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11.000 Utility and Large Industrial Sized Boilers/Furnaces (>250 million Btu/H)11.100 Solid Fuel & Solid Fuel Mixtures

11.110 Coal11.110 Liquid Fuel11.190 Other Solid Fuel

11.200 Liquid Fuel & Liquid Fuel Mixtures11.210 Residual Fuel11.220 Distillate Fuel11.900 Other Liquid Fuel

11.300 Gaseous Fuel & Gaseous Fuel Mixtures11.310 Natural Gas (includes propane and LPG)11.320 Landfill/Digester/Bio-Gas11.390 Other Gaseous Fuel & Fuel Mixtures

12.000 Industrial Size Boilers/Furnaces (more than 100 Btu/H, up to/including 250 million Btu/hr12.100 Solid Fuel & Solid Fuel Mixtures




13.000 Commerial/Institutional-Size Boilers/Furnaces (100 million Btu/H or less)13.100 Solid Fuel & Solid Fuel Mixtures




Industrial Size Boilers/Furnaces (more than 100 Btu/H, up to/including 250 million Btu/hr

RBLCID FACILITY CORPORAFACILITYSAGENCYNPERMITDATE FACILITYDPROCESSPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERA2 COAL-FIWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRI*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRIND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, JND-0018 ARCHER DARCHER DNORTH DAKOTA STA 7/9/1998 VEGETABLBOILER, JND-0018 ARCHER DARCHER DND 7/9/1998 VEGETABLBOILER, JPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERA2 COAL-FIVA-0268 THERMAL MARTINSVVIRGINIA ENVIRONM 2/15/2002 STEAM PRBOILER, MT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PMT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PAR-0074 PLUM POI PLUM POI AR 8/20/2003 BOILER , UAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI BOILER - GA-0114 INLAND P TEMPLE INGA 10/13/2004 THIS FAC BOILER, CGA-0114 INLAND P TEMPLE INGA 10/13/2004 THIS FAC BOILER, SWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRI*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZAR-0074 PLUM POI PLUM POI AR 8/20/2003 BOILER , UAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI BOILER - WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRIWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRIWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRI*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERA2 COAL-FI*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZGA-0114 INLAND P TEMPLE INGA 10/13/2004 THIS FAC BOILER, SAR-0074 PLUM POI PLUM POI AR 8/20/2003 BOILER , UAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI BOILER - WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRI*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRI*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZPA-0204 KIMBERLYKIMBERLYPA PENNSYLV 24-Jun-98 OP INCORPBOILER, CND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, JND-0018 ARCHER DARCHER DNORTH DAKOTA STA 7/9/1998 VEGETABLBOILER, JND-0018 ARCHER DARCHER DND 7/9/1998 VEGETABLBOILER, JPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERA2 COAL-FIVA-0268 THERMAL MARTINSVVIRGINIA ENVIRONM 2/15/2002 STEAM PRBOILER, MT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PMT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PAR-0074 PLUM POI PLUM POI AR 8/20/2003 BOILER , UAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI BOILER - WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRI*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, JND-0018 ARCHER DARCHER DNORTH DAKOTA STA 7/9/1998 VEGETABLBOILER, JND-0018 ARCHER DARCHER DND 7/9/1998 VEGETABLBOILER, J

VA-0268 THERMAL MARTINSVVIRGINIA ENVIRONM 2/15/2002 STEAM PRBOILER, WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRIPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERA2 COAL-FIVA-0268 THERMAL MARTINSVVIRGINIA ENVIRONM 2/15/2002 STEAM PRBOILER, MT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PMT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PAR-0074 PLUM POI PLUM POI AR 8/20/2003 BOILER , UAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI BOILER - GA-0114 INLAND P TEMPLE INGA 10/13/2004 THIS FAC BOILER, CGA-0114 INLAND P TEMPLE INGA 10/13/2004 THIS FAC BOILER, SWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRIWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAP46, S46,WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAP47, S47,WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAP50, S50,*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZWA-0336 GRAYS HARBOR PAPWASHINGTON STAT 11/17/2006 GHP IS ANUTILITY-AND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, JND-0018 ARCHER DARCHER DNORTH DAKOTA STA 7/9/1998 VEGETABLBOILER, JND-0018 ARCHER DARCHER DND 7/9/1998 VEGETABLBOILER, JPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERA2 COAL-FIVA-0268 THERMAL MARTINSVVIRGINIA ENVIRONM 2/15/2002 STEAM PRBOILER, MT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PMT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PAR-0074 PLUM POI PLUM POI AR 8/20/2003 BOILER , UAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI BOILER - WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRI*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZGA-0114 INLAND P TEMPLE INGA 10/13/2004 THIS FAC BOILER, SPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERA2 COAL-FIMT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PMT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PAR-0074 PLUM POI PLUM POI AR 8/20/2003 BOILER , UAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI BOILER - WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRI*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, JND-0018 ARCHER DARCHER DNORTH DAKOTA STA 7/9/1998 VEGETABLBOILER, JND-0018 ARCHER DARCHER DND 7/9/1998 VEGETABLBOILER, JPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERA2 COAL-FIPA-0204 KIMBERLYKIMBERLYPA PENNSYLV 24-Jun-98 OP INCORPBOILER, CPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERA2 COAL-FIVA-0268 THERMAL MARTINSVVIRGINIA ENVIRONM 2/15/2002 STEAM PRBOILER, MT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PMT-0022 BULL MOUBULL MOUMT 7/21/2003 COAL FIR BOILER, PAR-0074 PLUM POI PLUM POI AR 8/20/2003 BOILER , UAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI BOILER - GA-0114 INLAND P TEMPLE INGA 10/13/2004 THIS FAC BOILER, CGA-0114 INLAND P TEMPLE INGA 10/13/2004 THIS FAC BOILER, S

WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICASUPER CRI*TX-0499 SANDY CRSANDY CRTX TEXAS CO 7/24/2006 THE PROPPULVERIZ

PROCTYPEFUEL THRUPUT THRUPUTUPROCESSPOLLUTANT CONTROL11.11 BITUMINO 454 MW (NET) COMBINEDAmmonia (NH3) N11.11 PRB COAL 5173.07 MMBTU/H 500 MW CAAmmonia (NH3) P11.11 COAL 8185 MMBTU/H COAL (TY Ammonia (NH3) N11.11 PRB COAL 5173.07 MMBTU/H 500 MW CABeryllium / Beryllium Com A11.12 HULLS 280 MMBTU/H Carbon Monoxide N11.12 HULLS 280 MMBTU/H Carbon Monoxide N11.12 HULLS 280 MMBTU/H Carbon Monoxide N11.11 BITUMINO 454 MW (NET) COMBINEDCarbon Monoxide P11.11 COAL 120 MMBTU/H In order to Carbon Monoxide P11.11 COAL 390 MW Additional Carbon Monoxide N11.11 COAL 390 MW Stack testsCarbon Monoxide N11.11 SUB-BITU 800 MW THE BOILECarbon Monoxide P11.11 SUB-BITU 800 MW THE BOILECarbon Monoxide P11.11 COAL 565 MMBTU/H MODIFICATCarbon Monoxide P11.12 BARK 856 MMBTU/H BARK, WACarbon Monoxide P11.11 PRB COAL 5173.07 MMBTU/H 500 MW CACarbon Monoxide P11.11 COAL 8185 MMBTU/H COAL (TY Carbon Monoxide N11.11 SUB-BITU 800 MW THE BOILEFluorine A11.11 SUB-BITU 800 MW THE BOILEFluorine A11.11 PRB COAL 5173.07 MMBTU/H 500 MW CAFluorine A11.11 PRB COAL 5173.07 MMBTU/H 500 MW CAHazardous Air Pollutants ( P11.11 PRB COAL 5173.07 MMBTU/H 500 MW CAHydrochloric Acid A11.11 COAL 8185 MMBTU/H COAL (TY Hydrochloric Acid N11.11 BITUMINO 454 MW (NET) COMBINEDHydrogen Fluoride A11.11 COAL 8185 MMBTU/H COAL (TY Hydrogen Fluoride N11.12 BARK 856 MMBTU/H BARK, WAHydrogen Sulfide N11.11 SUB-BITU 800 MW THE BOILELead (Pb) / Lead CompounP11.11 SUB-BITU 800 MW THE BOILELead (Pb) / Lead CompounP11.11 PRB COAL 5173.07 MMBTU/H 500 MW CALead (Pb) / Lead CompounA11.11 COAL 8185 MMBTU/H COAL (TY Lead (Pb) / Lead CompounN11.11 PRB COAL 5173.07 MMBTU/H 500 MW CAMercury P11.11 COAL 8185 MMBTU/H COAL (TY Mercury N11.11 COAL 799 MMBTU/H BOILER LI Nitrogen Oxides (NOx) N11.12 HULLS 280 MMBTU/H Nitrogen Oxides (NOx) N11.12 HULLS 280 MMBTU/H Nitrogen Oxides (NOx) N11.12 HULLS 280 MMBTU/H Nitrogen Oxides (NOx) N11.11 BITUMINO 454 MW (NET) COMBINEDNitrogen Oxides (NOx) A11.11 COAL 120 MMBTU/H In order to Nitrogen Oxides (NOx) P11.11 COAL 390 MW Additional Nitrogen Oxides (NOx) B11.11 COAL 390 MW Stack testsNitrogen Oxides (NOx) B11.11 SUB-BITU 800 MW THE BOILENitrogen Oxides (NOx) A11.11 SUB-BITU 800 MW THE BOILENitrogen Oxides (NOx) P11.11 PRB COAL 5173.07 MMBTU/H 500 MW CANitrogen Oxides (NOx) B11.11 COAL 8185 MMBTU/H COAL (TY Nitrogen Oxides (NOx) A11.12 HULLS 280 MMBTU/H Particulate Matter (PM) A11.12 HULLS 280 MMBTU/H Particulate Matter (PM) A11.12 HULLS 280 MMBTU/H Particulate Matter (PM) A

11.11 COAL 120 MMBTU/H In order to Particulate Matter (PM) P11.11 PRB COAL 5173.07 MMBTU/H 500 MW CAParticulate Matter (PM) B11.11 BITUMINO 454 MW (NET) COMBINEDParticulate Matter < 10 μ A11.11 COAL 120 MMBTU/H In order to Particulate Matter < 10 μ P11.11 COAL 390 MW Additional Particulate Matter < 10 μ A11.11 COAL 390 MW Stack testsParticulate Matter < 10 μ A11.11 SUB-BITU 800 MW THE BOILEParticulate Matter < 10 μ A11.11 SUB-BITU 800 MW THE BOILEParticulate Matter < 10 μ A11.11 COAL 565 MMBTU/H MODIFICATParticulate Matter < 10 μ A11.12 BARK 856 MMBTU/H BARK, WAParticulate Matter < 10 μ A11.11 PRB COAL 5173.07 MMBTU/H 500 MW CAParticulate Matter < 10 μ B11.11 Particulate Matter < 10 μ A11.11 Particulate Matter < 10 μ A11.11 FABRIC F Particulate Matter < 10 μ B11.11 COAL 8185 MMBTU/H COAL (TY Particulate Matter < 10 μ N11.12 WOOD WA 379 MMBTU/H RILEY TYPParticulate Matter < 10 μ A11.12 HULLS 280 MMBTU/H Sulfur Dioxide (SO2) N11.12 HULLS 280 MMBTU/H Sulfur Dioxide (SO2) N11.12 HULLS 280 MMBTU/H Sulfur Dioxide (SO2) N11.11 BITUMINO 454 MW (NET) COMBINEDSulfur Dioxide (SO2) B11.11 COAL 120 MMBTU/H In order to Sulfur Dioxide (SO2) P11.11 COAL 390 MW Additional Sulfur Dioxide (SO2) A11.11 COAL 390 MW Stack testsSulfur Dioxide (SO2) A11.11 SUB-BITU 800 MW THE BOILESulfur Dioxide (SO2) A11.11 SUB-BITU 800 MW THE BOILESulfur Dioxide (SO2) A11.11 PRB COAL 5173.07 MMBTU/H 500 MW CASulfur Dioxide (SO2) B11.11 COAL 8185 MMBTU/H COAL (TY Sulfur Dioxide (SO2) N11.12 BARK 856 MMBTU/H BARK, WASulfur, Total Reduced (TRSN11.11 BITUMINO 454 MW (NET) COMBINEDSulfuric Acid (mist, vapors, A11.11 COAL 390 MW Additional Sulfuric Acid (mist, vapors, A11.11 COAL 390 MW Stack testsSulfuric Acid (mist, vapors, A11.11 SUB-BITU 800 MW THE BOILESulfuric Acid (mist, vapors, A11.11 SUB-BITU 800 MW THE BOILESulfuric Acid (mist, vapors, A11.11 PRB COAL 5173.07 MMBTU/H 500 MW CASulfuric Acid (mist, vapors, A11.11 COAL 8185 MMBTU/H COAL (TY Sulfuric Acid (mist, vapors, N11.12 HULLS 280 MMBTU/H Visible Emissions (VE) N11.12 HULLS 280 MMBTU/H Visible Emissions (VE) N11.12 HULLS 280 MMBTU/H Visible Emissions (VE) N11.11 BITUMINO 454 MW (NET) COMBINEDVisible Emissions (VE) A11.11 COAL 799 MMBTU/H BOILER LI Volatile Organic Compoun N11.11 BITUMINO 454 MW (NET) COMBINEDVolatile Organic Compoun P11.11 COAL 120 MMBTU/H In order to Volatile Organic Compoun P11.11 COAL 390 MW Additional Volatile Organic Compoun N11.11 COAL 390 MW Stack testsVolatile Organic Compoun N11.11 SUB-BITU 800 MW THE BOILEVolatile Organic Compoun P11.11 SUB-BITU 800 MW THE BOILEVolatile Organic Compoun P11.11 COAL 565 MMBTU/H MODIFICATVolatile Organic Compoun P11.12 BARK 856 MMBTU/H BARK, WAVolatile Organic Compoun P

11.11 PRB COAL 5173.07 MMBTU/H 500 MW CAVolatile Organic Compoun P11.11 COAL 8185 MMBTU/H COAL (TY Volatile Organic Compoun N

CTRLDESC EMISLIMITEMISLIMITEMISLIMI PCTEFFIC EMISLIMITEMISLIMITTHIS IS AMMONIA S 10 PPMDV @ 7% O2

3 PPMDV 3% O2 55.52 LB/H41 LB/H

FABRIC FILTER BA 1.3 LB/TRILLION-BTU0.63 LB/MMBTU0.63 LB/MMBTU0.63 LB/MMBTU

GOOD COMBUSTION 246.1 LB/H 94 PPMVD @7%O2GOOD COMBUSTION 0.44 LB/MMBTU 231.3 T/YR

602 LB/H 0.15 LB/MMBTU602 LB/H 0.15 LB/MMBTU

COMBUSTION CONT 0.16 LB/MMBTUCOMBUSTION CONT 0.16 LB/MMBTUSTAGED COMBUSTI 300 PPM @ 3% O2STAGED COMBUSTI 368 PPM @ 3% O2GOOD COMBUSTION 0.15 LB/MMBTUCALENDAR DAY AVG 3399 T/YR

2456 LB/H 1-HR 1228 LB/HDRY FGD/FABRIC FI 0.0004 LB/MMBTU 90DRY FGD/FABRIC FI 0.0004 LB/MMBTU 90DRY FGD, BAGHOUS 0.0002 LB/MMBTU 1.12 LB/HFABRIC FILTER BAGHOUSE, DRY FGD, GOOD COMBUSTION PRACTICESDRY FGD 10.94 LB/H 24 HR AVG.

72 LB/H 47 T/YRSCRUBBER 0.0005 LB/MMBTU 1.18 LB/H

23 LB/H 24 T/YRBOILER IS CONTROL 99 % REDUCTION 99FABRIC FILTER 2.56 E-5 LB/MMBTUFABRIC FILTER 2.56 E-5 LB/MMBTUFABRIC FILTER BA 0.13 LB/H

0.55 LB/H 0.41 T/YRFABRIC FILTER BAG 1.7 LB/TRILLI 12 MO. RO 83

0.94 LB/H 0.075 T/YR1090 T/YR Total, 3 Boilers

0.2 LB/MMBTU0.2 LB/MMBTU0.2 LB/MMBTU

SELECTIVE NON-CAT 57 PPMVD @ 7% O2GOOD COMBUSTION 0.4 LB/MMBTU 210.2 T/YRLOW NOX BURNER, O 280.9 LB/H rolling 24 90 0.07 LB/MMBTULOW NOX BURNER, O 280.9 LB/H rolling 24 90 0.07 LB/MMBTULOW NOX BURNERS 0.09 LB/MMBTULOW NOX BURNERS 0.09 LB/MMBTULOW NOX BURNERS, 0.07 LB/MMBTU30 DAY AVG. EXCL 0.06 LB/MMBTUAT THIS POINT, TH 1637 LB/H 1-HR 573 LB/HESP 0.24 LB/MMBTUESP 0.24 LB/MMBTUESP 0.24 LB/MMBTU

GOOD COMBUSTION 0.15 LB/MMBTU 78.8 T/YRFABRIC FILTER BAG 0.02 LB/MMBTU3 HR. AVG 103.52 LB/HELECTROSTATIC PR 73.8 LB/H SEE POLLUTANT NOTESGOOD COMBUSTION 0.14 LB/MMBTU 73.6 T/YRFABRIC FILTERS 60.2 LB/H 99.82 0.015 LB/MMBTUFABRIC FILTERS 60.2 LB/H 99.82 0.015 LB/MMBTUBAGHOUSE 0.018 LB/MMBTUBAGHOUSE 0.018 LB/MMBTUESP 0.05 LB/MMBTUESP 0.025 LB/MMBTUFABRIC FILTER BAG 0.018 LB/MMBTU3 HOUR AVG.FABRIC FILTER BA 0.02 GR/DSCF 0.65 LB/HFABRIC FILTER BA 0.02 GR/DSCF 0.65 LB/HFABRIC FILTER BAG 0.02 GR/DSCF 1.12 LB/H

123 LB/H 1-HR 327 LB/H1. MULTICLONES WI 52.5 LB/H CALENDAR DAY

0.002 LB/MMBTU0.002 LB/MMBTU0.002 LB/MMBTU

LOW-SULFUR COAL ( 9 PPMVD @ 7% O2 54.1 LB/HGOOD COMBUSTION 0.47 LB/MMBTU 247 T/YRDRY FLUE GAS DESU 481.6 LB/H rolling 24 94.5 0.12 LB/MMBTUDRY FLUE GAS DESU 481.6 LB/H rolling 24 94.5 0.12 LB/MMBTUDRY FLUE GAS DES 0.16 LB/MMBTUDRY FLUE GAS DES 0.16 LB/MMBTUDRY FGD, LIMIT ON 0.1 LB/MMBTU30 DAY AV 92 0.09 LB/MMBTU

2456 LB/H 1-HR 982 LB/HBOILER IS CONTROL 99 % REDUCTION 99SCRUBBER 0.64 PPMVD @ SULFURIC ACID MIS 5.9 LB/HDRY FLUE GAS DESU 25.7 LB/H 90 0.0064 LB/MMBTUDRY FLUE GAS DES 25.7 LB/H 90 0.0064 LB/MMBTUDRY FGD/FABRIC FI 0.0061 LB/MMBTUDRY FGD/FABRIC FI 0.0061 LB/MMBTUFGD SYSTEM 0.005 LB/MMBTU24 HR AVG.

127 LB/H 133 T/YR20 % OPACITY20 % OPACITY20 % OPACITY

ESP, SCRUBBER 20 % OPACIT6 MIN AV 27 %30 T/YR Rolling Avg Total From 3 Boilers

COMBUSTION CONT 7.7 PPMVD @ 7% O2 11.6 LB/HGOOD COMBUSTION 0.18 LB/MMBTU 94.6 T/YR

12 LB/H 0.003 LB/MMBTU12 LB/H 0.003 LB/MMBTU

COMBUSTION CONT 0.02 LB/MMBTUCOMBUSTION CONT 0.02 LB/MMBTUSTAGED COMBUSTIO 0.01 LB/MMBTUSTAGED COMBUSTI 0.05 LB/MMBTU

GOOD COMBUSTION 0.0036 LB/MMBTU 81.6 T/YR29 LB/H

EMISLIMI STDEMISSLSTDUNITLISTDLIMIT POLLUTANTCOMPLIANCENOTES STATE HAP

0.63 LB/MMBTU 0.63 LB/MMBTU 0.63 LB/MMBTU

PPMVD @7%O2 0.1 LB/MMBTU8 H BASIS 0.44 LB/MMBTU

LB/MMBTU 0.15 LB/MMBTU LB/MMBTU 0.15 LB/MMBTU

0.16 LB/MMBTU 0.16 LB/MMBTU

NOT AVAI PERMITTED LIMIT IS 300 PPM. EMISSION RATE LIMIT AS LB/MMBTU NOT AVAILABLE. NOT AVAI PERMIT LIMIT IS 368 PPM. EMISSION LIMIT AS LB/MMBTU IS NOT AVAILABLE.

12 MO. ROLLING INCL. STARTUP / SHU 30-DAY

% efficiency is 90% control by weight SOURCE SHALL MEET THE BACT PM AND SO2 LIMITS TO COMPLY WITH CASE BY CASE MACT FOR INORGANIC SOLID HAPS AND INORGANIC ACID HAPS. SOURCE SHALL MEET THE VOC BACT LIMIT TO COMPLY WITH MACT FOR ORGANIC HAPS. 99% DESTRUCTION OF H2S GASES.

0.2 LB/MMBTU0.2 LB/MMBTU 0.2 LB/MMBTU 0.2 LB/MMBTU 0.1 LB/MMBTU 0.4 LB/MMBTU

rolling 24 0.07 LB/MMBTU incremental cost effectiveness: $1332/t pollutant removed rolling 24 0.07 LB/MMBTU Incremental cost effectiveness: $1332/t pollutant removed.


12 MO. AVG. INCL. STARTUP / SHUTDOW COST EFFECTIVENESS BASED ON 30 DAY AVG. VALUE. 30-DAY


0.15 LB/MMBTU 3 HR. AVG. NOT AVAI POLLUTANT MEASUREMENT INCLUDES BACKHALF (METHOD 5 OR 5B + METHOD 202)

0.03 LB/MMBTUSEE POLL THE NEW PM10 LIMITS INDICATED ABOVE BECAME EFFECTIVE ON AUGUST 10, 2004. PREVIOUS LIMITS WERE 36.9 LB/H AND 0.015 LB/MMBTU. THE LIMITS WERE CHANGED BASED ON STACK TEST RESULTS. 0.14 LB/MMBTU

LB/MMBTU 0.015 LB/MMBTU Based on testing, Roundup Power is required to determine the feasibility of changing this limit to 48.2 lb/h (0.012 lb/mmbtu) based on a rolling 24-h average LB/MMBTU 0.015 LB/MMBTU


0.025 LB/MMBTU NOT AVAI INCLUDES BACKHALF NOT AVAI PM AND PM10 (INCL. M202 BACKHALF CATCH)

PM AND PM10 (INCL. M202 BACKHALF CATCH) 10% OPACITY NOT AVAI PM AND PM10 (INCL. M202 BACKHALF CATCH) 10% OPACITY

30-DAY AREA IS IN ATTAINMENT. THIS PROJECT DID NOT TRIGGER BACT ON THIS GRANDFATHERED HOG FUEL BOILER. INCREASED UTILIZATION TRIGGERED SOME IMPACTS ANALYSIS REQUIREMENT OF PSD FOR NOX, CO, AND PM10. PM10 WAS ONLY POLLUTANT THAT EVEN CAME CLOSE TO CHALLENGING ANY


3 H AV 0.022 LB/MMBTU 0.47 LB/MMBTU

rolling 24 0.12 LB/MMBTU rolling 24 0.12 LB/MMBTU


12 MO. ROLLING AVG. POLLUTANT LIMITS INCLUDE STARTUP / SHUTDOWN AND ATOMIZER CHANGEOUT. PERMITTEE MAY ONLY USE ACTUAL HOURS OF OPERATION WHEN DETERMINING TIME AVERAGED EMISSIONS. WHEN CONDUCTING MAINTENANCE ON CONTROL SYSTEM (ROUTINE ATOMIZER CHANGEOUT): 3491.8 POUNDS PER HOUR ON A 3-HOUR AVERAGE AND 1508.9 POUNDS PER HOUR ON A 24-HOUR AVERAGE. CONTROLLED EMISSIONS: SULFUR DIOXIDE EMISSIONS SHALL BE LIMITED TO 621 POUNDS PER HOUR AVERAGED OVER ANY CONSECUTIVE 3-HOUR PERIOD AND SULFUR DIOXIDE EMISSIONS SHALL BE LIMITED TO 589 POUNDS PER HOUR AVERAGED OVER ANY CONSECUTIVE 24-HOUR PERIOD 30-DAY

99% DESTRUCTION OF TRS GASES SULFURIC 0.0024 LB/MMBTUSULFURIC

LB/MMBTU same control as for SO2 LB/MMBTU Same controls as for SO2.

REGULATED POLLUTANT IS SULFURIC ACID MIST.

20 % OPACITY 20 % OPACITY 20 % OPACITY

1 6 MIN S 20 % OPACIT6 MIN AV 0.006 LB/MMBTU

ADDITIONAL EMISSION LIMIT: 0.0047 LB/MMBTU

LB/MMBTU LB/MMBTU

0.05 LB/MMBTU

12 MO. ROLLING, INCL. STARTUP / SHU

PERMITTED LIMIT IS 300 PPM. EMISSION RATE LIMIT AS LB/MMBTU NOT AVAILABLE. PERMIT LIMIT IS 368 PPM. EMISSION LIMIT AS LB/MMBTU IS NOT AVAILABLE.

SOURCE SHALL MEET THE BACT PM AND SO2 LIMITS TO COMPLY WITH CASE BY CASE MACT FOR INORGANIC SOLID HAPS AND INORGANIC ACID HAPS. SOURCE SHALL MEET THE VOC BACT LIMIT TO COMPLY WITH MACT FOR ORGANIC HAPS.

incremental cost effectiveness: $1332/t pollutant removed Incremental cost effectiveness: $1332/t pollutant removed.

COST EFFECTIVENESS BASED ON 30 DAY AVG. VALUE.

POLLUTANT MEASUREMENT INCLUDES BACKHALF (METHOD 5 OR 5B + METHOD 202) THE NEW PM10 LIMITS INDICATED ABOVE BECAME EFFECTIVE ON AUGUST 10, 2004. PREVIOUS LIMITS WERE 36.9 LB/H AND 0.015 LB/MMBTU. THE LIMITS WERE CHANGED BASED ON STACK TEST RESULTS.

Based on testing, Roundup Power is required to determine the feasibility of changing this limit to 48.2 lb/h (0.012 lb/mmbtu) based on a rolling 24-h average

PM AND PM10 (INCL. M202 BACKHALF CATCH) PM AND PM10 (INCL. M202 BACKHALF CATCH) 10% OPACITY PM AND PM10 (INCL. M202 BACKHALF CATCH) 10% OPACITY

AREA IS IN ATTAINMENT. THIS PROJECT DID NOT TRIGGER BACT ON THIS GRANDFATHERED HOG FUEL BOILER. INCREASED UTILIZATION TRIGGERED SOME IMPACTS ANALYSIS REQUIREMENT OF PSD FOR NOX, CO, AND PM10. PM10 WAS ONLY POLLUTANT THAT EVEN CAME CLOSE TO CHALLENGING ANY

POLLUTANT LIMITS INCLUDE STARTUP / SHUTDOWN AND ATOMIZER CHANGEOUT. PERMITTEE MAY ONLY USE ACTUAL HOURS OF OPERATION WHEN DETERMINING TIME AVERAGED EMISSIONS. WHEN CONDUCTING MAINTENANCE ON CONTROL SYSTEM (ROUTINE ATOMIZER CHANGEOUT): 3491.8 POUNDS PER HOUR ON A 3-HOUR AVERAGE AND 1508.9 POUNDS PER HOUR ON A 24-HOUR AVERAGE. CONTROLLED EMISSIONS: SULFUR DIOXIDE EMISSIONS SHALL BE LIMITED TO 621 POUNDS PER HOUR AVERAGED OVER ANY CONSECUTIVE 3-HOUR PERIOD AND SULFUR DIOXIDE EMISSIONS SHALL BE LIMITED TO 589 POUNDS PER HOUR AVERAGED OVER ANY CONSECUTIVE 24-HOUR PERIOD

REGULATED POLLUTANT IS SULFURIC ACID MIST.

ADDITIONAL EMISSION LIMIT: 0.0047 LB/MMBTU

THE NEW PM10 LIMITS INDICATED ABOVE BECAME EFFECTIVE ON AUGUST 10, 2004. PREVIOUS LIMITS WERE 36.9 LB/H AND 0.015 LB/MMBTU. THE LIMITS WERE CHANGED BASED ON STACK TEST RESULTS.

Based on testing, Roundup Power is required to determine the feasibility of changing this limit to 48.2 lb/h (0.012 lb/mmbtu) based on a rolling 24-h average



THE NEW PM10 LIMITS INDICATED ABOVE BECAME EFFECTIVE ON AUGUST 10, 2004. PREVIOUS LIMITS WERE 36.9 LB/H AND 0.015 LB/MMBTU. THE LIMITS WERE CHANGED BASED ON STACK TEST RESULTS.



