHV of the fuel (default value or, if available, the measured annual average value), to obtain an estimate of the annual heat input from component “i”;Page 29 of 78

(C) Calculate the annual CH 4 and N 2 O emissions from co mponent “i”, using Equation C

8, C
- 8a, C
- 8b, C

- 9a, or C
- 10 of this section, as applicable; (D) Sum the annual CH 4 emissions across all component fuels to obtain the annual CH 4 emissions for the blend. Similarly sum the annual N 2 O emissions across all compo nent fuels to obtain the annual N 2 O emissions for the blend. Report these annual emissions totals. (d) Calculation of CO2 from sorbent. (1) When a unit is a fluidized bed boiler, is equipped with a wet flue gas desulfurization sy stem, or uses other acid ga s emission controls with sorbent injection to remove acid gases, if the chemical reaction between the acid gas and the sorbent produces CO 2 emissions, use Equation C

- 11 of this section to calculate the CO 2 emissions from the sorbent, except when those CO 2 emissions are monitored by CEMS. When a sorbent other than CaCO 3 is used, determine site

- specific values of R and MW S .

Where: CO 2 = CO 2 emitted from sorbent for the reporting year (metric tons). S = L imestone or other sorbent used in the reporting year, from company records (short tons). R = The number of moles of CO 2 released upon capture of one mole of the acid gas species being removed (R = 1.00 when the sorbent is CaCO 3 and the targeted acid gas species is SO 2 ). MW CO2 = Molecular weight of carbon diox ide (44). MW S = Molecular weight of sorbent (100 if calcium carbonate). 0.91 = Conversion factor from short tons to metric tons.Page 30 of 78

(2) The total annual CO 2 mass emissions reported for the unit shall include the CO 2 emissions from the combustion process and the CO 2 emissions from the sorbent. (e) Biogenic CO2 emissions from combustion of biomass with other fuels. Use the applicable procedures of this paragraph (e) to estimate biogenic CO 2 emissions from units that combust a combination of biomass and fossil fu els ( i.e., either co

- fired or blended fuels). Separate reporting of biogenic CO 2 emissions from the combined combustion of biomass and fossil fuels is required for those biomass fuels listed in Table C

- 1 of this section and for municipal solid waste. In addition, when a biomass fuel that is not listed in Table C

- 1 is combusted in a un it that has a maximum rated heat input greater than 250 mmBtu/hr, if the biomass fuel accounts for 10% or more of the annual heat input to the unit, and if the unit does not use CEMS to quantify its annual CO 2 mass emissions, then, pursuant to §98.33(b)(3) (iii), Tier 3 must be used to determine the carbon content of the biomass fuel and to calculate the biogenic CO 2 emissions from combustion of the fuel. Notwithstanding these requirements, in accordance with §98.3(c)(12), separate reporting of biogenic CO 2 emissions is optional for the 2010 reporting year for units subject to subpart D of this part and for units that use the CO 2 mass emissions calculation methodologies in part 75 of this chapter, pursuant to paragraph (a)(5) of this section. However, if the owner or operator opts to report biogenic CO 2 emissions separatel y for these units, the appropriate method(s) in this paragraph (e) shall be used. Separate reporting of biogenic CO 2 emissions from the combustion of tires is also optional, but may be report ed b y following the provisions of paragraph (e)(3) of this section. (1) You may

use Equation C

- 1 of this subpart to calculate the annual CO 2 mass emissions from the combustion of the biomass fuels listed in Table C

- 1 of this subpart (except MSW and tires), in a unit of any size, including units equipped with a CO 2 CEMS, except when the use ofPage 31 of 78

Tier 2 is required as specified in paragraph (b)(1)(iv) of this section. Determine the quantity of biomass combusted using one of the following procedures in this para graph (e)(1), as appropriate, and document the selected procedures in the Monitoring Plan under §98.3(g): (i) Company

records. (ii) The procedures in paragraph (e)(4) of this section. (iii) The best available information for premixed fuels that contain bio mass and fossil fuels ( e.g., liquid fuel mixtures containing biodiesel). (2) You may

use the procedures of this paragraph if the following three conditions are met: First, a CO 2 CEMS (or a surrogate O 2 monitor) and a stack gas flow rate monitor are used to determine the annual CO 2 mass emissions (either according to part 75 of this chapter, the Tier 4 Calculation Methodology , or the alternative calculation methodology specified in paragraph (a)(5)(iii) of this section); second, neither MSW nor tires is comb usted in the unit during the reporting year; and third, the CO 2 emissions consist solely of combustion products ( i.e., no process or sorbent emissions included). (i) For each operating hour, use Equation C

- 12 of this section to determine the volume of CO 2 emitted.

Where: V CO2h = Hourly

volume of CO 2 emitted (scf). (%CO 2 ) h = Hourly

average CO 2 concentration, measured b y the CO 2 concentration monitor, or, if applicable, calculated from the hourly average O 2 concentration (%CO 2 ). Q h = Hourly

average stack ga s volumetric flow rate, measured by the stack gas volumetric flow rate monitor (scfh).Page 32 of 78

th = Source operating time (decimal fraction of the hour during which the source combusts fuel, i.e., 1.0 for a full operating hour, 0.5 for 30 minutes of operation, etc .). 100 = Conversion factor from percent to a decimal fraction. (ii) Sum all of the hourly

V CO2h values for the reporting ye ar, to obtain Vtotal , the total annual volume of CO 2 emitted. (iii) Calculate the annual volume of CO 2 emitted from fossil fuel combustion using Equation C

- 13 of this section. I f two or more types of fossil fuel are combusted during the ye ar, perform a separate calculation with Equation C

- 13 of this section for each fuel and sum the results.

Where: V ff = Annual volume of CO 2 emitted from combustion of a particular fossil fuel (scf). Fuel = Total quantity

of the fossil fuel combusted in the reporting year, from company records, as defined in §98.6 (lb for solid fuel, gallons for liquid fuel, and scf for gaseous fuel). F c = Fuel

- specific carbon based F

- factor, either a default value from Table 1 in section 3.3.5 of appendix F to part 75 of this chapter, or a site

- specific value determined under section 3.3.6 of appendix F to part 75 (scf CO 2 /mmBtu). H HV = High heat value of the fossil fuel, from fuel sampling and anal ys is (annual average value in Btu/lb for solid fuel, Btu/gal for liquid fuel and Btu/scf for gaseous fuel, sampled as specified (e.g., monthly, quarterly , semi

- annually , or by lot) in §98. 34(a)(2)). The average HHV shall be calculated according to the requirements of paragraph (a)(2)(ii) of this section. 10 6 = Conversion factor, Btu per mmBtu.Page 33 of 78

(iv) Subtract V ff from Vtotal to obtain Vbio , the annual volume of CO 2 from the combustion of biom ass. (v) Calculate the biogenic percentage of the annual CO 2 emissions, expressed as a decimal fraction, using Equation C

- 14 of this section:

(vi) Calculate the annual biogenic CO 2 mass emissions, in metric tons, by multiplying the results obtained from Equation C

- 14 of this section by the annual CO 2 mass emissions in metric tons, as determined: (A) Under paragraph (a)(4)(vi) of this section, for units using the Tier 4 Calculation Methodology
. (B) Under paragraph (a)(5)(iii)(B) of this section, for units using the alternative calculation methodology

specified in paragraph (a)(5)(iii). (C) From the electronic data report required under §75.64 of this chapter, for units in the Acid Rain Program and other units using CEMS to monitor and report CO 2 mass emissi ons according to part 75 of this chapter. However, before calculating the annual biogenic CO 2 mass emissions, multiply

the cumulative annual CO 2 mass emissions by 0.91 to convert from short tons to metric tons. (3) You must use the procedures in paragraphs (e)(3)(i) through (e)(3)(iii) of this section to determine the annual biogenic CO 2 emissions from the combustion of MSW, except as otherwise provided in paragraph (e)(3)(iv) of this section. These procedures also may be used for any unit that co

- fires bio mass and fossil fuels, including units equipped with a CO 2 CEMS, and units for which optional separate reporting of biogenic CO 2 emissions from the combustion of tires is selected.Page 34 of 78

(i) Use an applicable CO 2 emissions calculation method in this section to q uantify the total annual CO 2 mass emissions from the unit. (ii) Determine the relative proportions of biogenic and non

- biogenic CO 2 emissions in the flue gas on a quarterl y basis using the method specified in §98.34(d) (for units that combust MSW as the primary

fuel or as the onl y fuel with a biogenic component) or in §98.34(e) (for other units, including units that combust tires). (iii) Determine the annual biogenic CO 2 mass emissions from the unit by multiplying the total annual CO 2 mass emissions by the annual average biogenic decimal fraction obtained from §98.34(d) or §98.34(e), as applicable. (iv) If the combustion of MSW and/or tires provides no more than 10 percent of the annual heat input to a unit, or if a small, batch incinerator combusts no more than 1,000 tons per ye ar of MSW, you may

estimate the annual biogenic CO 2 emissions as follows, in lieu of following the procedures in paragraphs (e)(3)(i) through (e)(3)(iii) of this section: (A) Calculate the total annual CO 2 emissions from combustion of MSW and/or tires in the unit, using the Tier 1 calculation methodology in paragraph (a)(1) of this section. (B) Multiply

the result from paragraph (e)(3)(iv)(A) of this section by the appropriate default factor to determine the annual biogenic CO 2 emissions, in metric tons. For MSW, use a default factor of 0.60 and for tires, use a default factor of 0.20. (4) If Equation C

- 1 or Equation C

- 2a of this section is selected to calculate the annual biogenic mass emissions for wood, wood waste, or other s olid biomass

- derived fuel, Equation C

15 of this section may

be used to quantify

biogenic fuel consumption, provided that all of the required input parameters are accuratel y quantified. Similar equations and calculationPage 35 of 78

methodologies based on steam generation and boiler efficiency may be used, provided that they are documented in the GHG Monitoring Plan required by §98.3(g)(5).

