OXIDES OF SULFUR ANNUAL EMISSION REPORTCompany NameChevron Products CompanySite NameSalt Lake RefineryCompany ID - 95Site ID - 10119NOTE: Be aware that this report uses different methods of calculating emissions than are required forthe 2006 Emissions Inventory.Amount Units/Yr119983874 1a-1 10200701No 3084627.74mmscf/yr22006 (using 1998method ofcalculation)3874 1a-1 10200701No 3084457.43mmscf/yr32006 (if methodof calculation isdifferent from1998)3874 1a-1 10200701No 3084mmscf/yrAmount Units/Yr119983875 1a-210200701No30849870.00 gal/yr22006 (using 1998method ofcalculation)3875 1a-210200701No 30840.00gal/yr32006 (if methodof calculation isdifferent from1998)3875 1a-210200701No 30840.00gal/yr2006 CalculationsFuel oilYear DAQ IDPt SourceID SCCThroughput Generating Emissions42006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.Boilers 1 & 2Fuel GasBoilers 1 & 2Fuel GasBoilers 1 & 2Fuel GasDescription of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedThroughput Generating EmissionsThis form is to be used by sources that have emitted 100 tons or more of SOxin any calendar year after 1999, and that arenot subjectto acid rain continuous monitoring reportingrequirements (40CFR Part 75). Row 1 in the following table(s) contains historical inventory data for the listed component. Row 2 is used to calculate the2006 process emissions usingthe same method that was used in the historical data. The inputs required are in green font. To insertthe new data you type over the top of the old data. Row 3 (shaded) is used toshow and calculate any changes in the method of calculation from 1998 to 2006 (i.g. emission factors,% of sulfur, heating value, controls, breakdowns, estimation methods). If thecurrent method of calculating the SOxemissions does not work with the equation providedin row 3, the calculation should be provided in therow 4. Rows 3 and 4 should have the samecalculations as contained in the 2006 Emission Inventory.Year DAQ IDPt SourceID SCCDescription of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedBoilers #1 & 2Boilers #1 & 2Boilers #1 & 2Fuel oilFuel oil #6Page 1KChevron Products Co. - SL RefineryAmount Units/Yr119983876 1b-1 10200701No 3085512.25mmscf/yr22006 (using 1998method ofcalculation)3876 1b-1 10200701No 3085258.30mmscf/yr32006 (if methodof calculation isdifferent from1998)3876 1b-1 10200701No 3085mmscf/yrAmount Units/Yr1199838771b-210200701No30859870.00 gal/yr22006 (using 1998method ofcalculation)38771b-210200701No 30850.00gal/yr32006 (if methodof calculation isdifferent from1998)38771b-210200701No 30850.00gal/yrThroughput Generating EmissionsBoilers #3 & 4Fuel oil #6Raw Material or FuelusedThroughput Generating EmissionsBoilers #3 & 4Fuel oilBoilers 3 & 4Fuel GasYear DAQ IDPt SourceID SCC Description of ProcessNSPS(Yes/No)Boilers 3 & 4Fuel GasBoilers 3 & 4Fuel GasThroughput Generating EmissionsDescription of ProcessNSPS(Yes/No)AssociatedStack ID4Year DAQ IDPt SourceID SCCRaw Material or Fuelused42006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.AssociatedStack IDBoilers #3 & 4Fuel oil42006 CalculationsPage 2KChevron Products Co. - SL RefineryAmount Units/Yr119983878 2a-1 30600106No 3086968.551 mmscf/yr22006 (using 1998method ofcalculation)3878 2a-1 30600106No 3086955.92mmscf/yr32006 (if methodof calculation isdifferent from1998)3878 2a-1 30600106No 3086mmscf/yrAmount Units/Yr119983886 3a 30600106No 309064.364 mmscf/yr22006 (using 1998method ofcalculation)3886 3a 30600106No 3090139.82mmscf/yr32006 (if methodof calculation isdifferent from1998)3886 3a 