RBLCID FACILITY CORPORAFACILITYSAGENCYNPERMITDATE FACILITYDPROCESSSC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENT 1/5/2004 SEVEN BOAUXILIARYGA-0114 INLAND P TEMPLE INGA 10/13/2004 THIS FAC RECOVERYSC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENT 1/5/2004 SEVEN BOAUXILIARYSC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENT 1/5/2004 SEVEN BOAUXILIARYSC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENT 1/5/2004 SEVEN BOAUXILIARYSC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENT 1/5/2004 SEVEN BOAUXILIARYGA-0114 INLAND P TEMPLE INGA 10/13/2004 THIS FAC RECOVERY

PROCTYPEFUEL THRUPUT THRUPUTUPROCESSPOLLUTANCONTROLCTRLDESC11.22 NO. 2 FUE 350 MMBTU/H Beryllium P CLEAN BU11.22 NO. 2 FUE 350 MMBTU/H Carbon MoP GOOD COM11.22 FUEL OIL 227 MMBTU/H SAME AUXICarbon MoN11.22 FUEL OIL 850 mmbtu/h SEPARATECarbon MoP STAGED C11.22 NO. 2 FUE 350 MMBTU/H Nitrogen O P LOW NOX 11.22 FUEL OIL 227 MMBTU/H SAME AUXINitrogen O N11.22 NO. 2 FUE 350 MMBTU/H Particulate P COMBUSTI11.22 FUEL OIL 227 MMBTU/H SAME AUXIParticulate N11.22 NO. 2 FUE 350 MMBTU/H Sulfur DioxP COMBUSTI11.22 FUEL OIL 227 MMBTU/H SAME AUXISulfur DioxN11.22 NO. 2 FUE 350 MMBTU/H Visible EmiP GOOD COM11.22 NO. 2 FUE 350 MMBTU/H Volatile O P GOOD COM11.22 FUEL OIL 227 MMBTU/H SAME AUXIVolatile O N11.22 FUEL OIL 850 mmbtu/h SEPARATEVolatile O P STAGED C

EMISLIMITEMISLIMITEMISLIMI PCTEFFIC EMISLIMITEMISLIMITEMISLIMI STDEMISSL0.0011 LB/H

14 LB/H 0.0427.24 LB/H WITH FUEL OIL 48.23 T/YR WITH NAT 0.12

0.2 LB/MMBTU 0.242 LB/H 0.12

43.13 LB/H ON FUEL OIL 27.02 T/YR WITH NAT 0.1910.5 LB/H 0.039.08 LB/H WITH FUEL OIL 3.26 T/YR FOR NATU 0.04

21 LB/H 0.062.84 LB/H FOR FUEL OIL 0.33 T/YR FOR NATU 0.0125

20 % OPACITY 201.75 LB/H1.14 LB/H WITH FUEL OIL 1.76 T/YR WITH NATURAL GAS AND FUEL OIL0.02 LB/MMBTU

STDUNITLISTDLIMIT POLLUTANTCOMPLIANCENOTESACTUAL LIMIT IS 0.00105 LB/H

LB/MMBTU LB/MMBTUWITH FUELLIMITS ARE FOR FUEL OIL #2, EXCEPT 48.23 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS LB/MMBTU LB/MMBTU LB/MMBTUANNUAL ALIMITS FOR FUEL OIL #2, 27.02 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS LB/MMBTU LB/MMBTUWITH FUELLIMITS ARE FOR FUEL OIL, EXCEPT: 3.26 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS LB/MMBTU LB/MMBTUCALCULATADDITIONAL LIMITS FOR FUEL OIL: 0.50% BY WEIGHT. 0.33 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS % OPACITY STATE REGULATION, METHOD 9

WITH NATURAL GAS AND FUEL OIL ADDITIONAL LIMITS ARE FOR FUEL OIL: 0.005 LB/MMBTU. 1.76 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

LIMITS ARE FOR FUEL OIL #2, EXCEPT 48.23 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

LIMITS FOR FUEL OIL #2, 27.02 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

LIMITS ARE FOR FUEL OIL, EXCEPT: 3.26 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

ADDITIONAL LIMITS FOR FUEL OIL: 0.50% BY WEIGHT. 0.33 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

ADDITIONAL LIMITS ARE FOR FUEL OIL: 0.005 LB/MMBTU. 1.76 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

RBLCID FACILITY CORPORAFACILITYSAGENCYNPERMITDATE FACILITYDPROCESSTX-0481 AIR PRODAIR PROD TX TEXAS CO 11/2/2004 THIS FAC BOILER SAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI ATMOSPHEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROGEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROGEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI ATMOSPHETX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1TX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, MO-0051 PROCTOR Proctor & MO MISSOURI 1/1/1998 SANITARYTISSUE / TX-0259 FREEPORTBASF CORTX TEXAS CO 6/26/1998 CONSTRUCBOILER, BLA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T NO. 3 CTULA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T NO. 3 CTUTX-0429 VALERO REVALERO RETX TEXAS CO 2/23/2000 SITE IS A DUCT BUNM-0042 DEMING EDUKE ENENM NEW MEXI 12/29/2000 THIS FACI DB-1 & DTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMP(2) FURNACTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMP(6) FURNATX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, LA-0166 ORION REORION RELA LOUISIAN 1/10/2002 PETROLEUHEATER F-LA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOLA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLCOMBINATTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1TX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1VA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, TVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, TLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PREB RECOVLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PREB RECOVLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRPROCESS LA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRPROCESS LA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRPROCESS

LA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRPROCESS MN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDDUCT BUROH-0269 BIOMASS BIOMASS OHIO ENVIRONMENT 1/5/2004 SEVEN BOAUXILIARLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUFEED PRELA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUFEED PRENE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNI REHETX-0442 SHELL OI SHELL OI TX TEXAS CO 7/30/2004 ULTRA-LOCO BOILETX-0442 SHELL OI SHELL OI TX TEXAS CO 7/30/2004 ULTRA-LOCO BOILETX-0481 AIR PRODAIR PROD TX TEXAS CO 11/2/2004 THIS FAC BOILER SAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI STEAM BOIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI STEAM BOIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI ATMOSPHEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROGEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI ATMOSPHEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROGEWA-0301 BP CHERRBRITISH WA WASHINGT 4/20/2005 BRITISH BOILER, TX-0478 CITGO COCITGO RE TX TEXAS CO 4/20/2005 DHT STRITX-0478 CITGO COCITGO RE TX TEXAS CO 4/20/2005 NO.3 BOILTX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C AJAX DPCTX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C 3 AJAX DTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISLA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 DUCT BUR*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMA & B CRU*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMHYDROGEN*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMPLATFORME*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMBOILER NO.*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMA & B CRU*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMHYDROGEN*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMPLATFORME*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMBOILER NO.*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILER 401*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUHEATERS 20*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILERS B-*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILER 401*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILERS B-*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUHEATERS 20*MS-0086 CHEVRON CHEVRONMS MISSISSIP 5/8/2007 PETROLEUFOUR PLAIA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSNATURAL GWI-0245 WPSC - WWPSC - W WI WISCONSI 6/1/2007 BOILER B2

WI-0245 WPSC - WWPSC - W WI WISCONSI 6/1/2007 PROCESS BVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, TVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER DUCT BUOR-0039 COB ENERGPeoples EnOR OREGON D 12/30/2003 POWER GEDUCT BURMO-0051 PROCTOR Proctor & MO MISSOURI 1/1/1998 SANITARYTISSUE / TX-0259 FREEPORTBASF CORTX TEXAS CO 6/26/1998 CONSTRUCBOILER, BLA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T NO. 3 CTULA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T NO. 3 CTUTX-0429 VALERO REVALERO RETX TEXAS CO 2/23/2000 SITE IS A DUCT BUNM-0042 DEMING EDUKE ENENM NEW MEXI 12/29/2000 THIS FACI DB-1 & DTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPCOMBINED TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMP(2) FURNACTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMP(6) FURNATX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, LA-0166 ORION REORION RELA LOUISIAN 1/10/2002 PETROLEUHEATER F-LA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOLA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLCOMBINATTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1TX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1VA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, TMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDDUCT BUROH-0269 BIOMASS BIOMASS OHIO ENVIRONMENT 1/5/2004 SEVEN BOAUXILIARNE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNI REHETX-0481 AIR PRODAIR PROD TX TEXAS CO 11/2/2004 THIS FAC BOILER STX-0481 AIR PRODAIR PROD TX TEXAS CO 11/2/2004 THIS FAC BOILER STAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI STEAM BOIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI STEAM BOIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI ATMOSPHEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROGEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI ATMOSPHEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROGEWA-0301 BP CHERRBRITISH WA WASHINGT 4/20/2005 BRITISH BOILER,

TX-0478 CITGO COCITGO RE TX TEXAS CO 4/20/2005 DHT STRITX-0478 CITGO COCITGO RE TX TEXAS CO 4/20/2005 NO.3 BOILTX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C AJAX DPCTX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C 3 AJAX DTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISLA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 DUCT BUR*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMA & B CRU*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMHYDROGEN*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMPLATFORME*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMBOILER NO.*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMA & B CRU*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMHYDROGEN*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMPLATFORME*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMBOILER NO.*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUHEATERS 20*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILERS B-*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILERS B-*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUHEATERS 20*MS-0086 CHEVRON CHEVRONMS MISSISSIP 5/8/2007 PETROLEUFOUR PLAIA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSNATURAL GTX-0259 FREEPORTBASF CORTX TEXAS CO 6/26/1998 CONSTRUCBOILER, BLA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T NO. 3 CTULA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T NO. 3 CTUTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMP(2) FURNACTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMP(6) FURNALA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOLA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLCOMBINATTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1TX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1VA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER DUCT BUMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDDUCT BUROR-0039 COB ENERGPeoples EnOR OREGON D 12/30/2003 POWER GEDUCT BURTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSIS

TX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISIA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSNATURAL GLA-0128 CONVENT MOTIVA E LA LOUISIAN 8/12/1999 PETROLEUVPS1 ATMLA-0128 CONVENT MOTIVA E LA LOUISIAN 8/12/1999 PETROLEUVPS2 ATMLA-0128 CONVENT MOTIVA E LA LOUISIAN 8/12/1999 PETROLEUVPS1 ATMLA-0128 CONVENT MOTIVA E LA LOUISIAN 8/12/1999 PETROLEUVPS2 ATMNM-0042 DEMING EDUKE ENENM NEW MEXI 12/29/2000 THIS FACI DB-1 & DTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, LA-0166 ORION REORION RELA LOUISIAN 1/10/2002 PETROLEUHEATER F-LA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOLA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLCOMBINATVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, TVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, TLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PREB RECOVLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PREB RECOVLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRPROCESS LA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRPROCESS LA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRPROCESS LA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRPROCESS MN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDDUCT BUROH-0269 BIOMASS BIOMASS OHIO ENVIRONMENT 1/5/2004 SEVEN BOAUXILIARLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUFEED PRELA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUFEED PRETX-0481 AIR PRODAIR PROD TX TEXAS CO 11/2/2004 THIS FAC BOILER SAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI ATMOSPHEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROGEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI ATMOSPHEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROGETX-0478 CITGO COCITGO RE TX TEXAS CO 4/20/2005 DHT STRITX-0478 CITGO COCITGO RE TX TEXAS CO 4/20/2005 NO.3 BOILTX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C AJAX DPCTX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C 3 AJAX DTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISLA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 DUCT BUR*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMA & B CRU*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMHYDROGEN*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMPLATFORME*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMBOILER NO.*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMA & B CRU*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMHYDROGEN*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMPLATFORME

*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMBOILER NO.*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUHEATERS 20*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILERS B-*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILERS B-*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUHEATERS 20IA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSNATURAL GTX-0259 FREEPORTBASF CORTX TEXAS CO 6/26/1998 CONSTRUCBOILER, BLA-0149 LOUISIANAMARATHONLA LOUISIAN 10/21/1999 MARATHONCRUDE HELA-0149 LOUISIANAMARATHONLA LOUISIAN 10/21/1999 MARATHONHF ALKYLLA-0149 LOUISIANAMARATHONLA LOUISIAN 10/21/1999 MARATHONBOILER NOLA-0149 LOUISIANAMARATHONLA LOUISIAN 10/21/1999 MARATHONCRUDE HELA-0149 LOUISIANAMARATHONLA LOUISIAN 10/21/1999 MARATHONHF ALKYLLA-0149 LOUISIANAMARATHONLA LOUISIAN 10/21/1999 MARATHONBOILER NOTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMP(2) FURNACTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMP(6) FURNATX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, LA-0166 ORION REORION RELA LOUISIAN 1/10/2002 PETROLEUHEATER F-LA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOLA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLCOMBINATTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1TX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1VA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, TVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, TVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER DUCT BUMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDDUCT BUROR-0039 COB ENERGPeoples EnOR OREGON D 12/30/2003 POWER GEDUCT BUROH-0269 BIOMASS BIOMASS OHIO ENVIRONMENT 1/5/2004 SEVEN BOAUXILIARLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUFEED PRELA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUFEED PRENE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNI REHETX-0442 SHELL OI SHELL OI TX TEXAS CO 7/30/2004 ULTRA-LOCO BOILETX-0442 SHELL OI SHELL OI TX TEXAS CO 7/30/2004 ULTRA-LOCO BOILETX-0481 AIR PRODAIR PROD TX TEXAS CO 11/2/2004 THIS FAC BOILER SAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI ATMOSPHE

AZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROGEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI ATMOSPHEAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROGETX-0478 CITGO COCITGO RE TX TEXAS CO 4/20/2005 DHT STRITX-0478 CITGO COCITGO RE TX TEXAS CO 4/20/2005 NO.3 BOILTX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C AJAX DPCTX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C 3 AJAX DTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISLA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 DUCT BUR*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMA & B CRU*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMHYDROGEN*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMPLATFORME*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMBOILER NO.*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMA & B CRU*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMHYDROGEN*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMPLATFORME*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMBOILER NO.*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUHEATERS 20*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILERS B-*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILERS B-*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUHEATERS 20IA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSNATURAL GLA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOLA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLCOMBINATMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDDUCT BURLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUFEED PRELA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUFEED PRELA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 DUCT BURTX-0259 FREEPORTBASF CORTX TEXAS CO 6/26/1998 CONSTRUCBOILER, BSC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, TX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1TX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1OR-0039 COB ENERGPeoples EnOR OREGON D 12/30/2003 POWER GEDUCT BURIA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSNATURAL GTX-0259 FREEPORTBASF CORTX TEXAS CO 6/26/1998 CONSTRUCBOILER, BNM-0042 DEMING EDUKE ENENM NEW MEXI 12/29/2000 THIS FACI DB-1 & DTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE

TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMP(2) FURNACTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE TX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMP(6) FURNATX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICBOILERS, LA-0166 ORION REORION RELA LOUISIAN 1/10/2002 PETROLEUHEATER F-TX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1TX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO 3/14/2002 LYONDELLBOILERS 1VA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, TVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, TMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDDUCT BUROH-0269 BIOMASS BIOMASS OHIO ENVIRONMENT 1/5/2004 SEVEN BOAUXILIARNE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNI REHETX-0481 AIR PRODAIR PROD TX TEXAS CO 11/2/2004 THIS FAC BOILER STX-0478 CITGO COCITGO RE TX TEXAS CO 4/20/2005 DHT STRITX-0478 CITGO COCITGO RE TX TEXAS CO 4/20/2005 NO.3 BOILTX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C AJAX DPCTX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C 3 AJAX DTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSISLA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 DUCT BUR*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMA & B CRU*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMHYDROGEN*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMPLATFORME*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMBOILER NO.*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMA & B CRU*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMHYDROGEN*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMPLATFORME*LA-0211 GARYVILLMARATHONLA LOUISIAN 12/27/2006 PETROLEUMBOILER NO.*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUHEATERS 20*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILERS B-*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUBOILERS B-*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUHEATERS 20IA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSNATURAL G

PROCTYPEFUEL THRUPUT THRUPUTUPROCESSPOLLUTANCONTROLCTRLDESC11.39 NATURAL GAS CO EMISSAmmonia ( N11.39 NATURAL 346 MMBTU/H THIS UNITAmmonia ( N11.39 REFINERY 311 MMBTU/H THIS EQUIAmmonia ( N11.39 REFINERY 328 MMBTU/H THIS EQUIAmmonia ( N11.39 REFINERY 1435 MMBTU/H EQUIPMENTAmmonia ( N11.39 REFINERY 311 MMBTU/H THIS EQUIAmmonia ( N11.39 REFINERY 328 MMBTU/H THIS EQUIAmmonia ( N11.39 REFINERY 1435 MMBTU/H EQUIPMENTAmmonia ( N11.39 NATURAL 346 MMBTU/H THIS UNITAmmonia ( N11.39 366.83 MMBTU/H EMISSION Benzene N NONE IND11.39 PETRO RE 586 MMBTU/H BOTH BOI Benzene N NONE IND11.39 366.83 MMBTU/H EMISSION Benzene N NONE IND11.39 PETRO RE 586 MMBTU/H BOTH BOI Benzene N NONE IND11.31 NATURAL 350 MMBTU/H (EACH) Beryllium P COMBUSTI11.31 2286.4 MMCF/YR ADDITION Carbon MoP LOW NOX 11.39 H2-WASTE 325 MMBTU/H Carbon MoN NONE IND11.39 FUEL GAS 264 MMBTU/H Carbon MoP DESIGN A11.39 FUEL GAS 264 MMBTU/H Carbon MoP DESIGN A11.39 NATURAL 251 mmbtu/h FRESH AI Carbon MoN11.31 NATURAL 517 MMBTU/H DB-1 AND Carbon MoP GOOD COM11.39 ETHANE 350 MMBTU/H FEEDSTOCCarbon MoN NONE IND11.39 ETHANE 339 MMBTU/H 280 MMBTCarbon MoN NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCCarbon MoN NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCCarbon MoN NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCCarbon MoN NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCCarbon MoN NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCCarbon MoN NONE IND11.39 ETHANE 341 MMBTU/H,299 MMBTCarbon MoN NONE IND11.39 ETHANE 300 MMBTU/H FEEDSTOCCarbon MoN NONE IND11.39 ETHANE 300 MMBTU/H 265 MMBTCarbon MoN NONE IND11.39 ETHANE 333 MMBTU/H FEEDSTOCCarbon MoN NONE IND11.39 ETHANE 502 MMBTU/H 481 MMBUCarbon MoN NONE IND11.31 NATURAL 350 MMBTU/H (EACH) Carbon MoP GOOD COM11.39 REFINERY 528 MMBTU/H Carbon MoP GOOD DES11.31 NATURAL 987 MMBTU/H EMISSION Carbon MoP GOOD EQU

11.9 WOOD WAS 459.5 MMBTU/H EMISSIONCarbon MoP GOOD EQU11.39 366.83 MMBTU/H EMISSION Carbon MoN NONE IND11.39 PETRO RE 586 MMBTU/H BOTH BOI Carbon MoP GOOD COM11.39 366.83 MMBTU/H EMISSION Carbon MoN NONE IND11.39 PETRO RE 586 MMBTU/H BOTH BOI Carbon MoP GOOD COM11.31 NATURAL 1150 MMBTU/H TangentiallCarbon MoP GOOD COM11.31 NATURAL 2350 MMBTU/H TangentiallCarbon MoP GOOD COM11.31 269.3 MMBTU/H Carbon MoP GOOD COM11.31 269.3 MMBTU/H Carbon MoP GOOD COM11.39 PROCESS 298.9 MMBTU/H 194.9 MM Carbon MoP GOOD COM11.39 PROCESS 280 MMBTU/H 166.0 MM Carbon MoP GOOD COM11.39 PROCESS 298.9 MMBTU/H 194.9 MM Carbon MoP GOOD COM

11.39 PROCESS 280 MMBTU/H 166.0 MM Carbon MoP GOOD COM11.31 NATURAL 800 MMBTU/H RESTRICTCarbon MoA OXIDATIO11.31 NATURAL 247 MMBTU/H Carbon MoN11.39 PIPESTILLCarbon MoP GOOD ENG11.39 352 MMBTU/H THROUGHPCarbon MoP GOOD ENG11.39 PIPESTILLCarbon MoP GOOD ENG11.39 352 MMBTU/H THROUGHPCarbon MoP GOOD ENG11.31 NATURAL 133 MMBTU/H Carbon MoN11.39 CARBON MONOXIDE Carbon MoN11.39 CARBON MONOXIDE Carbon MoN11.39 NATURAL GAS CO EMISSCarbon MoN11.31 NATURAL 419 MMBTU/H EQUIPMENTCarbon MoN11.31 NATURAL 419 MMBTU/H EQUIPMENTCarbon MoN11.39 NATURAL 346 MMBTU/H THIS UNITCarbon MoN11.39 REFINERY 311 MMBTU/H THIS EQUICarbon MoN11.39 REFINERY 328 MMBTU/H THIS EQUICarbon MoN11.39 REFINERY 1435 MMBTU/H EQUIPMENTCarbon MoN11.39 NATURAL 346 MMBTU/H THIS UNITCarbon MoN11.39 REFINERY 311 MMBTU/H THIS EQUICarbon MoN11.39 REFINERY 328 MMBTU/H THIS EQUICarbon MoN11.39 REFINERY 1435 MMBTU/H EQUIPMENTCarbon MoN11.31 NATURAL 363 MMBTU/H Carbon MoP GOOD COM11.39 REFINERY FUEL GAS THE MDH Carbon MoN11.39 REFINERY 99 MMBTU/H UTILITY Carbon MoN11.39 GAS 0.75 LTPD Carbon MoN11.39 0.75 LTPD Carbon MoN11.39 FUEL GAS 250 MMBtu/h EMISSIONCarbon MoN11.39 FUEL GAS 250 mmbtu/h Carbon MoN11.39 FUEL GAS 250 MMBTU/h Carbon MoN11.39 250 MMBTU/H Carbon MoN11.31 759 MMBTU/H Carbon MoB CO OXIDA11.39 REFINERY FUEL GAS 1-08: 368. Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 PURGE G 1412.5 MMBTU/H AVG. HEATCarbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 7A-08: 47 Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY 525.7 MMBTU/H Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 1-08: 368. Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 PURGE G 1412.5 MMBTU/H AVG. HEATCarbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 7A-08: 47 Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY 525.7 MMBTU/H Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY 525 MM BTU/HBOILER A Carbon MoP PROPER E11.39 REFINERY FUEL GAS 2004-7: 8 Carbon MoP PROPER E11.39 REFINERY 461 MM BTU/H SOURCES Carbon MoP PROPER E11.39 REFINERY 525 MM BTU/HBOILER A Carbon MoP PROPER E11.39 REFINERY 461 MM BTU/H SOURCES Carbon MoP PROPER E11.39 REFINERY FUEL GAS 2004-7: 8 Carbon MoP PROPER E11.39 REFINERY 850 MMBTU/H Carbon MoN11.31 NATURAL 292.5 MMBTU/H THE PROJECarbon MoB ADVANCES11.31 NATURAL GAS Lead (Pb) P FIRING N

11.31 NATURAL GAS Lead (Pb) P USE OF N11.31 NATURAL 2350 MMBTU/H TangentiallNitrogen D P LOW NITR11.31 NATURAL 385 MMBTU/H DUCT BURNitrogen D N11.31 NATURAL 654 MMBTU/H ThroughputNitrogen D B DLN COMB11.31 2286.4 MMCF/YR ADDITION Nitrogen O P LOW NOX 11.39 H2-WASTE 325 MMBTU/H Nitrogen O N NONE IND11.39 FUEL GAS 264 MMBTU/H Nitrogen O P ULTRA LO11.39 FUEL GAS 264 MMBTU/H Nitrogen O P ULTRA LO11.39 NATURAL 251 mmbtu/h FRESH AI Nitrogen O N11.31 NATURAL 517 MMBTU/H DB-1 AND Nitrogen O P SELECTIV11.39 THE BURNINitrogen O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCNitrogen O N NONE IND11.39 ETHANE 339 MMBTU/H 280 MMBTNitrogen O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCNitrogen O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCNitrogen O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCNitrogen O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCNitrogen O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCNitrogen O N NONE IND11.39 ETHANE 341 MMBTU/H,299 MMBTNitrogen O N NONE IND11.39 ETHANE 300 MMBTU/H FEEDSTOCNitrogen O N NONE IND11.39 ETHANE 300 MMBTU/H 265 MMBTNitrogen O N NONE IND11.39 ETHANE 333 MMBTU/H FEEDSTOCNitrogen O N NONE IND11.39 ETHANE 502 MMBTU/H 481 MMBUNitrogen O B LOW NOX 11.31 NATURAL 350 MMBTU/H (EACH) Nitrogen O P LOW NOX 11.39 REFINERY 528 MMBTU/H Nitrogen O P LOW NOX 11.31 NATURAL 987 MMBTU/H EMISSION Nitrogen O P LOW-NOX

11.9 WOOD WAS 459.5 MMBTU/H EMISSIONNitrogen O P LOW-NOX11.39 366.83 MMBTU/H EMISSION Nitrogen O N11.39 PETRO RE 586 MMBTU/H BOTH BOI Nitrogen O N11.39 366.83 MMBTU/H EMISSION Nitrogen O N11.39 PETRO RE 586 MMBTU/H BOTH BOI Nitrogen O N11.31 NATURAL 1150 MMBTU/H TangentiallNitrogen O P LOW NOX 11.31 NATURAL 800 MMBTU/H RESTRICTNitrogen O A SCR11.31 NATURAL 247 MMBTU/H Nitrogen O N11.31 NATURAL 133 MMBTU/H Nitrogen O A ULTRA-LO11.39 NATURAL GAS CO EMISSNitrogen O N11.39 Nitrogen O N11.31 NATURAL 419 MMBTU/H EQUIPMENTNitrogen O P LOW NOX 11.31 NATURAL 419 MMBTU/H EQUIPMENTNitrogen O P LOW NOX 11.39 NATURAL 346 MMBTU/H THIS UNITNitrogen O A LOW NOX 11.39 REFINERY 311 MMBTU/H THIS EQUINitrogen O B LOW NOX 11.39 REFINERY 328 MMBTU/H THIS EQUINitrogen O B LOW NOX 11.39 REFINERY 1435 MMBTU/H EQUIPMENTNitrogen O B LOW NOX 11.39 NATURAL 346 MMBTU/H THIS UNITNitrogen O A LOW NOX 11.39 REFINERY 311 MMBTU/H THIS EQUINitrogen O B LOW NOX 11.39 REFINERY 328 MMBTU/H THIS EQUINitrogen O B LOW NOX 11.39 REFINERY 1435 MMBTU/H EQUIPMENTNitrogen O B LOW NOX 11.31 NATURAL 363 MMBTU/H Nitrogen O P ULNB + F

11.39 REFINERY FUEL GAS THE MDH Nitrogen O A LOW NOX 11.39 REFINERY 99 MMBTU/H UTILITY Nitrogen O N11.39 GAS 0.75 LTPD Nitrogen O N11.39 0.75 LTPD Nitrogen O N11.39 FUEL GAS 250 MMBtu/h EMISSIONNitrogen O B THE PYRO11.39 FUEL GAS 250 mmbtu/h Nitrogen O B THE PYRO11.39 FUEL GAS 250 MMBTU/h Nitrogen O B THE PYRO11.39 250 MMBTU/H Nitrogen O B THE PYRO11.31 759 MMBTU/H Nitrogen O B LOW NOX 11.39 REFINERY FUEL GAS 1-08: 368. Nitrogen O B ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC11.39 PURGE G 1412.5 MMBTU/H AVG. HEATNitrogen O B ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC11.39 REFINERY FUEL GAS 7A-08: 47 Nitrogen O P ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT11.39 REFINERY 525.7 MMBTU/H Nitrogen O P ULTRA LOW NOX BURNERS (ULNB) & FLUE GAS RECIRCULATION (FGR)11.39 REFINERY FUEL GAS 1-08: 368. Nitrogen O B ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC11.39 PURGE G 1412.5 MMBTU/H AVG. HEATNitrogen O B ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC11.39 REFINERY FUEL GAS 7A-08: 47 Nitrogen O P ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT11.39 REFINERY 525.7 MMBTU/H Nitrogen O P ULTRA LOW NOX BURNERS (ULNB) & FLUE GAS RECIRCULATION (FGR)11.39 REFINERY FUEL GAS 2004-7: 8 Nitrogen O P ULTRA LO11.39 REFINERY 461 MM BTU/H SOURCES Nitrogen O P LOW NOX 11.39 REFINERY 461 MM BTU/H SOURCES Nitrogen O P LOW NOX 11.39 REFINERY FUEL GAS 2004-7: 8 Nitrogen O P ULTRA LO11.39 REFINERY 850 MMBTU/H Nitrogen O P ULTRA LO11.31 NATURAL 292.5 MMBTU/H THE PROJENitrogen O B ADVANCED11.39 H2-WASTE 325 MMBTU/H Particulate P GOOD COM11.39 FUEL GAS 264 MMBTU/H Particulate P DESIGN, 11.39 FUEL GAS 264 MMBTU/H Particulate P DESIGN, 11.39 ETHANE 350 MMBTU/H FEEDSTOCParticulate N NONE IND11.39 ETHANE 339 MMBTU/H 280 MMBTParticulate N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCParticulate N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCParticulate N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCParticulate N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCParticulate N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCParticulate N NONE IND11.39 ETHANE 341 MMBTU/H,299 MMBTParticulate N NONE IND11.39 ETHANE 300 MMBTU/H FEEDSTOCParticulate N NONE IND11.39 ETHANE 300 MMBTU/H 265 MMBTParticulate N NONE IND11.39 ETHANE 333 MMBTU/H FEEDSTOCParticulate N NONE IND11.31 NATURAL 987 MMBTU/H EMISSION Particulate P FUELED B

11.9 WOOD WAS 459.5 MMBTU/H EMISSIONParticulate A WET SCRU11.39 366.83 MMBTU/H EMISSION Particulate P LOW S FUE11.39 PETRO RE 586 MMBTU/H BOTH BOI Particulate P LOW S FUE11.39 366.83 MMBTU/H EMISSION Particulate P LOW S FUE11.39 PETRO RE 586 MMBTU/H BOTH BOI Particulate P LOW S FUE11.31 NATURAL 385 MMBTU/H DUCT BURParticulate N11.31 NATURAL 800 MMBTU/H RESTRICTParticulate P CLEAN FU11.31 NATURAL 654 MMBTU/H ThroughputParticulate P CLEAN FU11.39 FUEL GAS 250 mmbtu/h Particulate N11.39 FUEL GAS 250 MMBTU/h Particulate N

11.39 250 MMBTU/H Particulate N11.31 NATURAL 292.5 MMBTU/H THE PROJEParticulate P NATURAL 11.39 REFINERY 263.6 MMBTU/H EMISSION Particulate P GOOD COM11.39 REFINERY 361 MMBTU/H EMISSION Particulate P GOOD COM11.39 REFINERY 263.6 MMBTU/H EMISSION Particulate P GOOD COM11.39 REFINERY 361 MMBTU/H EMISSION Particulate P GOOD COM11.31 NATURAL 517 MMBTU/H DB-1 AND Particulate P NATURAL 11.39 ETHANE 502 MMBTU/H 481 MMBUParticulate N NONE IND11.31 NATURAL 350 MMBTU/H (EACH) Particulate P CLEAN BU11.39 REFINERY 528 MMBTU/H Particulate P BURNING 11.31 NATURAL 987 MMBTU/H EMISSION Particulate P FUELED B

11.9 WOOD WAS 459.5 MMBTU/H EMISSIONParticulate A WET SCRU11.31 NATURAL 1150 MMBTU/H TangentiallParticulate P CLEAN FU11.31 NATURAL 2350 MMBTU/H TangentiallParticulate P CLEAN FU11.31 269.3 MMBTU/H Particulate P USE OF C11.31 269.3 MMBTU/H Particulate P USE OF C11.39 PROCESS 298.9 MMBTU/H 194.9 MM Particulate P USE OF C11.39 PROCESS 280 MMBTU/H 166.0 MM Particulate P USE OF C11.39 PROCESS 298.9 MMBTU/H 194.9 MM Particulate P USE OF C11.39 PROCESS 280 MMBTU/H 166.0 MM Particulate P USE OF C11.31 NATURAL 800 MMBTU/H RESTRICTParticulate P CLEAN FU11.31 NATURAL 247 MMBTU/H Particulate N11.39 PIPESTILLParticulate P GOOD ENG11.39 352 MMBTU/H THROUGHPParticulate P GOOD ENG11.39 PIPESTILLParticulate P GOOD ENG11.39 352 MMBTU/H THROUGHPParticulate P GOOD ENG11.39 NATURAL GAS CO EMISSParticulate N11.39 NATURAL 346 MMBTU/H THIS UNITParticulate N GOOD COM11.39 REFINERY 311 MMBTU/H THIS EQUIParticulate N11.39 REFINERY 328 MMBTU/H THIS EQUIParticulate N11.39 REFINERY 1435 MMBTU/H EQUIPMENTParticulate N11.39 NATURAL 346 MMBTU/H THIS UNITParticulate N GOOD COM11.39 REFINERY 311 MMBTU/H THIS EQUIParticulate N11.39 REFINERY 328 MMBTU/H THIS EQUIParticulate N11.39 REFINERY 1435 MMBTU/H EQUIPMENTParticulate N11.39 REFINERY FUEL GAS THE MDH Particulate N11.39 REFINERY 99 MMBTU/H UTILITY Particulate N11.39 GAS 0.75 LTPD Particulate N11.39 0.75 LTPD Particulate N11.39 FUEL GAS 250 MMBtu/h EMISSIONParticulate N11.31 759 MMBTU/H Particulate P USE OF C11.39 REFINERY FUEL GAS 1-08: 368. Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 PURGE G 1412.5 MMBTU/H AVG. HEATParticulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 7A-08: 47 Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY 525.7 MMBTU/H Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 1-08: 368. Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 PURGE G 1412.5 MMBTU/H AVG. HEATParticulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 7A-08: 47 Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES

11.39 REFINERY 525.7 MMBTU/H Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 2004-7: 8 Particulate P PROPER E11.39 REFINERY 461 MM BTU/H SOURCES Particulate P PROPER E11.39 REFINERY 461 MM BTU/H SOURCES Particulate P PROPER E11.39 REFINERY FUEL GAS 2004-7: 8 Particulate P PROPER E11.31 NATURAL 292.5 MMBTU/H THE PROJEParticulate P NATURAL 11.39 H2-WASTE 325 MMBTU/H Sulfur DioxP GOOD COM11.39 NAT & RE 281.1 MMBTU/H THE PERMSulfur DioxP LOW SULF11.39 NAT & RE 268.6 MMBTU/H THE PERMSulfur DioxP LOW SULF11.39 NAT & RE 350 MMBTU/H THE AFFE Sulfur DioxP USE OF L11.39 NAT & RE 281.1 MMBTU/H THE PERMSulfur DioxP LOW SULF11.39 NAT & RE 268.6 MMBTU/H THE PERMSulfur DioxP LOW SULF11.39 NAT & RE 350 MMBTU/H THE AFFE Sulfur DioxP USE OF L11.39 ETHANE 350 MMBTU/H FEEDSTOCSulfur DioxN NONE IND11.39 ETHANE 339 MMBTU/H 280 MMBTSulfur DioxN NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCSulfur DioxN NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCSulfur DioxN NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCSulfur DioxN NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCSulfur DioxN NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCSulfur DioxN NONE IND11.39 ETHANE 341 MMBTU/H,299 MMBTSulfur DioxN NONE IND11.39 ETHANE 300 MMBTU/H FEEDSTOCSulfur DioxN NONE IND11.39 ETHANE 300 MMBTU/H 265 MMBTSulfur DioxN NONE IND11.39 ETHANE 333 MMBTU/H FEEDSTOCSulfur DioxN NONE IND11.39 ETHANE 502 MMBTU/H 481 MMBUSulfur DioxN NONE IND11.31 NATURAL 350 MMBTU/H (EACH) Sulfur DioxP LOW SULF11.39 REFINERY 528 MMBTU/H Sulfur DioxP LOW SULF11.31 NATURAL 987 MMBTU/H EMISSION Sulfur DioxP FUELED B

11.9 WOOD WAS 459.5 MMBTU/H EMISSIONSulfur DioxB ADD-ON: 11.39 366.83 MMBTU/H EMISSION Sulfur DioxP LOW S FUE11.39 PETRO RE 586 MMBTU/H BOTH BOI Sulfur DioxP LOW S FUE11.39 366.83 MMBTU/H EMISSION Sulfur DioxP LOW S FUE11.39 PETRO RE 586 MMBTU/H BOTH BOI Sulfur DioxP LOW S FUE11.31 NATURAL 1150 MMBTU/H TangentiallSulfur DioxP LOW SULF11.31 NATURAL 2350 MMBTU/H TangentiallSulfur DioxP LOW SULF11.31 NATURAL 385 MMBTU/H DUCT BURSulfur DioxN11.31 NATURAL 800 MMBTU/H RESTRICTSulfur DioxP LOW SULF11.31 NATURAL 654 MMBTU/H ThroughputSulfur DioxP CLEAN FU11.31 NATURAL 247 MMBTU/H Sulfur DioxN11.39 PIPESTILLSulfur DioxP LIMIT CON11.39 352 MMBTU/H THROUGHPSulfur DioxP LIMIT CON11.39 PIPESTILLSulfur DioxP LIMIT CON11.39 352 MMBTU/H THROUGHPSulfur DioxP LIMIT CON11.31 NATURAL 133 MMBTU/H Sulfur DioxN11.39 CARBON MONOXIDE Sulfur DioxN11.39 CARBON MONOXIDE Sulfur DioxN11.39 NATURAL GAS CO EMISSSulfur DioxN11.39 NATURAL 346 MMBTU/H THIS UNITSulfur DioxP 35 PPM SU