Where: (Fuel) p = Quantity

of biomass consumed during the measurement period “p” (tons/year or tons/month, as applicable). H = Ave rage enthalp y of the boiler steam for the measurement period (Btu/lb). S = Total boiler steam production for the measurement period (lb/month or lb/year, as applicable). (HI) nb = Heat input from co

- fired fossil fuels and non

- biomass

- derived fuels for the
m easurement period, based on company records of fuel usage and default or measured HHV values (Btu/month or Btu/year, as applicable). (HHV) bio = Default or measured high heat value of the biomass fuel (Btu/lb). (Eff) bio = Percent efficiency of biomass

- to - en ergy

conversion, expressed as a decimal fraction. 2000 = Conversion factor (lb/ton). (5) For units subject to subpart D of this part and for units that use the methods in part 75 of this chapter to quantify CO 2 mass emissions in accordance with paragraph (a)(5) of this section, you may

calculate biogenic CO 2 emissions from the combustion of biomass fuels listed in Table C

- 1 of this subpart using Equation C

- 15a. This equation may not be used to calculate biogenic CO 2 emissions from the combustion of tires or MSW; the methods described in paragraph (e)(3) of this section must be used for those fuels. Whenever (HI) A , the annual heat input from combustion of biomass fuel in Equation C

- 15a, cannot be determined solely from thePage 36 of 78

information in the electronic emissions reports under §75.64 of this chapter ( e.g., in cases where a unit uses CEMS in combination with multiple F

- factors, a worst

- case F
- factor, or a prorated F

factor to report heat input rather than reporting h eat input based on fuel ty pe), use the best available information (as described in §§98.33(c)(4)(ii)(C) and (c)(4)(ii)(D)) to determine (HI) A . CO2 = 0.001 * (HI)A * EF (Eq. C

- 15a) where: CO 2 = Annual CO 2 mass emissions from the combustion of a particular typ e of biomass fuel listed in Table C

- 1 (metric tons) (HI) A = Annual heat input from the biomass fuel, obtained, where feasible, from the electronic emissions reports required under §75.64 of this chapter. Where this is not feasible use best available info rmation, as described in §§98.33(c)(4)(ii)(C) and (c)(4)(ii)(D) (mmBtu) EF = CO 2 emission factor for the biomass fuel, from Table C

- 1 (kg CO 2 /mmBtu) 0.001 = Conversion factor from kg to metric tons **§98.34 Monitoring and QA/QC requirements.**  The CO 2 mass emissions data for stationary fuel combustion sources shall be monitored as follows: (a) For the Tier 2 Calculation Methodology : (1) All fuel samples shall be taken at a location in the fuel handling s ys tem that provides a sample representative of th e fuel combusted. The fuel sampling and analy sis may be performed by either the owner or operator or the supplier of the fuel. (2) The minimum required frequency of the HHV sampling and anal ys is for each typ e of fuel or fuel mixture (blend) is specified in this paragraph. When the specified frequency for a particular fuel or blend is based on a specified time period ( e.g., week, month, quarter, or half

-Page 37 of 78

ye ar), fuel sampling and anal ys is is required onl y for those time periods in which the fuel or blend is co mbusted. The owner or operator may perform fuel sampling and anal ys is more often than the minimum required frequency , in order to obtain a more representative annual average HHV. (i) For natural gas, semiannual sampling and analy sis is required ( i.e., twic e in a calendar ye ar, with consecutive samples taken at least four months apart). (ii) For coal and fuel oil, and for any other solid or liquid fuel that is delivered in lots, anal ys is of at least one representative sample from each fuel lot is required. F or fuel oil, as an alternative to sampling each fuel lot, a sample may be taken upon each addition of oil to the unit's storage tank. Flow proportional sampling, continuous drip sampling, or daily manual oil sampling may

also be used, in lieu of sampling e ach fuel lot. If the daily manual oil sampling option is selected, sampling from a particular tank is required onl y on days when oil from the tank is combusted by

the unit (or units) served b y the tank. If you elect to sample from the storage tank upon eac h addition of oil to the tank, you must take at least one sample from each tank that is currentl y in service and whenever oil is added to the tank, for as long as the tank remains in service. You need not take any samples from a storage tank while it is out of service. Rather, take a sample when the tank is brought into service and whenever oil is added to the tank, for as long as the tank remains in service. If multiple additions of oil are made to a particular in

- service tank on a given day ( e.g., from mu ltiple deliveries), one sample taken after the final addition of oil is sufficient. For the purposes of this section, a fuel lot is defined as a shipment or delivery

of a single type of fuel ( e.g., ship load, barge load, group of trucks, group of railroad cars, oil delivery via pipeline from a tank farm, etc. ). However, if multiple deliveries of a particular ty

pe of fuel are received from the same supply source in a given calendar month, thePage 38 of 78

deliveries for that month may be considered, collectively , to comp rise a fuel lot, requiring onl y one representative sample, subject to the following conditions: (A) For coal, the “type” of fuel means the rank of the coal ( i.e., anthracite, bituminous, sub

- bituminous, or lignite). For fuel oil, the “type” of fuel means the grade number or classification of the oil ( e.g., No. 1 oil, No. 2 oil, kerosene, Jet A fuel, etc. ). (B) The owner or operator shall document in the monitoring plan under §98.3(g)(5) how the monthly

sampling of each type of fuel is performed. (iii) For l iquid fuels other than fuel oil, and for gaseous fuels other than natural gas (including biogas), sampling and anal ys is is required at least once per calendar quarter. To the extent practicable, consecutive quarterly samples shall be taken at least 30 day s apart. (iv) For other solid fuels (except MSW), weekly sampling is required to obtain composite samples, which are then anal yz ed monthl y. (v) For fuel blends that are received already mixed, or that are mixed on

- site without measuring the exact amount of each component, as described in paragraph (a)(3)(ii) of this section, determine the HHV of the blend as follows. For blends of solid fuels (except MSW), weekl y sampling is required to obtain composite samples, which are analyzed monthly . For blends of liqu id or gaseous fuels, sampling and analy sis is required at least once per calendar quarter. More frequent sampling is recommended if the composition of the blend varies significantl y during the year. (3) Special considerations for blending of fuels. Insitu ations where different ty pes of fuel listed in Table C

- 1 of this subpart (for example, different ranks of coal or different grades of fuel oil) are in the same state of matter ( i.e., solid, liquid, or gas), and are blended prior toPage 39 of 78

combustion, use the foll owing procedures to determine the appropriate CO 2 emission factor and HHV for the blend. (i) If the fuels to be blended are received separately, and if the quantity (mass or volume) of each fuel is measured before the fuels are mixed and combusted, then, f or each component of the blend, calculate the CO 2 mass emissions separately . Substitute into Equation C

- 2a of this subpart the total measured mass or volume of the component fuel (from company records), together with the appropriate default CO 2 emission fa ctor from Table C

- 1, and the annual average HHV, calculated according to §98.33(a)(2)(ii). In this case, the fact that the fuels are blended prior to combustion is of no consequence. (ii) If the fuel is received as a blend ( i.e., already mixed) or if the c omponents are mixed on site without precisely

measuring the mass or volume of each one individually , a reasonable estimate of the relative proportions of the components of the blend must be made, using the best available information ( e.g., the approximate annual average mass or volume percentage of each fuel, based on the typical or expected range of values). Determine the appropriate CO 2 emission factor and HHV for use in Equation C

- 2a of this subpart, as follows: (A) Consider the blend to be the “fuel ty p e,” measure its HHV at the frequency prescribed in paragraph (a)(2)(v) of this section, and determine the annual average HHV value for the blend according to §98.33(a)(2)(ii). (B) Calculate a heat

- weighted CO 2 emission factor, (EF) B , for the blend, using Equation C
- 16 of this section. The heat

- weighting in Equation C

- 16 is provided by the default HHVs (from Table C

- 1) and the estimated mass or volume percentages of the components of the blend. (C) Substitute into Equation C

- 2a of this subpart, the annual average HHV for the blend (from paragraph (a)(3)(ii)(A) of this section) and the calculated value of (EF) B , along with thePage 40 of 78

total mass or volume of the blend combusted during the reporting ye ar, to determine the annual CO 2 mass emissions from combustion of the blend.

where: (EF) B = Heat
- weighted CO 2 emission factor for the blend (kg CO 2 /mmBtu) (HHV) i = Default high heat value for fuel “i” in the blend, from Table C

- 1 (mmBtu per mass or volume) (%Fuel) i = Estimated mass or volume percentage of fuel “i ” (mass % or volume %, as applicable, expressed as a decimal fraction; e.g., 25% = 0.25) (EF) i = Default CO 2 emission factor for fuel “i” from Table C

- 1 (mmBtu per mass or volume) (HHV) B = Annual average high heat value for the blend, calculated according to §98.33(a)(2)(ii) (mmBtu per mass or volume) (iii) Note that for the case described in paragraph (a)(3)(ii) of this section, if measured HHV values for the individual fuels in the blend or for the blend itself are not routinely received at the minimum frequency prescribed in paragraph (a)(2) of this section (or at a greater frequency), and if the unit qualifies to use Tier 1, calculate (HHV) B *, the heat

- weighted default HHV for the blend, using Equation C

- 17 of this section. Then, use Equation C

- 16 of thi s section, replacing the term (HHV) B with (HHV) B * in the denominator, to determine the heat

- weighted CO 2 emission factor for the blend. Finall y, substitute into Equation C

- 1 of this subpart, the calculated values of (HHV) B * and (EF) B , along with the total mass or volume of the blend combusted during the reporting ye ar, to determine the annual CO 2 mass emissions from combustion of the blend.Page 41 of 78

where: (HHV) B * = Heat

- weighted default high heat value for the blend (mmBtu per mass or Volume) (HHV) i = Default high heat value for fuel “i” in the blend, from Table C