30600106No 3090mmscf/yrAmount Units/Yr119983887 3b 30600106No 3091172.955 mmscf/yrNSPS(Yes/No)AssociatedStack IDYear DAQ IDPt SourceIDCrude F-1and F2SCC Description of ProcessFuel GasFuel GasYear DAQ IDPt SourceID SCCRaw Material or FuelusedCrude F-1and F2Fuel GasAssociatedStack IDCrude F-1and F2Fuel GasDescription of ProcessNSPS(Yes/No)42006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.Raw Material or FuelusedThroughput Generating EmissionsFCC F-21Fuel GasFCC F-21FCC F-21Fuel GasYear DAQ IDPt SourceID SCC42006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedFCC F-23Fuel GasThroughput Generating EmissionsPage 3KChevron Products Co. - SL Refinery22006 (using 1998method ofcalculation)3887 3b 30600106No 3091123.65mmscf/yr32006 (if methodof calculation isdifferent from1998)3887 3b 30600106No 3091mmscf/yrAmount Units/Yr119983888 3c 30600201No 30928760 hr/yr22006 (using 1998method ofcalculation)3888 3c 30600201No 30927931.00hr/yr32006 (if methodof calculation isdifferent from1998)3888 3c 30600201No 30927931.00cuft/yrAmount Units/Yr119983889 3d 30600904No 3093 4816.18 mbbls/yr22006 (using 1998method ofcalculation)3889 3d 30600904No 30934793.33mbbls/yr32006 (if methodof calculation isdifferent from1998)3889 3d 30600904No 309314380.00mbbls/yrFCC F-23Fuel GasFCC F-23Fuel GasYear DAQ IDPt SourceID SCC42006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedFCC Reg./CO BoilerFuel GasThroughput Generating EmissionsFCC Reg./CO BoilerFuel GasFCC Reg./CO BoilerFuel GasYear DAQ IDPt SourceID SCC42006 Calculations: Stack Test changed drasticallybecause of addition of VGO unit and additive to flue gas.Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedCracker FlaregasThroughput Generating EmissionsCracker FlaregasCracker Flaregas2006 CalculationsPage 4KChevron Products Co. - SL RefineryAmount Units/Yr119983890 4 30600106No 3094159.492 mmscf/yr22006 (using 1998method ofcalculation)3890 4 30600106No 3094180.81mmscf/yr32006 (if methodof calculation isdifferent from1998)3890 4 30600106No 3094mmscf/yrAmount Units/Yr119983891 5a 30600106No 3095218.374 mmscf/yr22006 (using 1998method ofcalculation)3891 5a 30600106No 3095171.14mmscf/yr32006 (if methodof calculation isdifferent from1998)3891 5a 30600106No 3095mmscf/yrYear DAQ IDPt SourceID SCC4Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedHDN F7110 & F-7130Fuel GasThroughput Generating EmissionsHDN F7110 & F-7130Fuel GasHDN F7110 & F-7130Fuel GasYear DAQ IDPt SourceID SCC42006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedReformer F-1Fuel GasThroughput Generating EmissionsReformer F-1Fuel GasReformer F-1Fuel Gas42006 CalculationsThroughput Generating EmissionsPage 5KChevron Products Co. - SL RefineryAmount Units/Yr119983892 5b 30600106No 3096212.958 mmscf/yr22006 (using 1998method ofcalculation)3892 5b 30600106No 3096175.54mmscf/yr32006 (if methodof calculation isdifferent from1998)3892 5b 30600106No 3096mmscf/yrAmount Units/Yr119983893 5c 30600106No 3097106.885 mmscf/yr22006 (using 1998method ofcalculation)3893 5c 30600106No 309786.22mmscf/yr32006 (if methodof calculation isdifferent from1998)3893 5c 30600106No 3097mmscf/yrAmount Units/Yr119983894 6a-1 30600106No 3098522.746 mmscf/yrYear DAQ IDPt SourceID SCC Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedReformer F-2Fuel GasReformer F-2Fuel GasReformer F-2Fuel GasYear DAQ IDPt SourceID SCC42006 CalculationsDescription of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedReformer F-3Fuel GasThroughput Generating EmissionsReformer F-3Fuel GasReformer F-3Fuel