11.39 REFINERY 311 MMBTU/H THIS EQUISulfur DioxP 35 PPM SU11.39 REFINERY 328 MMBTU/H THIS EQUISulfur DioxP SULFUR LI11.39 REFINERY 1435 MMBTU/H EQUIPMENTSulfur DioxP S LIMITED11.39 NATURAL 346 MMBTU/H THIS UNITSulfur DioxP 35 PPM SU11.39 REFINERY 311 MMBTU/H THIS EQUISulfur DioxP 35 PPM SU11.39 REFINERY 328 MMBTU/H THIS EQUISulfur DioxP SULFUR LI11.39 REFINERY 1435 MMBTU/H EQUIPMENTSulfur DioxP S LIMITED11.39 REFINERY FUEL GAS THE MDH Sulfur DioxN11.39 REFINERY 99 MMBTU/H UTILITY Sulfur DioxN11.39 GAS 0.75 LTPD Sulfur DioxP LOWERED11.39 0.75 LTPD Sulfur DioxP LOWER T11.39 FUEL GAS 250 MMBtu/h EMISSIONSulfur DioxN11.39 FUEL GAS 250 mmbtu/h Sulfur DioxN11.39 FUEL GAS 250 MMBTU/h Sulfur DioxN11.39 250 MMBTU/H Sulfur DioxN11.31 759 MMBTU/H Sulfur DioxP USE OF LO11.39 REFINERY FUEL GAS 1-08: 368. Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS11.39 PURGE G 1412.5 MMBTU/H AVG. HEATSulfur DioxN USE OF LOW SULFUR FUEL GAS11.39 REFINERY FUEL GAS 7A-08: 47 Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS11.39 REFINERY 525.7 MMBTU/H Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS11.39 REFINERY FUEL GAS 1-08: 368. Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS11.39 PURGE G 1412.5 MMBTU/H AVG. HEATSulfur DioxN USE OF LOW SULFUR FUEL GAS11.39 REFINERY FUEL GAS 7A-08: 47 Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS11.39 REFINERY 525.7 MMBTU/H Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS11.39 REFINERY FUEL GAS 2004-7: 8 Sulfur DioxN USE OF PIPELINE QUALITY N11.39 REFINERY 461 MM BTU/H SOURCES Sulfur DioxN USE OF P11.39 REFINERY 461 MM BTU/H SOURCES Sulfur DioxN USE OF P11.39 REFINERY FUEL GAS 2004-7: 8 Sulfur DioxN USE OF PIPELINE QUALITY N11.31 NATURAL 292.5 MMBTU/H THE PROJESulfur DioxP NATURAL 11.31 NATURAL 987 MMBTU/H EMISSION Sulfur, To N

11.9 WOOD WAS 459.5 MMBTU/H EMISSIONSulfur, To N11.31 NATURAL 800 MMBTU/H RESTRICTSulfuric AciP LOW SULF11.39 PIPESTILLSulfuric AciP LIMIT CONCENTRATION OF H2S 11.39 352 MMBTU/H THROUGHPSulfuric AciP LIMIT CONCENTRATION OF H2S 11.39 PIPESTILLSulfuric AciP LIMIT CONCENTRATION OF H2S 11.39 352 MMBTU/H THROUGHPSulfuric AciP LIMIT CONCENTRATION OF H2S 11.31 759 MMBTU/H Sulfuric AciP USE OF LO11.39 H2-WASTE 325 MMBTU/H Visible EmiN NONE IND11.31 NATURAL 350 MMBTU/H (EACH) Visible EmiP GOOD COM11.39 366.83 MMBTU/H EMISSION Visible EmiN NONE IND11.39 PETRO RE 586 MMBTU/H BOTH BOI Visible EmiN NONE IND11.39 366.83 MMBTU/H EMISSION Visible EmiN NONE IND11.39 PETRO RE 586 MMBTU/H BOTH BOI Visible EmiN NONE IND11.31 NATURAL 654 MMBTU/H ThroughputVisible EmiN11.31 NATURAL 292.5 MMBTU/H THE PROJEVisible EmiP NATURAL 11.39 H2-WASTE 325 MMBTU/H Volatile O P GOOD CO11.31 NATURAL 517 MMBTU/H DB-1 AND Volatile O P GOOD COM11.39 ETHANE 350 MMBTU/H FEEDSTOCVolatile O N NONE IND

11.39 ETHANE 339 MMBTU/H 280 MMBTVolatile O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCVolatile O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCVolatile O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCVolatile O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCVolatile O N NONE IND11.39 ETHANE 350 MMBTU/H FEEDSTOCVolatile O N NONE IND11.39 ETHANE 341 MMBTU/H,299 MMBTVolatile O N NONE IND11.39 ETHANE 300 MMBTU/H FEEDSTOCVolatile O N NONE IND11.39 ETHANE 300 MMBTU/H 265 MMBTVolatile O N NONE IND11.39 ETHANE 333 MMBTU/H FEEDSTOCVolatile O N NONE IND11.39 ETHANE 502 MMBTU/H 481 MMBUVolatile O N NONE IND11.31 NATURAL 350 MMBTU/H (EACH) Volatile O P GOOD COM11.39 REFINERY 528 MMBTU/H Volatile O N NONE IND11.39 366.83 MMBTU/H EMISSION Volatile O N11.39 PETRO RE 586 MMBTU/H BOTH BOI Volatile O N NONE IND11.39 366.83 MMBTU/H EMISSION Volatile O N11.39 PETRO RE 586 MMBTU/H BOTH BOI Volatile O N NONE IND11.31 NATURAL 1150 MMBTU/H TangentiallVolatile O P GOOD COM11.31 NATURAL 2350 MMBTU/H TangentiallVolatile O P GOOD COM11.31 NATURAL 800 MMBTU/H RESTRICTVolatile O A OXIDATIO11.31 NATURAL 247 MMBTU/H Volatile O N11.31 NATURAL 133 MMBTU/H Volatile O N11.39 NATURAL GAS CO EMISSVolatile O N11.39 REFINERY FUEL GAS THE MDH Volatile O N11.39 REFINERY 99 MMBTU/H UTILITY Volatile O N11.39 GAS 0.75 LTPD Volatile O N11.39 0.75 LTPD Volatile O N11.39 FUEL GAS 250 MMBtu/h EMISSIONVolatile O N11.39 FUEL GAS 250 mmbtu/h Volatile O N11.39 FUEL GAS 250 MMBTU/h Volatile O N11.39 250 MMBTU/H Volatile O N11.31 759 MMBTU/H Volatile O B CO OXIDA11.39 REFINERY FUEL GAS 1-08: 368. Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 PURGE G 1412.5 MMBTU/H AVG. HEATVolatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 7A-08: 47 Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY 525.7 MMBTU/H Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 1-08: 368. Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 PURGE G 1412.5 MMBTU/H AVG. HEATVolatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 7A-08: 47 Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY 525.7 MMBTU/H Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES11.39 REFINERY FUEL GAS 2004-7: 8 Volatile O P PROPER E11.39 REFINERY 461 MM BTU/H SOURCES Volatile O P PROPER E11.39 REFINERY 461 MM BTU/H SOURCES Volatile O P PROPER E11.39 REFINERY FUEL GAS 2004-7: 8 Volatile O P PROPER E11.31 NATURAL 292.5 MMBTU/H THE PROJEVolatile O P GOOD COM

EMISLIMITEMISLIMITEMISLIMI PCTEFFIC EMISLIMITEMISLIMITEMISLIMI STDEMISSL2.45 LB/H 10.74 T/YR

5 PPMVD @ THREE-HOUR ROLLING AVERAGE5 PPMVD CORRECTED TO 0.0% OXYGEN, 3-HR AVERAGE5 PPMVD CORRECTED TO 0.0% OXYGEN - 3 HR AVERAGE5 PPMVD CORRECTED TO 0.0% OXYGEN - 3-HR AVERAGE5 PPMVD CORRECTED TO 0.0% OXYGEN, 3-HR AVERAGE5 PPMVD CORRECTED TO 0.0% OXYGEN - 3 HR AVERAGE5 PPMVD CORRECTED TO 0.0% OXYGEN - 3-HR AVERAGE5 PPMVD @ THREE-HOUR ROLLING AVERAGE

0.18 LB/H 0.79 T/YR0.29 LB/H EACH 1.26 T/YR EACH0.18 LB/H 0.79 T/YR0.29 LB/H EACH 1.26 T/YR EACH

0 LB/H SEE POLLUTANT NOTES0.173 LB/MMBTU 0.173

36.4 LB/H 159.2 T/YR 0.1125.3 LB/H* HOURLY MAXIMUM 23.1 T/YR* ANNUAL M 0.025.3 LB/H* HOURLY MAXIMUM 23.1 T/YR* ANNUAL M 0.020.1 MMBTU/H 0.1

45.9 LB/H 75 0.01627.5 LB/H 8.4 T/YR 0.0826.7 LB/H 10 T/YR 0.0827.5 LB/H 9 T/YR 0.0827.5 LB/H 7.9 T/YR 0.0827.5 LB/H 7.7 T/YR 0.0827.5 LB/H 9.3 T/YR 0.0827.5 LB/H 10.1 T/YR 0.0828.5 LB/H 9.92 T/YR 0.08

25 LB/H 10.1 T/YR 0.0825 LB/H 9.7 T/YR 0.0829 LB/H EACH 69.5 T/YR COMBINE 0.09

42.8 LB/H 18 T/YR 0.0921 LB/H 0.06

21.5 LB/H 92.5 T/YR 0.04176.31 LB/H 138.14 T/YR 0.07

1125.4 LB/H 1313.2 T/YR 2.4530.2 LB/H 132.3 T/YR 0.0848.3 LB/H EACH 211.4 T/YR EACH 0.0830.2 LB/H 132.3 T/YR 0.0848.3 LB/H EACH 211.4 T/YR EACH 0.0827.3 LB/H 363 T/YR 0.02455.7 LB/H 363 T/YR 0.02422.2 LB/H HOURLY MAXIMUM 0.0822.2 LB/H HOURLY MAXIMUM 0.0824.6 LB/H HOURLY MAXIMUM 0.0823.1 LB/H HOURLY MAXIMUM 0.0824.6 LB/H HOURLY MAXIMUM 0.08

23.1 LB/H HOURLY MAXIMUM 0.084 PPMVD @13-HOUR AVG.

27.17 LB/H WITH NATURAL GAS 48.23 T/YR WITH NAT 0.110.082 LB/MMBTU 0.0820.082 LB/MMBTU 0.0820.082 LB/MMBTU 0.0820.082 LB/MMBTU 0.0820.035 LB/MMBTU

500 PPMV500 PPMV

28.3 LB/H 123.8 T/YR0.016 LB/MMBTU3-HR AVERAGE 0.0160.016 LB/MMBTU3-HR AVERAGE 0.016

0.04 LB/MMBTUTHREE HOUR ROLLING AVERAGE 0.040.04 LB/MMBTU3-HR AVERAGE 0.040.04 LB/MMBTU3-HR AVERAGE 0.040.01 LB/MMBTU3-HR AVERAGE 0.010.04 LB/MMBTUTHREE HOUR ROLLING AVERAGE 0.040.04 LB/MMBTU3-HR AVERAGE 0.040.04 LB/MMBTU3-HR AVERAGE 0.040.01 LB/MMBTU3-HR AVERAGE 0.0118.1 LB/H 24 HR AVE 0.05

7 LB/H 28.3 T/YR8.1 LB/H 35.7 T/YR

0.53 LB/H 2.34 T/YR0.76 LB/H 3.34 T/YR

8.2 LB/H 35.92 T/YR12.57 LB/H 319.07 T/YR

8.54 LB/H 319.07 T/YR8.75 LB/H 28.47 T/YR

6.6 LB/H HOURLY MAXIMUM 28.9 T/YR ANNUAL MAXIMUMPROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04

43.24 LB/H HOURLY MAXIMUM 126.25 T/YR ANNUAL M 0.080.08 LB/MMBTUHOURLY AVERAGE

37.92 LB/H HOURLY MAXIMUM 110.74 T/YR ANNUAL M 0.0843.24 LB/H HOURLY MAXIMUM 126.25 T/YR ANNUAL M 0.0837.92 LB/H HOURLY MAXIMUM 110.74 T/YR ANNUAL M 0.08

0.08 LB/MMBTUHOURLY AVERAGE132.6 LB/H 3-HR AVERAGE 130.31 T/YR 12-MONTH 500.072 LB/MMBTU30-DAY ROLLING AV 92.24 T/YR 12-MONTH ROLLING TOTAL/ ALL TIMES

0.0001 LB/H NATURAL GAS

0 LB/H3066 T/YR 0.3

0.2 LB/MMBTU 1.6 LB/MW GROSS EN 0.2200 NG/J 0.47

0.115 LB/MMBTU 0.11524.38 LB/H COMBINATION H2 & 106.76 T/YR 0.06

25.7 LB/H* HOURLY MAXIMUM 93.7 T/YR* ANNUAL M 0.08125.7 LB/H* HOURLY MAXIMUM 93.7 T/YR* ANNUAL M 0.081

0.1 LB/MMBTU 0.17.3 LB/H 62 0.007

268.7 LB/H COMBINED 650 T/YR COMBINED62 LB/H 133.8 T/YR 0.177

33.9 LB/H 98.2 T/YR 0.162 LB/H 143.5 T/YR 0.17762 LB/H 125.8 T/YR 0.17762 LB/H 123.6 T/YR 0.17762 LB/H 161.1 T/YR 0.17762 LB/H 161.1 T/YR 0.177

40.9 LB/H EACH 78.5 T/YR EACH 0.0624 LB/H 78.8 T/YR 0.0824 LB/H 78.8 T/YR 0.08

26.64 LB/H EACH 399.1 T/YR COMBINE 0.0840.1 LB/H 126.4 T/YR 0.08

14 LB/H 0.0441.7 LB/H 183 T/YR 0.079

127.19 LB/H 230.24 T/YR 0.1128.7 LB/H 235.74 T/YR 0.1

29.3 LB/H 128.5 T/YR 0.0846.9 LB/H EACH 205.3 T/YR EACH 0.0829.3 LB/H 128.5 T/YR 0.0846.9 LB/H EACH 205.3 T/YR EACH 0.083066 T/YR 0.61

3 PPMVD @13-HOUR AVG14.82 LB/H WITH NATURAL GAS 27.02 T/YR WITH NAT 0.060.096 LB/MMBTU

6 LB/H 9.21 T/YR21 LB/H

0.0125 LB/MMBTU3-HR AVERAGE 0.01250.0125 LB/MMBTU3-HR AVERAGE 0.01250.0125 LB/MMBTUTHREE-HOUR ROLLING AVERAGE 0.01250.0125 LB/MMBTU3-HR AVERAGE 0.01250.0125 LB/MMBTU3-HR AVERAGE 0.01250.0125 LB/MMBTU3-HR AVERAGE 0.01250.0125 LB/MMBTUTHREE-HOUR ROLLING AVERAGE 0.01250.0125 LB/MMBTU3-HR AVERAGE 0.01250.0125 LB/MMBTU3-HR AVERAGE 0.01250.0125 LB/MMBTU3-HR AVERAGE 0.0125

10.1 LB/H CALENDAR 75 0.028

3 LB/H 12.2 T/YR11.9 LB/H 52 T/YR0.73 LB/H 3.19 T/YR1.53 LB/H 6.68 T/YR30.3 LB/H 132.71 T/YR

20.02 LB/H 720.54 T/YR19.29 LB/H 720.54 T/YR18.75 LB/H 65.7 T/YR

8.2 LB/H HOURLY MAXIMUM 35.9 T/YR ANNUAL MAXIMUMULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC 0.0125ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC 0.0125ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT 0.03ULTRA LOW NOX BURNERS (ULNB) & FLUE GAS RECIRCULATION (FGR) 0.2ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC 0.0125ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC 0.0125ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT 0.03ULTRA LOW NOX BURNERS (ULNB) & FLUE GAS RECIRCULATION (FGR) 0.2

0.04 LB/MMBTUTHREE 1-HOUR TEST AVERAGE36.84 LB/H HOURLY MAXIMUM 107.57 T/YR ANNUAL M 0.0836.84 LB/H HOURLY MAXIMUM 107.57 T/YR ANNUAL M 0.08

0.04 LB/MMBTUTHREE 1-HOUR TEST AVERAGE38.25 LB/H 3-HR AVERAGE 111.69 T/YR 12-MONTH 0.03

0.02 LB/MMBTU30-DAY ROLLING AV 25.62 T/Y 12-MONTH ROLLING TOTAL/ ALL TIMES4 LB/H 17.5 T/YR 0.012 LB/H HOURLY MAXIMUM 8.8 T/YR ANNUAL M 0.0082 LB/H HOURLY MAXIMUM 8.8 T/YR ANNUAL M 0.008

1.1 LB/H 3.2 T/YR 0.0031.05 LB/H 3.8 T/YR 0.003

1.1 LB/H 3.4 T/YR 0.0031.1 LB/H 3 T/YR 0.0031.1 LB/H 2.9 T/YR 0.0031.1 LB/H 3.5 T/YR 0.0031.1 LB/H 3.8 T/YR 0.003

1.05 LB/H EACH 4.04 T/YR EACH 0.0031 LB/H 4 T/YR 0.0031 LB/H 3.8 T/YR 0.003


32.42 LB/H 126.27 T/YR 0.12.73 LB/H 11.97 T/YR 0.0074.37 LB/H EACH 19.12 T/YR EACH 0.0072.73 LB/H 11.97 T/YR 0.0074.37 LB/H EACH 19.12 T/YR EACH 0.0070.03 LB/MMBTU 0.03

0.009 LB/MMBTU3-HOUR AVG. 22 LB/H 3-HOUR A 0.0090.03 LB/MMBTU 0.030.51 LB/H 18.99 T/YR0.51 LB/H 18.99 T/YR

0.99 LB/H 4.33 T/YR0.005 LB/MMBTUAVERATE OF 3 TEST RUNS

1.88 LB/H 5.88 T/YR 0.023.2 LB/H 14 T/YR 0.02

1.88 LB/H 5.88 T/YR 0.023.2 LB/H 14 T/YR 0.02

14.8 LB/H2 LB/H 8.4 T/YR 0.004

1.8 LB/H 0.0052.6 LB/H 11.6 T/YR 0.0056.9 LB/H 12.5 T/YR 0.007

32.42 LB/H 126.27 T/YR 0.1115 T/YR 0.023115 T/YR 0.011

2 LB/H HOURLY MAXIMUM 0.012 LB/H HOURLY MAXIMUM 0.01

2.2 LB/H HOURLY MAXIMUM 0.012.1 LB/H HOURLY MAXIMUM 0.012.2 LB/H HOURLY MAXIMUM 0.012.1 LB/H HOURLY MAXIMUM 0.01

0.009 LB/MMBTU3-HOUR AVG. 22 LB/H 3-HOUR A 0.0091.73 LB/H WITH NATURAL GAS 3.26 T/YR WITH NAT 0.007

0.008 LB/MMBTU 0.0080.008 LB/MMBTU 0.0080.008 LB/MMBTU 0.0080.008 LB/MMBTU 0.008

2.61 LB/H 11.43 T/YR0.0075 LB/MMBTUTHREE HOUR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTUTHREE HOUR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE 0.0075

0.64 LB/H 2.6 T/YR0.74 LB/H 3.2 T/YR0.05 LB/H 0.21 T/YR0.15 LB/H 0.64 T/YR

0.5 LB/H 2.2 T/YR11.9 LB/H HOURLY MAXIMUM 52.1 T/YR ANNUAL M 0.01

PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075

PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.00750.0074 LB/MMBTUANNUAL AVERAGE

3.43 LB/H HOURLY MAXIMUM 10.02 T/YR ANNUAL MAXIMUM3.43 LB/H HOURLY MAXIMUM 10.02 T/YR ANNUAL MAXIMUM

0.0074 LB/MMBTUANNUAL AVERAGE0.005 LB/MMBTUAVERAGE OF 3 TEST RUNS

0.23 LB/H 1.02 T/YR 0.000711.25 LB/H EACH 39.43 T/YR EACH 0.004410.75 LB/H 37.67 T/YR 0.0411.21 LB/H 8.31 T/YR 0.03211.25 LB/H EACH 39.43 T/YR EACH 0.004410.75 LB/H 37.67 T/YR 0.0411.21 LB/H 8.31 T/YR 0.032

1.6 LB/H 0.19 T/YR 0.0051.6 LB/H 0.2 T/YR 0.0051.6 LB/H 0.2 T/YR 0.0051.6 LB/H 0.18 T/YR 0.0051.6 LB/H 0.17 T/YR 0.0051.6 LB/H 0.21 T/YR 0.0051.6 LB/H 0.23 T/YR 0.005

1.46 LB/H EACH 0.22 T/YR EACH 0.0040.27 LB/H 0.22 T/YR 0.0010.27 LB/H 0.21 T/YR 0.001


0.63 LB/H 0.001814.2 LB/H 62.2 T/YR 0.0275126 LB/H 14.03 T/YR 5.19

37.37 LB/H 128.19 T/YR 0.739.4 LB/H 41.3 T/YR 0.026

15.1 LB/H EACH 33 T/YR EACH 0.0259.4 LB/H 41.3 T/YR 0.026

15.1 LB/H EACH 33 T/YR EACH 0.02514 T/YR 0.002814 T/YR 0.0014

0.2 LB/MMBTU 0.20.8 GR/100SCCALENDAR YR AVG.0.2 LB/MMBTU 0.2

0.15 LB/H WITH NATURAL GAS 0.33 T/YR WITH NAT 0.60.034 LB/MMBTU 0.034

0.1778 LB/MMBTU 0.17780.034 LB/MMBTU 0.034

0.1778 LB/MMBTU 0.17780.0006 LB/MMBTU

300 PPM300 PPM

24.2 LB/H 9.94 T/YR35 PPMV DAILY

35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE

1.9 LB/H 7.8 T/YR2.2 LB/H 9.8 T/YR

0.01 LB/H 0.01 T/YR0.01 LB/H 0.01 T/YR0.38 LB/H 1.7 T/YR0.38 LB/H 14.11 T/YR0.38 LB/H 14.11 T/YR0.41 LB/H 1.78 T/YR

3.8 LB/H HOURLY MAXIMUM 16.6 T/YR ANNUAL M 0.005USE OF LOW SULFUR REFINERY FUEL GAS 25USE OF LOW SULFUR FUEL GAS 25USE OF LOW SULFUR REFINERY FUEL GAS 25USE OF LOW SULFUR REFINERY FUEL GAS 25USE OF LOW SULFUR REFINERY FUEL GAS 25USE OF LOW SULFUR FUEL GAS 25USE OF LOW SULFUR REFINERY FUEL GAS 25USE OF LOW SULFUR REFINERY FUEL GAS 25USE OF PIPELINE QUALITY N SEE NOTE

11.79 LB/H HOURLY MAXIMUM 34.44 T/YR ANNUAL MAXIMUM11.79 LB/H HOURLY MAXIMUM 34.44 T/YR ANNUAL MAXIMUM

USE OF PIPELINE QUALITY N SEE NOTE0.0006 LB/MMBTU30-DAY ROLLING AVERAGE

0.48 LB/H 0.13 T/YR0.46 LB/H 1.58 T/YR

0.8 GR/100SCCALENDAR YR. AVG.LIMIT CONCENTRATION OF H2S SEE NOTELIMIT CONCENTRATION OF H2S SEE NOTELIMIT CONCENTRATION OF H2S SEE NOTELIMIT CONCENTRATION OF H2S SEE NOTE

3.2 LB/H *SEE NOTES. HOUR 14 T/YR ANNUAL MAXIMUM5 % OPACITY 5

20 % OPACITMethod 9 205 % OPACITY 55 % OPACITEACH 55 % OPACITY 55 % OPACITEACH 5

20 % OPACIT6-min avg 200 % SIX-MINUTE AVERAGE

0.46 LB/H 2 T/YR16.4 LB/H0.45 LB/H 1.3 T/YR

0.43 LB/H 1.6 T/YR0.45 LB/H 1.4 T/YR0.45 LB/H 1.2 T/YR0.45 LB/H 1.2 T/YR0.45 LB/H 1.5 T/YR0.45 LB/H 1.6 T/YR0.12 LB/H EACH 0.46 T/YR EACH0.39 LB/H 1.6 T/YR0.39 LB/H 1.5 T/YR2.07 LB/H EACH 11.3 T/YR EACH

0.4 LB/H 0.8 T/YR1.75 LB/H0.74 LB/H 3.3 T/YR1.98 LB/H 8.66 T/YR3.16 LB/H EACH 13.84 T/YR EACH1.98 LB/H 8.66 T/YR3.16 LB/H EACH 13.84 T/YR EACH

83 T/YR 0.0054 LB/MMBTU 0.005483 T/YR 0.0054 LB/MMBTU 0.0054

3.4 PPMVD @13-HOUR AVG.0.99 LB/H WITH NATURAL GAS 1.76 T/YR WITH NATURAL GAS AND FUEL OIL

0.0055 LB/MMBTU33.18 LB/H 9.21 T/YR

0.47 LB/H 1.9 T/YR0.5 LB/H 2.3 T/YR

0.34 LB/H 1.49 T/YR0.76 LB/H 3.34 T/YR

0.7 LB/H 3 T/YR2.73 LB/H 27.33 T/YR0.71 LB/H 27.33 T/YR2.31 LB/H 10.13 T/YR12.9 LB/H HOURLY MAXIMUM 56.5 T/YR ANNUAL M 0.017

PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015

0.0054 LB/MMBTUANNUAL AVERAGE2.48 LB/HR HOURLY MAXIMUM 7.25 TPY ANNUAL MAXIMUM2.48 LB/HR HOURLY MAXIMUM 7.25 TPY ANNUAL MAXIMUM

0.0054 LB/MMBTUANNUAL AVERAGE0.0054 LB/MMBTUAVERAGE OF 3 TEST RUNS

STDUNITLISTDLIMIT POLLUTANTCOMPLIANCENOTES LIMIT IS 4.08 X 10-6 LB/H.

LB/MMBTU LB/MMBTU LB/MMBTUCALCULAT*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 22.2 LB/H (HOURLY MAXIMUM) AND 96.9 T/YR (ANNUAL MAXIMUM). LB/MMBTUCALCULAT*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 22.2 LB/H (HOURLY MAXIMUM) AND 96.9 T/YR (ANNUAL MAXIMUM). MMBTU/H LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT MMBTU/H EACH, CA SUBJECT TO PSD REVIEW UNDER PSD-TX-302M1 LB/MMBTUCALCULAT LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUEACH, CA LB/MMBTUCALCULAT LB/MMBTUEACH, CA LB/MMBTU LB/MMBTU LB/MMBTUANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

LB/MMBTUANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. NOT AVAI LIMIT APPLIES TO COMBINED EMISSIONS FROM GAS FIRED TURBINE AND DUCT BURNER, W/TURBINE AT FULL LOAD. DUCT BURNER ONLY OPERATES W/TURBINE OPERATING AT FULL LOAD.

LB/MMBTUWITH NAT LIMITS ARE FOR NATURAL GAS, EXCEPT: 48.23 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTU LB/MMBTUTHREE HO LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUTHREE HO LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUCALCULATORIGINAL PERMIT LIMITED CO EMISSIONS TO 70 PPMDV, 24-HR AVG, @ 7% O2. THE AMENDED PERMIT HAS ELIMINATED THIS CONCENTRATION-BASED BACT LIMIT.

NOT AVAI STARTUP/SHUTDOWN (SU/SD) RATES HAVE ALSO BEEN ESTABLISHED FOR THE COMBINED TURBINE/DUCT BURNER STREAM. CO IS LIMITED TO 1530 LB/HR DURING SU. FACILITY-WIDE SU/SD EMISSIONS OF CO (FROM 2 TURBINES AND 2 DUCT BURNERS) ARE ALSO LIMITED TO 567.11 TPY. LB/MMBTU30-DAY RO LB/MMBTU30-DAY R LB/MMBTU30-DAY R LB/MMBTU30-DAY R LB/MMBTU30-DAY RO LB/MMBTU30-DAY R LB/MMBTU30-DAY R LB/MMBTU30-DAY R LB/MM BT HOURLY

LB/MMBTU LB/MM BT HOURLY LB/MMBTU

PPMVD @ 12-MONTH

12-MONTH ROLLING TOTAL/ ALL TIMES

LB/MMBTU LB/MMBTU LB/MMBTUcalculated LB/MMBTU LB/MMBTUWHEN FIRTHE EMISSION LIMIT WHEN FIRING A COMBINATION H2- WASTE AND NAT GAS IS 0.075 LB/MMBTU. LB/MMBTU* *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.06 LB/MMBTU, 15.8 LB/H (HOURLY MAXIMUM), AND 69.2 T/YR (ANNUAL MAXIMUM). LB/MMBTU* *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.06 LB/MMBTU, 15.8 LB/H (HOURLY MAXIMUM), AND 69.2 T/YR (ANNUAL MAXIMUM). LB/MMBTU LB/MMBTU

SEE ENTR LB/MMBTUHOURLY AFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKILB/MMBTUHOURLY AFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKILB/MMBTUHOURLY AFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKILB/MMBTUHOURLY AFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKILB/MMBTUHOURLY AFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKILB/MMBTUHOURLY FROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKILB/MMBTUHOURLY AFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKILB/MMBTUROLLING 1ADDITIONAL LIMITS OF: 0.12 LB/MMBTU ON AN HOURLY AVERAGE, AND 0.06 LB/MMBTU ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE LB/MMBTUHOURLY BADDITIONAL LIMITS OF: 0.065 LB/MMBTU 12 MO ROLLING AV. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE FURNACE IS IN ITS DECOKING CYCLE. LB/MMBTUHOURLY BADDITIONAL LIMITS OF 0.068 LB/MMBTU ROLLING 12- MO AV. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE FURNACE IS IN ITS DECOKING CYCLE. LB/MMBTUEACH, SE ADDITONAL LIMITS OF 0.08 LB/MMBTU AS AN HOURLY AVERAGE AND 0.05 LB/MMBTU ROLLING 12-MO AV. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE FURNLB/MMBTUHOURLY BADDITONAL LIMITS OF 0.06 LB/MMBTU AS A 12-MO ROLLING AV. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE FURNACE IS IN ITS DECOKING CYCLE. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUWHEN FIRBACT, USING LOW-NOX BURNERS, IS 0.10 LB/MMBTU WHEN FIRING NATURAL GAS AND 0.30 LB/MMBTU WHEN FIRING WOOD WASTE. LB/MMBTUCALCULAT LB/MMBTUEACH, CA LB/MMBTUCALCULAT LB/MMBTUEACH, CA LB/MMBTU

NOT AVAI LIMIT APPLIES TO COMBINED EMISSIONS FROM GAS FIRED TURBINE AND DUCT BURNER LB/MMBTUWITH NAT LIMITS ARE FOR NATURAL GAS, EXCEPT: 27.02 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

LB/MMBTU LB/MMBTU LB/MMBTUTHREE-HOTHE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTUTHREE-HOTHE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTUCALCULATORIGINAL PERMIT LIMITED NOX EMISSIONS TO 11 PPMVD, 24-HR AVG, @ 7% O2. ORIGINAL PERMIT LIMITED NOX EMISSIONS TO 0.018 LB/MMBTU, 24-HR AVG. THE AMENDED PERMIT HAS ELIMINATED THESE CONCENTRATION & MASS PER UNIT OF HEAT INPUT-BASED BACT LIMITS.

NOT AVAI STARTUP/SHUTDOWN (SU/SD) RATES HAVE ALSO BEEN ESTABLISHED FOR THE COMBINED TURBINE/DUCT BURNER STREAM. NOX IS LIMITED TO 220 LB/HR DURING SU. FACILITY-WIDE SU/SD EMISSIONS OF NOX (FROM 2 TURBINES AND 2 DUCT BURNERS) ARE ALSO LIMITED TO 74.33 TPY. LB/MMBTUANNUAL A LB/MMBTUANNUAL A LB/MMBTUANNUAL A LB/MMBTUANNUAL A LB/MMBTUANNUAL A LB/MMBTUANNUAL A LB/MMBTUANNUAL A LB/MMBTUANNUAL A

LB/MMBTU LB/MMBTU

LB/MMBTU12-MONTH

12-MONTH ROLLING TOTAL/ ALL TIMES LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUEACH, CA LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUEACH, CA SUBJECT TO PSD REVIEW UNDER PSD-TX-302M1 LB/MMBTU LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTU LB/MMBTU LIMITS APPLY TO COMBINED EMISSIONS FROM GAS FIRED TURBINE AND DUCT BURNER LB/MMBTU Limit does not apply during startup, shut down or malfunction.

PM LIMIT INCLUDES BOTH CONDENSABLE AND FILTERABLE FRACTIONS.

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI LB/MMBTUCALCULAT LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LM/MMBTU LIMITS APPLY TO COMBINED EMISSIONS FROM NG FIRED TURBINE AND DUCT BURNER LB/MMBTUWITH NAT LIMITS ARE FOR NATURAL GAS, EXCEPT: 3.26 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

LB/MMBTUTHREE HO LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUTHREE HO LB/MMBTU LB/MMBTU LB/MMBTU

LB/MMBTUANNUAL A*DOES NOT INCLUDE CONTRIBUTION FROM (NH4)2SO4. ADDITIONAL 4.3 LB/H ASSUMES 100% CONVERSION OF 3.2 LB/H H2SO4. LB/MMBTU3-H AV LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-H AV LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A

LB/MMBTU3-HOUR A

LB/MMBTUCALCULAT LB/MMBTUEACH, CA LB/MMBTUCALCULAT LB/MMBTU LB/MMBTUEACH, CA LB/MMBTUCALCULAT LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUEACH, CA LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUEACH, CA LB/MMBTUCALCULAT LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUEACH, CA LB/MMBTUCALCULAT LB/MMBTUEACH, CA LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI LIMIT IS FOR SULFUR CONTENT OF NG LB/MMBTU Limit does not apply during startup, shut down, or emergency conditions LB/MMBTUWITH NAT LIMITS ARE FOR NATURAL GAS, EXCEPT: 0.33 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT.

NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS.

LB/MMBTUANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A

NO EMISSION LIMITS NO EMISSION LIMITS LIMIT IS FOR SULFUR CONTENT OF NG FREGULATED POLLUTANT IS SULFURIC ACID MIST. UEL SULFUR LIMIT, NO EMISSION RATE LIMIT. REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL H2S LIMIT, NO EMISSION RATE LIMIT. FREGULATED POLLUTANT IS SULFURIC ACID MIST. UEL SULFUR LIMIT, NO EMISSION RATE LIMIT. REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL H2S LIMIT, NO EMISSION RATE LIMIT. REGULATED POLLUTANT IS SULFURIC ACID MIST. *3.8 LB/HR SO2 * 55% TO H2SO4 * 98 LB-MOLE/64 LB-MOLE

% OPACITY % OPACITY % OPACITY % OPACITEACH % OPACITY % OPACITEACH % OPACITY

ADDITIONAL EMISSION LIMIT: 001 LB/MMBTU

LB/MMBTU LB/MMBTU

LIMIT APPLIES TO COMBINE TURBINE AND DUCT BURNER EMISSIONS BOTH BURNING NG WITH NATURAL GAS AND FUEL OIL ADDITIONAL LIMITS ARE FOR NATURAL GAS: 0.004 LB/MMBTU. 1.76 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

LB/MMBTUANNUAL ASTARTUP/SHUTDOWN (SU/SD) RATES HAVE ALSO BEEN ESTABLISHED FOR THE COMBINED TURBINE/DUCT BURNER STREAM. VOC IS LIMITED TO 95 LB/HR DURING SU. FACILITY-WIDE SU/SD EMISSIONS OF VOC (FROM 2 TURBINES AND 2 DUCT BURNERS) ARE ALSO LIMITED TO 34.58 TPY. LB/MMBTU3-H AV LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-H AV LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A

*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 22.2 LB/H (HOURLY MAXIMUM) AND 96.9 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 22.2 LB/H (HOURLY MAXIMUM) AND 96.9 T/YR (ANNUAL MAXIMUM).

ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LIMIT APPLIES TO COMBINED EMISSIONS FROM GAS FIRED TURBINE AND DUCT BURNER, W/TURBINE AT FULL LOAD. DUCT BURNER ONLY OPERATES W/TURBINE OPERATING AT FULL LOAD. LIMITS ARE FOR NATURAL GAS, EXCEPT: 48.23 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

ORIGINAL PERMIT LIMITED CO EMISSIONS TO 70 PPMDV, 24-HR AVG, @ 7% O2. THE AMENDED PERMIT HAS ELIMINATED THIS CONCENTRATION-BASED BACT LIMIT.

STARTUP/SHUTDOWN (SU/SD) RATES HAVE ALSO BEEN ESTABLISHED FOR THE COMBINED TURBINE/DUCT BURNER STREAM. CO IS LIMITED TO 1530 LB/HR DURING SU. FACILITY-WIDE SU/SD EMISSIONS OF CO (FROM 2 TURBINES AND 2 DUCT BURNERS) ARE ALSO LIMITED TO 567.11 TPY.

THE EMISSION LIMIT WHEN FIRING A COMBINATION H2- WASTE AND NAT GAS IS 0.075 LB/MMBTU. *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.06 LB/MMBTU, 15.8 LB/H (HOURLY MAXIMUM), AND 69.2 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.06 LB/MMBTU, 15.8 LB/H (HOURLY MAXIMUM), AND 69.2 T/YR (ANNUAL MAXIMUM).

FROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKIFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKIFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKIFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKIFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKIFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKIFROM FURNACES AF-01, CF-01, DF-01, EF-01, FF-01, GF-01: NOX EMISSIONS SHALL BE LIMITED TO 0.1 LB/MMBTU WHEN CRACKING LIQUID FEEDSTOCKS AND 0.13 LB/MMBTU WHEN CRACKING GASEOUS FEEDSTOCKS AS A ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKIADDITIONAL LIMITS OF: 0.12 LB/MMBTU ON AN HOURLY AVERAGE, AND 0.06 LB/MMBTU ROLLING 12 MO AVE. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE ADDITIONAL LIMITS OF: 0.065 LB/MMBTU 12 MO ROLLING AV. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE FURNACE IS IN ITS DECOKING CYCLE. ADDITIONAL LIMITS OF 0.068 LB/MMBTU ROLLING 12- MO AV. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE FURNACE IS IN ITS DECOKING CYCLE. ADDITONAL LIMITS OF 0.08 LB/MMBTU AS AN HOURLY AVERAGE AND 0.05 LB/MMBTU ROLLING 12-MO AV. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE FURNADDITONAL LIMITS OF 0.06 LB/MMBTU AS A 12-MO ROLLING AV. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE FURNACE IS IN ITS DECOKING CYCLE.

BACT, USING LOW-NOX BURNERS, IS 0.10 LB/MMBTU WHEN FIRING NATURAL GAS AND 0.30 LB/MMBTU WHEN FIRING WOOD WASTE.

LIMIT APPLIES TO COMBINED EMISSIONS FROM GAS FIRED TURBINE AND DUCT BURNER LIMITS ARE FOR NATURAL GAS, EXCEPT: 27.02 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. ORIGINAL PERMIT LIMITED NOX EMISSIONS TO 11 PPMVD, 24-HR AVG, @ 7% O2. ORIGINAL PERMIT LIMITED NOX EMISSIONS TO 0.018 LB/MMBTU, 24-HR AVG. THE AMENDED PERMIT HAS ELIMINATED THESE CONCENTRATION & MASS PER UNIT OF HEAT INPUT-BASED BACT LIMITS.

STARTUP/SHUTDOWN (SU/SD) RATES HAVE ALSO BEEN ESTABLISHED FOR THE COMBINED TURBINE/DUCT BURNER STREAM. NOX IS LIMITED TO 220 LB/HR DURING SU. FACILITY-WIDE SU/SD EMISSIONS OF NOX (FROM 2 TURBINES AND 2 DUCT BURNERS) ARE ALSO LIMITED TO 74.33 TPY.

LIMITS APPLY TO COMBINED EMISSIONS FROM GAS FIRED TURBINE AND DUCT BURNER

PM LIMIT INCLUDES BOTH CONDENSABLE AND FILTERABLE FRACTIONS.

ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LIMITS APPLY TO COMBINED EMISSIONS FROM NG FIRED TURBINE AND DUCT BURNER LIMITS ARE FOR NATURAL GAS, EXCEPT: 3.26 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

*DOES NOT INCLUDE CONTRIBUTION FROM (NH4)2SO4. ADDITIONAL 4.3 LB/H ASSUMES 100% CONVERSION OF 3.2 LB/H H2SO4.

Limit does not apply during startup, shut down, or emergency conditions LIMITS ARE FOR NATURAL GAS, EXCEPT: 0.33 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT.

THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS.

FREGULATED POLLUTANT IS SULFURIC ACID MIST. UEL SULFUR LIMIT, NO EMISSION RATE LIMIT. REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL H2S LIMIT, NO EMISSION RATE LIMIT. FREGULATED POLLUTANT IS SULFURIC ACID MIST. UEL SULFUR LIMIT, NO EMISSION RATE LIMIT. REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL H2S LIMIT, NO EMISSION RATE LIMIT. REGULATED POLLUTANT IS SULFURIC ACID MIST. *3.8 LB/HR SO2 * 55% TO H2SO4 * 98 LB-MOLE/64 LB-MOLE

LIMIT APPLIES TO COMBINE TURBINE AND DUCT BURNER EMISSIONS BOTH BURNING NG ADDITIONAL LIMITS ARE FOR NATURAL GAS: 0.004 LB/MMBTU. 1.76 T/YR IS TOTAL FOR AUXILIARY BOILER, ALL FUELS

STARTUP/SHUTDOWN (SU/SD) RATES HAVE ALSO BEEN ESTABLISHED FOR THE COMBINED TURBINE/DUCT BURNER STREAM. VOC IS LIMITED TO 95 LB/HR DURING SU. FACILITY-WIDE SU/SD EMISSIONS OF VOC (FROM 2 TURBINES AND 2 DUCT BURNERS) ARE ALSO LIMITED TO 34.58 TPY.

*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 22.2 LB/H (HOURLY MAXIMUM) AND 96.9 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 22.2 LB/H (HOURLY MAXIMUM) AND 96.9 T/YR (ANNUAL MAXIMUM).


ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LIMIT APPLIES TO COMBINED EMISSIONS FROM GAS FIRED TURBINE AND DUCT BURNER, W/TURBINE AT FULL LOAD. DUCT BURNER ONLY OPERATES W/TURBINE OPERATING AT FULL LOAD.

ORIGINAL PERMIT LIMITED CO EMISSIONS TO 70 PPMDV, 24-HR AVG, @ 7% O2. THE AMENDED PERMIT HAS ELIMINATED THIS CONCENTRATION-BASED BACT LIMIT.


*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.06 LB/MMBTU, 15.8 LB/H (HOURLY MAXIMUM), AND 69.2 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.06 LB/MMBTU, 15.8 LB/H (HOURLY MAXIMUM), AND 69.2 T/YR (ANNUAL MAXIMUM).



ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT.

ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.


ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

RBLCID FACILITY CORPORAFACILITYSAGENCYNPERMITDATEFACILITYDPROCESSAR-0045 COLUMBIAColumbian AR ARKANSAS 9-Aug-01 CHEMICALCOAL-FIRELA-0126 JOYCE MI WEST FRASLA LOUISIAN 4/24/2002 JOYCE MI MCBURNEYLA-0126 JOYCE MI WEST FRASLA LOUISIAN 4/24/2002 JOYCE MI MCBURNEYMO-0074 CITY UTIL CITY UTIL MO MISSOURI 8-Mar-07 REPLACEMUNIT 4 ANC-0092 RIEGELWOINTERNATNC NORTH CA 10-May-01 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 10-May-01 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 10-May-01 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 10-May-01 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 10-May-01 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, NC-0092 RIEGELWOINTERNATNC NORTH CA 5/10/2001 PAPER MI BOILER, ND-0016 AMERICANAMERICANND NORTH DA 11-Jun-97 PULP DRYND-0016 AMERICANAMERICANND NORTH DA 11-Jun-97 PULP DRYND-0016 AMERICANAMERICANND NORTH DA 11-Jun-97 PULP DRYND-0016 AMERICANAMERICANND NORTH DA 11-Jun-97 PULP DRYND-0016 AMERICANAMERICANND NORTH DA 11-Jun-97 PULP DRYND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILERS, ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILERS, ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILERS, ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILERS, ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILERS, ND-0020 RICHARDTRED TRAILND NORTH DA 4-Aug-04 ETHANOL BOILER, CND-0020 RICHARDTRED TRAILND NORTH DA 4-Aug-04 ETHANOL BOILER, CND-0020 RICHARDTRED TRAILND NORTH DA 4-Aug-04 ETHANOL BOILER, CND-0020 RICHARDTRED TRAILND NORTH DA 4-Aug-04 ETHANOL BOILER, CND-0020 RICHARDTRED TRAILND NORTH DA 4-Aug-04 ETHANOL BOILER, CND-0020 RICHARDTRED TRAILND NORTH DA 4-Aug-04 ETHANOL BOILER, CND-0020 RICHARDTRED TRAILND NORTH DA 4-Aug-04 ETHANOL BOILER, CNE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULATNE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULATNE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULATNE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULATNE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULATNE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULAT

NE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULATNE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULATNE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULATNE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULATNE-0037 CARGILL, CARGILL, NE NEBRASKA 8-Sep-06 A WET COCIRCULATOH-0241 MILLER B MILLER B OH HAMILTON 27-May-04 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 27-May-04 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 27-May-04 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 27-May-04 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 27-May-04 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 27-May-04 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 27-May-04 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON 5/27/2004 BEER BREBOILER (2PA-0204 KIMBERLYKIMBERLYPA PENNSYLV 24-Jun-98 OP INCORPBOILER, VPA-0204 KIMBERLYKIMBERLYPA PENNSYLV 24-Jun-98 OP INCORPBOILER, VPA-0204 KIMBERLYKIMBERLYPA PENNSYLV 24-Jun-98 OP INCORPBOILER, VPA-0204 KIMBERLYKIMBERLYPA PENNSYLV 24-Jun-98 OP INCORPBOILER, VVA-0267 VPI POWEVPI UNIVEVA VIRGINIA 30-Aug-01 COAL-FIR BOILER, VA-0267 VPI POWEVPI UNIVEVA VIRGINIA 30-Aug-01 COAL-FIR BOILER, VA-0267 VPI POWEVPI UNIVEVA VIRGINIA 30-Aug-01 COAL-FIR BOILER, VA-0267 VPI POWEVPI UNIVEVA VIRGINIA 30-Aug-01 COAL-FIR BOILER, VA-0267 VPI POWEVPI UNIVEVA VIRGINIA 30-Aug-01 COAL-FIR BOILER, VA-0267 VPI POWEVPI UNIVEVA VIRGINIA 30-Aug-01 COAL-FIR BOILER,

AR-0045 *LA-0218 FLORIEN BOISE BU LOUISIANA DEPARTMEN7/18/2007 FACILITYLA-0126 *LA-0218 FLORIEN BOISE BU LOUISIANA DEPARTMEN7/18/2007 FACILITYLA-0126 *LA-0218 FLORIEN BOISE BU LOUISIANA DEPARTMEN7/18/2007 FACILITYMO-0074 *LA-0218 FLORIEN BOISE BU LOUISIANA DEPARTMEN7/18/2007 FACILITYNC-0092 CA-0930 SIERRA P SIERRA P CALIFORNIA, OTHER 5/13/1998 LUMBER MNC-0092 CA-0930 SIERRA P SIERRA P CALIFORNIA, OTHER 5/13/1998 LUMBER MNC-0092 CA-0930 SIERRA P SIERRA P CALIFORNIA, OTHER 5/13/1998 LUMBER MNC-0092 CA-0930 SIERRA P SIERRA P CALIFORNIA, OTHER 5/13/1998 LUMBER MNC-0092 LA-0126 JOYCE MI WEST FRASLOUISIANA DEPARTMEN4/24/2002 JOYCE MINC-0092 MN-0058 VIRGINIA CITY OF VMINNESOTA POLL CTRL 6/30/2005NC-0092 MN-0058 VIRGINIA CITY OF VMINNESOTA POLL CTRL 6/30/2005NC-0092 MN-0058 VIRGINIA CITY OF VMINNESOTA POLL CTRL 6/30/2005NC-0092 MN-0058 VIRGINIA CITY OF VMINNESOTA POLL CTRL 6/30/2005NC-0092 MN-0059 HIBBING PHIBBING MINNESOTA POLL CTRL 6/30/2005NC-0092 MN-0059 HIBBING PHIBBING MINNESOTA POLL CTRL 6/30/2005NC-0092 MN-0059 HIBBING PHIBBING MINNESOTA POLL CTRL 6/30/2005NC-0092 MN-0059 HIBBING PHIBBING MINNESOTA POLL CTRL 6/30/2005

NC-0092 MT-0007 PLUM CREPLUM CREMONTANA DEPT OF EN 2/15/1997NC-0092 MT-0007 PLUM CREPLUM CREMONTANA DEPT OF EN 2/15/1997NC-0092 NC-0092 RIEGELWOINTERNATNORTH CAROLINA DIV 5/10/2001 PAPER MINC-0092 NC-0092 RIEGELWOINTERNATNORTH CAROLINA DIV 5/10/2001 PAPER MINC-0092 NC-0092 RIEGELWOINTERNATNORTH CAROLINA DIV 5/10/2001 PAPER MINC-0092 NC-0092 RIEGELWOINTERNATNORTH CAROLINA DIV 5/10/2001 PAPER MINC-0092 NC-0092 RIEGELWOINTERNATNORTH CAROLINA DIV 5/10/2001 PAPER MIND-0016 NC-0092 RIEGELWOINTERNATNORTH CAROLINA DIV 5/10/2001 PAPER MIND-0016 NC-0092 RIEGELWOINTERNATNORTH CAROLINA DIV 5/10/2001 PAPER MIND-0016 NC-0092 RIEGELWOINTERNATNORTH CAROLINA DIV 5/10/2001 PAPER MIND-0016 NC-0092 RIEGELWOINTERNATNORTH CAROLINA DIV 5/10/2001 PAPER MIND-0016 NC-0092 RIEGELWOINTERNATNORTH CAROLINA DIV 5/10/2001 PAPER MIND-0018 ND-0018 ARCHER DARCHER DNORTH DAKOTA STATE 7/9/1998 VEGETABLND-0018 ND-0018 ARCHER DARCHER DND 7/9/1998 VEGETABLND-0018 ND-0018 ARCHER DARCHER DNORTH DAKOTA STATE 7/9/1998 VEGETABLND-0018 ND-0018 ARCHER DARCHER DND 7/9/1998 VEGETABLND-0018 ND-0018 ARCHER DARCHER DNORTH DAKOTA STATE 7/9/1998 VEGETABLND-0020 ND-0018 ARCHER DARCHER DND 7/9/1998 VEGETABLND-0020 ND-0018 ARCHER DARCHER DNORTH DAKOTA STATE 7/9/1998 VEGETABLND-0020 ND-0018 ARCHER DARCHER DND 7/9/1998 VEGETABLND-0020 ND-0018 ARCHER DARCHER DNORTH DAKOTA STATE 7/9/1998 VEGETABLND-0020 ND-0018 ARCHER DARCHER DND 7/9/1998 VEGETABLND-0020 OH-0241 MILLER B MILLER B OH 5/27/2004 BEER BREND-0020 OH-0241 MILLER B MILLER B OH 5/27/2004 BEER BRENE-0037 OH-0241 MILLER B MILLER B OH 5/27/2004 BEER BRENE-0037 OH-0241 MILLER B MILLER B OH 5/27/2004 BEER BRENE-0037 OH-0241 MILLER B MILLER B OH 5/27/2004 BEER BRENE-0037 OH-0241 MILLER B MILLER B OH 5/27/2004 BEER BRENE-0037 OH-0241 MILLER B MILLER B OH 5/27/2004 BEER BRENE-0037 OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENTAL 1/5/2004 SEVEN BONE-0037 OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENTAL 1/5/2004 SEVEN BONE-0037 OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENTAL 1/5/2004 SEVEN BONE-0037 OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENTAL 1/5/2004 SEVEN BONE-0037 OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENTAL 1/5/2004 SEVEN BONE-0037 OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENTAL 1/5/2004 SEVEN BOOH-0241 OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENTAL 1/5/2004 SEVEN BOOH-0241 OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENTAL 1/5/2004 SEVEN BOOH-0241 OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENTAL 1/5/2004 SEVEN BOOH-0241 OH-0269 BIOMASS BIOMASS OHIO ENVIRONMENTAL 1/5/2004 SEVEN BOOH-0241 VA-0268 THERMAL MARTINSVVIRGINIA ENVIRONMENT2/15/2002 STEAM PROH-0241 VA-0268 THERMAL MARTINSVVIRGINIA ENVIRONMENT2/15/2002 STEAM PROH-0241 VA-0268 THERMAL MARTINSVVIRGINIA ENVIRONMENT2/15/2002 STEAM PROH-0241 VA-0268 THERMAL MARTINSVVIRGINIA ENVIRONMENT2/15/2002 STEAM PROH-0241 VA-0268 THERMAL MARTINSVVIRGINIA ENVIRONMENT2/15/2002 STEAM PROH-0241 VA-0268 THERMAL MARTINSVVIRGINIA ENVIRONMENT2/15/2002 STEAM PROH-0241 WA-0336 GRAYS HARBOR PAPWASHINGTON STATE D ### GHP IS ANOH-0241OH-0241

OH-0241PA-0204PA-0204PA-0204PA-0204VA-0267VA-0267VA-0267VA-0267VA-0267VA-0267

PROCTYPEFUEL THRUPUT THRUPUTUPROCESSPOLLUTANCONTROLCTRLDESC12.11 SUB-BITU 8700 MMBTU/H CO catalystCarbon MoP (NO CONT12.12 WOOD WA 154.2 MMBTU/H EMISSION Carbon MoN12.12 WOOD WA 154.2 MMBTU/H EMISSION Carbon MoN12.11 COAL UPGRADE Carbon MoA 1) GOOD 12.11 COAL 249 MMBTU/H POWER BOICarbon MoP GOOD COM12.11 COAL 249 MMBTU/H POWER BOICarbon MoP GOOD COM12.12 WOODWAS 600 MMBTU/H THROUGHPCarbon MoP GOOD COM12.12 WOODWAS 600 MMBTU/H THROUGHPCarbon MoP GOOD COM12.11 COAL 249 MMBTU/H POWER BOINitrogen O P GOOD COM12.11 COAL 249 MMBTU/H POWER BOINitrogen O P GOOD COM12.12 WOODWAS 600 MMBTU/H THROUGHPNitrogen O P GOOD COM12.12 WOODWAS 600 MMBTU/H THROUGHPNitrogen O P GOOD COM12.11 COAL 249 MMBTU/H POWER BOIParticulate A MULTICLO12.11 COAL 249 MMBTU/H POWER BOIParticulate A MULTICLO12.12 WOODWAS 600 MMBTU/H THROUGHPParticulate A MULTICLO12.12 WOODWAS 600 MMBTU/H THROUGHPParticulate A MULTICLO12.11 COAL 249 MMBTU/H POWER BOISulfur DioxA MULTICLO12.11 COAL 249 MMBTU/H POWER BOISulfur DioxA MULTICLO12.12 WOODWAS 600 MMBTU/H THROUGHPSulfur DioxA MULTICLO12.12 WOODWAS 600 MMBTU/H THROUGHPSulfur DioxA MULTICLO12.11 COAL 249 MMBTU/H POWER BOIVolatile O P GOOD COM12.11 COAL 249 MMBTU/H POWER BOIVolatile O P GOOD COM12.12 WOODWAS 600 MMBTU/H THROUGHPVolatile O P GOOD COM12.12 WOODWAS 600 MMBTU/H THROUGHPVolatile O P GOOD COM12.11 COAL 230.3 MMBTU/H PARTICULCarbon MoN12.11 COAL 230.3 MMBTU/H PARTICULNitrogen O N12.11 COAL 230.3 MMBTU/H PARTICULParticulate A WET SCR12.11 COAL 230.3 MMBTU/H PARTICULSulfur DioxA WET SCRU12.11 COAL 230.3 MMBTU/H PARTICULVolatile O N12.12 HULLS 200 MMBTU/H THROUGHPCarbon MoN12.12 HULLS 200 MMBTU/H THROUGHPNitrogen O N12.12 HULLS 200 MMBTU/H THROUGHPParticulate A ESP12.12 HULLS 200 MMBTU/H THROUGHPSulfur DioxN12.12 HULLS 200 MMBTU/H THROUGHPVisible EmiN12.11 LIGNITE 250 MMBTU/H BOILER A Carbon MoP GOOD COM12.11 LIGNITE 250 MMBTU/H BOILER A Nitrogen O A SNCR12.11 LIGNITE 250 MMBTU/H BOILER A Particulate A BAGHOUS12.11 LIGNITE 250 MMBTU/H BOILER A Particulate A BAGHOUS12.11 LIGNITE 250 MMBTU/H BOILER A Sulfur DioxP LIMESTONE12.11 LIGNITE 250 MMBTU/H BOILER A Visible EmiA BAGHOUS12.11 LIGNITE 250 MMBTU/H BOILER A Volatile O P GOOD COM12.11 COAL 1500 MMBTU/H ALLOWED Carbon MoN COMBUST12.11 COAL 1500 MMBTU/H ALLOWED HydrochloriP LIME INJE12.11 COAL 1500 MMBTU/H ALLOWED Hydrogen FB LIMESTONE12.11 COAL 1500 MMBTU/H ALLOWED Hydrogen SB LIMESTONE12.11 COAL 1500 MMBTU/H ALLOWED Mercury P SORBENT 12.11 COAL 1500 MMBTU/H ALLOWED Nitrogen O A COMBUSTI

12.11 COAL 1500 MMBTU/H ALLOWED Particulate A FABRIC FI12.11 COAL 1500 MMBTU/H ALLOWED Particulat N12.11 COAL 1500 MMBTU/H ALLOWED Particulate A FABRIC FI12.11 COAL 1500 MMBTU/H ALLOWED Sulfur DioxP LIMESTON12.11 COAL 1500 MMBTU/H ALLOWED Volatile O N COMBUST12.11 COAL 238 MMBTU/H TWO BOILCarbon MoN12.11 COAL 238 MMBTU/H TWO BOILCarbon MoN12.11 COAL 238 MMBTU/H TWO BOILHydrochloriN12.11 COAL 238 MMBTU/H TWO BOILHydrochloriN12.11 COAL 238 MMBTU/H TWO BOILHydrogen FN12.11 COAL 238 MMBTU/H TWO BOILHydrogen FN12.11 COAL 238 MMBTU/H TWO BOILNitrogen O P OVERFIRE12.11 COAL 238 MMBTU/H TWO BOILNitrogen O P OVERFIRE12.11 COAL 238 MMBTU/H TWO BOILParticulate A BAGHOUS12.11 COAL 238 MMBTU/H TWO BOILParticulate A BAGHOUS12.11 COAL 238 MMBTU/H TWO BOILSulfur DioxN12.11 COAL 238 MMBTU/H TWO BOILSulfur DioxN12.11 COAL 238 MMBTU/H TWO BOILVolatile O N12.11 COAL 238 MMBTU/H TWO BOILVolatile O N12.11 COAL 249 MMBTU/H BOILER LI Nitrogen O N12.11 COAL 198 MMBTU/H BOILER LI Nitrogen O N12.11 COAL 249 MMBTU/H BOILER LI Volatile O N12.11 COAL 198 MMBTU/H BOILER LI Volatile O N12.11 COAL 146.7 MMBTU/H No. 11 boil Carbon MoP CONTINUO12.11 COAL 146.7 MMBTU/H No. 11 boil Nitrogen O P LOW EXCE12.11 COAL 146.7 MMBTU/H No. 11 boil Particulate A BAGHOUS12.11 COAL 146.7 MMBTU/H No. 11 boil Particulate A BAGHOUS12.11 COAL 146.7 MMBTU/H No. 11 boil Sulfur DioxA DRY SCRU12.11 COAL 146.7 MMBTU/H No. 11 boil Volatile O P CONTINUO

HOGGED F 12.12 WOOD 225 MMBTU/HR Carbon MoPHOGGED F 12.12 WOOD 225 MMBTU/HR Nitrogen OPHOGGED F 12.12 WOOD 225 MMBTU/HR Particulate BHOGGED F 12.12 WOOD 225 MMBTU/HR Volatile O PBOILER, 12.12 WOOD 245.3 MMBTU/H PERFORMACarbon MoPBOILER, 12.12 WOOD 245.3 MMBTU/H PERFORMANitrogen OABOILER, 12.12 WOOD 245.3 MMBTU/H PERFORMAParticulate ABOILER, 12.12 WOOD 245.3 MMBTU/H PERFORMAVolatile O PMCBURNEY 12.12 WOOD WA 154.2 MMBTU/H EMISSION Carbon MoNBOILER, 12.12 WOOD 230 mmbtu/h Carbon MoPBOILER, 12.12 WOOD 230 mmbtu/h Nitrogen OABOILER, 12.12 WOOD 230 mmbtu/h Particulate ABOILER, 12.12 WOOD 230 mmbtu/h Particulate ABOILER, 12.12 WOOD 230 mmbtu/h Carbon MoPBOILER, 12.12 WOOD 230 mmbtu/h Nitrogen OABOILER, 12.12 WOOD 230 mmbtu/h Particulate ABOILER, 12.12 WOOD 230 mmbtu/h Particulate A

RILEY ST 12.12 HOG FUEL 225 MMBTU/H PERMIT A Carbon MoPRILEY ST 12.12 HOG FUEL 225 MMBTU/H PERMIT A Nitrogen D NBOILER, 12.11 COAL 249 MMBTU/H POWER BOICarbon MoPBOILER, 12.11 COAL 249 MMBTU/H POWER BOINitrogen OPBOILER, 12.11 COAL 249 MMBTU/H POWER BOIParticulate ABOILER, 12.11 COAL 249 MMBTU/H POWER BOISulfur DioxABOILER, 12.11 COAL 249 MMBTU/H POWER BOIVolatile O PBOILER, 12.12 WOODWAS 600 MMBTU/H THROUGHPCarbon MoPBOILER, 12.12 WOODWAS 600 MMBTU/H THROUGHPNitrogen OPBOILER, 12.12 WOODWAS 600 MMBTU/H THROUGHPParticulate ABOILER, 12.12 WOODWAS 600 MMBTU/H THROUGHPSulfur DioxABOILER, 12.12 WOODWAS 600 MMBTU/H THROUGHPVolatile O PBOILERS, 12.12 HULLS 200 MMBTU/H THROUGHPCarbon MoNBOILERS, 12.12 HULLS 200 MMBTU/H THROUGHPCarbon MoNBOILERS, 12.12 HULLS 200 MMBTU/H THROUGHPNitrogen ONBOILERS, 12.12 HULLS 200 MMBTU/H THROUGHPNitrogen ONBOILERS, 12.12 HULLS 200 MMBTU/H THROUGHPParticulate ABOILERS, 12.12 HULLS 200 MMBTU/H THROUGHPParticulate ABOILERS, 12.12 HULLS 200 MMBTU/H THROUGHPSulfur DioxNBOILERS, 12.12 HULLS 200 MMBTU/H THROUGHPSulfur DioxNBOILERS, 12.12 HULLS 200 MMBTU/H THROUGHPVisible EmiNBOILERS, 12.12 HULLS 200 MMBTU/H THROUGHPVisible EmiNBOILER (2 12.11 COAL 238 MMBTU/H TWO BOILCarbon MoNBOILER (2 12.11 COAL 238 MMBTU/H TWO BOILHydrochloriNBOILER (2 12.11 COAL 238 MMBTU/H TWO BOILHydrogen FNBOILER (2 12.11 COAL 238 MMBTU/H TWO BOILNitrogen OPBOILER (2 12.11 COAL 238 MMBTU/H TWO BOILParticulate ABOILER (2 12.11 COAL 238 MMBTU/H TWO BOILSulfur DioxNBOILER (2 12.11 COAL 238 MMBTU/H TWO BOILVolatile O NWOOD FIRE 12.12 WOOD 175 MMBTU/H OXIDATIO Ammonia (NWOOD FIRE 12.12 WOOD 175 MMBTU/H OXIDATIO Carbon MoAWOOD FIRE 12.12 WOOD 175 MMBTU/H OXIDATIO HydrochloriAWOOD FIRE 12.12 WOOD 175 MMBTU/H OXIDATIO Lead (Pb) AWOOD FIRE 12.12 WOOD 175 MMBTU/H OXIDATIO Mercury NWOOD FIRE 12.12 WOOD 175 MMBTU/H OXIDATIO Nitrogen OAWOOD FIRE 12.12 WOOD 175 MMBTU/H OXIDATIO Particulate AWOOD FIRE 12.12 WOOD 175 MMBTU/H OXIDATIO Sulfur DioxAWOOD FIRE 12.12 WOOD 175 MMBTU/H OXIDATIO Visible EmiAWOOD FIRE 12.12 WOOD 175 MMBTU/H OXIDATIO Volatile O ABOILER, 12.12 WOOD 120 MMBTU/H Wood limit Carbon MoPBOILER, 12.12 WOOD 120 MMBTU/H Wood limit Nitrogen D PBOILER, 12.12 WOOD 120 MMBTU/H Wood limit Particulate PBOILER, 12.12 WOOD 120 MMBTU/H Wood limit Particulate PBOILER, 12.12 WOOD 120 MMBTU/H Wood limit Sulfur DioxPBOILER, 12.12 WOOD 120 MMBTU/H Wood limit Volatile O PINDUSTRI 12.12 WOOD WA 227 MMBTU/H BOILER #6Particulate A

EMISLIMITEMISLIMITEMISLIMI PCTEFFIC EMISLIMITEMISLIMITEMISLIMI STDEMISSL100 PPM 24 hr. average

279.1 LB/H 1222.5 T/YR 1.81279.1 LB/H 1222.5 T/YR 1.81

0.35 LB/MMBTU30-DAY ROLLING AVERAGE 0.350.208 LB/MMBTU 0.2080.208 LB/MMBTU 0.208


0.35 LB/MMBTU 0.350.35 LB/MMBTU 0.350.16 LB/MMBTU 0.160.16 LB/MMBTU 0.160.25 LB/MMBTU 0.250.25 LB/MMBTU 0.25

0.8 LB/MMBTU 0.80.8 LB/MMBTU 0.8

0.024 LB/MMBTU 0.0240.024 LB/MMBTU 0.024

0.0029 LB/MMBTU 0.00290.0029 LB/MMBTU

0.213 LB/MMBTU0.213 LB/MMBTU

461 LB/H 0 2100 LB/H 0 0.43

52 LB/H 0 0.2363.3 LB/H 0 0.2792.1 LB/H 0 0.390.63 LB/MMBTU 0.63

0.2 LB/MMBTU 0.20.24 LB/MMBTU 0.24

0.002 LB/MMBTU 0.00220 % OPACITY 20

0.11 LB/MMBTU3 HOUR ROLLING AVERAGE 0.110.1 LB/MMBTU30 DAY R 76 0.1

0.048 LB/MMBTU3 HOUR A 99.8 0.0480.02 LB/MMBTU3-HOUR A 99.8 0.020.09 LB/MMBTU30 DAY RO 93 0.09

20 % OPACITY 99.8 208.83 LB/H 3 HOUR ROLLING AVERGAE 0.035320.12 LB/MMBTU30-DAY ROLLING A 180 LB/H 30-DAY R 0.120.02 LB/MMBTUTEST METHOD AVERAGE 0.02

0.0012 LB/MMBTUTEST METHOD AVERAGE 0.00120.01 LB/MMBTUTEST METHOD AVERAGE 0.01

0 LB/MMBTUTEST METHOD AVERAGE 00.08 LB/MMBTU30-DAY ROLLING A 120 LB/H 30-DAY R 0.08

0.012 LB/MMBTUTEST METHOD AVERAGE 0.0120.03 LB/MMBTUTEST METHOD AVERAGE 0.03

0.012 LB/MMBTUTEST METHOD AVERAGE 0.0120.11 LB/MMBTU30-DAY AV 90 887 T/YR 12-MONTH 0.11

0.007 LB/MMBTUTEST METHOD AVERAGE 0.0075.2 LB/H EACH BOILER 87.6 T/YR EACH BOIL 0.0225.2 LB/H EACH BOILER 87.6 T/YR EACH BOIL 0.022

21.4 LB/H EACH BOILER 187.6 T/YR BOTH BOI 0.08991621.4 LB/H EACH BOILER 187.6 T/YR BOTH BOILERS TOGETHER, PER ROLLIN

1.6 LB/H EACH BOILER 17.7 T/YR BOTH BOI 1.61.6 LB/H EACH BOILER 17.7 T/YR BOTH BOILERS TOGETHER, PER ROLLIN0.7 LB/MMBTU 1375.9 T/YR BOTH BOI 0.70.7 LB/MMBTU 1375.9 T/YR BOTH BOI 0.7

