(a)
For each chemical recovery furnace located at a kraft or soda facility, you must determine CO2, biogenic CO2, CH4, and N2 O emissions using the procedures in paragraphs (a)(1) through (a)(3) of this section. CH4 and N2 O emissions must be calculated as the sum of emissions from combustion of fossil fuels and combustion of biomass in spent liquor solids.
(1)
Calculate fossil fuel-based CO2 emissions from direct measurement of fossil fuels consumed and default emissions factors according to the Tier 1 methodology for stationary combustion sources in § 98.33(a)(1). A higher tier from § 98.33(a) may be used to calculate fossil fuel-based CO2 emissions if the respective monitoring and QA/QC requirements described in § 98.34 are met.
(2)
Calculate fossil fuel-based CH4 and N2 O emissions from direct measurement of fossil fuels consumed, default or site-specific HHV, and default emissions factors and convert to metric tons of CO2 equivalent according to the methodology for stationary combustion sources in § 98.33(c).
(3)
Calculate biogenic CO2 emissions and emissions of CH4 and N2 O from biomass using measured quantities of spent liquor solids fired, site-specific HHV, and default or site-specific emissions factors, according to Equation AA-1 of this section:
(b)
For each chemical recovery combustion unit located at a sulfite or stand-alone semichemical facility, you must determine CO2, CH4, and N2 O emissions using the procedures in paragraphs (b)(1) through (b)(4) of this section:
(1)
Calculate fossil CO2 emissions from fossil fuels from direct measurement of fossil fuels consumed and default emissions factors according to the Tier 1 Calculation Methodology for stationary combustion sources in § 98.33(a)(1). A higher tier from § 98.33(a) may be used to calculate fossil fuel-based CO2 emissions if the respective monitoring and QA/QC requirements described in § 98.34 are met.
(2)
Calculate CH4 and N2 O emissions from fossil fuels from direct measurement of fossil fuels consumed, default or site-specific HHV, and default emissions factors and convert to metric tons of CO2 equivalent according to the methodology for stationary combustion sources in § 98.33(c).
(3)
Calculate biogenic CO2 emissions using measured quantities of spent liquor solids fired and the carbon content of the spent liquor solids, according to Equation AA-2 of this section:
(4)
Calculate CH4 and N2 O emissions from biomass using Equation AA-1 of this section and the default CH4 and N2 O emissions factors for kraft facilities in Table AA-1 of this subpart and convert the CH4 or N2 O emissions to metric tons of CO2 equivalent by multiplying each annual CH4 and N2 O emissions total by the appropriate global warming potential (GWP) factor from Table A-1 of subpart A of this part.
(c)
For each pulp mill lime kiln located at a kraft or soda facility, you must determine CO2, CH4, and N2 O emissions using the procedures in paragraphs (c)(1) through (c)(3) of this section:
(1)
Calculate CO2 emissions from fossil fuel from direct measurement of fossil fuels consumed and default HHV and default emissions factors, according to the Tier 1 Calculation Methodology for stationary combustion sources in § 98.33(a)(1). A higher tier from § 98.33(a) may be used to calculate fossil fuel-based CO2 emissions if the respective monitoring and QA/QC requirements described in § 98.34 are met.
(2)
Calculate CH4 and N2 O emissions from fossil fuel from direct measurement of fossil fuels consumed, default or site-specific HHV, and default emissions factors and convert to metric tons of CO2 equivalent according to the methodology for stationary combustion sources in § 98.33(c); use the default HHV listed in Table C-1 of subpart C and the default CH4 and N2 O emissions factors listed in Table AA-2 of this subpart.
(3)
Biogenic CO2 emissions from conversion of CaCO3 to CaO are included in the biogenic CO2 estimates calculated for the chemical recovery furnace in paragraph (a)(3) of this section.
(d)
For makeup chemical use, you must calculate CO2 emissions by using direct or indirect measurement of the quantity of chemicals added and ratios of the molecular weights of CO2 and the makeup chemicals, according to Equation AA-3 of this section:
Code of Federal Regulations
[74 FR 56374, Oct. 30, 2009, as amended at 75 FR 79166, Dec. 17, 2010]