- 1 (mmBtu per mass or volume) (%Fuel) i = Estimated mass or volume percentage of fuel “i” in the blend (mass % or volume %, as applicable, expressed as a decimal fraction) (iv) If the fuel blend described in paragraph (a)(3)(ii) of this section consists of a mixture of fuel(s) listed in Table C

- 1 of this subpart and one or more fuels not listed in Table C

- 1, calculate CO 2 and other GHG emissions only for the Table C

- 1 fuel(s), using the best available estim ate of the mass or volume percentage(s) of the Table C

- 1 fuel(s) in the blend. In this case, Tier 1 shall be used, with the following modifications to Equations C

- 17 and C

- 1, to account for the fact that not all of the fuels in the blend are listed in Tabl e C
- 1: (A) In Equation C

- 17, apply the term (Fuel) i only

to the Table C

- 1 fuels. For each Table C
- 1 fuel, (Fuel) i will be the estimated mass or volume percentage of the fuel in the blend, divided by the sum of the mass or volume percentages of the Table C

- 1 fuels. For example, suppose that a blend consists of two Table C

- 1 fuels (“A” and “B”) and one fuel ty pe (“C”) not listed in the Table, and that the volume percentages of fuels A, B, and C in the blend, expressed as decimal fractions, are, respectively, 0.50, 0.30, and 0.20. The term (Fuel) i in Equation C

- 17 for fuel A will be 0.50/(0.50 + 0.30) = 0.625, and for fuel B, (Fuel) i will be 0.30/(0.50 + 0.30) = 0.375. (B) In Equation C

- 1, the term “Fuel” will be equal to the total mass or volume of the blended fuel combusted during the ye ar multiplied by the sum of the mass or volume percentagesPage 42 of 78

of the Table C

- 1 fuels in the blend. For the example in paragraph (a)(3)(iv)(A) of this section, “Fuel” = (Annual volume of the blend combusted)(0.80). (4) If, for a particular typ e of fuel, HHV sampling and anal ys is is performed more often than the minimum frequency specified in paragraph (a)(2) of this section, the results of all valid fuel anal ys es shall be used in the GHG emission calculations. (5) If, for a particul ar typ e of fuel, valid HHV values are obtained at less than the minimum frequency

specifed in paragraph (a)(2) of this section, appropriate substitute data values shall be used in the emissions calculations, in accordance with missing data procedures of §9 8.35. (6) You must use one of the following appropriate fuel sampling and anal ys is methods. The HHV may

be calculated using chromatographic anal ys is together with standard heating values of the fuel constituents, provided that the gas chromatograph is operated, maintained, and calibrated according to the manufacturer's instructions. Alternativel y, you may use a method published by

a consensus - based standards organization if such a method exists, or you may use industry standard practice to determine the high heat values. Consensus

- based standards organizations include, but are not limited to, the following: ASTM International (100 Barr Harbor Drive, P.O. Box CB700, West Conshohocken, Pennsylvania 19428

- B2959, (800) 262

- 1373, http://www.astm.org), the American National Standards Institute (ANSI , 1819 L Street, NW., 6th floor, Washington, DC 20036, (202) 293

- 8020, http://www.ansi.org), the American Gas Association (AGA, 400 North Capitol Street, NW., 4th Floor, Washington, DC 20001, (202) 824
- 7000, http://www.aga.org), the American Society of Mechanical Engineers (ASME, Three Park Avenue, New York, NY 10016

- 5990, (800) 843

- 2763, http://www.asme.org), the American Petroleum Institute (API, 1220 LStreet, NW., Washington, DC 20005

- 4070, (202) 682

- 8000,Page 43 of 78

http://www.api.org), and the North American Energy Standards Board (NAESB, 801 Travis Street, Suite 1675, Houston, TX 77002, (713) 356

- 0060, http://www.api.org). The method(s) used shall be documented in the Monitoring Plan required under §98.3(g)(5). (b) For the Tier 3 Calculation Methodology : (1) You must calibrate each oil and gas flow meter according to §98.3(i) and the provisions of this paragraph (b)(1). (i) Perform calibrations using any of the test methods and procedures in this paragraph (b)(1)(i) . The method(s) used shall be documented in the Monitoring Plan required under §98.3(g)(5). (A) You may

use the calibration procedures specified by the flow meter manufacturer. (B) You may

use an appropriate flow meter calibration method published by a con sensus based standards organization, if such a method exists. Consensus

- based standards organizations include, but are not limited to, the following: ASTM International (100 Barr Harbor Drive, P.O. Box CB700, West Conshohocken, Penns yl vania 19428

- B2959, (8 00) 262

- 1373, http://www.astm.org), the American National Standards Institute (ANSI, 1819 LStreet, NW., 6th floor, Washington, DC 20036, (202) 293

- 8020, http://www.ansi.org), the American Gas Association (AGA, 400 North Capitol Street, NW., 4th Floor, Was hington, DC 20001, (202) 824
- 7000, http://www.aga.org), the American Society of Mechanical Engineers (ASME, Three Park Avenue, New York, NY 10016

- 5990, (800) 843

- 2763, http://www.asme.org), the American Petroleum Institute (API, 1220 LStreet, NW., Washington, DC 20005
- 4070, (202) 682

- 8000, http://www.api.org), and the North American Energy Standards Board (NAESB, 801 Travis Street, Suite 1675, Houston, TX 77002, (713) 356

- 0060, http://www.api.org). (C) You may

use an industry

- accepted practice.Page 44 of 7 8

(ii) In addition to the initial calibration required b y §98.3(i), recalibrate each fuel flow meter (except as otherwise provided in paragraph (b)(1)(iii) of this section) according to one of the following. You may

recalibrate annuall y, at the minimum frequency spe cified b y the manufacturer, or at the interval specified by industry standard practice. (iii) Fuel billing meters are exempted from the initial and ongoing calibration requirements of this paragraph and from the Monitoring Plan and recordkeeping requirements of §§98.3(g)(5)(i)(C), (g)(6), and (g)(7), provided that the fuel supplier and the unit combusting the fuel do not have any common owners and are not owned by subsidiaries or affiliates of the same company. Meters used exclusively to measure the flow rates of fuels that are only used for unit startup are also exempted from the initial and ongoing calibration requirements of this paragraph. (iv) For the initial calibration of an orifice, nozzle, or venturi meter; in

- situ calibration of the transmitters is sufficient. A primary element inspection (PEI) shall be performed at least once every three years. (v) For the continuously

- operating units and processes described in §98.3(i)(6), the required flow meter recalibrations and, if necessary, the PEIs may be p ostponed until the next scheduled maintenance outage. (vi) If a mixture of liquid or gaseous fuels is transported by a common pipe, you may either separatel y meter each of the fuels prior to mixing, using flow meters calibrated according to §98.3(i), or co nsider the fuel mixture to be the “fuel ty pe” and meter the mixed fuel, using a flow meter calibrated according to §98.3(i). (2) Oil tank drop measurements (if used to determine liquid fuel use volume) shall be performed according to any an appropriate method published by a consensus - based standards organization (e.g., the American Petroleum Institute).Page 45 of 78

(3) The carbon content and, if applicable, molecular weight of the fuels shall be determined according to the procedures in this paragraph (b)(3). (i) All f uel samples shall be taken at a location in the fuel handling s ys tem that provides a sample representative of the fuel combusted. The fuel sampling and anal ys is may be performed by either the owner or operator or b y the supplier of the fuel. (ii) For each ty

pe of fuel, the minimum required frequency for collecting and anal yz ing samples for carbon content and (if applicable) molecular weight is specified in this paragraph. When the sampling frequency is based on a specified time period ( e.g., week, month, qu arter, or half

- ye ar), fuel sampling and anal ys is is required for only those time periods in which the fuel is combusted. (A) For natural gas, semiannual sampling and analy sis is required ( i.e., twice in a calendar year, with consecutive samples taken at le ast four months apart). (B) For coal and fuel oil and for any other solid or liquid fuel that is delivered in lots, anal ys is of at least one representative sample from each fuel lot is required. For fuel oil, as an alternative to sampling each fuel lot, a sample may be taken upon each addition of oil to the storage tank. Flow proportional sampling, continuous drip sampling, or daily manual oil sampling may

also be used, in lieu of sampling each fuel lot. If the daily manual oil sampling option is selected, sampling from a particular tank is required onl y on days when oil from the tank is combusted by

the unit (or units) served b y the tank. If you elect to sample from the storage tank upon each addition of oil to the tank, you must take at least one sample from each tank that is currentl y in service and whenever oil is added to the tank, for as long as the tank remains in service. You need not take any samples from a storage tank while it is out of service. Rather, take a sample when the tank is brought into s ervice and whenever oil is added to thePage 46 of 78

tank, for as long as the tank remains in service. If multiple additions of oil are made to a particular in service tank on a given day ( e.g., from multiple deliveries), one sample taken after the final addition of oi l is sufficient. For the purposes of this section, a fuel lot is defined as a shipment or delivery

of a single type of fuel ( e.g., ship load, barge load, group of trucks, group of railroad cars, oil delivery via pipeline from a tank farm, etc. ). However, i f multiple deliveries of a particular ty

pe of fuel are received from the same supply source in a given calendar month, the deliveries for that month may be considered, collectively , to comprise a fuel lot, requiring onl y one representative sample, subject to the following conditions: ( 1 ) For coal, the “ty

pe” of fuel means the rank of the coal ( i.e., anthracite, bituminous, sub

- bituminous, or lignite). For fuel oil, the “type” of fuel means the grade number or classification of the oil ( e.g., No. 1 oil, No. 2 oil, kerosene, Jet A fuel, etc. ). ( 2 ) The owner or operator shall document in the monitoring plan under §98.3(g)(5) how the monthly

sampling of each type of fuel is performed. (C) For liquid fuels other than fuel oil and for biogas, sampling and anal ys is is required at least once per calendar quarter. To the extent practicable, consecutive quarterly samples shall be taken at least 30 day s apart. (D) For other solid fuels (except MSW), weekly sampling is required to obtain composite samples, which are then anal yz ed monthl y. (E) For gaseous fuels other than natural gas and biogas ( e.g., process gas), daily sampling and anal ys is to determine the carbon content and molecular weight of the fuel is required if continuous, on