0.01 GR/ACF 122.9 T/YR BOTH BOI 0.0310.01 GR/ACF 122.9 T/YR BOTH BOI 0.031

1.6 LB/MMBTU 2758 T/YR BOTH BOI 1.61.6 LB/MMBTU 2758 T/YR BOTH BOI 1.6

0.62 LB/H EACH BOILER 11.5 T/YR EACH BOIL0.0026050.62 LB/H EACH BOILER 11.5 T/YR EACH BOILER, ON A ROLLING 12-MO.1090 T/YR Total, 3 Boilers 0.21090 T/YR Total, 3 Boilers 0.2

30 T/YR Rolling Avg From 3 Boilers 0.00630 T/YR Rolling Avg Total From 3 Boilers 0.006

33.2 LB/H 126 T/YR 0.2336.1 LB/H 136.9 T/YR 0.25

2.9 LB/H 11.1 T/YR 0.022.9 LB/H 10 T/YR 0.02

23.6 LB/H 89.4 T/YR 0.160.3 LB/H 1.1 T/YR 0.002

HIGH PRE 135 LB/HR HOURLY MAXIMUM 591.3 TPY ANNUAL MGOOD COM 49.5 LB/HR HOURLY MAXIMUM 216.81 TPY ANNUAL MMULTI-CL 22.5 LB/HR HOURLY MAXIMUM 98.55 TPY ANNUAL MHIGH PRE 3.83 LB/HR HOURLY MAXIMUM 16.75 TPY ANNUAL MHIGH PRE 963 PPM @ 12% CO2 282 LB/HSNCR 115 PPM @ 12% CO2 56.4 LB/HMULTICLO 0.015 GR/DSCF @ 12% CO2 8.6 LB/HHIGH PRE 102 PPM 12.3 LB/H

279.1 LB/H 1222.5 T/YRGOOD CO 0.3 LB/MMBTU4-HOUR BLOCK AVERAGESELECTIV 0.15 LB/MMBTU30 DAY A 50ESP 0.025 LB/MMBTU3-HR TEST 98ESP 0.025 LB/MMBTU3-HR TEST 98GOOD CO 0.3 LB/MMBTU4-HOUR BLOCK AVERAGESELECTIV 0.15 LB/MMBTU30-DAY R 50ESP 0.025 LB/MMBTU3-H TEST 98ESP 0.025 LB/MMBTU3-HR TEST 90

GOOD CO 506 LB/HOUR 0 0104 LB/HOUR 0 0

GOOD COM 0.208 LB/MMBTUGOOD COM 0.4 LB/MMBTUMULTICLO 0.16 LB/MMBTUMULTICLO 0.8 LB/MMBTUGOOD COM 0.0029 LB/MMBTUGOOD COM 0.5 LB/MMBTUGOOD COM 0.35 LB/MMBTUMULTICLO 0.25 LB/MMBTUMULTICLO 0.024 LB/MMBTUGOOD COM 0.213 LB/MMBTU



ESP 0.24 LB/MMBTUESP 0.24 LB/MMBTU


20 % OPACITY20 % OPACITY

5.2 LB/H EACH BOILER 87.6 T/YR EACH BOIL21.4 LB/H EACH BOILER 187.6 T/YR BOTH BOILERS TOGETHER, PER ROLLIN

1.6 LB/H EACH BOILER 17.7 T/YR BOTH BOILERS TOGETHER, PER ROLLINOVERFIRE 0.7 LB/MMBTU 1375.9 T/YR BOTH BOIBAGHOUS 0.01 GR/ACF 122.9 T/YR BOTH BOI

1.6 LB/MMBTU 2758 T/YR BOTH BOI0.62 LB/H EACH BOILER 11.5 T/YR EACH BOILER, ON A ROLLING 12-MO.2.29 LB/H 10.03 T/YR

CATALYTI 31.8 LB/H 50 139.28 T/YR PER ROLLDRY SODI 3.01 LB/H 63.4 13.18 T/YRPULSE JE 0.006 LB/H 85 0.026 T/YR PER ROLL

0.013 T/YRSELECTIV 27.98 LB/H 80 122.55 T/YR PER ROLLPULSE JET 3.97 LB/H 98 17.39 T/YR PER ROLLDRY SODI 22.13 LB/H 20 96.93 T/YR PER ROLLPULSE JE 20 % OPACITAS A SIX 98CATALYTI 4.06 LB/H 25 17.78 T/YR PER ROLLING 12-MONTHSGOOD COM 0.44 LB/MMBTU 231.3 T/YRGOOD COM 0.4 LB/MMBTU 210.4 T/YRGOOD COM 0.15 LB/MMBTU 78.8 T/YRGOOD COM 0.14 LB/MMBTU 73.6 T/YRGOOD COM 0.47 LB/MMBTU 247 T/YRGOOD COM 0.18 LB/MMBTU 94.6 T/YR1. MULTIC 78.4 LB/H CALENDAR DAY

STDUNITLISTDLIMIT POLLUTANTCOMPLIANCENOTES

LB/MMBTUCALCULATTHE UNITS THAT EMIT CO ARE NOT BEING PHYSICALLY MODIFIED, THEREFORE, NO BACT ANALYSIS IS REQUIRED. LB/MMBTUCALCULATTHE UNITS THAT EMIT CO ARE NOT BEING PHYSICALLY MODIFIED, THEREFORE, NO BACT ANALYSIS IS REQUIRED. LB/MMBTULB/MMBTULB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTULB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTULB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTULB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

LB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU % OPACITY Information about regulatory basis unavailable. LB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTU% OPACITYLB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTU

LB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTU LB/MMBTU

BOTH BOILERS TOGETHER, PER ROLLIN LIMITS HAVE INCREASED IN THIS MODIFICATION. LB/H

BOTH BOILERS TOGETHER, PER ROLLIN LB/MMBTULB/MMBTU LB/MMBTULB/MMBTU LB/MMBTULB/MMBTU PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET. LB/MMBTU

EACH BOILER, ON A ROLLING 12-MO. LB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTULB/MMBTU

0.6 LB/MMBTUHOURLY 0.22 LB/MMBTUHOURLY

0.1 LB/MMBTUHOURLY 0.017 LB/MMBTUHOURLY


0.035 LB/MMBTU 0.05 LB/MMBTU 1.81 LB/MMBTUCALCULATTHE UNITS THAT EMIT CO ARE NOT BEING PHYSICALLY MODIFIED, THEREFORE, NO BACT ANALYSIS IS REQUIRED.





0 0



0.5 LB/MMBTU


0.024 LB/MMBTU





20 % OPACITY Information about regulatory basis unavailable. 20 % OPACITY Information about regulatory basis unavailable.

0.022 LB/MMBTU BOTH BOILERS TOGETHER, PER ROLLIN LIMITS HAVE INCREASED IN THIS MODIFICATION. BOTH BOILERS TOGETHER, PER ROLLIN


1.6 LB/MMBTU PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET. EACH BOILER, ON A ROLLING 12-MO.

LIMITS ARE FOR EACH OF 7 BOILERS 0.1 LB/MMBTU LIMITS ARE FOR EACH OF 7 BOILERS.

LIMITS ARE FOR EACH OF 7 BOILERS 0.0001 LB/MMBTU LIMITS ARE FOR EACH OF 7 BOILERS

0 LB/MMBTUSEE NOTELIMIT IS FOR EACH OF 7 BOILERS 0.000009 LB/MMBTU HG 0.44 LB/MMBTUMANUFACTLIMITS ARE FOR EACH OF 7 BOILERS.

0.0125 LB/MMBTU LIMITS ARE FOR EACH OF 7 BOILERS. ADDITIONAL LIMIT: 0.0064 GR/DSCF 0.087 LB/MMBTU LIMITS ARE FOR EACH OF 7 BOILERS

20 % OPACITAS A SIX LIMIT IS FOR EACH OF 7 BOILERS PER ROLLING 12-MONTHS ADDITIONAL LIMIT: 0.013 LB/MMBTU. LIMITS ARE FOR EACH OF 7 BOILERS.



INCREASED UTILIZATION OF THE BOILER DUE TO INSTALLATION OF THE 7.5 MW STEAM TURBINE/GENERATOR TRIGGERED PSD REQUIREMENTS FOR NOX, CO, AND PSD. SINCE NO MODIFICATIONS TO BOILER, NO BACT TRIGGERED. NAAQS IMPACTS, INCREMENT, AND CLASS I IMPACTS EVALUATED. AS

THE UNITS THAT EMIT CO ARE NOT BEING PHYSICALLY MODIFIED, THEREFORE, NO BACT ANALYSIS IS REQUIRED. THE UNITS THAT EMIT CO ARE NOT BEING PHYSICALLY MODIFIED, THEREFORE, NO BACT ANALYSIS IS REQUIRED.

PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET.

THE UNITS THAT EMIT CO ARE NOT BEING PHYSICALLY MODIFIED, THEREFORE, NO BACT ANALYSIS IS REQUIRED.

PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET.

LIMIT IS FOR EACH OF 7 BOILERS 0.000009 LB/MMBTU HG

LIMITS ARE FOR EACH OF 7 BOILERS. ADDITIONAL LIMIT: 0.0064 GR/DSCF

ADDITIONAL LIMIT: 0.013 LB/MMBTU. LIMITS ARE FOR EACH OF 7 BOILERS.


RBLCID FACILITY CORPORAFACILITYSAGENCYNPERMITDAFACILITYDPROCESSNJ-0031 UNIVERSI UNIVERSI NJ NEW JERS6/26/1997 BOILER, NAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, FFL-0182 RAYONIER,RAYONIER,FL FLORIDA ### PULP MILLINDUSTRIANC-0092 RIEGELWOINTERNATNC NORTH CA5/10/2001 PAPER MI BOILER, PNC-0092 RIEGELWOINTERNATNC NORTH CA5/10/2001 PAPER MI BOILER, PAR-0045 COLUMBIAColumbian AR ARKANSAS9-Aug-01 CHEMICALCOAL-FIREVA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - VA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #6VA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - VA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #2VA-0278 VCU EASTVirginia C VA 3/31/2003 STEAM GEBOILER, #6AR-0074 PLUM POI PLUM POI AR 8/20/2003 AUXILLARAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI AUXILIARYOH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)VA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - VA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - NJ-0031 UNIVERSI UNIVERSI NJ NEW JERS6/26/1997 BOILER, NFL-0182 RAYONIER,RAYONIER,FL FLORIDA ### PULP MILLINDUSTRIANC-0092 RIEGELWOINTERNATNC NORTH CA5/10/2001 PAPER MI BOILER, PNC-0092 RIEGELWOINTERNATNC NORTH CA5/10/2001 PAPER MI BOILER, PVA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #6VA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #2VA-0278 VCU EASTVirginia C VA 3/31/2003 STEAM GEBOILER, #6AR-0074 PLUM POI PLUM POI AR 8/20/2003 AUXILLARAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI AUXILIARYOH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)PA-0246 NAVAL SUUS NAVY PA PHILADEL ### SHIP SYS BOILERS, (AL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, FAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, FFL-0182 RAYONIER,RAYONIER,FL FLORIDA ### PULP MILLINDUSTRIANC-0092 RIEGELWOINTERNATNC NORTH CA5/10/2001 PAPER MI BOILER, PNC-0092 RIEGELWOINTERNATNC NORTH CA5/10/2001 PAPER MI BOILER, PVA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #6VA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - VA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #2VA-0278 VCU EASTVirginia C VA 3/31/2003 STEAM GEBOILER, #6VA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - FL-0182 RAYONIER,RAYONIER,FL FLORIDA ### PULP MILLINDUSTRIAVA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - VA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #6VA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER -

VA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #2VA-0278 VCU EASTVirginia C VA 3/31/2003 STEAM GEBOILER, #6AR-0074 PLUM POI PLUM POI AR 8/20/2003 AUXILLARAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI AUXILIARYOH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)FL-0182 RAYONIER,RAYONIER,FL FLORIDA ### PULP MILLINDUSTRIANC-0092 RIEGELWOINTERNATNC NORTH CA5/10/2001 PAPER MI BOILER, PNC-0092 RIEGELWOINTERNATNC NORTH CA5/10/2001 PAPER MI BOILER, PVA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - VA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #6VA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - VA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #2VA-0278 VCU EASTVirginia C VA 3/31/2003 STEAM GEBOILER, #6AR-0074 PLUM POI PLUM POI AR 8/20/2003 AUXILLARAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI AUXILIARYOH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)AR-0074 PLUM POI PLUM POI AR 8/20/2003 AUXILLARAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI AUXILIARYAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, FAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, FFL-0182 RAYONIER,RAYONIER,FL FLORIDA ### PULP MILLINDUSTRIANC-0092 RIEGELWOINTERNATNC NORTH CA5/10/2001 PAPER MI BOILER, PNC-0092 RIEGELWOINTERNATNC NORTH CA5/10/2001 PAPER MI BOILER, PVA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - VA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #6VA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER - VA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, #2VA-0278 VCU EASTVirginia C VA 3/31/2003 STEAM GEBOILER, #6AR-0074 PLUM POI PLUM POI AR 8/20/2003 AUXILLARAR-0079 PLUM POI PLUM POI AR 8/20/2003 PLUM POI AUXILIARYOH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2)

PROCTYPEFUEL THRUPUT THRUPUTUPROCESSPOLLUTANCONTROLCTRLDESC12.21 NO.6 FUEL 112 MMBTU/H SEPARATECarbon MoN12.22 FUEL OIL 190 MMBTU/H NATURAL Carbon MoA12.21 NO. 6 FUE 212 MMBTU/H STACK TECarbon MoN12.21 NO. 6 FUE 249 MMBTU/H POWER BOICarbon MoP GOOD COM12.21 NO. 6 FUE 249 MMBTU/H POWER BOICarbon MoP GOOD COM12.11 SUB-BITU 8700 MMBTU/H CO catalystCarbon MoP (NO CONT12.21 FUEL OIL 150 MMBTU/H This is one Carbon MoP GOOD COM12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Carbon MoP GOOD COM12.22 FUEL OIL 150 MMBTU This is one Carbon MoP GOOD COM12.22 NO. 2 FUE 150.6 MMBTU/H Throughput Carbon MoP GOOD COM12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Carbon MoP GOOD COM12.22 #2 FUEL O 175 MMBTU/H Carbon MoP COMBUST12.22 #2 FUEL O 175 MMBTU Carbon MoP COMBUST12.21 NO. 6 FUE 238 MMBTU/H TWO BOILECarbon MoN12.21 NO. 6 FUE 238 MMBTU/H TWO BOILECarbon MoN12.22 NO. 2 FUE 238 MMBTU/H TWO BOILECarbon MoN12.22 NO. 2 FUE 238 MMBTU/H TWO BOILECarbon MoN12.21 FUEL OIL 150 MMBTU/H This is one Nitrogen D B GOOD COM12.22 FUEL OIL 150 MMBTU This is one Nitrogen D B GOOD COM12.21 NO.6 FUEL 112 MMBTU/H SEPARATENitrogen O N12.21 NO. 6 FUE 212 MMBTU/H STACK TENitrogen O P LOW-NOX 12.21 NO. 6 FUE 249 MMBTU/H POWER BOINitrogen O P GOOD COM12.21 NO. 6 FUE 249 MMBTU/H POWER BOINitrogen O P GOOD COM12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Nitrogen O P LOW NOX 12.22 NO. 2 FUE 150.6 MMBTU/H Throughput Nitrogen O P LOW NOX 12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Nitrogen O P LOW NOX 12.22 #2 FUEL O 175 MMBTU/H Nitrogen O A LOW NOX 12.22 #2 FUEL O 175 MMBTU Nitrogen O B LOW NOX 12.21 NO. 6 FUE 238 MMBTU/H TWO BOILENitrogen O P OVERFIRE12.21 NO. 6 FUE 238 MMBTU/H TWO BOILENitrogen O P OVERFIRE12.22 NO. 2 FUE 238 MMBTU/H TWO BOILENitrogen O P OVERFIRE12.22 NO. 2 FUE 238 MMBTU/H TWO BOILENitrogen O P OVERFIRE12.21 NO.6 FUEL 125 mmbtu/h FUELS ARENitrogen O N12.22 FUEL OIL 190 MMBTU/H NATURAL Particulate A12.22 FUEL OIL 190 MMBTU/H NATURAL Particulate A12.21 NO. 6 FUE 212 MMBTU/H STACK TEParticulate N12.21 NO. 6 FUE 249 MMBTU/H POWER BOIParticulate A MULTICLO12.21 NO. 6 FUE 249 MMBTU/H POWER BOIParticulate A MULTICLO12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Particulate N12.22 FUEL OIL 150 MMBTU This is one Particulate P GOOD COM12.22 NO. 2 FUE 150.6 MMBTU/H Throughput Particulate N12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Particulate N12.21 FUEL OIL 150 MMBTU/H This is one Particulate P GOOD COM12.21 NO. 6 FUE 212 MMBTU/H STACK TEParticulate N12.21 FUEL OIL 150 MMBTU/H This is one Particulate P GOOD COM12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Particulate N12.22 FUEL OIL 150 MMBTU This is one Particulate P GOOD COM

12.22 NO. 2 FUE 150.6 MMBTU/H Throughput Particulate N12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Particulate N12.22 #2 FUEL O 175 MMBTU/H Particulate P LOW ASH 12.22 #2 FUEL O 175 MMBTU Particulate P LOW ASH 12.21 NO. 6 FUE 238 MMBTU/H TWO BOILEParticulate A BAGHOUS12.21 NO. 6 FUE 238 MMBTU/H TWO BOILEParticulate A BAGHOUS12.22 NO. 2 FUE 238 MMBTU/H TWO BOILEParticulate A BAGHOUS12.22 NO. 2 FUE 238 MMBTU/H TWO BOILEParticulate A BAGHOUS12.21 NO. 6 FUE 212 MMBTU/H STACK TESulfur DioxN12.21 NO. 6 FUE 249 MMBTU/H POWER BOISulfur DioxA MULTICLO12.21 NO. 6 FUE 249 MMBTU/H POWER BOISulfur DioxA MULTICLO12.21 FUEL OIL 150 MMBTU/H This is one Sulfur DioxP GOOD COM12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Sulfur DioxP FUEL SULF12.22 FUEL OIL 150 MMBTU This is one Sulfur DioxN GOOD COM12.22 NO. 2 FUE 150.6 MMBTU/H Throughput Sulfur DioxP FUEL SULF12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Sulfur DioxP FUEL SULF12.22 #2 FUEL O 175 MMBTU/H Sulfur DioxP LOW SULF12.22 #2 FUEL O 175 MMBTU Sulfur DioxP LOW SULFU12.21 NO. 6 FUE 238 MMBTU/H TWO BOILESulfur DioxN12.21 NO. 6 FUE 238 MMBTU/H TWO BOILESulfur DioxN12.22 NO. 2 FUE 238 MMBTU/H TWO BOILESulfur DioxN12.22 NO. 2 FUE 238 MMBTU/H TWO BOILESulfur DioxN12.22 #2 FUEL O 175 MMBTU/H Sulfuric AciP LOW SULF12.22 #2 FUEL O 175 MMBTU Sulfuric AciP LOW SULF12.22 FUEL OIL 190 MMBTU/H NATURAL Visible EmiA12.22 FUEL OIL 190 MMBTU/H NATURAL Volatile O A12.21 NO. 6 FUE 212 MMBTU/H STACK TEVolatile O N12.21 NO. 6 FUE 249 MMBTU/H POWER BOIVolatile O P GOOD COM12.21 NO. 6 FUE 249 MMBTU/H POWER BOIVolatile O P GOOD COM12.21 FUEL OIL 150 MMBTU/H This is one Volatile O P GOOD COM12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Volatile O P GOOD CO12.22 FUEL OIL 150 MMBTU This is one Volatile O P GOOD COM12.22 NO. 2 FUE 150.6 MMBTU/H Throughput Volatile O P GOOD COM12.21 # 6 FUEL O 150.6 MMBTU/H Throughput Volatile O P GOOD CO12.22 #2 FUEL O 175 MMBTU/H Volatile O P COMBUST12.22 #2 FUEL O 175 MMBTU Volatile O P COMBUST12.21 NO. 6 FUE 238 MMBTU/H TWO BOILEVolatile O N12.21 NO. 6 FUE 238 MMBTU/H TWO BOILEVolatile O N12.22 NO. 2 FUE 238 MMBTU/H TWO BOILEVolatile O N12.22 NO. 2 FUE 238 MMBTU/H TWO BOILEVolatile O N

EMISLIMITEMISLIMITEMISLIMI PCTEFFIC EMISLIMITEMISLIMITEMISLIMI STDEMISSL

0.18 LB/MMBTU 34.2 LB/H 0.1831 T/YR

0.033 LB/MMBTU 0.0330.033 LB/MMBTU 0.033

100 PPM 24 hr. average15.8 LB/H each unit 0.10515.8 LB/H 0.115.8 LB/H each unit 0.10515.8 LB/H 0.115.8 LB/H 0.1

1.6 T/YR 0.0361.6 T/YR 0.036

8.15 LB/H EACH BOILER 87.6 T/YR EACH BOIL 0.0348.15 LB/H EACH BOILER 87.6 T/YR EACH BOIL 0.034

8.5 LB/H EACH BOILER 87.6 T/YR EACH BOIL 0.0368.5 LB/H EACH BOILER 87.6 T/YR EACH BOIL 0.0360.4 LB/MMBTUeach unit 57.5 LB/H each unit 0.40.2 LB/MMBTUeach unit 30.1 LB/H each unit 0.2

0.55 LB/MMBTU 0.550.425 LB/MMBTU 20 395 T/YR 0.4250.367 LB/MMBTU 0.3670.367 LB/MMBTU 0.367

57.5 LB/H 145.6 T/YR combined op 0.430.1 LB/H 0.257.5 LB/H 145.6 T/YR combined op 0.4

4.4 T/YR 0.14.4 T/YR 0.10.7 LB/MMBTU 1375.9 T/YR BOTH BOI 0.70.7 LB/MMBTU 1375.9 T/YR BOTH BOI 0.70.7 LB/MMBTU 1375.9 T/YR BOTH BOI 0.70.7 LB/MMBTU 1375.9 T/YR BOTH BOI 0.7534 T/YR SEE NOTE3.8 LB/H

0.15 LB/MMBTU 28.5 LB/H 0.1521 T/YR

0.0562 LB/MMBTU 0.05620.0562 LB/MMBTU 0.0562

9.3 LB/H 23.3 T/YR combined op 0.063.3 LB/H each unit 0.0223.3 LB/H 0.029.3 LB/H 23.3 T/YR combined op 0.069.3 LB/H each unit 0.06321 T/YR

8 LB/H each unit 0.058 LB/H 20 T/YR combined op 0.05

1.7 LB/H each unit

1.7 LB/H 0.018 LB/H 20 T/YR combined op 0.05

0.4 T/YR 0.00710.4 T/YR 0.0071

0.01 GR/ACF 122.9 T/YR BOTH BOI 0.1250.01 GR/ACF 122.9 T/YR BOTH BOI 0.1250.01 GR/ACF 122.9 T/YR BOTH BOI 0.020.01 GR/ACF 122.9 T/YR BOTH BOI 0.02244 T/YR0.8 LB/MMBTU 0.80.8 LB/MMBTU 0.8

78.5 LB/H each unit 3hr rolling avg 0.5278.5 LB/H 196.3 T/YR combined op 0.5278.5 LB/H each unit 3hr rolling avg 0.5378.5 LB/H 0.578.5 LB/H 196.3 T/YR combined op 0.52

2.3 T/YR 0.0512.3 T/YR 0.0511.6 LB/MMBTU 2758 T/YR BOTH BOI 1.61.6 LB/MMBTU 2758 T/YR BOTH BOI 1.61.6 LB/MMBTU 2758 T/YR BOTH BOI 1.61.6 LB/MMBTU 2758 T/YR BOTH BOI 1.6

0.03 T/YR 0.00080.03 T/YR 0.0008

10 % OPACITY 101.9 LB/H

7 T/YR0.0019 LB/MMBTU0.0019 LB/MMBTU

2.1 LB/H each unit2.1 LB/H2.1 LB/H each unit2.1 LB/H2.1 LB/H0.1 T/YR 0.00150.1 T/YR 0.0015 LB/MMBTU1.2 LB/H EACH BOILER 11.5 T/YR EACH BOILER, ON A ROLLING 12-MO.1.2 LB/H EACH BOILER 11.5 T/YR EACH BOILER, ON A ROLLING 12-MO.

0.38 LB/H EACH BOILER 11.5 T/YR EACH BOILER, ON A ROLLING 12-MO.0.38 LB/H EACH BOILER 11.5 T/YR EACH BOILER, ON A ROLLING 12-MO.


LB/MMBTU NOT AVAI

LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTUcalculated LB/MMBTU LB/MMBTUcalculated LB/MMBTUcalculated LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

SEE NOTERACT CAP, NO EMISSION RATE LIMITS AS LB/MMBTU. THIS RACT MODIFICATION IS TO FACILITATE THE DETERMINATION OF EMISSION REDUCTION CREDITS. THESE BOILERS ARE IN DECOMMISSIONED STATUS. NOT AVAI

LB/MMBTU NOT AVAI

LB/MMBTU LB/MMBTU LB/MMBTUcalculated LB/MMBTU LB/MMBTUcalculated LB/MMBTUcalculated LB/MMBTU

NOT AVAI LB/MMBTU LB/MMBTUcalculated

NOT AVAI

LB/MMBTU LB/MMBTUcalculated LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUcalculated LB/MMBTU LB/MMBTUcalculated LB/MMBTUcalculated LB/MMBTU LB/MMBTU LB/MMBTU PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET. LB/MMBTU PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET. LB/MMBTU PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET. LB/MMBTU PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET. LB/MMBTU LB/MMBTU % OPACITY

LB/MMBTU

EACH BOILER, ON A ROLLING 12-MO. EACH BOILER, ON A ROLLING 12-MO. EACH BOILER, ON A ROLLING 12-MO. EACH BOILER, ON A ROLLING 12-MO.

RACT CAP, NO EMISSION RATE LIMITS AS LB/MMBTU. THIS RACT MODIFICATION IS TO FACILITATE THE DETERMINATION OF EMISSION REDUCTION CREDITS. THESE BOILERS ARE IN DECOMMISSIONED STATUS.

PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET. PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET. PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET. PERMIT MODIFIED FROM 1.4 LB SO2/MMBTU WHICH COULD NOT BE MET.

RACT CAP, NO EMISSION RATE LIMITS AS LB/MMBTU. THIS RACT MODIFICATION IS TO FACILITATE THE DETERMINATION OF EMISSION REDUCTION CREDITS. THESE BOILERS ARE IN DECOMMISSIONED STATUS.

RBLCID FACILITY CORPORAFACILITYSAGENCYNPERMITDAFACILITYDPROCESSTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLCA-1113 PRAXAIR PRAXAIR CA SOUTH CO3/15/2002 HEATER-OAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI VACUUM CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI VACUUM CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE C*TX-0496 INEOS CHINEOS US TX TEXAS CO8/29/2006 THE NO. FURNACE TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLIN-0075 GRAIN PRGRAIN PR IN INDIANA D6/10/1997 BOILERS NNJ-0031 UNIVERSI UNIVERSI NJ NEW JERS6/26/1997 BOILER, NAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, NAL-0115 ALABAMA ALABAMA AL ALABAMA ### DUCT BUAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, AL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, MO-0051 PROCTOR Proctor & MO MISSOURI 1/1/1998 SANITARYBOILERS, PA-0152 PEI POWEPEI POWEPA PENNSYLV5/22/1998 BOILER, CTX-0259 FREEPORTBASF CORTX TEXAS CO6/26/1998 CONSTRUCBOILER, BND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, LA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, LA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, NLA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, LA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, NAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO. 1 RETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO 1 INTTX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO. 1 RE

TX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO 1 INTTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE AR-0045 COLUMBIAColumbian AR ARKANSAS9-Aug-01 CHEMICALCOAL-FIRE*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARYTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLCA-1113 PRAXAIR PRAXAIR CA SOUTH CO3/15/2002 HEATER-OTN-0153 WILLIAMS WILLIAMS TN MEMPHIS 4/3/2002 PETROLEUBOILER, NTX-0437 HARTBURGHARTBURGTX TEXAS CO 7/5/2002 LOCATED ADUCT BUAR-0070 GENOVA AGENOVA AAR ARKANSAS8/23/2002 COMBINEDDUCT BULA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRBZ RECOVLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRBZ RECOVLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRREHEATERLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRREHEATERVA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER NVA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, NLA-0184 TITANIUM LOUISIAN LA LOUISIAN 5/13/2003 TITANIUM UTILITY BPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODINORTH CRPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED PA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODINORTH CRPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED LA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPOWERFORLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPOWERFOROH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2TX-0442 SHELL OI SHELL OI TX TEXAS CO7/30/2004 ULTRA-LOTWENTY OTX-0442 SHELL OI SHELL OI TX TEXAS CO7/30/2004 ULTRA-LODHT H2 HTX-0442 SHELL OI SHELL OI TX TEXAS CO7/30/2004 ULTRA-LOTWENTY OTX-0442 SHELL OI SHELL OI TX TEXAS CO7/30/2004 ULTRA-LODHT H2 HWI-0228 WPS - WE WISCONSIWI WISCONSI ### ELECTRICAAUXILLIARAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI VACUUM CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROCRAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI DISTILLAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI VACUUM CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROCRA

AZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI DISTILLAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CTX-0478 CITGO COCITGO RE TX TEXAS CO4/20/2005 MIXED DITX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C 1.8 MMBTTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSITX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 REBOILER LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS A LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS C LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS A LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS C NC-0101 FORSYTH FORSYTH NC FORSYTH 9/29/2005 THREE COAUXILLIARMN-0062 HEARTLAND CORN MN MINNESOT ### BOILERMN-0066 NORTHERNNORTHERNMN MINNESOT5/16/2006 POWER PLBOILER, A*TX-0499 SANDY CRSANDY CRTX TEXAS CO7/24/2006 THE PROPAUXILLAR*TX-0496 INEOS CHINEOS US TX TEXAS CO8/29/2006 THE NO. FURNACE NV-0043 LASCO B LASCO B NV CLARK CO ### A BATHWAFUEL BUR*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMA & B VAC*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMNAPHTHA *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMSATS GAS *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMA & B VAC*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMNAPHTHA *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMSATS GAS *LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUREBOILER 2*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUREBOILER 2*MS-0086 CHEVRON CHEVRONMS MISSISSIP 5/8/2007 PETROLEUREFORMATWI-0228 WPS - WE WISCONSIWI WISCONSI ### ELECTRICAAUXILLIARWI-0228 WPS - WE WISCONSIWI WISCONSI ### ELECTRICAAUXILLIARWI-0228 WPS - WE WISCONSIWI WISCONSI ### ELECTRICAAUXILLIARWI-0228 WPS - WE WISCONSIWI WISCONSI ### ELECTRICAAUXILLIAROR-0040 KLAMATH KLAMATH OR OREGON D3/12/2003 POWER GEDUCT BUVA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER NIN-0075 GRAIN PRGRAIN PR IN INDIANA D6/10/1997 BOILERS NNJ-0031 UNIVERSI UNIVERSI NJ NEW JERS6/26/1997 BOILER, NAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, NAL-0115 ALABAMA ALABAMA AL ALABAMA ### DUCT BUAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, AL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, MO-0051 PROCTOR Proctor & MO MISSOURI 1/1/1998 SANITARYBOILERS, PA-0152 PEI POWEPEI POWEPA PENNSYLV5/22/1998 BOILER, CTX-0259 FREEPORTBASF CORTX TEXAS CO6/26/1998 CONSTRUCBOILER, BND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, LA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, LA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, NLA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, LA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, N

TX-0429 VALERO REVALERO RETX TEXAS CO2/23/2000 SITE IS A BOILERS AK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO. 1 RETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO 1 INTTX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO. 1 RETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO 1 INTTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE *NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARYTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLCA-1113 PRAXAIR PRAXAIR CA SOUTH CO3/15/2002 HEATER-OTN-0153 WILLIAMS WILLIAMS TN MEMPHIS 4/3/2002 PETROLEUBOILER, NLA-0121 CONVENT MOTIVA E LA LOUISIAN 5/17/2002 PERMIT ISHDS-1 HELA-0121 CONVENT MOTIVA E LA LOUISIAN 5/17/2002 PERMIT ISHDS-1 HEAR-0070 GENOVA AGENOVA AAR ARKANSAS8/23/2002 COMBINEDDUCT BUVA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, NOK-0089 TPI PETR TPI PETROOK OKLAHOMA6/9/2003 FACILITY CRUDE UNOK-0089 TPI PETR TPI PETROOK OKLAHOMA6/9/2003 FACILITY CRUDE UNLA-0197 ALLIANCE CONOCOPHLA LOUISIAN 10/3/2003 CLEAN FULOW SULFPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODINORTH CRPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED PA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODINORTH CRPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED OK-0098 PONCA CI CONOCOPHOK OKLAHOMA3/31/2004 CRUDE OICRUDE VAOK-0098 PONCA CI CONOCOPHOK OKLAHOMA3/31/2004 CRUDE OICRUDE CHID-0015 J R SIMPL J R SIMP ID IDAHO DE 4/5/2004 THE DON SBOILER, 1OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2WI-0228 WPS - WE WISCONSIWI WISCONSI ### ELECTRICAAUXILLIARAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI VACUUM CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROCRAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI DISTILLAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI VACUUM CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROCRA

AZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI DISTILLAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CTX-0478 CITGO COCITGO RE TX TEXAS CO4/20/2005 MIXED DITX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C 1.8 MMBTTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSITX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 REBOILER LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS A LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS C LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS A LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS C NC-0101 FORSYTH FORSYTH NC FORSYTH 9/29/2005 THREE COAUXILLIARMN-0062 HEARTLAND CORN MN MINNESOT ### BOILER*TX-0499 SANDY CRSANDY CRTX TEXAS CO7/24/2006 THE PROPAUXILLAR*TX-0496 INEOS CHINEOS US TX TEXAS CO8/29/2006 THE NO. FURNACE NV-0043 LASCO B LASCO B NV CLARK CO ### A BATHWAFUEL BUR*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMA & B VAC*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMNAPHTHA *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMSATS GAS *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMA & B VAC*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMNAPHTHA *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMSATS GAS *LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUREBOILER 2*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUREBOILER 2*MS-0086 CHEVRON CHEVRONMS MISSISSIP 5/8/2007 PETROLEUREFORMATAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, NAL-0115 ALABAMA ALABAMA AL ALABAMA ### DUCT BUAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, AL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, TX-0259 FREEPORTBASF CORTX TEXAS CO6/26/1998 CONSTRUCBOILER, BND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, LA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, LA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, NLA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, LA-0119 LAKE CHACONOCO ILA LOUISIAN 8/12/1999 PERMIT T HEATER, NAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HETX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE *NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARYTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYL

TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLVA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER N*TX-0499 SANDY CRSANDY CRTX TEXAS CO7/24/2006 THE PROPAUXILLARIN-0075 GRAIN PRGRAIN PR IN INDIANA D6/10/1997 BOILERS NMO-0051 PROCTOR Proctor & MO MISSOURI 1/1/1998 SANITARYBOILERS, LA-0128 CONVENT MOTIVA E LA LOUISIAN 8/12/1999 PETROLEUVPS1 ATMLA-0128 CONVENT MOTIVA E LA LOUISIAN 8/12/1999 PETROLEUCRU CHARLA-0128 CONVENT MOTIVA E LA LOUISIAN 8/12/1999 PETROLEUCRU INTELA-0128 CONVENT MOTIVA E LA LOUISIAN 8/12/1999 PETROLEUVPS1 ATMLA-0128 CONVENT MOTIVA E LA LOUISIAN 8/12/1999 PETROLEUCRU CHARLA-0128 CONVENT MOTIVA E LA LOUISIAN 8/12/1999 PETROLEUCRU INTETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO. 1 RETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO 1 INTTX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO. 1 RETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO 1 INTTN-0153 WILLIAMS WILLIAMS TN MEMPHIS 4/3/2002 PETROLEUBOILER, NLA-0121 CONVENT MOTIVA E LA LOUISIAN 5/17/2002 PERMIT ISHDS-1 HELA-0121 CONVENT MOTIVA E LA LOUISIAN 5/17/2002 PERMIT ISHDS-1 HEAR-0070 GENOVA AGENOVA AAR ARKANSAS8/23/2002 COMBINEDDUCT BULA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRBZ RECOVLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRBZ RECOVLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRREHEATERLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRREHEATERVA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER NVA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, NPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED PA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED LA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPOWERFORLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPOWERFOROK-0098 PONCA CI CONOCOPHOK OKLAHOMA3/31/2004 CRUDE OICRUDE VAOK-0098 PONCA CI CONOCOPHOK OKLAHOMA3/31/2004 CRUDE OICRUDE CHOH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2WI-0228 WPS - WE WISCONSIWI WISCONSI ### ELECTRICAAUXILLIARAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI VACUUM CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROCRAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI DISTILLAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI VACUUM CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROCRA

AZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI DISTILLAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CTX-0478 CITGO COCITGO RE TX TEXAS CO4/20/2005 MIXED DITX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C 1.8 MMBTTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSITX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 REBOILER LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS A LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS C LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS A LA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BBOILERS C NC-0101 FORSYTH FORSYTH NC FORSYTH 9/29/2005 THREE COAUXILLIAR*TX-0496 INEOS CHINEOS US TX TEXAS CO8/29/2006 THE NO. FURNACE NV-0043 LASCO B LASCO B NV CLARK CO ### A BATHWAFUEL BUR*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMA & B VAC*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMNAPHTHA *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMSATS GAS *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMA & B VAC*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMNAPHTHA *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMSATS GAS *LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUREBOILER 2*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUREBOILER 2NV-0043 LASCO B LASCO B NV CLARK CO ### A BATHWAFUEL BURIN-0075 GRAIN PRGRAIN PR IN INDIANA D6/10/1997 BOILERS NTX-0259 FREEPORTBASF CORTX TEXAS CO6/26/1998 CONSTRUCBOILER, BND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, LA-0149 LOUISIANAMARATHONLA LOUISIAN ### MARATHONCOKER HELA-0149 LOUISIANAMARATHONLA LOUISIAN ### MARATHONDEASPHALLA-0149 LOUISIANAMARATHONLA LOUISIAN ### MARATHONCOKER HELA-0149 LOUISIANAMARATHONLA LOUISIAN ### MARATHONDEASPHALAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO. 1 RETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO 1 INTTX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO. 1 RETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO 1 INTTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE *NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARYTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NO

TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLVA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER NVA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, NOK-0095 ARDMORE TPI PETROOK OKLAHOMA9/3/2003 HOT OIL LA-0197 ALLIANCE CONOCOPHLA LOUISIAN 10/3/2003 CLEAN FULOW SULFPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODINORTH CRPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED PA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODINORTH CRPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED LA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPOWERFORLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPOWERFOROH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2TX-0442 SHELL OI SHELL OI TX TEXAS CO7/30/2004 ULTRA-LOTWENTY OTX-0442 SHELL OI SHELL OI TX TEXAS CO7/30/2004 ULTRA-LODHT H2 HTX-0442 SHELL OI SHELL OI TX TEXAS CO7/30/2004 ULTRA-LOTWENTY OTX-0442 SHELL OI SHELL OI TX TEXAS CO7/30/2004 ULTRA-LODHT H2 HWI-0228 WPS - WE WISCONSIWI WISCONSI ### ELECTRICAAUXILLIARAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI VACUUM CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROCRAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI DISTILLAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI VACUUM CAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI HYDROCRAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI CATALYTIAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI DISTILLAAZ-0046 ARIZONA ARIZONA AZ ARIZONA 4/14/2005 OIL REFI BUTANE CTX-0478 CITGO COCITGO RE TX TEXAS CO4/20/2005 MIXED DITX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C 1.8 MMBTTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSITX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 REBOILER *TX-0499 SANDY CRSANDY CRTX TEXAS CO7/24/2006 THE PROPAUXILLAR*TX-0496 INEOS CHINEOS US TX TEXAS CO8/29/2006 THE NO. FURNACE *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMA & B VAC*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMNAPHTHA *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMSATS GAS *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMA & B VAC*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMNAPHTHA *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMSATS GAS

*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUREBOILER 2*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUREBOILER 2NC-0101 FORSYTH FORSYTH NC FORSYTH 9/29/2005 THREE COAUXILLIARLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPOWERFORLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPIPESTILLA-0206 BATON ROEXXONMOBLA LOUISIAN 2/18/2004 PETROLEUPOWERFORWI-0228 WPS - WE WISCONSIWI WISCONSI ### ELECTRICAAUXILLIARPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED PA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED AL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, NAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, AL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, TX-0259 FREEPORTBASF CORTX TEXAS CO6/26/1998 CONSTRUCBOILER, BND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, AK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0037 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HETX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLVA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, NIN-0075 GRAIN PRGRAIN PR IN INDIANA D6/10/1997 BOILERS NAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, NAL-0115 ALABAMA ALABAMA AL ALABAMA ### DUCT BUAL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, AL-0115 ALABAMA ALABAMA AL ALABAMA ### BOILER, MO-0051 PROCTOR Proctor & MO MISSOURI 1/1/1998 SANITARYBOILERS, TX-0259 FREEPORTBASF CORTX TEXAS CO6/26/1998 CONSTRUCBOILER, BTX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO. 1 RETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO 1 INTTX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO. 1 RETX-0395 DIAMOND DIAMOND TX TEXAS CO5/23/2000 NO 1 INTTX-0339 BAYTOWN EXXON MOTX TEXAS CO 4/5/2001 THE COMPFURNACE *NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARYTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO. TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBOILER NOTX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLBTU-NO.

TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLISOM II TX-0375 LYONDELL LYONDELL TX TEXAS CO3/14/2002 LYONDELLORTHOXYLAR-0070 GENOVA AGENOVA AAR ARKANSAS8/23/2002 COMBINEDDUCT BUVA-0270 VCU EASTVIRGINIA VA VIRGINIA 3/31/2003 BOILER NVA-0278 VCU EASTVirginia C VA VIRGINIA 3/31/2003 STEAM GEBOILER, NLA-0197 ALLIANCE CONOCOPHLA LOUISIAN 10/3/2003 CLEAN FULOW SULFPA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED PA-0231 UNITED R UNITED R PA PENNSYLV10/9/2003 THE MODIDELAYED OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2OH-0241 MILLER B MILLER B OH HAMILTON5/27/2004 BEER BREBOILER (2WI-0228 WPS - WE WISCONSIWI WISCONSI ### ELECTRICAAUXILLIARTX-0478 CITGO COCITGO RE TX TEXAS CO4/20/2005 MIXED DITX-0492 VIRTEX P VIRTEX P TX TEXAS CO 5/5/2005 VIRTEX C 1.8 MMBTTX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 PYROLYSITX-0475 FORMOSA FORMOSA TX TEXAS CO 5/9/2005 REBOILER NC-0101 FORSYTH FORSYTH NC FORSYTH 9/29/2005 THREE COAUXILLIARMN-0066 NORTHERNNORTHERNMN MINNESOT5/16/2006 POWER PLBOILER, A*TX-0499 SANDY CRSANDY CRTX TEXAS CO7/24/2006 THE PROPAUXILLAR*TX-0496 INEOS CHINEOS US TX TEXAS CO8/29/2006 THE NO. FURNACE NV-0043 LASCO B LASCO B NV CLARK CO ### A BATHWAFUEL BUR*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMA & B VAC*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMNAPHTHA *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMSATS GAS *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMA & B VAC*LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMNAPHTHA *LA-0211 GARYVILLMARATHONLA LOUISIAN ### PETROLEUMSATS GAS *LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUREBOILER 2*LA-0213 ST. CHAR VALERO RLA LOUISIAN 2/8/2007 PETROLEUREBOILER 2

PROCTYPEFUEL THRUPUT THRUPUTUPROCESSPOLLUTANCONTROLCTRLDESC12.39 121.74 MMBTU/H EMISSION Ammonia ( P LEAK DET12.39 104.25 MMBTU/H EMISSION Ammonia ( P LEAK DET12.39 226.42 MMBTU/H EMISSION Ammonia ( P LEAK DET12.39 121.74 MMBTU/H EMISSION Ammonia ( P LEAK DET12.39 104.25 MMBTU/H EMISSION Ammonia ( P LEAK DET12.39 226.42 MMBTU/H EMISSION Ammonia ( P LEAK DET12.39 WASTE G 117.6 MMBTU/H EQUIP: , Ammonia ( N12.39 REFINERY 101 MMBTU/H THIS UNITAmmonia ( N12.39 REFINERY 122 MMBTU/H THIS UNITAmmonia ( N12.39 REFINERY 192 MMBTU/H THIS EQUIAmmonia ( N12.39 REFINERY 129 MMBTU/H THIS EQUIAmmonia ( N12.39 REFINERY 222 MMBTU/H THIS EQUIAmmonia ( N12.39 REFINERY 101 MMBTU/H THIS UNITAmmonia ( N12.39 REFINERY 122 MMBTU/H THIS UNITAmmonia ( N12.39 REFINERY 192 MMBTU/H THIS EQUIAmmonia ( N12.39 REFINERY 129 MMBTU/H THIS EQUIAmmonia ( N12.39 REFINERY 222 MMBTU/H THIS EQUIAmmonia ( N12.39 EMISSIONAmmonia ( N12.39 245 MMBTU/H EMISSION Benzene N NONE IND12.39 121.74 MMBTU/H EMISSION Benzene N NONE IND12.39 104.25 MMBTU/H EMISSION Benzene N NONE IND12.39 226.42 MMBTU/H EMISSION Benzene N12.39 245 MMBTU/H EMISSION Benzene N NONE IND12.39 121.74 MMBTU/H EMISSION Benzene N NONE IND12.39 104.25 MMBTU/H EMISSION Benzene N NONE IND12.39 226.42 MMBTU/H EMISSION Benzene N12.39 NATURAL 244 MMBTU/H STACK TESCarbon MoP GOOD CO12.31 NATURAL 112 MMBTU/H SEPARATECarbon MoN12.31 NATURAL 190 MMBTU/H NATURAL Carbon MoA12.39 NAT GAS/ 260 MMBTU/H Carbon MoP GOOD COM12.39 HYDROGE 190 MMBTU/H NATURAL Carbon MoA12.39 NAT GAS/ 190 MMBTU/H NATURAL Carbon MoA12.31 NATURAL 1095 MMCF/YR ADDITION Carbon MoP LOW NOX 12.39 LANDFILL 249 MMBTU/H MFG. BY Carbon MoN12.39 H2 WASTE 213 MMBTU/H HYDROGENCarbon MoN NONE IND12.31 NATURAL 189 MMBTU/H No add-on cCarbon MoN12.39 NATURAL 150 MMBTU/H HEATER BCarbon MoP ULTRA LO12.39 NATURAL 237 MMBTU/H UNIT BUR Carbon MoP ULTRA LO12.39 NATURAL 150 MMBTU/H HEATER BCarbon MoP ULTRA LO12.39 NATURAL 237 MMBTU/H UNIT BUR Carbon MoP ULTRA LO12.39 NATURAL 140 MMBTU/H INSTALLE Carbon MoN NONE IND12.39 NATURAL 165 MMBTU/H DESIGN CACarbon MoN NONE IND12.39 NATURAL 140 MMBTU/H INSTALLE Carbon MoN NONE IND12.39 NATURAL 165 MMBTU/H DESIGN CACarbon MoN NONE IND12.39 REFINERY 248 MMBTU/H Carbon MoN12.39 REFINERY 147.2 MMBTU/H Carbon MoN12.39 REFINERY 248 MMBTU/H Carbon MoN

12.39 REFINERY 147.2 MMBTU/H Carbon MoN12.39 ETHANE 238 MMBTU/H 200 MMBTCarbon MoN NONE IND12.11 SUB-BITU 8700 MMBTU/H CO catalystCarbon MoP (NO CONT12.31 NATURAL 120 MMBTU/H Carbon MoP GOOD COM12.31 NATURAL 120 MMBTU/H Carbon MoP GOOD COM12.39 245 MMBTU/H EMISSION Carbon MoN NONE IND12.39 121.74 MMBTU/H EMISSION Carbon MoN NONE IND12.39 104.25 MMBTU/H EMISSION Carbon MoN NONE IND12.39 226.42 MMBTU/H EMISSION Carbon MoN NONE IND12.39 245 MMBTU/H EMISSION Carbon MoN NONE IND12.39 121.74 MMBTU/H EMISSION Carbon MoN NONE IND12.39 104.25 MMBTU/H EMISSION Carbon MoN NONE IND12.39 226.42 MMBTU/H EMISSION Carbon MoN NONE IND12.39 WASTE G 117.6 MMBTU/H EQUIP: , Carbon MoN12.31 NATURAL 180 MMBTU/H annual capaCarbon MoN12.31 NATURAL GAS Carbon MoP GOOD COM12.31 NATURAL 200 MMBTU/H 2 DUCT B Carbon MoP GOOD COM12.31 182.1 MMBTU/H Carbon MoP GOOD COM12.31 182.1 MMBTU/H Carbon MoP GOOD COM12.39 NATURAL 195 MMBTU/H 84.6 MMB Carbon MoP GOOD COM12.39 NATURAL 195 MMBTU/H 84.6 MMB Carbon MoP GOOD COM12.31 NATURAL 150 MMBTU/H This is one Carbon MoP GOOD COM12.31 NATURAL 150.6 MMBTU/H Throughput Carbon MoP GOOD COM12.31 NATURAL 135 MMBTU/H Carbon MoP GOOD EQU12.39 REFINERY 147 MMBTU/H The north cCarbon MoP BACT AND12.39 REFINERY 116 MMBTU/H The unit i Carbon MoP GOOD COM12.39 REFINERY 147 MMBTU/H The north cCarbon MoP BACT AND12.39 REFINERY 116 MMBTU/H The unit i Carbon MoP GOOD COM12.39 PIPESTILLCarbon MoP GOOD ENG12.39 POWERFORCarbon MoP GOOD ENG12.39 PIPESTILLCarbon MoP GOOD ENG12.39 POWERFORCarbon MoP GOOD ENG12.31 NATURAL 238 MMBTU/H TWO BOILECarbon MoN12.31 NATURAL 238 MMBTU/H TWO BOILECarbon MoN12.39 REFINERY FUEL GAS Carbon MoN12.39 HYDROGEN Carbon MoN12.39 REFINERY FUEL GAS Carbon MoN12.39 HYDROGEN Carbon MoN12.31 NATURAL 229.8 MMBTU/H THE AUXI Carbon MoP NATURAL 12.39 REFINERY 101 MMBTU/H THIS UNITCarbon MoN12.39 REFINERY 211 MMBTU/H THIS UNITCarbon MoN12.39 REFINERY 122 MMBTU/H THIS UNITCarbon MoN12.39 REFINERY 192 MMBTU/H THIS EQUICarbon MoN12.39 REFINERY 129 MMBTU/H THIS EQUICarbon MoN12.39 REFINERY 117 MMBTU/H THIS EQUICarbon MoN12.39 REFINERY 222 MMBTU/H THIS EQUICarbon MoN12.39 REFINERY 101 MMBTU/H THIS UNITCarbon MoN12.39 REFINERY 211 MMBTU/H THIS UNITCarbon MoN

12.39 REFINERY 122 MMBTU/H THIS UNITCarbon MoN12.39 REFINERY 192 MMBTU/H THIS EQUICarbon MoN12.39 REFINERY 129 MMBTU/H THIS EQUICarbon MoN12.39 REFINERY 117 MMBTU/H THIS EQUICarbon MoN12.39 REFINERY 222 MMBTU/H THIS EQUICarbon MoN12.39 REFINERY 82 MMBTU/H THE MDH Carbon MoN12.39 SWEET NA 1.8 MMBTU Carbon MoN12.39 FUEL GAS 250 MMBtu/H Carbon MoN12.39 FUEL GAS 250 MMBtu Carbon MoN12.39 250 MMBTU/H Carbon MoP GOOD COM12.39 250 MMBTU/H Carbon MoP GOOD COM12.39 250 MMBTU/H Carbon MoP GOOD COM12.39 250 MMBTU/H Carbon MoP GOOD COM12.31 NATURAL 110.2 MMBTU/H Carbon MoP LOW-NOX 12.31 NATURAL 198 MMBTU/H INCLUDESCarbon MoN12.31 NATURAL 160 mmbtu/h Carbon MoP GOOD CO12.31 NATURAL 175 MMBTU/H Carbon MoN12.39 EMISSIONCarbon MoN12.31 PROPANE 6.3 MMBTU/H THERMOSECarbon MoN N/A12.39 REFINERY 155.2 MMBTU/H EA. Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY FUEL GAS 6-08: 138 Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY 183.3 MMBTU/H Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY 155.2 MMBTU/H EA. Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY FUEL GAS 6-08: 138 Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY 183.3 MMBTU/H Carbon MoP PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY FUEL GAS 6-81: 135 Carbon MoP PROPER E12.39 REFINERY FUEL GAS 6-81: 135 Carbon MoP PROPER E12.39 REFINERY 160 MMBTU/H Carbon MoN12.31 NATURAL 229.8 MMBTU/H THE AUXI Fluorine P NATURAL 12.31 NATURAL 229.8 MMBTU/H THE AUXI Hazardous P GOOD COM12.31 NATURAL 229.8 MMBTU/H THE AUXI Lead (Pb) P NATURAL 12.31 NATURAL 229.8 MMBTU/H THE AUXI Mercury P NATURAL 12.31 NATURAL 250 MMBTU/H Throughput Nitrogen D B DLN COMB12.31 NATURAL 150 MMBTU/H This is one Nitrogen D B GOOD COM12.39 NATURAL 244 MMBTU/H STACK TESNitrogen O P LOW NOX 12.31 NATURAL 112 MMBTU/H SEPARATENitrogen O N12.31 NATURAL 190 MMBTU/H NATURAL Nitrogen O A LOW NOX 12.39 NAT GAS/ 260 MMBTU/H Nitrogen O P12.39 HYDROGE 190 MMBTU/H NATURAL Nitrogen O A12.39 NAT GAS/ 190 MMBTU/H NATURAL Nitrogen O A12.31 NATURAL 1095 MMCF/YR ADDITION Nitrogen O P LOW NOX F12.39 LANDFILL 249 MMBTU/H MFG. BY Nitrogen O P LNB WITH12.39 H2 WASTE 213 MMBTU/H HYDROGENNitrogen O N NONE IND12.31 NATURAL 189 MMBTU/H No add-on cNitrogen O N12.39 NATURAL 150 MMBTU/H HEATER BNitrogen O P ULTRA LO12.39 NATURAL 237 MMBTU/H UNIT BUR Nitrogen O P ULTRA LO12.39 NATURAL 150 MMBTU/H HEATER BNitrogen O P ULTRA LO12.39 NATURAL 237 MMBTU/H UNIT BUR Nitrogen O P ULTRA LO

12.39 NATURAL GAS FUELS ARNitrogen O P ULTRA LO12.39 NATURAL 140 MMBTU/H INSTALLE Nitrogen O N NONE IND12.39 NATURAL 165 MMBTU/H DESIGN CANitrogen O N NONE IND12.39 NATURAL 140 MMBTU/H INSTALLE Nitrogen O N NONE IND12.39 NATURAL 165 MMBTU/H DESIGN CANitrogen O N NONE IND12.39 REFINERY 248 MMBTU/H Nitrogen O N12.39 REFINERY 147.2 MMBTU/H Nitrogen O N12.39 REFINERY 248 MMBTU/H Nitrogen O N12.39 REFINERY 147.2 MMBTU/H Nitrogen O N12.39 ETHANE 238 MMBTU/H 200 MMBTNitrogen O N NONE IND12.31 NATURAL 120 MMBTU/H Nitrogen O P LIMITED O12.31 NATURAL 120 MMBTU/H Nitrogen O P LIMITED O12.39 245 MMBTU/H EMISSION Nitrogen O N12.39 121.74 MMBTU/H EMISSION Nitrogen O A SCR12.39 104.25 MMBTU/H EMISSION Nitrogen O A SCR12.39 226.42 MMBTU/H EMISSION Nitrogen O A SCR12.39 245 MMBTU/H EMISSION Nitrogen O N12.39 121.74 MMBTU/H EMISSION Nitrogen O A SCR12.39 104.25 MMBTU/H EMISSION Nitrogen O A SCR12.39 226.42 MMBTU/H EMISSION Nitrogen O A SCR12.39 WASTE G 117.6 MMBTU/H EQUIP: , Nitrogen O A SCR SYST12.31 NATURAL 180 MMBTU/H annual capaNitrogen O N12.39 FUEL GAS 140 MMBTU/H EMISSION Nitrogen O P ULTRA LO12.39 FUEL GAS 140 MMBTU/H EMISSION Nitrogen O P ULTRA LO12.31 NATURAL 200 MMBTU/H 2 DUCT B Nitrogen O B LOW NOX 12.31 NATURAL 150.6 MMBTU/H Throughput Nitrogen O P LOW NOX 12.39 145 MMBTU/H Nitrogen O P ULTRA LO12.39 135 MMBTU/H Nitrogen O P ULTRA LO12.39 FUEL GAS 138.12 MMBTU/H AVERAGE Nitrogen O P ULTRA LO12.39 REFINERY 147 MMBTU/H The north cNitrogen O P LOW NOX 12.39 REFINERY 116 MMBTU/H The unit i Nitrogen O P LOW NOX 12.39 REFINERY 147 MMBTU/H The north cNitrogen O P LOW NOX 12.39 REFINERY 116 MMBTU/H The unit i Nitrogen O P LOW NOX 12.39 REFINERY FUEL GAS Compliance Nitrogen O P ULTRA LO12.39 REFINERY FUEL GAS Compliance Nitrogen O B ULTRA LO12.31 NATURAL 175 MMBTU/H HPB&W BONitrogen O P LOW-NOX12.31 NATURAL 238 MMBTU/H TWO BOILENitrogen O P OVERFIRE12.31 NATURAL 238 MMBTU/H TWO BOILENitrogen O P OVERFIRE12.31 NATURAL 229.8 MMBTU/H THE AUXI Nitrogen O P NATURAL 12.39 REFINERY 101 MMBTU/H THIS UNITNitrogen O A LOW NOX 12.39 REFINERY 211 MMBTU/H THIS UNITNitrogen O A LOW-NOX12.39 REFINERY 122 MMBTU/H THIS UNITNitrogen O A LOW NOX 12.39 REFINERY 192 MMBTU/H THIS EQUINitrogen O A LOW NOX 12.39 REFINERY 129 MMBTU/H THIS EQUINitrogen O A LOW NOX 12.39 REFINERY 117 MMBTU/H THIS EQUINitrogen O P LOW NOX 12.39 REFINERY 222 MMBTU/H THIS EQUINitrogen O B LOW NOX 12.39 REFINERY 101 MMBTU/H THIS UNITNitrogen O A LOW NOX 12.39 REFINERY 211 MMBTU/H THIS UNITNitrogen O A LOW-NOX

12.39 REFINERY 122 MMBTU/H THIS UNITNitrogen O A LOW NOX 12.39 REFINERY 192 MMBTU/H THIS EQUINitrogen O A LOW NOX 12.39 REFINERY 129 MMBTU/H THIS EQUINitrogen O A LOW NOX 12.39 REFINERY 117 MMBTU/H THIS EQUINitrogen O P LOW NOX 12.39 REFINERY 222 MMBTU/H THIS EQUINitrogen O B LOW NOX 12.39 REFINERY 82 MMBTU/H THE MDH Nitrogen O A LOW NOX 12.39 SWEET NA 1.8 MMBTU Nitrogen O N12.39 FUEL GAS 250 MMBtu/H Nitrogen O B THE PYRO12.39 FUEL GAS 250 MMBtu Nitrogen O B THE PYRO12.39 250 MMBTU/H Nitrogen O B LOW NOX 12.39 250 MMBTU/H Nitrogen O A LOW NOX 12.39 250 MMBTU/H Nitrogen O B LOW NOX 12.39 250 MMBTU/H Nitrogen O A LOW NOX 12.31 NATURAL 110.2 MMBTU/H Nitrogen O P LOW-NOX 12.31 NATURAL 198 MMBTU/H INCLUDESNitrogen O N12.31 NATURAL 175 MMBTU/H Nitrogen O N12.39 EMISSIONNitrogen O N12.31 PROPANE 6.3 MMBTU/H THERMOSENitrogen O N N/A12.39 REFINERY 155.2 MMBTU/H EA. Nitrogen O B ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC12.39 REFINERY FUEL GAS 6-08: 138 Nitrogen O P ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT12.39 REFINERY 183.3 MMBTU/H Nitrogen O P ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT12.39 REFINERY 155.2 MMBTU/H EA. Nitrogen O B ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC12.39 REFINERY FUEL GAS 6-08: 138 Nitrogen O P ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT12.39 REFINERY 183.3 MMBTU/H Nitrogen O P ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT12.39 REFINERY FUEL GAS 6-81: 135 Nitrogen O P ULTRA LO12.39 REFINERY FUEL GAS 6-81: 135 Nitrogen O P ULTRA LO12.39 REFINERY 160 MMBTU/H Nitrogen O P ULTRA LO12.31 NATURAL 190 MMBTU/H NATURAL Particulate A12.39 NAT GAS/ 260 MMBTU/H Particulate P GOOD COM12.39 HYDROGE 190 MMBTU/H NATURAL Particulate A12.39 NAT GAS/ 190 MMBTU/H NATURAL Particulate A12.39 H2 WASTE 213 MMBTU/H HYDROGENParticulate P USE OF G12.31 NATURAL 189 MMBTU/H No add-on cParticulate N12.39 NATURAL 150 MMBTU/H HEATER BParticulate P GOOD COM12.39 NATURAL 237 MMBTU/H UNIT BUR Particulate P GOOD COM12.39 NATURAL 150 MMBTU/H HEATER BParticulate P GOOD COM12.39 NATURAL 237 MMBTU/H UNIT BUR Particulate P GOOD COM12.39 NATURAL 140 MMBTU/H INSTALLE Particulate N NONE IND12.39 NATURAL 165 MMBTU/H DESIGN CAParticulate N NONE IND12.39 NATURAL 140 MMBTU/H INSTALLE Particulate N NONE IND12.39 NATURAL 165 MMBTU/H DESIGN CAParticulate N NONE IND12.39 ETHANE 238 MMBTU/H 200 MMBTParticulate N NONE IND12.31 NATURAL 120 MMBTU/H Particulate P GOOD COM12.31 NATURAL 120 MMBTU/H Particulate P GOOD COM12.39 245 MMBTU/H EMISSION Particulate P LOW S FUE12.39 121.74 MMBTU/H EMISSION Particulate P LOW S FUE12.39 104.25 MMBTU/H EMISSION Particulate P LOW S FUE12.39 226.42 MMBTU/H EMISSION Particulate P LOW SULF

12.39 245 MMBTU/H EMISSION Particulate P LOW S FUE12.39 121.74 MMBTU/H EMISSION Particulate P LOW S FUE12.39 104.25 MMBTU/H EMISSION Particulate P LOW S FUE12.39 226.42 MMBTU/H EMISSION Particulate P LOW SULF12.31 NATURAL 150 MMBTU/H This is one Particulate P GOOD COM12.31 NATURAL 175 MMBTU/H Particulate N12.39 NATURAL 244 MMBTU/H STACK TESParticulate N12.31 NATURAL 1095 MMCF/YR ADDITION Particulate P LOW NOX 12.39 REFINERY 201 MMBTU/H EMISSION Particulate P GOOD COM12.39 REFINERY 144 MMBTU/H EMISSION Particulate P GOOD COM12.39 REFINERY 140 MMBTU/H EMISSION Particulate P GOOD COM12.39 REFINERY 201 MMBTU/H EMISSION Particulate P GOOD COM12.39 REFINERY 144 MMBTU/H EMISSION Particulate P GOOD COM12.39 REFINERY 140 MMBTU/H EMISSION Particulate P GOOD COM12.39 REFINERY 248 MMBTU/H Particulate N12.39 REFINERY 147.2 MMBTU/H Particulate N12.39 REFINERY 248 MMBTU/H Particulate N12.39 REFINERY 147.2 MMBTU/H Particulate N12.31 NATURAL 180 MMBTU/H annual capaParticulate N12.39 FUEL GAS 140 MMBTU/H EMISSION Particulate P GOOD COM12.39 FUEL GAS 140 MMBTU/H EMISSION Particulate P GOOD COM12.31 NATURAL 200 MMBTU/H 2 DUCT B Particulate P GOOD COM12.31 182.1 MMBTU/H Particulate P USE OF C12.31 182.1 MMBTU/H Particulate P USE OF C12.39 NATURAL 195 MMBTU/H 84.6 MMB Particulate P USE OF C12.39 NATURAL 195 MMBTU/H 84.6 MMB Particulate P USE OF C12.31 NATURAL 150 MMBTU/H This is one Particulate P GOOD COM12.31 NATURAL 150.6 MMBTU/H Throughput Particulate N12.39 REFINERY 116 MMBTU/H The unit i Particulate P SPRAY CH12.39 REFINERY 116 MMBTU/H The unit i Particulate P SPRAY CH12.39 PIPESTILLParticulate P GOOD ENG12.39 POWERFORParticulate P GOOD ENG12.39 PIPESTILLParticulate P GOOD ENG12.39 POWERFORParticulate P GOOD ENG12.39 REFINERY FUEL GAS Compliance Particulate P GOOD COM12.39 REFINERY FUEL GAS Compliance Particulate P GOOD COM12.31 NATURAL 238 MMBTU/H TWO BOILEParticulate A BAGHOUS12.31 NATURAL 238 MMBTU/H TWO BOILEParticulate A BAGHOUS12.31 NATURAL 229.8 MMBTU/H THE AUXI Particulate P NATURAL 12.39 REFINERY 101 MMBTU/H THIS UNITParticulate N12.39 REFINERY 211 MMBTU/H THIS UNITParticulate N12.39 REFINERY 122 MMBTU/H THIS UNITParticulate N12.39 REFINERY 192 MMBTU/H THIS EQUIParticulate N12.39 REFINERY 129 MMBTU/H THIS EQUIParticulate N12.39 REFINERY 117 MMBTU/H THIS EQUIParticulate N12.39 REFINERY 222 MMBTU/H THIS EQUIParticulate N12.39 REFINERY 101 MMBTU/H THIS UNITParticulate N12.39 REFINERY 211 MMBTU/H THIS UNITParticulate N