GasYear DAQ IDPt SourceID SCC42006 CalculationsDescription of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedAlkylation F-3617 (fuel gas) Fuel GasThroughput Generating EmissionsPage 6KChevron Products Co. - SL Refinery22006 (using 1998method ofcalculation)3894 6a-1 30600106No 3098477.68mmscf/yr32006 (if methodof calculation isdifferent from1998)3894 6a-1 30600106No 3098mmscf/yrAmount Units/Yr119983895 6a-2 30600106No 309874.55 mgal/yr22006 (using 1998method ofcalculation)3895 6a-2 30600106No 309876.91mgal/yr32006 (if methodof calculation isdifferent from1998)3895 6a-2 30600106No 3098mgal/yrAmount Units/Yr119983896 6b 30600904No 3099 4816.175 mbbls/yr22006 (using 1998method ofcalculation)3896 6b 30600904No 30994793.33mbbls/yr32006 (if methodof calculation isdifferent from1998)3896 6b 30600904No 309914380.00mbbls/yrAlkylation F-3617 (fuel gas) Fuel GasAlkylation F-3617 (fuel gas) Fuel GasYear DAQ IDPt SourceID SCC42006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedAlkylation F-3617 (polymer fueled)PolymerThruput Generating EmissionsAlkylation F-3617 (polymer fueled)PolymerAlkylation F-3617 (polymer fueled)PolymerYear DAQ IDPt SourceID SCC42006 Calculations: The percentage of sulfur changed in the fuel. This is not a change in method.From 2006 AEI Spreadsheet calculations - Sox = %S*157*#of Polymer/2000/7.786/1000=0.266 tonDescription of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedAlky FlareGasThruput Generating EmissionsAlky FlareGasAlky FlareGas2006 CalculationsPage 7KChevron Products Co. - SL RefineryAmount Units/Yr119983897 7a 30600106No 3100245.108 mmscf/yr22006 (using 1998method ofcalculation)3897 7a 30600106No 3100395.14mmscf/yr32006 (if methodof calculation isdifferent from1998)3897 7a 30600106No 3100mmscf/yrAmount Units/Yr119983898 7b 30600904No 3101 4816.175 mbbls/yr2method ofcalculation)3898 7b 30600904No 31014793.33mbbls/yr32006 (if methodof calculation isdifferent from1998)3898 7b 30600904No 310114380.00mbbls/yrAmount Units/YrYear DAQ IDPt SourceID SCC4Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedCoker F-7001Fuel GasThruput Generating EmissionsCoker F-7001Fuel GasCoker F-7001Fuel GasYear DAQ IDPt SourceID SCC42006 Calculations: The percentage of sulfur changed in the fuel. This is not a change in method.Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedCoker FlareGasThruput Generating EmissionsCoker FlareGasCoker FlareGasYear DAQ IDPt SourceID SCC42006 CalculationsDescription of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedThruput Generating EmissionsPage 8KChevron Products Co. - SL Refinery119983899 8a 30600106No 310240.969 mmscf/yr22006 (using 1998method ofcalculation)3899 8a 30600106No 310257.08mmscf/yr32006 (if methodof calculation isdifferent from1998)3899 8a 30600106No 310257.08mmscf/yrAmount Units/Yr119984333 8b 30600106No 310386.052 mmscf/yr22006 (using 1998method ofcalculation)4333 8b 30600106No 310394.16mmscf/yr32006 (if methodof calculation isdifferent from1998)4333 8b 30600106No 310394.16mmscf/yrAmount Units/Yr119984334 9 30609904No 310411.916 mmscf/yr22006 (using 1998method ofcalculation)4334 9 30609904No 310413.07mmscf/yrHDS F-10Fuel GasHDS F-10Fuel GasHDS F-10Fuel GasYear DAQ IDPt SourceID SCC42006 Calculations: The percentage of sulfur changed in the fuel. This is not a change in method.Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedHDS F-11Fuel GasThruput Generating EmissionsHDS F-11Fuel GasHDS F-11Fuel GasYear DAQ IDPt SourceID SCC42006 Calculations: The percentage of sulfur changed in the fuel. This is not a change in method.Description of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedSulfur PlantFuel GasThruput Generating EmissionsSulfur PlantFuel GasPage 9KChevron Products Co. - SL Refinery32006 (if methodof calculation isdifferent from1998)4334 9 30609904No 3104mmscf/yrAmount Units/Yr119985479 10 20200202No 090.621 mmscf/yr22006 (using 1998method ofcalculation)5479 10 20200202No 082.52mmscf/yr32006 (if methodof calculation isdifferent from1998)5479 10 20200202No 082.52mmscf/yrEQUIPMENT NOT RUN IN 1998 THAT EMITS SOx2006 SOxHow sulfur content was calculated Tons/year171147 320330225529.7351489701766620.087401770290.0051770300.00717703210.6511770332.282TOTAL22.7674Tier 2 Diesel Eng. 100% Conversion of Fuel SulfurSulfur PlantFuel GasYear DAQ IDPt SourceID SCC42006 CalculationsFrom 2006 AEI Spreadsheet calculations - Sox = CEMdata (563,434 lb/yr)/2000 = 281.717 tonDescription of ProcessNSPS(Yes/No)AssociatedStack IDRaw Material or FuelusedReform. Comp. DriversNatural GasThruput Generating EmissionsReform. Comp. DriversNatural GasReform. Comp. DriversNatural GasDAQ IDPointSource IDDescription of ProcessTemporary boiler42006 CalculationsBoiler #5Emission FactorsFCC Emergency Air Compressors Emission FactorsDiesel GeneratorsEmission FactorsBoiler #5Emission FactorsTier 1 Diesel Eng100% Conversion of Fuel SulfurVGO Furnace F66100Agreed per 1990 PM10 SIPVGO Furnace F66200Agreed per 1990 PM10 SIPPage 10KChevron Products Co. - SL RefineryPage 11KChevron Products Co. - SL RefineryOXIDES OF SULFUR ANNUAL EMISSION REPORTSecondary Control111.6 mmbtu/hr 1253btu/cf0.0007CEM111.6 mmbtu/hr 1393btu/cf0.0003 CEM111.6 mmbtu/hrbtu/cfCEMSecondary Control111.6 mmbtu/hr 6000000 btu/bbl 0.8028Explain111.6 mmbtu/hr 6000000 btu/bbl1.0000 Explain111.6 mmbtu/hr 6000000 btu/bbl0.0000 ExplainHow Sulfur Content iscalculated%AshControlCode (SeeList)HeatingValue Units%SulfurDesignRate UnitsPrimary ControlHeatingValue Units%SulfurHow Sulfur Content iscalculatedDesignRate UnitsPrimary ControlIf Throughput is a Fuel%AshName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)If Throughput is a FuelControlCode (SeeList)Name ofPrimary ControlName ofSecondary ControlPage 12KChevron Products Co. - SL RefinerySecondary Control100.8 mmbtu/hr 1189btu/cf0.0007CEM100.8 mmbtu/hr1393btu/cf0.0003CEM100.8 mmbtu/hrbtu/cf0.0000 CEMSecondary Control108mmbtu/hr6000000btu/bbl0.8028Explain108mmbtu/hr6000000btu/bbl0.9951Explain100.8mmbtu/hr6000000btu/bbl0.0000 ExplainSecondary ControlDesignRate UnitsDesignRate UnitsIf Throughput is a FuelPrimary ControlHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)If Throughput is a FuelPrimary ControlHeatingValue Units%SulfurName ofSecondary ControlControlCode (SeeList)ControlCode (SeeList)Name ofPrimary ControlHow Sulfur Content iscalculated%AshControlControlPrimary ControlIf Throughput is a FuelPage 13KChevron Products Co. - SL Refinerymmbtu/hr 1189 btu/cf 0.0014CEM159.3mmbtu/hr1393btu/cf0.0003CEMmmbtu/hr0btu/ctCEMSecondary Controlmmbtu/hr 1189 btu/cf 0.0014CEM50.3 mmbtu/hr 1393 btu/cf0.0003 CEMmmbtu/hr btu/cf0.0003 CEMSecondary Controlmmbtu/hr 1189 btu/cf 0.0014CEMUnits%SulfurDesignRateName ofSecondary ControlControlCode (SeeList)How Sulfur Content iscalculated%AshName ofPrimary ControlControlCode (SeeList)UnitsHeatingValueDesignRate UnitsIf Throughput is a FuelPrimary ControlName of Primary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)HeatingValue Units%SulfurHow Sulfur Content iscalculated%AshHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName of Primary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelPage 14KChevron Products Co. - SL Refinery50.3mmbtu/hr1393btu/cf0.0003CEM0mmbtu/hr0btu/cfCEMSecondary Controlmmbtu/hr 1189 btu/cf 0.0014CEM97.3mmbtu/hr1393btu/cf0.0003CEMmmbtu/hr btu/cfCEMSecondary Controlmmbtu/hr23mmbtu/hr23023HeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName of Primary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName of Primary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)FlaringDesignRate UnitsIf Throughput is a FuelFlaringFlaringPage 15KChevron Products Co. - SL RefinerySecondary Controlmmbtu/hr 1189 btu/cf 0.0014CEM43.5mmbtu/hr1393btu/cf0.0003CEMmmbtu/hr btu/cfCEMSecondary Controlmmbtu/hr 1189 btu/cf 0.0014CEM52.3mmbtu/hr1393btu/cf0.0003CEMmmbtu/hr btu/cfCEMSecondary ControlHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelPrimary ControlIf Throughput is a FuelPage 16KChevron Products Co. - SL Refinerymmbtu/hr 1189 btu/cf 0.0014CEM45mmbtu/hr1393btu/cf0.0003CEMmmbtu/hr btu/cfCEMSecondary Controlmmbtu/hr 1189 btu/cf 0.0014CEM31.7mmbtu/hr1393btu/cf0.0003CEMmmbtu/hr btu/cfCEMSecondary Controlmmbtu/hr 1189 btu/cf 0.0014CEMHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelPage 17KChevron Products Co. - SL Refinery90mmbtu/hr1393btu/cf0.0003CEMmmbtu/hr btu/cf0.0000 CEMSecondary Controlmmbtu/hr 6000000 btu/bbl 0.0014lab analysis90mmbtu/hr 6000000 btu/bbl 0.0441lab analysis90mmbtu/hr0btu/bbl0.0441 lab analysisSecondary Controlmmbtu/hr23mmbtu/hr23mmbtu/hr23HeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName of Primary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)FlaringDesignRate UnitsIf Throughput is a FuelFlaringFlaringPage 18KChevron Products Co. - SL RefinerySecondary Controlmmbtu/hr 1189 btu/cf 0.0014CEM71.1 mmbtu/hr1393btu/cf0.0003CEMmmbtu/hr btu/cfCEMSecondary Controlmmbtu/hr23mmbtu/hr23mmbtu/hr23Secondary ControlHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)FlaringDesignRate UnitsIf Throughput is a FuelFlaringFlaringHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelPage 19KChevron Products Co. - SL Refinerymmbtu/hr 1189 btu/cf 0.0014CEM13.8mmbtu/hr 1393 btu/cf 0.0014CEM13.8mmbtu/hr1393btu/cf0.0003 CEMSecondary Controlmmbtu/hr 1189 btu/cf 0.0014CEM20.6mmbtu/hr 1393 btu/cf0.0003CEM20.6mmbtu/hr1393btu/cf0.0003CEMSecondary Controlmmbtu/hr 1189 btu/cf 0.0014CEM45 Direct Flame Afterburner 214.5mmbtu/hr1393btu/cf0.0003CEM45 Direct Flame Afterburner 21HeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)Sulfur PlantDesignRate UnitsIf Throughput is a FuelSulfur PlantPage 20KChevron Products Co. - SL Refinery4.5mmbtu/hr1393btu/cf0.0003 CEM45 Direct Flame Afterburner 21Secondary Control1035 mmbtu/hr 0 0 0.0010From Natural Gas supplier1035 mmbtu/hr 1060 btu/cf0.0011 From Natural Gas supplier1035 mmbtu/hr1060btu/cf0.0011 From Natural Gas supplierSulfur PlantHeatingValue Units%SulfurHow Sulfur Content iscalculated%AshPrimary ControlName ofPrimary ControlControlCode (SeeList)Name ofSecondary ControlControlCode (SeeList)DesignRate UnitsIf Throughput is a FuelPage 21KChevron Products Co. - SL RefineryPage 22KChevron Products Co. - SL Refinery6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf1.199 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.507 lbs/mmcf0.006lbs/mmcf8 AP-42 5th Edition, Table 1.3-1 (9/98) EF = 157 X(.8028%) 126.040 lbs/mmcf0.008 AP-42 5th Edition, Table 1.3-1 (9/98) EF = 157 X(.9951%)156.230lbs/mmcf0.00 0AP-42 5th Edition, Section 1.3lbs/10^3 galsEmissionsfromBreakdown(tons/year)EstimateCode Estimate