- line equipment, such as a gas chromat ograph, is in place to make these measurements. Otherwise, weekl y sampling and analy sis shall be performed.Page 47 of 78

(F) For mixtures (blends) of solid fuels, weekl y sampling is required to obtain composite samples, which are anal yzed monthly . For blends of liquid fuels, and for gas mixtures consisting only of natural gas and biogas, sampling and anal ysis is required at least once per calendar quarter. For gas mixtures that contain gases other than natural gas (including biogas), daily sampling and anal ys is to deter mine the carbon content and molecular weight of the fuel is required if continuous, on

- line equipment is in place to make these measurements. Otherwise, weekl y sampling and analy sis shall be performed. (iii) If, for a particular type of fuel, sampling and anal ys is for carbon content and molecular weight is performed more often than the minimum frequency specified in paragraph (b)(3) of this section, the results of all valid fuel analy ses shall be used in the GHG emission calculations. (iv) If, for a particular type of fuel, sampling and anal ys is for carbon content and molecular weight is performed at less than the minimum frequency specified in paragraph (b)(3) of this section, appropriate substitute data values shall be used in the emissions calculations, in accordance with the missing data procedures of §98.35. (v) To calculate the CO 2 mass emissions from combustion of a blend of fuels in the same state of matter (solid, liquid, or gas), you may either: (A) Appl y Equation C

- 3, C
- 4 or C
- 5 of this subpart (as applicable) to each component of the blend, if the mass or volume, the carbon content, and (if applicable), the molecular weight of each component are accuratel y measured prior to blending; or (B) Consider the blend to be the “fuel ty pe.” Then, at the fre quency specified in paragraph (b)(3)(ii)(F) of this section, measure the carbon content and, if applicable, the molecular weight of the blend and calculate the annual average value of each parameter in thePage 48 of 78

manner described in §98.33(a)(2)(ii). Also measure the mass or volume of the blended fuel combusted during the reporting ye ar. Substitute these measured values into Equation C

- 3, C
- 4, or C
- 5 of this subpart (as applicable). (4) You must use one of the following appropriate fuel sampling and anal ys is metho ds. The results of chromatographic analy sis of the fuel may be used, provided that the gas chromatograph is operated, maintained, and calibrated according to the manufacturer's instructions. Alternatively, you may use a method published by a consensus - base d standards organization if such a method exists, or you may use industry

standard practice to determine the carbon content and molecular weight (for gaseous fuel) of the fuel. Consensus

- based standards organizations include, but are not limited to, the fo llowing: ASTM International (100 Barr Harbor Drive, P.O. Box CB700, West Conshohocken, Pennsylvania 19428

- B2959, (800) 262

- 1373, http://www.astm.org), the American National Standards Institute (ANSI , 1819 L Street, NW., 6th floor, Washington, DC 20036, (20 2) 293

- 8020, http://www.ansi.org), the American Gas Association (AGA, 400 North Capitol Street, NW., 4th Floor, Washington, DC 20001, (202) 824
- 7000, http://www.aga.org), the American Society of Mechanical Engineers (ASME, Three Park Avenue, New York, NY 1 0016
- 5990, (800) 843

- 2763, http://www.asme.org), the American Petroleum Institute (API, 1220 LStreet, NW., Washington, DC 20005

- 4070, (202) 682

- 8000, http://www.api.org), and the North American Energy Standards Board (NAESB, 801 Travis Street, Suite 1675, Houston, TX 77002, (713) 356

- 0060, http://www.api.org). The method(s) used shall be documented in the Monitoring Plan required under §98.3(g)(5). (c) For the Tier 4 Calculation Methodology , the CO 2 , flow rate, and (if applicable) moisture monitors must be certified prior to the applicable deadline specified in §98.33(b)(5).Page 49 of 78

(1) For initial certification, you may use any one of the following three procedures in this paragraph. (i) §§75.20(c)(2), (c)(4), and (c)(5) through (c)(7) of this chapter and appendix A to part 75 of this chapter. (ii) The calibration drift test and relative accuracy test audit (RATA) procedures of Performance Specification 3 in appendix B to part 60 of this chapter (for the CO 2 concentration monitor) and Performance Specification 6 in appendix B to part 60 of this chapter (for the continuous emission rate monitoring sy stem (CERMS)). (iii) The provisions of an applicable State continuous monitoring program. (2) If an O 2 concentration monitor is used to determine CO 2 concentrations, the applicable provisions of part 75 of this chapter, part 60 of this chapter, or an applicable State continuous monitoring program shall be followed for initial certification and on

- going quality assurance, and all required RATAs of the m onitor shall be done on a percent CO 2 basis. (3) For ongoing quality

assurance, follow the applicable procedures in either appendix B to part 75 of this chapter, appendix F to part 60 of this chapter, or an applicable State continuous monitoring program. I f appendix F to part 60 of this chapter is selected for on

- going quality assurance, perform dail y calibration drift assessments for both the CO 2 monitor (or surrogate O 2 monitor) and the flow rate monitor, conduct cylinder gas audits of the CO 2 concentrati on monitor in three of the four quarters of each ye ar (except for non

- operating quarters), and perform annual RATAs of the CO 2 concentration monitor and the CERMS. (4) For the purposes of this part, the stack gas volumetric flow rate monitor RATAs required by

appendix B to part 75 of this chapter and the annual RATAs of the CERMS required by appendix F to part 60 of this chapter need onl y be done at one operating level, representingPage 50 of 78

normal load or normal process operating conditions, both for initial certif ication and for ongoing quality assurance. (5) If, for any source operating hour, quality assured data are not obtained with a CO 2 monitor (or surrogate O 2 monitor), flow rate monitor, or (if applicable) moisture monitor, use appropriate substitute data values in accordance with the missing data provisions of §98.35. (6) For certain applications where combined process emissions and combustion emissions are measured, the CO 2 concentrations in the flue gas may be considerabl y higher than for combustion emissi ons alone. In such cases, the span of the CO 2 monitor may , if necessary , be set higher than the specified levels in the applicable regulations. If the CO 2 span value is set higher than 20 percent CO 2 , the cylinder gas audits of the CO 2 monitor under appendix F to part 60 of this chapter may

be performed at 40 to 60 percent and 80 to 100 percent of span, in lieu of the prescribed calibration levels of 5 to 8 percent CO 2 and 10 to 14 percent CO 2 . (7) Hourl y average data from the CEMS shall be validated in a manner consistent with one of the following: §§60.13(h)(2)(i) through (h)(2)(vi) of this chapter; §75.10(d)(1) of this chapter; or the hourl y data validation requirements of an applicable State CEM regulation. (d) Except as otherwise provided in §98.33 (b) (1)(vi) and (b)(1)(vii), when municipal solid waste (MSW) is either the primary fuel combusted in a unit or the only fuel with a biogenic component combusted in the unit, determine the biogenic portion of the CO 2 emissions using ASTM D6866
- 12 Standard T est Methods for Determining the Biobased Content of Solid, Liquid, and Gaseous Samples Using Radiocarbon Analy sis (incorporated by reference, see §98.7) and ASTM D7459

- 08 Standard Practice for Collection of Integrated Samples for the Speciation of Biomass (Biogenic) and Fossil

- Derived Carbon Dioxide Emitted from Stationary Emissions Sources (incorporated b y reference, see §98.7). Perform the ASTM D7459

- 08Page 51 of 78

sampling and the ASTM D6866

- 12 anal ys is at least once in every calendar quarter in which MSW is comb usted in the unit. Collect each gas sample during normal unit operating conditions for at least 24 total (not necessarily consecutive) hours, or longer if the facility deems it necessary to obtain a representative sample. Notwithstanding this requirement, if the ty pes of fuels combusted and their relative proportions are consistent throughout the year, the minimum required sampling time may be reduced to 8 hours if at least two 8

- hour samples and one 24

- hour sample are collected under normal operating condi tions, and arithmetic average of the biogenic fraction of the flue gas from the 8

- hour samples (expressed as a decimal) is within ±5 percent of the biogenic fraction from the 24

- hour test. There must be no overlapping of the 8

- hour and 24

- hour test periods . Document the results of the demonstration in the unit's monitoring plan. If the ty pes of fuels and their relative proportions are not consistent throughout the year, an optional sampling approach that facilities may wish to consider to obtain a more representative sample is to collect an integrated sample by extracting a small amount of flue gas ( e.g., 1 to 5 cc) in each unit operating hour during the quarter. Separate the total annual CO 2 emissions into the biogenic and non

- biogenic fractions using the average proportion of biogenic emissions of all samples anal yz ed during the reporting ye ar. Express the results as a decimal fraction ( e.g., 0.30, if 30 percent of the CO 2 is biogenic). When MSW is the primary fuel for multiple units at the facility , and th e units are fed from a common fuel source, testing at onl y one of the units is sufficient. (e) For other units that combust combinations of biomass fuel(s) (or heterogeneous fuels that have a biomass component, e.g., tires) and fossil (or other non