12.39 REFINERY 122 MMBTU/H THIS UNITParticulate N12.39 REFINERY 192 MMBTU/H THIS EQUIParticulate N12.39 REFINERY 129 MMBTU/H THIS EQUIParticulate N12.39 REFINERY 117 MMBTU/H THIS EQUIParticulate N12.39 REFINERY 222 MMBTU/H THIS EQUIParticulate N12.39 REFINERY 82 MMBTU/H THE MDH Particulate N12.39 SWEET NA 1.8 MMBTU Particulate N12.39 FUEL GAS 250 MMBtu/H Particulate N12.39 FUEL GAS 250 MMBtu Particulate N12.39 250 MMBTU/H Particulate P GOOD COM12.39 250 MMBTU/H Particulate P GOOD COM12.39 250 MMBTU/H Particulate P GOOD COM12.39 250 MMBTU/H Particulate P GOOD COM12.31 NATURAL 110.2 MMBTU/H Particulate N LOW-NOX 12.39 EMISSIONParticulate N12.31 PROPANE 6.3 MMBTU/H THERMOSEParticulate N N/A12.39 REFINERY 155.2 MMBTU/H EA. Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY FUEL GAS 6-08: 138 Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY 183.3 MMBTU/H Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY 155.2 MMBTU/H EA. Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY FUEL GAS 6-08: 138 Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY 183.3 MMBTU/H Particulate P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY FUEL GAS 6-81: 135 Particulate P PROPER E12.39 REFINERY FUEL GAS 6-81: 135 Particulate P PROPER E12.31 PROPANE 6.3 MMBTU/H THERMOSEStyrene N N/A12.39 NATURAL 244 MMBTU/H STACK TESSulfur DioxP GOOD COM12.39 H2 WASTE 213 MMBTU/H HYDROGENSulfur DioxP USE OF G12.31 NATURAL 189 MMBTU/H No add-on cSulfur DioxP NATURAL 12.39 241.1 MMBTU/H Sulfur DioxP USE OF L12.39 NAT & RE 221 MMBTU/H THE PERMSulfur DioxP LOW SULF12.39 241.1 MMBTU/H Sulfur DioxP USE OF L12.39 NAT & RE 221 MMBTU/H THE PERMSulfur DioxP LOW SULF12.39 NATURAL 140 MMBTU/H INSTALLE Sulfur DioxN NONE INDICATED AS SOURCE WAS INSTALLED PRIOR TO 1975 AND IS NOT SUBJECT TO BACT-PSD.12.39 NATURAL 165 MMBTU/H DESIGN CASulfur DioxP FUEL SULFUR CONTENT LIMITS 12.39 NATURAL 140 MMBTU/H INSTALLE Sulfur DioxN NONE INDICATED AS SOURCE WAS INSTALLED PRIOR TO 1975 AND IS NOT SUBJECT TO BACT-PSD.12.39 NATURAL 165 MMBTU/H DESIGN CASulfur DioxP FUEL SULFUR CONTENT LIMITS 12.39 REFINERY 248 MMBTU/H Sulfur DioxN12.39 REFINERY 147.2 MMBTU/H Sulfur DioxN12.39 REFINERY 248 MMBTU/H Sulfur DioxN12.39 REFINERY 147.2 MMBTU/H Sulfur DioxN12.39 ETHANE 238 MMBTU/H 200 MMBTSulfur DioxN NONE IND12.31 NATURAL 120 MMBTU/H Sulfur DioxP NATURAL 12.31 NATURAL 120 MMBTU/H Sulfur DioxP NATURAL 12.39 245 MMBTU/H EMISSION Sulfur DioxP LOW S FUE12.39 121.74 MMBTU/H EMISSION Sulfur DioxP LOW S FUE12.39 104.25 MMBTU/H EMISSION Sulfur DioxP LOW S FUE12.39 226.42 MMBTU/H EMISSION Sulfur DioxP LOW SULF12.39 245 MMBTU/H EMISSION Sulfur DioxP LOW S FUE

12.39 121.74 MMBTU/H EMISSION Sulfur DioxP LOW S FUE12.39 104.25 MMBTU/H EMISSION Sulfur DioxP LOW S FUE12.39 226.42 MMBTU/H EMISSION Sulfur DioxP LOW SULF12.31 NATURAL 150 MMBTU/H This is one Sulfur DioxP GOOD COM12.31 NATURAL 150.6 MMBTU/H Throughput Sulfur DioxP LOW SULF12.39 Sulfur DioxP LOW SULF12.39 FUEL GAS 138.12 MMBTU/H AVERAGE Sulfur DioxP COMBUSTI12.39 REFINERY 147 MMBTU/H The north cSulfur DioxP USE OF D12.39 REFINERY 116 MMBTU/H The unit i Sulfur DioxP LOW SULF12.39 REFINERY 147 MMBTU/H The north cSulfur DioxP USE OF D12.39 REFINERY 116 MMBTU/H The unit i Sulfur DioxP LOW SULF12.39 PIPESTILLSulfur DioxP LIMIT CON12.39 POWERFORSulfur DioxP LIMIT CON12.39 PIPESTILLSulfur DioxP LIMIT CON12.39 POWERFORSulfur DioxP LIMIT CON12.31 NATURAL 238 MMBTU/H TWO BOILESulfur DioxN12.31 NATURAL 238 MMBTU/H TWO BOILESulfur DioxN12.39 REFINERY FUEL GAS Sulfur DioxN12.39 HYDROGEN Sulfur DioxN12.39 REFINERY FUEL GAS Sulfur DioxN12.39 HYDROGEN Sulfur DioxN12.31 NATURAL 229.8 MMBTU/H THE AUXI Sulfur DioxP NATURAL 12.39 REFINERY 101 MMBTU/H THIS UNITSulfur DioxN12.39 REFINERY 211 MMBTU/H THIS UNITSulfur DioxP S LIMITED12.39 REFINERY 122 MMBTU/H THIS UNITSulfur DioxP SULFUR LI12.39 REFINERY 192 MMBTU/H THIS EQUISulfur DioxP S LIMITED12.39 REFINERY 129 MMBTU/H THIS EQUISulfur DioxP S LIMITED12.39 REFINERY 117 MMBTU/H THIS EQUISulfur DioxP S LIMITED12.39 REFINERY 222 MMBTU/H THIS EQUISulfur DioxP SULFUR LI12.39 REFINERY 101 MMBTU/H THIS UNITSulfur DioxN12.39 REFINERY 211 MMBTU/H THIS UNITSulfur DioxP S LIMITED12.39 REFINERY 122 MMBTU/H THIS UNITSulfur DioxP SULFUR LI12.39 REFINERY 192 MMBTU/H THIS EQUISulfur DioxP S LIMITED12.39 REFINERY 129 MMBTU/H THIS EQUISulfur DioxP S LIMITED12.39 REFINERY 117 MMBTU/H THIS EQUISulfur DioxP S LIMITED12.39 REFINERY 222 MMBTU/H THIS EQUISulfur DioxP SULFUR LI12.39 REFINERY 82 MMBTU/H THE MDH Sulfur DioxN12.39 SWEET NA 1.8 MMBTU Sulfur DioxN12.39 FUEL GAS 250 MMBtu/H Sulfur DioxN12.39 FUEL GAS 250 MMBtu Sulfur DioxN12.31 NATURAL 175 MMBTU/H Sulfur DioxN12.39 EMISSIONSulfur DioxN12.39 REFINERY 155.2 MMBTU/H EA. Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS12.39 REFINERY FUEL GAS 6-08: 138 Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS12.39 REFINERY 183.3 MMBTU/H Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS12.39 REFINERY 155.2 MMBTU/H EA. Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS12.39 REFINERY FUEL GAS 6-08: 138 Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS12.39 REFINERY 183.3 MMBTU/H Sulfur DioxN USE OF LOW SULFUR REFINERY FUEL GAS

12.39 REFINERY FUEL GAS 6-81: 135 Sulfur DioxN USE OF PIPELINE QUALITY N12.39 REFINERY FUEL GAS 6-81: 135 Sulfur DioxN USE OF PIPELINE QUALITY N12.31 NATURAL 110.2 MMBTU/H Sulfur Oxi P LOW-NOX 12.39 PIPESTILLSulfuric AciP LIMIT CONCENTRATION OF H2S 12.39 POWERFORSulfuric AciP LIMIT CONCENTRATION OF H2S 12.39 PIPESTILLSulfuric AciP LIMIT CONCENTRATION OF H2S 12.39 POWERFORSulfuric AciP LIMIT CONCENTRATION OF H2S 12.31 NATURAL 229.8 MMBTU/H THE AUXI Sulfuric AciP NATURAL 12.39 REFINERY 116 MMBTU/H The unit i Total Susp P SPRAY CH12.39 REFINERY 116 MMBTU/H The unit i Total Susp P SPRAY CH12.31 NATURAL 190 MMBTU/H NATURAL Visible EmiA12.39 HYDROGE 190 MMBTU/H NATURAL Visible EmiA12.39 NAT GAS/ 190 MMBTU/H NATURAL Visible EmiA12.39 H2 WASTE 213 MMBTU/H HYDROGENVisible EmiN NONE IND12.31 NATURAL 189 MMBTU/H No add-on cVisible EmiN12.39 NATURAL 140 MMBTU/H INSTALLE Visible EmiN NONE IND12.39 NATURAL 165 MMBTU/H DESIGN CAVisible EmiN NONE IND12.39 NATURAL 140 MMBTU/H INSTALLE Visible EmiN NONE IND12.39 NATURAL 165 MMBTU/H DESIGN CAVisible EmiN NONE IND12.39 245 MMBTU/H EMISSION Visible EmiN NONE IND12.39 121.74 MMBTU/H EMISSION Visible EmiN NONE IND12.39 104.25 MMBTU/H EMISSION Visible EmiN NONE IND12.39 226.42 MMBTU/H EMISSION Visible EmiN12.39 245 MMBTU/H EMISSION Visible EmiN NONE IND12.39 121.74 MMBTU/H EMISSION Visible EmiN NONE IND12.39 104.25 MMBTU/H EMISSION Visible EmiN NONE IND12.39 226.42 MMBTU/H EMISSION Visible EmiN12.31 NATURAL 150.6 MMBTU/H Throughput Visible EmiN12.39 NATURAL 244 MMBTU/H STACK TESVolatile O P GOOD COM12.31 NATURAL 190 MMBTU/H NATURAL Volatile O A12.39 NAT GAS/ 260 MMBTU/H Volatile O P12.39 HYDROGE 190 MMBTU/H NATURAL Volatile O A12.39 NAT GAS/ 190 MMBTU/H NATURAL Volatile O A12.31 NATURAL 1095 MMCF/YR ADDITION Volatile O P LOW NOX 12.39 H2 WASTE 213 MMBTU/H HYDROGENVolatile O P GOOD COM12.39 REFINERY 248 MMBTU/H Volatile O N12.39 REFINERY 147.2 MMBTU/H Volatile O N12.39 REFINERY 248 MMBTU/H Volatile O N12.39 REFINERY 147.2 MMBTU/H Volatile O N12.39 ETHANE 238 MMBTU/H 200 MMBTVolatile O N NONE IND12.31 NATURAL 120 MMBTU/H Volatile O P GOOD COM12.31 NATURAL 120 MMBTU/H Volatile O P GOOD COM12.39 245 MMBTU/H EMISSION Volatile O N NONE IND12.39 121.74 MMBTU/H EMISSION Volatile O N NONE IND12.39 104.25 MMBTU/H EMISSION Volatile O N NONE IND12.39 226.42 MMBTU/H EMISSION Volatile O N NONE IND12.39 245 MMBTU/H EMISSION Volatile O N NONE IND12.39 121.74 MMBTU/H EMISSION Volatile O N NONE IND

12.39 104.25 MMBTU/H EMISSION Volatile O N NONE IND12.39 226.42 MMBTU/H EMISSION Volatile O N NONE IND12.31 NATURAL 200 MMBTU/H 2 DUCT B Volatile O P GOOD COM12.31 NATURAL 150 MMBTU/H This is one Volatile O P GOOD COM12.31 NATURAL 150.6 MMBTU/H Throughput Volatile O P GOOD COM12.39 FUEL GAS 138.12 MMBTU/H AVERAGE Volatile O P GOOD COM12.39 REFINERY 116 MMBTU/H The unit i Volatile O P GOOD COM12.39 REFINERY 116 MMBTU/H The unit i Volatile O P GOOD COM12.31 NATURAL 238 MMBTU/H TWO BOILEVolatile O N12.31 NATURAL 238 MMBTU/H TWO BOILEVolatile O N12.31 NATURAL 229.8 MMBTU/H THE AUXI Volatile O P NATURAL 12.39 REFINERY 82 MMBTU/H THE MDH Volatile O N12.39 SWEET NA 1.8 MMBTU Volatile O N12.39 FUEL GAS 250 MMBtu/H Volatile O N12.39 FUEL GAS 250 MMBtu Volatile O N12.31 NATURAL 110.2 MMBTU/H Volatile O P LOW-NOX 12.31 NATURAL 160 mmbtu/h Volatile O P GOOD CO12.31 NATURAL 175 MMBTU/H Volatile O N12.39 EMISSIONVolatile O N12.31 PROPANE 6.3 MMBTU/H THERMOSEVolatile O N N/A12.39 REFINERY 155.2 MMBTU/H EA. Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY FUEL GAS 6-08: 138 Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY 183.3 MMBTU/H Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY 155.2 MMBTU/H EA. Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY FUEL GAS 6-08: 138 Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY 183.3 MMBTU/H Volatile O P PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES12.39 REFINERY FUEL GAS 6-81: 135 Volatile O P PROPER E12.39 REFINERY FUEL GAS 6-81: 135 Volatile O P PROPER E

EMISLIMITEMISLIMITEMISLIMI PCTEFFIC EMISLIMITEMISLIMITEMISLIMI STDEMISSL0.5 LB/H SEE NOTES 2.17 T/YR SEE NOTES

0.42 LB/H 1.86 T/YR0.92 LB/H SEE NOTES 4.04 T/YR SEE NOTES

0.5 LB/H SEE NOTES 2.17 T/YR SEE NOTES0.42 LB/H 1.86 T/YR0.92 LB/H SEE NOTES 4.04 T/YR SEE NOTES

5 PPMVD@31 H5 PPMVD THREE-HOUR ROLLING AVG5 PPMVD CORRECTED TO 0.0% OXYGEN ON A 3-HR AVG.5 PPMVD CORRECTED TO 0.0% OXYGEN - 3-HR AVG.5 PPMVD CORRECTED TO 0.0% OXYGEN - 3-HR AVERAGE5 PPMVD CORRECTED TO 0.0% OXYGEN - 3-HR AVERAGE5 PPMVD THREE-HOUR ROLLING AVG5 PPMVD CORRECTED TO 0.0% OXYGEN ON A 3-HR AVG.5 PPMVD CORRECTED TO 0.0% OXYGEN - 3-HR AVG.5 PPMVD CORRECTED TO 0.0% OXYGEN - 3-HR AVERAGE5 PPMVD CORRECTED TO 0.0% OXYGEN - 3-HR AVERAGE

27.47 LB/H 120.33 T/YR0.12 LB/H 0.53 T/YR0.06 LB/H 0.26 T/YR0.05 LB/H 0.22 T/YR0.11 LB/H 0.49 T/YR0.12 LB/H 0.53 T/YR0.06 LB/H 0.26 T/YR0.05 LB/H 0.22 T/YR0.11 LB/H 0.49 T/YR0.04 LB/MMBTU 0 0 0.04

0.17 LB/MMBTU 32.3 LB/H 0.170.07 LB/MMBTUABOVE 130 MMBTU/ 18.2 LB/H ABOVE 13 0.070.17 LB/MMBTU 32.3 LB/H 0.170.17 LB/MMBTU 32.3 LB/H 0.170.15 LB/MMBTU 0.150.15 LB/MMBTU 0 37 LB/H 0.1540.7 LB/H 175 T/YR 0.190.08 LB/MMBTU 0.08

3 LB/H* HOURLY MAXIMUM 13.1 T/YR* ANNUAL MAXIMUM4.7 LB/H* HOURLY MAXIMUM 20.8 T/YR* ANNUAL M 0.02

3 LB/H* HOURLY MAXIMUM 13.1 T/YR* ANNUAL MAXIMUM4.7 LB/H* HOURLY MAXIMUM 20.8 T/YR* ANNUAL M 0.02

0.04 LB/MMBTU 0.040.04 LB/MMBTU 0.040.04 LB/MMBTU 0.040.04 LB/MMBTU 0.046.95 LB/H 30.42 T/YR 0.034.13 LB/H 18.06 T/YR 0.036.95 LB/H 30.42 T/YR 0.03

4.13 LB/H 18.06 T/YR 0.0318.7 LB/H 7.3 T/YR 0.08100 PPM 24 hr. average

6 LB/H 10.8 T/YR 0.056 LB/H 10.8 T/YR 0.05

20.2 LB/H 88.4 T/YR 0.0810 LB/H 43.9 T/YR 0.082

8.6 LB/H 37.6 T/YR 0.08218.6 LB/H 81.7 T/YR 0.08220.2 LB/H 88.4 T/YR 0.08

10 LB/H 43.9 T/YR 0.0828.6 LB/H 37.6 T/YR 0.082

18.6 LB/H 81.7 T/YR 0.0824000 PPMVD @ 1H0.18 LB/MMBTU 0.180.03 LB/MMBTU 0.030.25 LB/MMBTU 0.25

15 LB/H HOURLY MAXIMUM 0.0815 LB/H HOURLY MAXIMUM 0.08

16.1 LB/H HOURLY MAXIMUM 0.0816.1 LB/H HOURLY MAXIMUM 0.0814.9 LB/H each unit 0.114.9 LB/H 0.1

12.229 LB/H HOURLY MAXIMUM 48.695 T/YR ANNUAL M 0.0919.27 LB/H 40.6 T/YR 0.0638.28 LB/H 36.3 T/YR 0.079.27 LB/H 40.6 T/YR 0.0638.28 LB/H 36.3 T/YR 0.07


20 LB/H EACH BOILER 87.6 T/YR EACH BOIL 0.08420 LB/H EACH BOILER 87.6 T/YR EACH BOIL 0.084

500 PPMV500 PPMV500 PPMV500 PPMV

0.08 LB/MMBTU2000 H / 12 MO. ROL 18.4 LB/H 0.080.04 LB/MMBTUTHREE-HOUR ROLLING AVG 0.040.04 LB/MMBTUTHREE-HOUR ROLLING AVG 0.040.04 LB/MMBTU3-HR AVERAGE0.04 LB/MMBTU3-HR AVERAGE 0.040.04 LB/MMBTU3-HR AVERAGE 0.040.04 LB/MMBTU3-HR AVERAGE 0.040.04 LB/MMBTU3-HR AVERAGE0.04 LB/MMBTUTHREE-HOUR ROLLING AVG 0.040.04 LB/MMBTUTHREE-HOUR ROLLING AVG 0.04

0.04 LB/MMBTU3-HR AVERAGE0.04 LB/MMBTU3-HR AVERAGE 0.040.04 LB/MMBTU3-HR AVERAGE 0.040.04 LB/MMBTU3-HR AVERAGE 0.040.04 LB/MMBTU3-HR AVERAGE



9.08 LB/H based on 3-hour average 0.08240.04 LB/MMBTU0.08 LB/MMBTU3-HR AVERAGE 0.08

6.1 LB/H200.78 LB/H 879.41 T/YR

0.13 LB/H 0 0.14 T/YRPROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.04

0.08 LB/MMBTUHOURLY AVERAGE0.08 LB/MMBTUHOURLY AVERAGE

24.96 LB/H 3-HR ROLLING AVE 24.53 T/YR 12-MONTH 500.0003 LB/MMBTU2000 H / 12 MO. ROLLING LIMIT

400 PPM CO @ 3% O20 LB/MMBTU2000 H / 12 MO. ROLLING

0.0001 LB/H 2000 H / 12 MO. ROLLING0.2 LB/MMBTU 0.20.1 LB/MMBTUeach unit 15.6 LB/H each unit 0.1

0.05 LB/MMBTU 0 0 0.050.55 LB/MMBTU 0.550.05 LB/MMBTU 9.5 LB/H 0.05

0.2 LB/MMBTU 34 LB/H0.07 LB/MMBTU 13.3 LB/H 0.070.07 LB/MMBTU 13.3 LB/H 0.070.08 LB/MMBTU 0.080.06 LB/MMBTU 0 15 LB/H 0.06

122.1 LB/H 535 T/YR 0.570.053 LB/MMBTU 0.053

6.8 LB/H* HOURLY MAXIMUM 25 T/YR* ANNUAL M 0.0389.1 LB/H* HOURLY MAXIMUM 33.2 T/YR* ANNUAL M 0.0326.8 LB/H* HOURLY MAXIMUM 25 T/YR* ANNUAL M 0.0389.1 LB/H* HOURLY MAXIMUM 33.2 T/YR* ANNUAL M 0.032

0.06 LB/MMBTU 0.060.25 LB/MMBTU 0.250.06 LB/MMBTU 0.060.25 LB/MMBTU 0.250.06 LB/MMBTU 0.0612.4 LB/H 54.32 T/YR 0.057.36 LB/H 32.24 T/YR 0.0512.4 LB/H 54.32 T/YR 0.057.36 LB/H 32.24 T/YR 0.0542.1 LB/H 52.6 T/YR 0.177

0.036 LB/MMBTU 4.32 LB/H 0.0360.036 LB/MMBTU 4.32 LB/H 0.036

19.6 LB/H 85.8 T/YR 0.084.4 LB/H SEE NOTES 19.2 T/YR SEE NOTE 0.0363.8 LB/H SEE NOTES 16.4 T/YR SEE NOTE 0.0368.2 LB/H SEE NOTES 35.7 T/YR SEE NOTE 0.036

19.6 LB/H 85.8 T/YR 0.084.4 LB/H SEE NOTES 19.2 T/YR SEE NOTE 0.0363.8 LB/H SEE NOTES 16.4 T/YR SEE NOTE 0.0368.2 LB/H SEE NOTES 35.7 T/YR SEE NOTE 0.03650 PPMVD @ 1H 0.061

0.06 LB/MMBTU 0.065.6 LB/H 17.52 T/YR 0.045.6 LB/H 17.52 T/YR 0.04

0.08 LB/MMBTU 0.0815.6 LB/H 0.1 LB/MMBTU30-day roll 0.08

0.045 LB/MMBTU 28.6 T/YR 0.0450.059 LB/MMBTU 34.9 T/YR 0.059

4.6 LB/H HOURLY MAXIMUM 20.17 T/YR ANNUAL M 0.046.68 LB/H 29.5 T/YR 0.0454.04 LB/H 17.7 T/YR 0.0356.68 LB/H 29.5 T/YR 0.0454.04 LB/H 17.7 T/YR 0.0353.73 LB/H 365 day rol 58 16.36 T/YR 0.0358.75 LB/H 365 day average 38.33 T/YR 0.05

7 LB/H 30.7 T/YR 0.040.7 LB/MMBTU 1375.9 T/YR BOTH BOI 0.70.7 LB/MMBTU 1375.9 T/YR BOTH BOI 0.70.1 LB/MMBTU2000 H / 12 MO. ROL 22.9 LB/H

0.0125 LB/MMBTUTHREE-HOUR ROLLING AVG 0.1250.025 LB/MMBTUTHREE HOUR ROLLING AVG 0.025

0.0125 LB/MMBTU3-HR AVERAGE 0.01250.0125 LB/MMBTU3-HOUR AVERAGE 0.01250.0125 LB/MMBTU3-HR AVERAGE 0.0125

0.032 LB/MMBTU3-HR AVERAGE 0.0320.0125 LB/MMBTU3-HR AVERAGE 0.01250.0125 LB/MMBTUTHREE-HOUR ROLLING AVG 0.125

0.025 LB/MMBTUTHREE HOUR ROLLING AVG 0.025

0.0125 LB/MMBTU3-HR AVERAGE 0.01250.0125 LB/MMBTU3-HOUR AVERAGE 0.01250.0125 LB/MMBTU3-HR AVERAGE 0.0125

0.032 LB/MMBTU3-HR AVERAGE 0.0320.0125 LB/MMBTU3-HR AVERAGE 0.0125

9.9 LB/H 43.3 T/YR0.17 LB/H 0.76 T/YR

18.75 LB/H 65.7 T/YR1.82 LB/H 7.97 T/YR0.04 LB/MMBTU24-HR ROLLING AVG BASED ON A 1-HR AVG 0.04

0.012 LB/MMBTU 0.0120.04 LB/MMBTU24-HR ROLLING AVG BASED ON A 1-HR AVG 0.04

0.012 LB/MMBTU 0.01215.13 LB/H based on 3-hour average 0.137

0.04 LB/MMBTU 0.041.8 LB/H

401.91 LB/H 1760.37 T/YR0.96 LB/H 0 1.06 T/YR

ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC 0.0125ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT 0.03ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT 0.03ULTRA LOW NOX BURNERS (ULNB) AND SELECTIVE CATALYTIC REDUCTION (SC 0.0125ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT 0.03ULTRA LOW NOX BURNERS (ULNB) WITHOUT AIR PREHEAT 0.03

0.04 LB/MMBTUTHREE 1-HOUR TEST AVERAGE0.04 LB/MMBTUTHREE 1-HOUR TEST AVERAGE

7.2 LB/H 3-HR ROLLING AVE 21.02 T/YR 12-MONTH 0.030.01 LB/MMBTU 1.9 LB/H 0.010.02 LB/MMBTU 2.9 LB/H 0.020.01 LB/MMBTU 1.9 LB/H 0.010.01 LB/MMBTU 1.9 LB/H 0.010.11 LB/H 0.48 T/YR 0.0005

0.014 LB/MMBTU 0.0141.1 LB/H HOURLY MAXIMUM 5 T/YR ANNUAL MAXIMUM1.8 LB/H HOURLY MAXIMUM 7.9 T/YR ANNUAL M 0.0081.1 LB/H HOURLY MAXIMUM 5 T/YR ANNUAL MAXIMUM1.8 LB/H HOURLY MAXIMUM 7.9 T/YR ANNUAL M 0.008



1.83 LB/H 8 T/YR 0.0071.56 LB/H SEE NOTES 6.8 T/YR SEE NOTE 0.0131.33 LB/H SEE NOTES 5.82 T/YR SEE NOTE 0.0132.89 LB/H SEE NOTES 12.65 T/YR SEE NOTE 0.013

1.83 LB/H 8 T/YR 0.0071.56 LB/H SEE NOTES 6.8 T/YR SEE NOTE 0.0131.33 LB/H SEE NOTES 5.82 T/YR SEE NOTE 0.0132.89 LB/H SEE NOTES 12.65 T/YR SEE NOTE 0.013

1.2 LB/H each unit 0.010.88 LB/H

5 LB/MMCF NG 0 2.44 LB/H EACH0.007 LB/MMBTU 0.007

1.56 LB/H 4.9 T/YR 0.021.29 LB/H 4.05 T/YR 0.021.36 LB/H 4.24 T/YR 0.021.56 LB/H 4.9 T/YR 0.021.29 LB/H 4.05 T/YR 0.021.36 LB/H 4.24 T/YR 0.022.64 LB/H 11.56 T/YR1.57 LB/H 6.86 T/YR2.64 LB/H 11.56 T/YR1.57 LB/H 6.86 T/YR

0.0075 LB/MMBTU 0.00751.04 LB/H 3.26 T/YR 0.021.04 LB/H 3.26 T/YR 0.020.02 LB/MMBTU 0.02

1.4 LB/H HOURLY MAXIMUM 0.011.4 LB/H HOURLY MAXIMUM 0.011.5 LB/H HOURLY MAXIMUM 0.011.5 LB/H HOURLY MAXIMUM 0.011.2 LB/H each unit 0.011.2 LB/H 0.0080.1 LB/H 0.4 T/YR 0.00090.1 LB/H 0.4 T/YR 0.0009


0.8 LB/H 365 day average 3.48 T/YR 0.00751.31 LB/H 365 day average 5.75 T/YR 0.00750.01 GR/ACF 122.9 T/YR BOTH BOI 0.020.01 GR/ACF 122.9 T/YR BOTH BOI 0.02

0.0075 LB/MMBTU2000 H / 12 MO. ROL 1.712 LB/H0.0075 LB/MMBTUTHREE-HOUR AVERAGE 0.00750.0075 LB/MMBTUTHREE-HOUR AVG 0.00750.0075 LB/MMBTU3-HR AVG.0.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE0.0075 LB/MMBTUTHREE-HOUR AVERAGE 0.00750.0075 LB/MMBTUTHREE-HOUR AVG 0.0075

0.0075 LB/MMBTU3-HR AVG.0.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE 0.00750.0075 LB/MMBTU3-HR AVERAGE

0.61 LB/H 2.7 T/YR0.01 LB/H 0.06 T/YR

0.5 LB/H 2.2 T/YR0.03 LB/H 0.13 T/YR

0.005 LB/MMBTUTHREE ONE-HOUR TEST AVERAGE 0.0050.005 LB/MMBTU 0.0050.005 LB/MMBTUTHREE ONE-HOUR TEST AVERAGE 0.0050.005 LB/MMBTU 0.005

0.82 LB/H based on 3-hour average 0.00732.65 LB/H 143 T/YR

0.03 LB/H 0 0.03 T/YRPROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0075

0.0074 LB/MMBTUANNUAL AVERAGE0.0074 LB/MMBTUANNUAL AVERAGE

0.02 LB/H 0 0.02 T/YR0.64 T/YR (EACH)0.01 LB/H 0.04 T/YR 0.0001

0.2 LB/MMBTU 0.29.64 LB/H 33.77 T/YR 0.048.85 LB/H 31 T/YR 0.049.64 LB/H 33.77 T/YR 0.048.85 LB/H 31 T/YR 0.04

NONE INDICATED AS SOURCE WAS INSTALLED PRIOR TO 1975 AND IS NOT SUBJECT TO BACT-PSD.FUEL SULFUR CONTENT LIMITS SEE POLLUTANT NOTESNONE INDICATED AS SOURCE WAS INSTALLED PRIOR TO 1975 AND IS NOT SUBJECT TO BACT-PSD.FUEL SULFUR CONTENT LIMITS SEE POLLUTANT NOTES



6.3 LB/H 27.6 T/YR 0.0263.1 LB/H 13.7 T/YR 0.0252.7 LB/H 11.7 T/YR 0.0265.8 LB/H 25.5 T/YR 0.0266.3 LB/H 27.6 T/YR 0.026

3.1 LB/H 13.7 T/YR 0.0252.7 LB/H 11.7 T/YR 0.0265.8 LB/H 25.5 T/YR 0.0260.1 LB/H each unit 3hr rolling avg 0.0010.1 LB/H 0.0007160 S02 PPMDfuel limit3.1 LB/H HOURLY MAXIMUM 13.56 T/YR ANNUAL M 0.0269

46.22 LB/H 202.5 T/YR 0.32.71 LB/H 11.9 T/YR 0.023

46.22 LB/H 202.5 T/YR 0.32.71 LB/H 11.9 T/YR 0.023

0.034 LB/MMBTU 0.0340.1778 LB/MMBTU 0.1778

0.034 LB/MMBTU 0.0340.1778 LB/MMBTU 0.1778

1.6 LB/MMBTU 2758 T/YR BOTH BOI 1.61.6 LB/MMBTU 2758 T/YR BOTH BOI 1.6300 PPM300 PPMV300 PPM300 PPMV

0.0006 LB/MMBTU2000 H / 12 MO. ROL 0.14 LB/H35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE35 PPMV DAILY AVERAGE

5.7 LB/H 99.8 25 T/YR0.01 LB/H 0.01 T/YR0.41 LB/H 1.78 T/YR0.02 LB/H 0.1 T/YR0.11 LB/H

61.37 LB/H 13.44 T/YRUSE OF LOW SULFUR REFINERY FUEL GAS 25USE OF LOW SULFUR REFINERY FUEL GAS 25USE OF LOW SULFUR REFINERY FUEL GAS 25USE OF LOW SULFUR REFINERY FUEL GAS 25USE OF LOW SULFUR REFINERY FUEL GAS 25USE OF LOW SULFUR REFINERY FUEL GAS 25

USE OF PIPELINE QUALITY N SEE NOTEUSE OF PIPELINE QUALITY N SEE NOTE

0.61 LB/H based on 3-hour average 0.0055LIMIT CONCENTRATION OF H2S SEE NOTELIMIT CONCENTRATION OF H2S SEE NOTELIMIT CONCENTRATION OF H2S SEE NOTELIMIT CONCENTRATION OF H2S SEE NOTE

0.021 LB/H 2000 H / 12 MO. ROLLING LIMIT0.75 LB/H 3.3 T/YR 0.00650.75 LB/H 3.3 T/YR 0.0065

10 % OPACITY 1010 % OPACITY 1010 % OPACITY 1020 % OPACIT6 MIN AVER 2020 % OPACITY 2020 % OPACITEXCEPT FOR 3 MINUTES IN AN ANY ONE HOUR 2020 % OPACITEXCEPT FOR 3 MINUTES IN ANY ONE HOUR 2020 % OPACITEXCEPT FOR 3 MINUTES IN AN ANY ONE HOUR 2020 % OPACITEXCEPT FOR 3 MINUTES IN ANY ONE HOUR 20

5 % OPACITY 55 % OPACITY 55 % OPACITY 55 % OPACITY 55 % OPACITY 55 % OPACITY 55 % OPACITY 55 % OPACITY 5

10 % OPACITY 20 % OPACIT6-min perio 101.82 T/YR (EACH)

1 LB/H3.4 LB/H1.7 LB/H1.7 LB/H

0.052 LB/MMBTU 0.0520.3 LB/H 1.31 T/YR


0.3 LB/H 1.2 T/YR0.48 LB/H 0.864 T/YR0.48 LB/H 0.864 T/YR1.32 LB/H 5.79 T/YR0.66 LB/H 2.88 T/YR0.56 LB/H 2.46 T/YR1.22 LB/H 5.35 T/YR1.32 LB/H 5.79 T/YR0.66 LB/H 2.88 T/YR

0.56 LB/H 2.46 T/YR1.22 LB/H 5.35 T/YR0.06 LB/MMBTU

2.1 LB\H each unit2.1 LB/H

0.62 LB/H HOURLY MAXIMUM 2.72 TYR ANNUAL MAXIMUM0.545 LB/H 2.4 T/YR0.545 LB/H 2.4 T/YR

2.6 LB/H EACH BOILER 11.5 T/YR EACH BOILER, ON A ROLLING 12-MO.2.6 LB/H EACH BOILER 11.5 T/YR EACH BOILER, ON A ROLLING 12-MO.

0.0054 LB/MMBTU2000 H / 12 MO. ROL 1.24 LB/H0.44 LB/H 1.9 T/YR0.01 LB/H 0.04 T/YR2.31 LB/H 10.13 T/YR0.08 LB/H 0.36 T/YR0.59 LB/H based on 3-hour average

0.005 LB/MMBTU3-HR AVERAGE0.7 LB/H

23.63 LB/H 103.49 T/YR0.03 LB/H 0 0.04 T/YR

PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015PROPER DESIGN, OPERATION, AND GOOD ENGINEERING PRACTICES 0.0015

0.0054 LB/MMBTUANNUAL AVERAGE0.0054 LB/MMBTUANNUAL AVERAGE

STDUNITLISTDLIMIT POLLUTANTCOMPLIANCENOTESADDITIONAL EMISSION LIMIT: 10 PPMVD @ 3% O2. EMISSION LIMITS ARE POST-INSTALLATION OF SCR. ADDITIONAL LIMIT OF 10 PPMVD @3% O2. EMISSION LIMITS ARE APPLICABLE POST INSTALLATION OF SCR. ADDITIONAL EMISSION LIMIT: 10 PPMVD @ 3% O2. EMISSION LIMITS ARE POST-INSTALLATION OF SCR. ADDITIONAL LIMIT OF 10 PPMVD @3% O2. EMISSION LIMITS ARE APPLICABLE POST INSTALLATION OF SCR. THIS LIMIT IS 5.0 PPMVD BASED ON 0% OXYGEN THIS LIMIT IS 5.0 PPMVD BASED ON 0% OXYGEN

LB/MMBTU

LB/MMBTU LB/MMBTUABOVE 13LIMIT WHEN OPERATING BELOW A HEAT INPUT OF 130 MMBTU/H: 0.1 LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUCALCULATEMISSION LIMIT IN STANDARDIZED UNITS CALCULATED FROM THE HOURLY EMISSION LIMIT AND THE THROUGHPUT. LB/MMBTU

*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 12.6 LB/H (HOURLY MAXIMUM) AND 55.2 T/YR (ANNUAL MAXIMUM). LB/MMBTUCALCULAT*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 19.9 LB/H (HOURLY MAXIMUM) AND 87.2 T/YR (ANNUAL MAXIMUM).