MethodEmissionFactorEmissions(tons/yr)EmissionFactor UnitsControlEfficiency(%)EmissionsfromBreakdown(tons/year)EstimateCodeEmissions(tons/yr)Estimate Method0.620.380.1160.00ControlEfficiency(%)Units0.000.00Page 23KChevron Products Co. - SL Refinery6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf1.199 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.507 lbs/mmcf0.00 6lbs/mmcf8AP-42 5th Edition, Table 1.3-1, 9/98 EF = 157 x .8028%126.040lbs/mmcf0.008AP-42 5th Edition, Table 1.3-1, 9/98 EF = 157 x .8028%156.231 lbs/mmcf0.008lbs/10^3 galsControlEmissionsfrom0.62EmissionFactor UnitsControlEfficiency(%)Emissions(tons/yr)EmissionsfromBreakdown(tons/year)EstimateCode Estimate Method0.310.065ControlEfficiency(%)EstimateCode Estimate MethodEmissionFactor Units0.00Emissions(tons/yr)EmissionsfromBreakdown(tons/year)0.000.00Page 24KChevron Products Co. - SL Refinery6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.199 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.507 lbs/mmcf0.006lbs/mmcf6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.199 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.507lbs/mmcf0.006lbs/mmcf6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.199 lbs/mmcfControlEfficiency(%)Emissions(tons/yr)fromBreakdown(tons/year)0.58EstimateCode Estimate MethodEmissionFactor Units0.2420.00Estimate MethodEmissionFactorControlEfficiency(%) Emissions (tons/year)EmissionsfromBreakdown(tons/year)EstimateCode0.04Units0.0350.00EmissionFactor UnitsControlEfficiency(%) Emissions (tons/year)EmissionsfromBreakdown(tons/year)0.10EstimateCode Estimate MethodPage 25KChevron Products Co. - SL Refinery0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.507 lbs/mmcf0.006Agreed to per 1990 PM10 SIPlbs/mmcf4 Source Test77.1 lbs/hr0.004 Source Test18lbs/hr0.004Stack Test8AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on1/3 of crude unit throughput26.9 lbs/mbbls2.008AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on1/3 of crude unit throughput26.9 lbs/mbbls2.008Based on 2006 Engineering Data -Flowmeters; H2SAnalysis0.22lbs/mbblsEmission factor divided by3 so thruput should not be.0.000.031EmissionFactor UnitsControlEfficiency(%) Emissions (tons/year)EmissionsfromBreakdown(tons/year)337.70EstimateCode Estimate Method0.0071.38EmissionFactor UnitsControlEfficiency(%) Emissions (tons/year)EmissionsfromBreakdown(tons/year)64.78EstimateCode Estimate Method3.5866.47Page 26KChevron Products Co. - SL Refinery6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.50659631 lbs/mmcf0.006lbs/mmcf6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.50659631 lbs/mmcf0.006lbs/mmcfEmissionFactor UnitsControlEfficiency(%) Emissions (tons/year)EmissionsfromBreakdown(tons/year)0.10EstimateCode Estimate Method0.000.046EmissionFactor UnitsControlEfficiency(%) Emissions (tons/year)EmissionsfromBreakdown(tons/year)0.13EstimateCode Estimate Method0.000.043EmissionsPage 27KChevron Products Co. - SL Refinery6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.50659631 lbs/mmcf0.006lbs/mmcf6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.50659631 lbs/mmcf0.006lbs/mmcf6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mmcfEmissionFactor UnitsControlEfficiency(%) Emissions (tons/year)EmissionsfromBreakdown(tons/year)0.13EstimateCode Estimate Method0.000.044EmissionFactor UnitsControlEfficiency(%) Emissions (tons/year)EmissionsfromBreakdown(tons/year)0.06EstimateCode Estimate Method0.000.022EmissionFactor UnitsControlEfficiency(%)Emissions(tons/yr)EmissionsfromBreakdown(tons/year)0.31EstimateCode