- biogeni c) fuel(s), in any proportions, ASTM D6866

- 12 (incorporated b y reference, see §98.7) and ASTM D7459

- 08 (incorporated b y reference, see §98.7) may be used to determine the biogenic portion of the CO 2 emissions in every

calendar quarter in which biomass and non

- biogenic fuels are co

- fired in thePage 52 of 78

unit. Follow the procedures in paragraph (d) of this section. If the primary fuel for multiple units at the facility consists of tires, and the units are fed from a common fuel source, testing at onl y one of the un its is sufficient. (f) The records required under §98.3(g)(2)(i) shall include an explanation of how the following parameters are determined from company records (or, if applicable, from the best available information): (1) Fuel consumption, when the Tier 1 and Tier 2 Calculation Methodologies are used, including cases where §98.36(c)(4) applies. (2) Fuel consumption, when solid fuel is combusted and the Tier 3 Calculation Methodology

is used. (3) Fossil fuel consumption when §98.33(e)(2) applies to a unit that uses CEMS to quantify CO 2 emissions and that combusts both fossil and biomass fuels. (4) Sorbent usage, when §98.33(d) applies. (5) Quantity of steam generated b y a unit when §98.33(a)(2)(iii) applies. (6) Biogenic fuel consumption and high heating va lue, as applicable, under §§98.33(e)(5) and (e)(6). (7) Fuel usage for CH 4 and N 2 O emissions calculations under §98.33(c)(4)(ii). (8) Mass of biomass combusted, for premixed fuels that contain biomass and fossil fuels under §98.33(e)(1)(iii). [74 FR 56374, Oct. 30, 2009, as amended at 75 FR 79146, Dec. 17, 2010]Page 53 of 78

**§98.35 Procedures for estimating missing data.**  Whenever a quality

- assured value of a required parameter is unavailable (e.g., if a CEMS malfunctions during unit operation or if a required fuel sampl e is not taken), a substitute data value for the missing parameter shall be used in the calculations. (a) For all units subject to the requirements of the Acid Rain Program, and all other stationary combustion units subject to the requirements of this part that monitor and report emissions and heat input data year - round in accordance with part 75 of this chapter, the missing data substitution procedures in part 75 of this chapter shall be followed for CO 2 concentration, stack gas flow rate, fuel flow rate, high heating value, and fuel carbon content. (b) For units that use the Tier 1, Tier 2, Tier 3, and Tier 4 Calculation Methodologies, perform missing data substitution as follows for each parameter: (1) For each missing value of the high heating value, carbon content, or molecular weight of the fuel, substitute the arithmetic average of the quality

- assured values of that parameter immediately

preceding and immediately following the missing data incident. I f the “after” value has not been obtained b y the time that the GHG emissions report is due, you may use the “before” value for missing data substitution or the best available estimate of the parameter, based on all available process data (e.g., electrical load, steam production, operating hours). If, for a particular parameter, no quality

- assured data are available prior to the missing data incident, the substitute data value shall be the first quality

- assured value obtained after the missing data period. (2) For missing records of CO 2 concentration, stac k gas flow rate, percent moisture, fuel usage, and sorbent usage, the substitute data value shall be the best available estimate of thePage 54 of 78

parameter, based on all available process data (e.g., electrical load, steam production, operating hours, etc.). You mus t document and retain records of the procedures used for all such estimates. **§ 98. 36**  **Data reporting requirements.** (a) In addition to the facility

- level information required under § 98. 3, the annual GHG emissions report shall contain the unit

- level or process

- level data specified in paragraphs (b) through ( f

) of this section , as applicable , for each stationary fuel combustion source (e.g., individual unit, aggregation of units, common pipe, or common stack) except as otherwise provided in this paragraph. For the 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), and (e)(2)(iv)(A), (e)(2)(iv)(C), (e)(2)(iv)(F), and (e)(2)(ix)(D) through (F) of this section, the owner or operator of a stationary fuel combustion source that does not meet the criteria specified in paragraph (f) of this section may elect either to report the data specified in this sentence in the annual report or to use verification software according to § 98.5(b) in lieu of reporting these data. If you elect to use th is verification software, you must use the verification software according to § 98.5(b) for all of these data that apply to the stationary

fuel combustion source. (b) Units that use the four tiers
. You shall report the following information for stationary combustion units that use the Tier 1, Tier 2, Tier 3, or Tier 4 methodology in § 98. 33(a) to calculate CO 2 emissions, except as otherwise provided in para graphs (c) and (d) of this section: (1) The unit ID number. (2) A code representing the ty pe of unit. (3) Maximum rated heat input capacity of the unit, in mmBtu/hr. (4) Each typ e of fuel combusted in the unit during the report year.Page 55 of 78

(5) The methodology

( i .e., tier) used to calculate the CO 2 emissions for each ty pe of fuel combusted ( i.e., Tier 1, 2, 3, or 4). (6) The methodology

start date, for each fuel ty pe. (7) The methodology

end date, for each fuel type. (8) For a unit that uses Tiers 1, 2, or 3: (i) The annual CO 2 mass emissions (including biogenic CO 2 ), and the annual CH 4 , and N 2 O mass emissions for each type of fuel combusted during the reporting year, expressed in metric tons of each gas and in metric tons of CO 2 e; and (ii) Metric tons of biogenic CO 2 emissions (if applicable). (9) For a unit that uses Tier 4: (i) If the total annual CO 2 mass emissions measured by the CEMS consists entirely of
non - biogenic CO 2 ( i.e., CO 2 from fossil fuel combustion plus, if applicable, CO 2 from sorbent and/or proces s CO 2 ), report the total annual CO 2 mass emissions, expressed in metric tons. You are not required to report the combustion CO 2 emissions by fuel type. (ii) Report the total annual CO 2 mass emissions measured b y the CEMS. If this total includes both biogen ic and non

- biogenic CO 2 , separatel y report the annual non

- biogenic CO 2 mass emissions and the annual CO 2 mass emissions from biomass combustion, each expressed in metric tons. You are not required to report the combustion CO 2 emissions by fuel type. (iii) An estimate of the heat input from each type of fuel listed in Table C

- 2 of this subpart that was combusted in the unit during the report year (iv) The annual CH 4 and N 2 O emissions for each type of fuel listed in Table C

–2 of this subpart that was combuste d in the unit during the report year, expressed in metric tons of each gas and in metric tons of CO 2 e.Page 56 of 78

(10) Annual CO 2 emissions from sorbent (if calculated using Equation C

- 11 of this subpart), expressed in metric tons. (11) If applicable, the plant code (as defined in § 98. 6). (c) Reporting alternatives for units using the four Tiers
. You may use any of the applicable reporting alternatives of this paragraph to simplify the unit

- level reporting required under paragraph (b) of this section: (1) Aggregation of units
. If a facility contains two or more units ( e.g., boilers or combustion turbines), each of which has a maximum rated heat input capacity of 250 mmBtu/hr or less, you may

report the combined GHG emissions for the group of units in lieu of reporting GHG emissions from the individual units, provided that the use of Tier 4 is not required or elected for any of the units and the units use the same tier for any common fuels combusted. If this option is selected, the following information shall be reporte d instead of the information in paragraph (b) of this section: (i) Group ID number, beginning with the prefix “GP”. (ii) [Reserved] (iii) Cumulative maximum rated heat input capacity of the group (mmBtu/hr). The cumulative maximum rated heat input capacity shall be determined as the sum of the maximum rated heat input capacities for all units in the group, excluding units less than 10 (mmBtu/hr). (iv) The highest maximum rated heat input capacity of any unit in the group (mmBtu/hr). (v) Each typ e of fuel combusted in the group of units during the reporting year. (vi) Annual CO 2 mass emissions and annual CH 4 , and N 2 O mass emissions, aggregated for each type of fuel combusted in the group of units during the report year, expressed in metric tons of eac h gas and in metric tons of CO 2 e. If any of the units burn both fossil fuels andPage 57 of 78

biomass, report also the annual CO 2 emissions from combustion of all fossil fuels combined and annual CO 2 emissions from combustion of all biomass fuels combined, expressed in metric tons. (vii) The methodology

( i.e., tier) used to calculate the CO 2 mass emissions for each typ e of fuel combusted in the units ( i.e., Tier 1, Tier 2, or Tier 3). (viii) The methodology

start date, for each fuel type. (ix) The methodology

end date, for each fuel type. (x) The calculated CO 2 mass emissions (if any) from sorbent expressed in metric tons. (xi) I f applicable, the plant code (as defined in § 98. 6). (2) Monitored common stack or duct configurations
. When the flue gases from two or more stationary

fuel combustion units at a facility are combined together in a common stack or duct before exiting to the atmosphere and if CEMS are used to continuously monitor CO 2 mass emissions at the common stack or duct according to the Tier 4 Calculation Methodology , you may report the combined emissions from the units sharing the common stack or duct, in lieu of separately reporting the GHG emissions from the individual units. This monitoring and reporting alternative may

also be used when process off

- gases or a mixture of combustion products and process gases are combined together in a common stack or duct before exiting to the atmosphere. Whenever the common stack or duct monitoring option is applied, the following information shall be reported instead of the information in paragraph (b) of this section: (i) Common stack or duct identification number, beginning with the prefix “CS”. (ii) Number of units sharing the common stack or duct. Report “1” when the flue gas flowing through the common stack or duct in cludes combustion products and/or process off

gases, and all of the effluent comes from a single unit ( e.g., a furnace, kiln, petrochemical production unit, or smelter).Page 58 of 78

(iii) Combined maximum rated heat input capacity of the units sharing the common stack or duct (mmBtu/hr). This data element is required only when all of the units sharing the common stack are stationary

fuel combustion units. (iv) Each type of fuel combusted in the units during the ye ar. (v) The methodology

(tier) used to calculate the CO 2 mass emissions, i.e., Tier 4. (vi) The methodology

start date. (vii) The methodology

end date. (viii) Total annual CO 2 mass emissions measured by the CEMS, expressed in metric tons. If any of the units burn both fossil fuels and biomass, separatel y report the annual non

- biogenic CO 2 mass emissions ( i.e., CO 2 from fossil fuel combustion plus, if applicable, CO 2 from sorbent and/or process CO 2 ) and the annual CO 2 mass emissions from biomass combustion, each expressed in metric tons. (ix) An estimate of the h eat input from each type of fuel listed in Table C

- 2 of this subpart that was combusted in the units sharing the common stack or duct during the report ye ar. (x) For each type of fuel listed in Table C

–2 of this subpart that was combusted during the report ye ar in the units sharing the common stack or duct during the report year, the annual CH 4 and N 2 O mass emissions from the units sharing the common stack or duct, expressed in metric tons of each gas and in metric tons of CO 2 e . (xi) I f applicable, the plant code (as defined in § 98. 6). (3) Common pipe configurations
. When two or more stationary combustion units at a facility combust the same ty

pe of liquid or gaseous fuel and the fuel is fed to the individual units through a comm on supply line or pipe, you may

report the combined emissions from the units served b y the common supply line, in lieu of separately reporting the GHG emissions from thePage 59 of 78

individual units, provided that the total amount of fuel combusted b y the units is accuratel y measured at the common pipe or supply line using a fuel flow meter, or, for natural gas, the amount of fuel combusted may be obtained from gas billing records. For Tier 3 applications, the flow meter shall be calibrated in accordance with § 98. 34(b ). If a portion of the fuel measured (or obtained from gas billing records) at the main supply line is diverted to either: A flare; or another stationary fuel combustion unit (or units), including units that use a CO 2 mass emissions calculation method in p art 75 of this chapter; or a chemical or industrial process (where it is used as a raw material but not combusted), and the remainder of the fuel is distributed to a group of combustion units for which you elect to use the common pipe reporting option, you may use company records to subtract out the diverted portion of the fuel from the fuel measured (or obtained from gas billing records) at the main supply line prior to performing the GHG emissions calculations for the group of units using the common pipe option. If the diverted portion of the fuel is combusted, the GHG emissions from the diverted portion shall be accounted for in accordance with the applicable provisions of this part. When the common pipe option is selected, the applicable tier shall be us ed based on the maximum rated heat input capacity of the largest unit served by the common pipe configuration, except where the applicable tier is based on criteria other than unit size. For example, if the maximum rated heat input capacity of the largest unit is greater than 250 mmBtu/hr, Tier 3 will apply , unless the fuel transported through the common pipe is natural gas or distillate oil, in which case Tier 2 may be used, in accordance with § 98. 33(b)(2)(ii). As a second example, in accordance with § 98
. 33(b)(1)(v), Tier 1 may be used regardless of unit size when natural gas is transported through the common pipe, if the annual fuel consumption is obtained from gas billing records in units ofPage 60 of 78

therms or mmBtu. When the common pipe reporting option is sele cted, the following information shall be reported instead of the information in paragraph (b) of this section: (i) Common pipe identification number, beginning with the prefix “CP”. (ii) Cumulative maximum rated heat input capacity of the units served by

the common pipe (mmBtu/hr). The cumulative maximum rated heat input capacity shall be determined as the sum of the maximum rated heat input capacities for all units served b y the common pipe, excluding units less than 10 (mmBtu/hr). (iii) The highest maximum rated heat input capacity of any unit served b y the common pipe (mmBtu/hr). (iv) The fuels combusted in the units during the reporting ye ar. (v) The methodology

used to calculate the CO 2 mass emissions ( i.e., Tier 1, Tier 2, or Tier 3). (vi) If the any of the units burns both fossil fuels and biomass, the annual CO 2 mass emissions from combustion of all fossil fuels and annual CO 2 emissions from combustion of all biomass fuels from the units served b y the common pipe, expressed in metric tons. (vii) Annual CO 2 mass emissions and annual CH 4 and N 2 O emissions from each fuel ty pe for the units served b y the common pipe, expressed in metric tons of each gas and in metric tons of CO 2 e. (viii) Methodology

start date. (ix) Methodology

end date. (x) I f applicable, the plant code (as defined in § 98. 6). (4) The following alternative reporting option applies to facilities at which a common liquid or gaseous fuel supply is shared between one or more large combustion units, such asPage 61 of 78

boilers or combustion tur bines (including units subject to subpart D of this part and other units subject to part 75 of this chapter) and small combustion sources, including, but not limited to, space heaters, hot water heaters, and lab burners. In this case, you may simplify repo rting b y attributing all of the GHG emissions from combustion of the shared fuel to the large combustion unit(s), provided that: (i) The total quantity

of the fuel combusted during the report ye ar in the units sharing the fuel supply

is measured, either at the “gate” to the facility or at a point inside the facility , using a fuel flow meter, billing meter, or tank drop measurements (as applicable); (ii) On an annual basis, at least 95 percent (b y mass or volume) of the shared fuel is combusted in the large combustion unit(s), and the remainder is combusted in the small combustion sources. Company records may

be used to determine the percentage distribution of the shared fuel to the large and small units; and (iii) The use of this reporting option is document ed in the Monitoring Plan required under § 98. 3(g)(5). Indicate in the Monitoring Plan which units share the common fuel supply and the method used to demonstrate that this alternative reporting option applies. For the small combustion sources, a descripti on of the ty pes of units and the approximate number of units is sufficient. (d) Units subject to part 75 of this chapter
. (1) For stationary combustion units that are subject to subpart D of this part, you shall report the following unit

- level information: (i) Unit or stack identification numbers. Use exact same unit, common stack, common pipe, or multiple stack identification numbers that represent the monitored locations ( e.g., 1, 2, CS001, MS1A, CP001, etc
. ) that are reported under § 75.64 of this chapter.Page 62 of 78

(ii) Annual CO 2 emissions at each monitored location, expressed in both short tons and metric tons. Separate reporting of biogenic CO 2 emissions under § 98. 3(c)(4)(ii) and § 98. 3(c)(4)(iii)(A) is optional only for the 2010 reporting ye ar, as provi ded in § 98. 3(c)(12). (iii) Annual CH 4 and N 2 O emissions at each monitored location, for each fuel ty pe listed in Table C

- 2 that was combusted during the ye ar (except as otherwise provided in § 98. 33(c)(4)(ii)(B)), expressed in metric tons of CO 2 e. (iv) Th e total heat input from each fuel listed in Table C

- 2 that was combusted during the ye ar (except as otherwise provided in § 98. 33(c)(4)(ii)(B)), expressed in mmBtu. (v) Identification of the Part 75 methodology used to determine the CO 2 mass emissions. (vi ) Methodology

start date. (vii) Methodology

end date. (viii) Acid Rain Program indicator. (ix) Annual CO 2 mass emissions from the combustion of biomass, expressed in metric tons of CO 2 e, except where the reporting provisions of § § 98. 3(c)(12)(i) through (c )(12)(iii) are implemented for the 2010 reporting year. (x) I f applicable, the plant code (as defined in § 98. 6). (2) For units that use the alternative CO 2 mass emissions calculation methods provided in § 98. 33(a)(5), you shall report the following unit

- l evel information: (i) Unit, stack, or pipe ID numbers. Use exact same unit, common stack, common pipe, or multiple stack identification numbers that represent the monitored locations ( e.g., 1, 2, CS001, MS1A, CP001, etc
. ) that are reported under §75.64 of this chapter.Page 63 of 78

(ii) For units that use the alternative methods specified in § 98. 33(a)(5)(i) and (ii) to monitor and report heat input data year - round according to appendix D to part 75 of this chapter or §75.19 of this chapter: (A) Each ty

pe of fuel combus ted in the unit during the reporting ye ar. (B) The methodology

used to calculate the CO 2 mass emissions for each fuel ty pe. (C) Methodology

start date. (D) Methodology

end date. (E) A code or flag to indicate whether heat input is calculated according to appendix D to part 75 of this chapter or §75.19 of this chapter. (F) Annual CO 2 emissions at each monitored location, across all fuel types, expressed in metric tons of CO 2 e. (G) Annual heat input from each type of fuel listed in Table C

- 2 of this subpart that was combusted during the reporting ye ar, expressed in mmBtu. (H) Annual CH 4 and N 2 O emissions at each monitored location, from each fuel ty pe listed in Table C

- 2 of this subpart that was combusted during the reporting year (except as otherwise provide d in § 98. 33(c)(4)(ii)(D)), expressed in metric tons CO 2 e. (I) Annual CO 2 mass emissions from the combustion of biomass, expressed in metric tons CO 2 e, except where the reporting provisions of § § 98. 3(c)(12)(i) through (c)(12)(iii) are implemented for the 2010 reporting year. (J) I f applicable, the plant code (as defined in § 98. 6). (iii) For units with continuous monitoring sy stems that use the alternative method for units with continuous monitoring s ys tems in § 98. 33(a)(5)(iii) to monitor heat input year - round according to part 75 of this chapter:Page 64 of 78

(A) Each ty

pe of fuel combusted during the reporting year. (B) Methodology

used to calculate the CO 2 mass emissions. (C) Methodology

start date. (D) Methodology

end date. (E) A code or flag to indicate that the h eat input data is derived from CEMS measurements. (F) The total annual CO 2 emissions at each monitored location, expressed in metric tons of CO 2 e. (G) Annual heat input from each type of fuel listed in Table C

- 2 of this subpart that was combusted during th e reporting ye ar, expressed in mmBtu. (H) Annual CH 4 and N 2 O emissions at each monitored location, from each fuel ty pe listed in Table C