Estimate MethodPage 28KChevron Products Co. - SL Refinery0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.50659631lbs/mmcf0.006lbs/mmcf8 AP-42 5th Edition, Table 1.3-1, 9/98 EF = 157 x .10% 15.7 lbs/10^3 gals0.008 AP-42 5th Edition, Table 1.3-1, 9/98 EF = 157 x .04%6.9237lbs/10^3 gals0.008AP-42 5th Edition, Table 1.3-1, 9/98 EF = 157 x .04% lbs/10^3 gals8AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on 1/3 of crude unit throughput26.9 lbs/mbbls0.008AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on 1/3 of crude unit throughput26.9 lbs/mbbls0.008Based on 2006 Engineering Data -Flowmeters; H2SAnalysis0.19lbs/mbblsEmission factor divided by3 so thruput should not be.0.000.121EmissionFactor UnitsControlEfficiency(%)Emissions(tons/yr)EmissionsfromBreakdown(tons/year)0.59EstimateCode Estimate Method0.000.27EmissionFactor UnitsControlEfficiency(%)Emissions(tons/yr)EmissionsfromBreakdown(tons/year)64.78EstimateCode Estimate Method1.3764.47Page 29KChevron Products Co. - SL Refinery6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.50659631lbs/mmcf0.006lbs/mmcf8AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on1/3 of crude unit throughput26.9 lbs/mbbs90.738AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on1/3 of crude unit throughput26.9 lbs/mbbsBased 1/3 of throughputgoing through one of three90.738Based on 2006 Engineering Data -Flowmeters; H2SAnalysis79.5lbs/mbbsThese emissions are basedon continuous releasemonitor, not 1/3 orthroughput.EmissionFactor UnitsControlEfficiency(%)Emissions(tons/yr)EmissionsfromBreakdown(tons/year)0.15EstimateCode Estimate Method0.000.10EmissionFactor UnitsControlEfficiency(%)Emissions(tons/yr)EmissionsfromBreakdown(tons/year)64.78EstimateCode Estimate Method662.34155.20EmissionFactor UnitsControlEfficiency(%)Emissions(tons/yr)EmissionsfromBreakdown(tons/year)EstimateCode Estimate MethodPage 30KChevron Products Co. - SL Refinery6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf1.19894459 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.50659631 lbs/mmcf0.006Agreed to per 1990 PM10 SIPlbs/mmcf6Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mmcf0.006Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) *(lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf0.50659631 lbs/mmcf0.006Agreed to per 1990 PM10 SIPlbs/mmcf1 CEMNA lbs/mmcf129.571 CEM563434 lbs/year0.0250.000.014EmissionFactor UnitsControlEfficiency(%)Emissions(tons/yr)EmissionsfromBreakdown(tons/year)0.05EstimateCode Estimate Method0.000.024EmissionFactor UnitsControlEfficiency(%)Emissions(tons/yr)EmissionsfromBreakdown(tons/year)308.80EstimateCode Estimate Method411.29Page 31KChevron Products Co. - SL Refinery0.001 CEMlbs/mmcf3 Agreed to per 1990 PM10 SIP EF = ((7.1 ppm*32*2)/379 1.19894459 lbs/mmcf0.003 Agreed to per 1990 PM10 SIP EF = ((7.1 ppm*32*2)/379 1.19894459 lbs/mmcf0.003AP-42 Table 3.2-20.000588lbs/10^6 btuComponent Amount SIP Amount3874 0.116 0.1163875 0.00 0.0003876 0.065 0.0653877 0.00 0.0003878 0.242 0.2423886 0.035 0.0353887 0.031 0.0313888 71.38 71.3793889 3.58 66.473890 0.046 0.0463891 0.043 0.0433892 0.04 0.0443893 0.022 0.0223894 0.12 0.1213895 0.27 0.2663896 1.37 64.473897 0.10 0.1000.00EmissionFactor UnitsControlEfficiency(%)Emissions(tons/yr)EmissionsfromBreakdown(tons/year)0.05EstimateCode Estimate Method0.0260.05Page 32KChevron Products Co. - SL Refinery3898 662.34 155.203899 0.014 0.0144333 0.024 0.0244334 411.29 411.2875479 0.03 0.026After 1999 22.7674 22.767TOTAL 1173.913 792.771Page 33KChevron Products Co. - SL Refinery