- 2 of this subpart that was combusted during the reporting year (except as otherwise provided in § 98. 33(c)(4)(ii)(B)), expressed in metric tons CO 2 e. (I) Annual CO 2 mass emissions from the combustion of biomass, expressed in metric tons CO 2 e, except where the reporting provisions of § § 98. 3(c)(12)(i) through (c)(12)(iii) are implemented for the 2010 reporting year. (J) I f applicable, the plant code (as defined in § 98. 6). (e) Verification data
. You must keep on file, in a format suitable for inspection and auditing, sufficient data to verify the reported GHG emissions. This data and information must, where indicated in this paragraph (e), be included in the annual GHG emissions report. (1) The applicable verification data specified in this paragraph (e) are not required to be kept on file or reported for units that meet any one of the three following conditions: (i) Are subj ect to the Acid Rain Program.Page 65 of 78

(ii) Use the alternative methods for units with continuous monitoring sy stems provided in § 98. 33(a)(5). (iii) Are not in the Acid Rain Program, but are required to monitor and report CO 2 mass emissions and heat input data year - round, in accordance with part 75 of this chapter. (2) For stationary

combustion sources using the Tier 1, Tier 2, Tier 3, and Tier 4 Calculation Methodologies in § 98. 33(a) to quantify CO 2 emissions, the following additional information shall be kept on file and included in the GHG emissions report, where indicated: (i) For the Tier 1 Calculation Methodology , report : (A) T he total quantity of each type of fuel combusted in the unit or group of aggregated units (as applicable) during the reporting ye ar, in short tons for solid fuels, gallons for liquid fuels and standard cubic feet for gaseous fuels, or, if applicable, therms or mmBtu for natural gas. (B) If applicable, the moisture content used to calculate the wood and wood residuals wet basis HHV for u se in Equations C

- 1 and C

- 8, in percent. (ii) For the Tier 2 Calculation Methodology , report: (A) The total quantity of each type of fuel combusted in the unit or group of aggregated units (as applicable) during each month of the reporting ye ar. Express the quantity of each fuel combusted during the measurement period in short tons for solid fuels, gallons for liquid fuels, and scf for gaseous fuels. (B) The frequency

of the HHV determinations ( e.g., once a month, once per fuel lot). (C) The high heat values used in the CO 2 emissions calculations for each type of fuel combusted during the reporting ye ar, in mmBtu per short ton for solid fuels, mmBtu per gallon for liquid fuels, and mmBtu per scf for gaseous fuels. Report a HHV value for each calendarPage 66 of 78

mo nth in which HHV determination is required. If multiple values are obtained in a given month, report the arithmetic average value for the month. (D) If Equation C

- 2c of this subpart is used to calculate CO 2 mass emissions, report the total quantity

( i.e., pounds) of steam produced from MSW or solid fuel combustion during each month of the reporting ye ar, and the ratio of the maximum rate heat input capacity to the design rated steam output capacity of the unit, in mmBtu per lb of steam. (E) For each HHV us ed in the CO 2 emissions calculations for each typ e of fuel combusted during the reporting ye ar, indicate whether the HHV is a measured value or a substitute data value. (iii) For the Tier 2 Calculation Methodology , keep records of the methods used to deter mine the HHV for each type of fuel combusted and the date on which each fuel sample was taken, except where fuel sampling data are received from the fuel supplier. In that case, keep records of the dates on which the results of the fuel analy ses for HHV are received. (iv) For the Tier 3 Calculation Methodology , report: (A) The quantity

of each ty

pe of fuel combusted in the unit or group of units (as applicable) during each month of the reporting year, in short tons for solid fuels, gallons for liquid fuels, and scf for gaseous fuels. (B) The frequency

of carbon content and, if applicable, molecular weight determinations for each type of fuel for the reporting ye ar ( e.g., daily , weekl y, monthly, semiannually, once per fuel lot). (C) The carbon content and, if applicable, gas molecular weight values used in the emission calculations (including both valid and substitute data values). For each calendar month of the reporting ye ar in which carbon content and, if applicable, molecular weight determinationPage 67 of 78

is required, report a value of each parameter. If multiple values of a parameter are obtained in a given month, report the arithmetic average value for the month. Express carbon content as a decimal fraction for solid fuels, kg C per gallon for liquid fuels, and kg C per kg of fuel for gaseous fuels. Express the gas molecular weights in units of kg per kg

- mole. (D) The total number of valid carbon content determinations and, if applicable, molecular weight determinations made during the reporting year, for each fuel ty pe. (E) The number of substitute data values used for carbon content and, if applicable, molecular weight used in the annual GHG emissions calculations. (F) The annual average HHV, when measured HHV data, rather than a default HHV from Table C

- 1 of this subpart, are used to calculate CH 4 and N 2 O emissions for a Tier 3 unit, in accordance with § 98. 33(c)(1). (G) The value of the molar volume constant (MVC) used in Equation C

- 5 (if applicable). (v) For the Tier 3 Calculation Methodology , keep records of th e following: (A) For liquid and gaseous fuel combustion, the dates and results of the initial calibrations and periodic recalibrations of the required fuel flow meters. (B) For fuel oil combustion, the method from § 98. 34(b) used to make tank drop measurements (if applicable). (C) The methods used to determine the carbon content and (if applicable) the molecular weight of each ty

pe of fuel combusted. (D) The methods used to calibrate the fuel flow meters). (E) The date on which each fuel sample was taken, except where fuel sampling data are received from the fuel supplier. In that case, keep records of the dates on which the results of the fuel anal ys es for carbon content and (if applicable) molecular weight are received.Page 68 of 78

(vi) For the Tier 4 Calculation Methodology , report: (A) The total number of source operating hours in the reporting year. (B) The cumulative CO 2 mass emissions in each quarter of the reporting ye ar, i.e., the sum of the hourly

values calculated from Equation C

- 6 or C
- 7 of this subpart (as applicable), in metric tons. (C) For CO 2 concentration, stack gas flow rate, and (if applicable) stack gas moisture content, the percentage of source operating hours in which a substitute data value of each parameter was used in the emissions calcul ations. (vii) For the Tier 4 Calculation Methodology , keep records of: (A) Whether the CEMS certification and quality assurance procedures of part 75 of this chapter, part 60 of this chapter, or an applicable State continuous monitoring program were used. (B) The dates and results of the initial certification tests of the CEMS. (C) The dates and results of the major quality assurance tests performed on the CEMS during the reporting ye ar, i.e., linearity checks, cylinder gas audits, and relative accuracy tes t audits (RATAs). (viii) If CO 2 emissions that are generated from acid gas scrubbing with sorbent injection are not captured using CEMS, report: (A) The total amount of sorbent used during the report year, in short tons. (B) The molecular weight of the sor bent. (C) The ratio (“R”) in Equation C

- 11 of this subpart. (ix) For units that combust both fossil fuel and biomass, when biogenic CO 2 is determined according to § 98. 33(e)(2), you shall report the following additional information, as applicable:Page 69 of 78

(A) The annual volume of CO 2 emitted from the combustion of all fuels, i.e., Vtotal , in scf. (B) The annual volume of CO 2 emitted from the combustion of fossil fuels, i.e., V ff , in scf. If more than one typ e of fossil fuel was combusted, report the combustion volum e of CO 2 for each fuel separatel y as well as the total. (C) The annual volume of CO 2 emitted from the combustion of biomass, i.e., Vbio , in scf. (D) The carbon

- based F

- factor used in Equation C

- 13 of this subpart, for each ty pe of fossil fuel combusted, in scf CO 2 per mmBtu. (E) The annual average HHV value used in Equation C

- 13 of this subpart, for each type of fossil fuel combusted, in Btu/lb, Btu/gal, or Btu/scf, as appropriate. (F) The total quantity

of each type of fossil fuel combusted during the repor ting ye ar, in lb, gallons, or scf, as appropriate. (G) Annual biogenic CO 2 mass emissions, in metric tons. (x) When ASTM methods D7459

- 08 (incorporated by reference, see § 98. 7) and D6866

- 12 (incorporated b y reference, see § 98. 7) are used to determine the biogenic portion of the annual CO 2 emissions from MSW combustion, as described in § 98. 34(d), report: (A) The results of each quarterl y sample anal ys is, expressed as a decimal fraction ( e.g., if the biogenic fraction of the CO 2 emissions from MSW combu stion is 30 percent, report 0.30). (B) The annual biogenic CO 2 mass emissions from MSW combustion, in metric tons. (xi) When ASTM methods D7459

- 08 (incorporated by reference, see § 98. 7) and D6866

- 12 (incorporated b y reference, see § 98. 7) are used in a ccordance with § 98. 34(e) to determine the biogenic portion of the annual CO 2 emissions from a unit that co

- fires biogenic fuels (or partly

- biogenic fuels, including tires if you are electing to report biogenic CO 2 emissions from tire combustion) and non

- b iogenic fuels, you shall report the results of each quarterl y samplePage 70 of 78

anal ys is, expressed as a decimal fraction ( e.g., if the biogenic fraction of the CO 2 emissions is 30 percent, report 0.30). (3) Within 30 day s of receipt of a written request from the Adm inistrator, you shall submit explanations of the following: (i) An explanation of how company records are used to quantify fuel consumption, if the Tier 1 or Tier 2 Calculation Methodology is used to calculate CO 2 emissions. (ii) An explanation of how comp an y records are used to quantify fuel consumption, if solid fuel is combusted and the Tier 3 Calculation Methodology is used to calculate CO 2 emissions. (iii) An explanation of how sorbent usage is quantified. (iv) An explanation of how company records are used to quantify fossil fuel consumption in units that uses CEMS to quantify CO 2 emissions and combusts both fossil fuel and biomass. (v) An explanation of how company records are used to measure steam production, when it is used to calculate CO 2 mass emissions under § 98. 33(a)(2)(iii) or to quantify solid fuel usage under § 98. 33(c)(3). (4) Within 30 day s of receipt of a written request from the Administrator, you shall submit the verification data and information described in paragraphs (e)(2)(i ii), (e)(2)(v), and (e)(2)(vii) of this section. (f) Each stationary

fuel combustion source (e.g., individual unit, aggregation of units, common pipe, or common stack) subject to reporting under paragraph (b) or (c) of this section must indicate if both of the following two conditions are met : (1) T he stationary

fuel combustion source contains at least one combustion unit connected to a fuel

- fired electric generator owned or operated b y an entity that is subject toPage 71 of 78

regulation of customer billing rates b y th e public utility commission (excluding generators that are connected to combustion units that are subject to subpart D of this part). (2) The stationary

fuel combustion source is located at a facility for which the sum of the nameplate capacities for all e lectric generators specified in paragraph (f)(1) of this section is greater than or equal to 1 megawatt electric output
. **§ 98. 37**  **Records that must be retained.** In addition to the requirements of § 98. 3(g), you must retain : (a) T he applicable records speci fied in § § 98. 34(f) , 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 certain 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), and (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 b y the verification software for the applicable data specified in paragraphs (b)(1) through (b) (3 6 ) of this section. Retention of this file satisfies the recordkeeping requirement for the data in paragraphs (b)(1) through (b) (3 6 ) 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/ye ar) (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 combuste d (scf/year) (Equation C

- 2a).Page 72 of 78

(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 b y municipal solid waste or each solid fuel combustion durin g the reporting ye ar (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 (sho rt 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 ).Page 73 of 78

( 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/ye ar) (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). (2 5 ) Identify

for each fuel if you will use the default high heat value from Table C

- 1, or actual high heat value data (Equation C

- 8 of § 98.33 ). (2 6 ) High heat value of each solid fuel (mmBtu/tons) (Equation C

- 8). (2 7 ) High heat value of each liquid fuel (mmBtu/gallon) (Equation C

- 8). ( 2 8 ) High heat value of each gaseous fuel (mmBtu/scf) (Equation C

- 8). (2 9 ) 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

- 1 of § 98.33 3). (3 1 ) Total quantity

of each liquid fossil fuel combusted in the reporting year, as defined in § 98.6 (gallons) (Equation C

- 13). (3 2 ) Total quantity

of each gaseous fossil fuel combusted in the reportin g ye ar, as defined in § 98.6 (scf) (Equation C

- 13). (3 3 ) High heat value of the each solid fossil fuel (Btu/lb) (Equation C

- 13).Page 74 of 78

(3 4 ) High heat value of the each liquid fossil fuel (Btu/gallons) (Equation C

- 13). (3 5 ) High heat value of the each gaseous fos sil fuel (Btu/scf) (Equation C

- 13). (3 6 ) Fuel

- specific carbon based F

- factor per fuel (scf CO 2 /mmBtu) (Equation C

- 13). (37) Moisture content used to calculate the wood and wood residuals wet basis HHV (percent), if applicable (Equations C

- 1 and C

- 8). **§98.38 Definitions.**  All terms used in this subpart have the same meaning given in the Clean Air Act and subpart A of this part. **Table C -**  **1 to Subpart C of Part 98**

**— Default CO**  **2 Emission Factors and High Heat Values**  **for Various Types of Fuel Default CO**  **2 Emis**  **sion Factors and High Heat Values for Various Types of Fuel**

**Fuel type Default high heat value**  **Default CO 2**  **emission factor**  Coal and coke mmBtu/short ton kg CO 2 /mmBtu Anthracite 25.09 103.69 Bituminous 24.93 93.28 Subbituminous 17.25 97.17 Li gnite 14.21 97.72 Coal Coke 24.80 113.67 Mixed (Commercial sector) 21.39 94.27 Mixed (Industrial coking) 26.28 93.90 Mixed (Industrial sector) 22.35 94.67 Mixed (Electric Power sector) 19.73 95.52

Natural gas mmBtu/scf kg CO 2 /mmBtu (Weighted U.S. Average) 1.026 × 10 − 3 53.06 Petroleum products

—liquid mmBtu/gallon kg CO 2 /mmBtu Distillate Fuel Oil No. 1 0.139 73.25Page 75 of 78

Distillate Fuel Oil No. 2 0.138 73.96 Distillate Fuel Oil No. 4 0.146 75.04 Residual Fuel Oil No. 5 0.140 72.93 Residual Fuel Oil No. 6 0.150 75.10 Used Oil 0.138 74.00 Kerosene 0.135 75.20 Liquefied petroleum gases (LPG) 1 0.092 61.71 Propane 1 0.091 62.87 Propylene 2 0.091 67.77 Ethane 1 0.068 59.60 Ethanol 0.084 68.44 Ethylene 2 0.058 65.96 Isobutane 1 0.099 64.94 Isobutyl ene 1 0.103 68.86 Butane 1 0.103 64.77 Butylene 1 0.105 68.72 Naphtha (<401 deg F) 0.125 68.02 Natural Gasoline 0.110 66.88 Other Oil (>401 deg F) 0.139 76.22 Pentanes Plus 0.110 70.02 Petrochemical Feedstocks 0.125 71.02 Special Naphtha 0.125 72.34 Unfinished Oils 0.139 74.54 Heav y Gas Oils 0.148 74.92 Lubricants 0.144 74.27 Motor Gasoline 0.125 70.22 Aviation Gasoline 0.120 69.25 Kerosene
- Ty

pe Jet Fuel 0.135 72.22 Asphalt and Road Oil 0.158 75.36 Crude Oil 0.138 74.54Page 76 of 78 Petroleum products

— solid mmBtu/short ton kg CO 2 /mmBtu Petroleum Coke 30.00 102.41 Petroleum products

—gaseous mmBtu/scf kg CO 2 /mmBtu Propane Gas 2.516 × 10 − 3 61.46

Other fuels

— solid mmBtu/short ton kg CO 2 /mmBtu Municipal Solid Waste 9.95 3 90.7 Tires 28.00 85.97 Plastics 38.00 75.00

Other fuels

— gaseous mmBtu/scf kg CO 2 /mmBtu Blast Furnace Gas 0.092 × 10 − 3 274.32 Coke Oven Gas 0.599 × 10 − 3 46.85 Fuel Gas 4 1.388 × 10 − 3 59.00

Biomass fuels

— solid mmBtu/short ton kg CO 2 /mmBtu Wood and Wood Residuals (dry basis) 5 17.48 93.80 Agricultural By

products 8.25 118.17 Peat 8.00 111.84 Solid By products 10.39 105.51 Biomass fuels

— gaseous mmBtu/scf kg CO 2 /mmBtu Landfill Gas 0.485 × 10 − 3 52.07 Other Biomass Gases 0.655 × 10 − 3 52.07

Biomass Fuels

—Li quid mmBtu/gallon kg CO 2 /mmBtu Ethanol 0.084 68.44 Biodiesel (100%) 0.128 73.84 Rendered Animal Fat 0.125 71.06 Vegetable Oil 0.120 81.55
1 The HHV for components of LPG determined at 60 °F and saturation pressure with the exception of ethylene.
2 Ethylene HHV determined at 41 °F (5 °C) and saturation pressure.
3 Use of this default HHV is allowed only for: (a) Units that combust MSW, do not generate steam, and are allowed to use Tier 1; (b) units that derive no more than 10 percent of their annualPage 77 of 78

heat input from MSW and/or tires; and (c) small batch incinerators that combust no more than 1,000 tons of MSW per year.
4 Reporters subject to subpart X of this part that are complying with §98.243(d) or subpart Y of this part may

onl y use the default HHV and the default CO 2 emission factor for fuel gas combustion under the conditions prescribed in §98.243(d)(2)(i) and (d)(2)(ii) and §98.252(a)(1) and (a)(2), respectivel y. Otherwise, reporters subject to s ubpart X or subpart Y shall use either Tier 3 (Equation C

- 5) or Tier 4.
5 Use the following formula to calculate a wet basis HHV for use in Equation C

- 1: HHV w = ((100 − M)/100)*HHV d where HHV w = wet basis HHV, M = moisture content (percent) and HHV d = dry b asis HHV from Table C

- 1. **Table C -**  **2 to Subpart C of Part 98**

**— Default CH**  **4 and N**  **2 O Emission Factors for Various**  **Types of Fuel Fuel type**  **Default CH 4**  **emission factor (kg CH**  **4 /mmBtu)**  **Default N 2**  **O emission factor (kg N**  **2 O/mmBtu)**  Coal and Coke (All fuel ty pes in Table C
- 1) 1.1 × 10 − 02 1.6 × 10 − 03 Natural Gas 1.0 × 10 − 03 1.0 × 10 − 04 Petroleum Products (All fuel ty pes in Table C

- 1) 3.0 × 10 − 03 6.0 × 10 − 04 Fuel Gas 3.0 × 10 − 03 6.0 × 10 − 04 Other Fuels

— Solid 3.2 × 10 − 02 4.2 × 10 − 03 Blast Furnace Gas 2.2 × 10 − 05 1.0 × 10 − 04 Coke Oven Gas 4.8 × 10 − 04 1.0 × 10 − 04 Biomass Fuels

— Solid (All fuel ty pes in Table C

- 1, except wood and wood residuals) 3.2 × 10 − 02 4.2 × 10 − 03

Wood and wood residuals 7.2 × 10 − 03 3.6 × 10 − 03 Biomass Fuels

—Gaseous (All fuel ty pes in Table C

- 1) 3.2 × 10 − 03 6.3 × 10 − 04 Biomass Fuels

—Li quid (All fuel ty pes in Table C

- 1) 1.1 × 10 − 03 1.1 × 10 − 04 Note: Those emplo yi ng this table are assumed to fall under the IPCC definitions of the “Energy Industry” or “Manufacturing Industries and Construction”. In all fuels except for coal the values for these two categories are identical. For coal combustion, those who fall within the IPCC “Energy Industry” category

may employ a value of 1g of CH 4/mmBtu.Page 78 of 78