*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 12.6 LB/H (HOURLY MAXIMUM) AND 55.2 T/YR (ANNUAL MAXIMUM). LB/MMBTUCALCULAT*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 19.9 LB/H (HOURLY MAXIMUM) AND 87.2 T/YR (ANNUAL MAXIMUM). LB/MMBTU ESTIMATED EMISSIONS ARE 24.5 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. LB/MMBTU ADDITIONAL ESTIMATED EMISSIONS ARE 28.9 T/YR, BUT THIS IS NOT A LIMIT. LB/MMBTU ESTIMATED EMISSIONS ARE 24.5 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. LB/MMBTU ADDITIONAL ESTIMATED EMISSIONS ARE 28.9 T/YR, BUT THIS IS NOT A LIMIT. LB/MMBTU LB/MMBTUCALCULAT LB/MMBTU

LB/MMBTUCALCULAT LB/MMBTUCALCULAT

LB/MMBTU LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT

NOT AVAL LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTU LB/MMBTUcalculated LB/MMBTUANNUAL A LB/MMBTUCalculated This modification is subject to PSD for CO emissions and BACT is required for this pollutant. LB/MMBTUCalculated This modification is subject to PSD for CO emissions and BACT is required for this pollutant. LB/MMBTUCalculated This modification is subject to PSD for CO emissions and BACT is required for this pollutant. LB/MMBTUCalculated This modification is subject to PSD for CO emissions and BACT is required for this pollutant. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTU LB/MMBTU


NOT AVAI LB/MMBTU LB/MMBTU


NOT AVAI

LB/MMBTUTHREE ON LB/MMBTUTHREE ON LB/MMBTUTHREE ON LB/MMBTUTHREE ON LB/MMBTUcalculated

LB/MMBTU

LB/MM BT 30-DAY R LB/MMBTU30-DAY R LB/MMBTU30-DAY R LB/MM BT 30-DAY R LB/MMBTU30-DAY R LB/MMBTU30-DAY R

PPMVD @ 12-MONTH CASE BY CASE MACT 8.84 E-8 LBS/MMBTU

LB/MMBTU Limit applies at all times, including startup and shut down. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUCALCULATEMISSION LIMIT IN STANDARDIZED UNITS CALCULATED FROM THE HOURLY EMISSION LIMIT AND THE THROUGHPUT. LB/MMBTU LB/MMBTU* *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.03 LB/MMBTU, 4.5 LB/H (HOURLY MAXIMUM), AND 19.7 T/YR (ANNUAL MAXIMUM). LB/MMBTU *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 7.1 LB/H (HOURLY MAXIMUM) AND 33.1 T/YR (ANNUAL MAXIMUM). LB/MMBTU* *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.03 LB/MMBTU, 4.5 LB/H (HOURLY MAXIMUM), AND 19.7 T/YR (ANNUAL MAXIMUM). LB/MMBTU *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 7.1 LB/H (HOURLY MAXIMUM) AND 33.1 T/YR (ANNUAL MAXIMUM).

LB/MMBTU LB/MMBTU ESTIMATED EMISSIONS ARE 153.3 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. LB/MMBTU ESTIMATED EMISSIONS ARE 43.4 T/YR, BUT THIS IS NOT A LIMIT. LB/MMBTU ESTIMATED EMISSIONS ARE 153.3 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. LB/MMBTU ESTIMATED EMISSIONS ARE 43.4 T/YR, BUT THIS IS NOT A LIMIT. LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUHOURLY AADDITIONAL LIMITS: 0.060 LB/MMBTU ROLLING 12-MO AV. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE FURNACE IS IN ITS DECOKING CYCLE. LB/MMBTU LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUCALCULATADDITIONAL EMISSION LIMITS: PRE-INSTALLATION OF SCR: 8.50 LB/H AND 37.30 T/YR. LB/MMBTUCALCULATADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 7.30 LB/H AND 32.00 T/YR. LB/MMBTUCALCULATADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 15.80 LB/H AND 69.40 T/YR. LB/MMBTUCALCULAT LB/MMBTUCALCULATADDITIONAL EMISSION LIMITS: PRE-INSTALLATION OF SCR: 8.50 LB/H AND 37.30 T/YR. LB/MMBTUCALCULATADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 7.30 LB/H AND 32.00 T/YR. LB/MMBTUCALCULATADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 15.80 LB/H AND 69.40 T/YR. LB/MMBTU LB/MMBTU LB/MMBTUCALCULATEMISSION LIMIT IN STANDARDIZED UNITS CALCULATED BY DIVIDING THE HOURLY EMISSION LIMIT BY THE HOURLY THROUGHPUT: 5.6 LB/H / 140 MMBTU/H. LB/MMBTUCALCULATEMISSION LIMIT IN STANDARDIZED UNITS CALCULATED BY DIVIDING THE HOURLY EMISSION LIMIT BY THE HOURLY THROUGHPUT: 5.6 LB/H / 140 MMBTU/H. LB/MMBTU LB/MMBTUannual avg LB/MMBTU LB/MMBTU LB/MMBTUANNUAL A LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTU LB/MMBTU Because of operational mode, heater is not able to reach 0.035 lb/mmbtu LB/MMBTU30-DAY R LB/MMBTU LB/MMBTU

NOT AVAI HIGH HEAT RELEASE RATE BOILER (NSPS LIMIT OF 0.2 LBS/MMBTU) LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU

LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. LB/MMBTU LB/MMBTU THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE.

LB/MMBTU LB/MMBTU24-HR RO LB/MMBTU LB/MMBTU24-HR RO LB/MMBTUcalculated LB/MMBTU

LB/MMBTUANNUAL A LB/MMBTUANNUAL A LB/MMBTUANNUAL A LB/MMBTUANNUAL A LB/MMBTUANNUAL A LB/MMBTUANNUAL A

LB/MMBTU12-MONTH LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUCALCULATEMISSION LIMIT IN STANDARDIZED UNITS CALCULATED FROM THE HOURLY EMISSION LIMIT AND THE THROUGHPUT. LB/MMBTU

LB/MMBTUCALCULAT

LB/MMBTUCALCULAT LB/MMBTU SOURCE IS SUBJECT TO STATE EMISSION LIMITS FOR PM. ESTIMATED EMISSIONS ARE 3.07 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. LB/MMBTU ESTIMATED EMISSIONS ARE 3.61 T/YR BUT THIS IS NOT A LIMIT. SUBJECT TO PM LIMITS BY THE STATE OF ALASKA. LB/MMBTU SOURCE IS SUBJECT TO STATE EMISSION LIMITS FOR PM. ESTIMATED EMISSIONS ARE 3.07 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. LB/MMBTU ESTIMATED EMISSIONS ARE 3.61 T/YR BUT THIS IS NOT A LIMIT. SUBJECT TO PM LIMITS BY THE STATE OF ALASKA. LB/MMBTUCALCULAT LB/MMBTU LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUCALCULATADDITONAL EMISSION LIMITS PRIOR TO INSTALLATION OF SCR: 0.91 LB/H AND 3.97 T/YR. LB/MMBTUCALCULATADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 0.78 LB/H AND 3.40 T/YR. LB/MMBTUCALCULATADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO THE INSTALLATION OF SCR: 1.69 LB/H AND 7.39 T/YR.

LB/MMBTUCALCULAT LB/MMBTUCALCULATADDITONAL EMISSION LIMITS PRIOR TO INSTALLATION OF SCR: 0.91 LB/H AND 3.97 T/YR. LB/MMBTUCALCULATADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 0.78 LB/H AND 3.40 T/YR. LB/MMBTUCALCULATADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO THE INSTALLATION OF SCR: 1.69 LB/H AND 7.39 T/YR. LB/MMBTU

NOT AVAI

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTU EMISSION LIMIT IN STANDARDIZED UNITS APPLY WHILE BURNING REFINERY FUEL GAS. LB/MMBTU EMISSION LIMIT IN STANDARDIZED UNITS APPLY WHILE BURNING REFINERY FUEL GAS. LB/MMBTU LB/MMBTUANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTUANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. LB/MMBTU LB/MMBTUcalculated LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

BOTH PM AND PM10 (INCLUDES BACKHALF M202 CATCH) LB/MMBTU LB/MMBTU

NOT AVAI LB/MMBTU LB/MMBTU LB/MMBTU


NOT AVAI LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI

LB/MMBTU LB/MMBTUTHREE ON LB/MMBTU LB/MMBTUTHREE ON LB/MMBTUcalculated

LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A

NOT AVAI LB/MMBTUCALCULATEMISSION LIMIT IN STANDARDIZED UNITS CALCULATED FROM THE HOURLY EMISSION LIMIT AND THE THROUGHPUT. LB/MMBTU LB/MMBTU LB/MMBTUCALCULAT LB/MMBTU LB/MMBTUCALCULAT

NONE INDICATED AS SOURCE WAS INSTALLED PRIOR TO 1975 AND IS NOT SUBJECT TO BACT-PSD. SOURCE IS NOT SUBJECT TO PSD REQUIREMENTS BECAUSE IT WAS INSTALLED PRIOR TO 1975. ESTIMATED EMISSIONS ARE 18.4 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. EMISSIONS INFORMATION IS PROVIDED FOR SO2 AND H2S TOGETHER. THIS SOURCE IS ALSO SUBJECT TO NSPS FOR SO2. LIMITS ARE PROVIDED BASED ON FUEL CONTENT (SEE POLLUTION PREVENTION DESCRIPTION). ESTIMATED EMISSIONS ARE 21.7 T/YR, BUT THIS IS NOT A LIMIT. ADDITION

NONE INDICATED AS SOURCE WAS INSTALLED PRIOR TO 1975 AND IS NOT SUBJECT TO BACT-PSD. SOURCE IS NOT SUBJECT TO PSD REQUIREMENTS BECAUSE IT WAS INSTALLED PRIOR TO 1975. ESTIMATED EMISSIONS ARE 18.4 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. EMISSIONS INFORMATION IS PROVIDED FOR SO2 AND H2S TOGETHER. THIS SOURCE IS ALSO SUBJECT TO NSPS FOR SO2. LIMITS ARE PROVIDED BASED ON FUEL CONTENT (SEE POLLUTION PREVENTION DESCRIPTION). ESTIMATED EMISSIONS ARE 21.7 T/YR, BUT THIS IS NOT A LIMIT. ADDITION

LB/MMBTUCALCULAT LB/MMBTU LB/MMBTU LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT

LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTU LB/MMBTUcalculated

see note limit is fuel H2S content limit, no emission rate limit. LB/MMBTUANNUAL A LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI THIS LIMIT IS FOR SULFUR, AS H2S, AND IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS LIMIT ON SULFUR, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. NOT AVAI THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS LIMIT IS FOR SULFUR, AS H2S, AND IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS LIMIT ON SULFUR, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. NOT AVAI THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. NOT AVAI THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS.

PPMV AS ANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A PPMV AS ANNUAL A

NO EMISSION LIMITS NO EMISSION LIMITS

LB/MMBTUcalculated REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL LIMIT, NO EMISSION RATE LIMIT. REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL H2S LIMIT, NO EMISSION RATE LIMIT REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL LIMIT, NO EMISSION RATE LIMIT. REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL H2S LIMIT, NO EMISSION RATE LIMIT REGULATED POLLUTANT IS SULFURIC ACID MIST.

LB/MMBTUCalculated Best available technology (BAT) review done. LB/MMBTUCalculated Best available technology (BAT) review done. % OPACITY % OPACITY % OPACITY % OPACIT6 MIN AVE % OPACITY % OPACITEXCEPT FSOURCE IS SUBJECT TO STATE EMISSION LIMITS FOR VE. % OPACITEXCEPT FALL SOURCES ARE SUBJECT TO VE LIMITATIONS BY THE STATE OF ALASKA. % OPACITEXCEPT FSOURCE IS SUBJECT TO STATE EMISSION LIMITS FOR VE. % OPACITEXCEPT FALL SOURCES ARE SUBJECT TO VE LIMITATIONS BY THE STATE OF ALASKA. % OPACITY % OPACITY % OPACITY % OPACITY % OPACITY % OPACITY % OPACITY % OPACITY % OPACITY

NOT AVAI NOT AVAI

LB/MMBTU ADDITIONAL EMISSION LIMIT: 0.004 LB/MMBTU. ADDITIONAL EMISSION LIMIT: 0.004 LB/MMBTU.

ADDITIONAL LIMIT: 0.0054 LB/MMBTU ANNUAL AVERAGE Best available technology (BAT) review done. Best available technology (BAT) review done.

EACH BOILER, ON A ROLLING 12-MO. EACH BOILER, ON A ROLLING 12-MO.

LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A LB/MMBTU3-HOUR A

ADDITIONAL EMISSION LIMIT: 10 PPMVD @ 3% O2. EMISSION LIMITS ARE POST-INSTALLATION OF SCR.

ADDITIONAL LIMIT OF 10 PPMVD @3% O2. EMISSION LIMITS ARE APPLICABLE POST INSTALLATION OF SCR. ADDITIONAL EMISSION LIMIT: 10 PPMVD @ 3% O2. EMISSION LIMITS ARE POST-INSTALLATION OF SCR.

ADDITIONAL LIMIT OF 10 PPMVD @3% O2. EMISSION LIMITS ARE APPLICABLE POST INSTALLATION OF SCR.

LIMIT WHEN OPERATING BELOW A HEAT INPUT OF 130 MMBTU/H: 0.1 LB/MMBTU

EMISSION LIMIT IN STANDARDIZED UNITS CALCULATED FROM THE HOURLY EMISSION LIMIT AND THE THROUGHPUT.

*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 12.6 LB/H (HOURLY MAXIMUM) AND 55.2 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 19.9 LB/H (HOURLY MAXIMUM) AND 87.2 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 12.6 LB/H (HOURLY MAXIMUM) AND 55.2 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 19.9 LB/H (HOURLY MAXIMUM) AND 87.2 T/YR (ANNUAL MAXIMUM). ESTIMATED EMISSIONS ARE 24.5 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. ADDITIONAL ESTIMATED EMISSIONS ARE 28.9 T/YR, BUT THIS IS NOT A LIMIT. ESTIMATED EMISSIONS ARE 24.5 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. ADDITIONAL ESTIMATED EMISSIONS ARE 28.9 T/YR, BUT THIS IS NOT A LIMIT.

ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

This modification is subject to PSD for CO emissions and BACT is required for this pollutant. This modification is subject to PSD for CO emissions and BACT is required for this pollutant. This modification is subject to PSD for CO emissions and BACT is required for this pollutant. This modification is subject to PSD for CO emissions and BACT is required for this pollutant.


*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.03 LB/MMBTU, 4.5 LB/H (HOURLY MAXIMUM), AND 19.7 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 7.1 LB/H (HOURLY MAXIMUM) AND 33.1 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.03 LB/MMBTU, 4.5 LB/H (HOURLY MAXIMUM), AND 19.7 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 7.1 LB/H (HOURLY MAXIMUM) AND 33.1 T/YR (ANNUAL MAXIMUM).

ESTIMATED EMISSIONS ARE 153.3 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. ESTIMATED EMISSIONS ARE 43.4 T/YR, BUT THIS IS NOT A LIMIT. ESTIMATED EMISSIONS ARE 153.3 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. ESTIMATED EMISSIONS ARE 43.4 T/YR, BUT THIS IS NOT A LIMIT.

ADDITIONAL LIMITS: 0.060 LB/MMBTU ROLLING 12-MO AV. NOX LIMITS ARE NOT APPLICABLE WHEN THE CRACKING FURNACE IS IN ITS DECOKING CYCLE; HOWEVER THE NOX MASS EMISSIONS RATES SPECIFIED SHALL NOT BE EXCEEDED WHEN THE FURNACE IS IN ITS DECOKING CYCLE.

ADDITIONAL EMISSION LIMITS: PRE-INSTALLATION OF SCR: 8.50 LB/H AND 37.30 T/YR. ADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 7.30 LB/H AND 32.00 T/YR. ADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 15.80 LB/H AND 69.40 T/YR.

ADDITIONAL EMISSION LIMITS: PRE-INSTALLATION OF SCR: 8.50 LB/H AND 37.30 T/YR. ADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 7.30 LB/H AND 32.00 T/YR. ADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 15.80 LB/H AND 69.40 T/YR.

EMISSION LIMIT IN STANDARDIZED UNITS CALCULATED BY DIVIDING THE HOURLY EMISSION LIMIT BY THE HOURLY THROUGHPUT: 5.6 LB/H / 140 MMBTU/H. EMISSION LIMIT IN STANDARDIZED UNITS CALCULATED BY DIVIDING THE HOURLY EMISSION LIMIT BY THE HOURLY THROUGHPUT: 5.6 LB/H / 140 MMBTU/H.

Because of operational mode, heater is not able to reach 0.035 lb/mmbtu

HIGH HEAT RELEASE RATE BOILER (NSPS LIMIT OF 0.2 LBS/MMBTU) THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE.

THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE.

THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE. THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE.


THE INITIAL LIMIT FOR NOX IS 0.0125 LB PER MMBTU HEAT INPUT (HHV). AFTER THE FIRST 24 MONTHS, A NEW LIMIT IS TO BE ESTABLISHED BASED ON THE PERFORMANCE OF THE UNIT. A LIMIT OF 0.006 LB PER MMBTU MAY BE TAKEN WITHOUT REGARD TO THE UNIT PERFORMANCE.


SOURCE IS SUBJECT TO STATE EMISSION LIMITS FOR PM. ESTIMATED EMISSIONS ARE 3.07 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. ESTIMATED EMISSIONS ARE 3.61 T/YR BUT THIS IS NOT A LIMIT. SUBJECT TO PM LIMITS BY THE STATE OF ALASKA. SOURCE IS SUBJECT TO STATE EMISSION LIMITS FOR PM. ESTIMATED EMISSIONS ARE 3.07 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. ESTIMATED EMISSIONS ARE 3.61 T/YR BUT THIS IS NOT A LIMIT. SUBJECT TO PM LIMITS BY THE STATE OF ALASKA.

ADDITONAL EMISSION LIMITS PRIOR TO INSTALLATION OF SCR: 0.91 LB/H AND 3.97 T/YR. ADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 0.78 LB/H AND 3.40 T/YR. ADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO THE INSTALLATION OF SCR: 1.69 LB/H AND 7.39 T/YR.

ADDITONAL EMISSION LIMITS PRIOR TO INSTALLATION OF SCR: 0.91 LB/H AND 3.97 T/YR. ADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO INSTALLATION OF SCR: 0.78 LB/H AND 3.40 T/YR. ADDITIONAL EMISSION LIMITS APPLICABLE PRIOR TO THE INSTALLATION OF SCR: 1.69 LB/H AND 7.39 T/YR.

EMISSION LIMIT IN STANDARDIZED UNITS APPLY WHILE BURNING REFINERY FUEL GAS. EMISSION LIMIT IN STANDARDIZED UNITS APPLY WHILE BURNING REFINERY FUEL GAS.

ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.


SOURCE IS NOT SUBJECT TO PSD REQUIREMENTS BECAUSE IT WAS INSTALLED PRIOR TO 1975. ESTIMATED EMISSIONS ARE 18.4 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. EMISSIONS INFORMATION IS PROVIDED FOR SO2 AND H2S TOGETHER. THIS SOURCE IS ALSO SUBJECT TO NSPS FOR SO2. LIMITS ARE PROVIDED BASED ON FUEL CONTENT (SEE POLLUTION PREVENTION DESCRIPTION). ESTIMATED EMISSIONS ARE 21.7 T/YR, BUT THIS IS NOT A LIMIT. ADDITIONSOURCE IS NOT SUBJECT TO PSD REQUIREMENTS BECAUSE IT WAS INSTALLED PRIOR TO 1975. ESTIMATED EMISSIONS ARE 18.4 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. EMISSIONS INFORMATION IS PROVIDED FOR SO2 AND H2S TOGETHER. THIS SOURCE IS ALSO SUBJECT TO NSPS FOR SO2. LIMITS ARE PROVIDED BASED ON FUEL CONTENT (SEE POLLUTION PREVENTION DESCRIPTION). ESTIMATED EMISSIONS ARE 21.7 T/YR, BUT THIS IS NOT A LIMIT. ADDITION

THIS LIMIT IS FOR SULFUR, AS H2S, AND IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS LIMIT ON SULFUR, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS LIMIT IS FOR SULFUR, AS H2S, AND IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS LIMIT ON SULFUR, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS. THIS SULFUR LIMIT, AS H2S, IS A LIMIT ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS.

REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL LIMIT, NO EMISSION RATE LIMIT. REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL H2S LIMIT, NO EMISSION RATE LIMIT REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL LIMIT, NO EMISSION RATE LIMIT. REGULATED POLLUTANT IS SULFURIC ACID MIST. FUEL H2S LIMIT, NO EMISSION RATE LIMIT

ALL SOURCES ARE SUBJECT TO VE LIMITATIONS BY THE STATE OF ALASKA.

ALL SOURCES ARE SUBJECT TO VE LIMITATIONS BY THE STATE OF ALASKA.

*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 12.6 LB/H (HOURLY MAXIMUM) AND 55.2 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 19.9 LB/H (HOURLY MAXIMUM) AND 87.2 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 12.6 LB/H (HOURLY MAXIMUM) AND 55.2 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 19.9 LB/H (HOURLY MAXIMUM) AND 87.2 T/YR (ANNUAL MAXIMUM).

*AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.03 LB/MMBTU, 4.5 LB/H (HOURLY MAXIMUM), AND 19.7 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 7.1 LB/H (HOURLY MAXIMUM) AND 33.1 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 0.03 LB/MMBTU, 4.5 LB/H (HOURLY MAXIMUM), AND 19.7 T/YR (ANNUAL MAXIMUM). *AS SET BY PSD-LA-584(M-3), DATED SEPTEMBER 20, 2002. PSD-LA-584(M-2) ORIGINALLY ESTABLISHED LIMITS AT 7.1 LB/H (HOURLY MAXIMUM) AND 33.1 T/YR (ANNUAL MAXIMUM).


EMISSION LIMIT IN STANDARDIZED UNITS CALCULATED BY DIVIDING THE HOURLY EMISSION LIMIT BY THE HOURLY THROUGHPUT: 5.6 LB/H / 140 MMBTU/H. EMISSION LIMIT IN STANDARDIZED UNITS CALCULATED BY DIVIDING THE HOURLY EMISSION LIMIT BY THE HOURLY THROUGHPUT: 5.6 LB/H / 140 MMBTU/H.




SOURCE IS NOT SUBJECT TO PSD REQUIREMENTS BECAUSE IT WAS INSTALLED PRIOR TO 1975. ESTIMATED EMISSIONS ARE 18.4 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. EMISSIONS INFORMATION IS PROVIDED FOR SO2 AND H2S TOGETHER. THIS SOURCE IS ALSO SUBJECT TO NSPS FOR SO2. LIMITS ARE PROVIDED BASED ON FUEL CONTENT (SEE POLLUTION PREVENTION DESCRIPTION). ESTIMATED EMISSIONS ARE 21.7 T/YR, BUT THIS IS NOT A LIMIT. ADDITIONSOURCE IS NOT SUBJECT TO PSD REQUIREMENTS BECAUSE IT WAS INSTALLED PRIOR TO 1975. ESTIMATED EMISSIONS ARE 18.4 T/YR, BUT THIS IS NOT AN EMISSION LIMIT. EMISSIONS INFORMATION IS PROVIDED FOR SO2 AND H2S TOGETHER. THIS SOURCE IS ALSO SUBJECT TO NSPS FOR SO2. LIMITS ARE PROVIDED BASED ON FUEL CONTENT (SEE POLLUTION PREVENTION DESCRIPTION). ESTIMATED EMISSIONS ARE 21.7 T/YR, BUT THIS IS NOT A LIMIT. ADDITION

THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT.

THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT. THE 35 PPMV SULFUR LIMIT, AS H2S, IS A RESTRICTION ON THE INLET CONCENTRATION OF THE REFINERY FUEL GAS BEING FIRED IN THE UNIT.

EMISSIONS INFORMATION IS PROVIDED FOR SO2 AND H2S TOGETHER. THIS SOURCE IS ALSO SUBJECT TO NSPS FOR SO2. LIMITS ARE PROVIDED BASED ON FUEL CONTENT (SEE POLLUTION PREVENTION DESCRIPTION). ESTIMATED EMISSIONS ARE 21.7 T/YR, BUT THIS IS NOT A LIMIT. ADDITION

EMISSIONS INFORMATION IS PROVIDED FOR SO2 AND H2S TOGETHER. THIS SOURCE IS ALSO SUBJECT TO NSPS FOR SO2. LIMITS ARE PROVIDED BASED ON FUEL CONTENT (SEE POLLUTION PREVENTION DESCRIPTION). ESTIMATED EMISSIONS ARE 21.7 T/YR, BUT THIS IS NOT A LIMIT. ADDITION

RBLCID FACILITY CORPORAFACILITYSAGENCYNPERMITDAFACILITYDPROCESSNC-0093 GREENVILWEYERHANC NORTH CA9/26/1997 SAWMILL THERMAL NC-0093 GREENVILWEYERHANC NORTH CA9/26/1997 SAWMILL THERMAL AL-0107 WELLBORNWELLBORNAL ALABAMA 2/3/1998 BOILER, 2AL-0107 WELLBORNWELLBORNAL ALABAMA 2/3/1998 BOILER, 2AL-0122 GULF STAGULF STAAL ALABAMA ### BOILER, AL-0122 GULF STAGULF STAAL ALABAMA ### BOILER, NC-0072 WEYERHAEWEYERHANC NORTH CA7/13/1999 SAWMILL THERMAL NC-0072 WEYERHAEWEYERHANC NORTH CA7/13/1999 SAWMILL THERMAL OH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, OH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, TX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DTX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DLA-0126 JOYCE MI WEST FRASLA LOUISIAN 4/24/2002 JOYCE MI KIPPER BOLA-0126 JOYCE MI WEST FRASLA LOUISIAN 4/24/2002 JOYCE MI KIPPER BOAR-0065 WEST FRASWEST FRAZAR ARKANSAS11/7/2002 PINE LUMBBOILER, AR-0065 WEST FRASWEST FRAZAR ARKANSAS11/7/2002 PINE LUMBBOILER, AR-0075 DELTIC T DELTIC T AR ARKANSAS8/20/2003 LUMBER ABOILER, AR-0075 DELTIC T DELTIC T AR ARKANSAS8/20/2003 LUMBER ABOILER, WI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OAL-0107 WELLBORNWELLBORNAL ALABAMA 2/3/1998 BOILER, 2AL-0107 WELLBORNWELLBORNAL ALABAMA 2/3/1998 BOILER, 2OH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, OH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, NC-0093 GREENVILWEYERHANC NORTH CA9/26/1997 SAWMILL THERMAL NC-0093 GREENVILWEYERHANC NORTH CA9/26/1997 SAWMILL THERMAL AL-0122 GULF STAGULF STAAL ALABAMA ### BOILER, AL-0122 GULF STAGULF STAAL ALABAMA ### BOILER, TX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DTX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DAR-0065 WEST FRASWEST FRAZAR ARKANSAS11/7/2002 PINE LUMBBOILER, AR-0065 WEST FRASWEST FRAZAR ARKANSAS11/7/2002 PINE LUMBBOILER, AL-0213 WELLBORNWELLBORNAL ALABAMA 4/16/2003 (3) WOODAL-0213 WELLBORNWELLBORNAL ALABAMA 4/16/2003 (3) WOODAR-0075 DELTIC T DELTIC T AR ARKANSAS8/20/2003 LUMBER ABOILER, AR-0075 DELTIC T DELTIC T AR ARKANSAS8/20/2003 LUMBER ABOILER, WI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OAL-0122 GULF STAGULF STAAL ALABAMA ### BOILER,

AL-0122 GULF STAGULF STAAL ALABAMA ### BOILER, TX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DTX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL ONC-0093 GREENVILWEYERHANC NORTH CA9/26/1997 SAWMILL THERMAL NC-0093 GREENVILWEYERHANC NORTH CA9/26/1997 SAWMILL THERMAL TN-0084 BRUCE HABRUCE HATN TENNESSE7/10/1998 WOODWORKBOILER, TN-0084 BRUCE HABRUCE HATN TENNESSE7/10/1998 WOODWORKBOILER, OH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, OH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, TX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DTX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DAR-0065 WEST FRASWEST FRAZAR ARKANSAS11/7/2002 PINE LUMBBOILER, AR-0065 WEST FRASWEST FRAZAR ARKANSAS11/7/2002 PINE LUMBBOILER, AR-0075 DELTIC T DELTIC T AR ARKANSAS8/20/2003 LUMBER ABOILER, AR-0075 DELTIC T DELTIC T AR ARKANSAS8/20/2003 LUMBER ABOILER, WI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OOH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, OH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, TX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DTX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DOH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, OH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, TX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DTX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DNC-0093 GREENVILWEYERHANC NORTH CA9/26/1997 SAWMILL THERMAL NC-0093 GREENVILWEYERHANC NORTH CA9/26/1997 SAWMILL THERMAL AL-0122 GULF STAGULF STAAL ALABAMA ### BOILER, AL-0122 GULF STAGULF STAAL ALABAMA ### BOILER, OH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, OH-0244 DUKE SOLDuke Ener OH HAMILTON ### STEAM ANBOILER, TX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER DTX-0345 DIBOLL P TEMPLE-I TX TEXAS CO9/28/2001 TEMPLE-I SANDER D*AL-0225 T.R. MILL T.R. MILL AL ALABAMA 5/16/2002 SAWMILL WOOD-FIR*AL-0225 T.R. MILL T.R. MILL AL ALABAMA 5/16/2002 SAWMILL WOOD-FIRAR-0065 WEST FRASWEST FRAZAR ARKANSAS11/7/2002 PINE LUMBBOILER, AR-0065 WEST FRASWEST FRAZAR ARKANSAS11/7/2002 PINE LUMBBOILER, AR-0075 DELTIC T DELTIC T AR ARKANSAS8/20/2003 LUMBER ABOILER,

AR-0075 DELTIC T DELTIC T AR ARKANSAS8/20/2003 LUMBER ABOILER, WI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI6/17/2004 OSB MILL THERMAL O

PROCTYPEFUEL THRUPUT THRUPUTUPROCESSPOLLUTANCONTROLCTRLDESC13.12 WOODWAS 57.2 MMBTU/H Carbon MoP STAGED C13.12 WOODWAS 57.2 MMBTU/H Carbon MoP STAGED C13.12 WOOD 29.5 MMBTU/H WILL TES Carbon MoP BOILER D13.12 WOOD 29.5 MMBTU/H WILL TES Carbon MoP BOILER D13.12 WOOD 98 MMBTU/H Carbon MoN13.12 WOOD 98 MMBTU/H Carbon MoN13.12 WOOD WA 98 MMBTU/H THE CO BACarbon MoP COMBUST13.12 WOOD WA 98 MMBTU/H THE CO BACarbon MoP COMBUST13.12 WOOD 28.7 MMBTU/H Carbon MoN13.12 WOOD 28.7 MMBTU/H Carbon MoN13.12 WOOD 40 MMBTU/H FUEL: EI Carbon MoN NONE IND13.12 WOOD 40 MMBTU/H FUEL: EI Carbon MoN NONE IND13.12 WOOD WA 58.3 MMBTU/H EMISSION Carbon MoN13.12 WOOD WA 58.3 MMBTU/H EMISSION Carbon MoN13.12 WOOD WA 29.63 MMBTU/H WELLONS BCarbon MoP GOOD COM13.12 WOOD WA 29.63 MMBTU/H WELLONS BCarbon MoP GOOD COM13.12 WOOD WA 64.3 MMBTU/H Carbon MoP GOOD COM13.12 WOOD WA 64.3 MMBTU/H Carbon MoP GOOD COM13.12 WOOD 19.4 MMBTU/H STACK S11Carbon MoP GOOD COM13.12 WOOD 23.8 MMBTU/H STACK S21Carbon MoP GOOD COM13.12 WOOD 19.4 MMBTU/H STACK S11Carbon MoP GOOD COM13.12 WOOD 23.8 MMBTU/H STACK S21Carbon MoP GOOD COM13.12 WOOD 19.4 MMBTU/H STACK S11Carbon MoP GOOD COM13.12 WOOD 23.8 MMBTU/H STACK S21Carbon MoP GOOD COM13.12 WOOD 29.5 MMBTU/H WILL TES Nitrogen D P BOILER D13.12 WOOD 29.5 MMBTU/H WILL TES Nitrogen D P BOILER D13.12 WOOD 28.7 MMBTU/H Nitrogen D N13.12 WOOD 28.7 MMBTU/H Nitrogen D N13.12 WOODWAS 57.2 MMBTU/H Nitrogen O P STAGED C13.12 WOODWAS 57.2 MMBTU/H Nitrogen O P STAGED C13.12 WOOD 98 MMBTU/H Nitrogen O N13.12 WOOD 98 MMBTU/H Nitrogen O N13.12 WOOD 40 MMBTU/H FUEL: EI Nitrogen O N NONE IND13.12 WOOD 40 MMBTU/H FUEL: EI Nitrogen O N NONE IND13.12 WOOD WA 29.63 MMBTU/H WELLONS BNitrogen O P OVERFIRE13.12 WOOD WA 29.63 MMBTU/H WELLONS BNitrogen O P OVERFIRE13.12 WOOD WA 29.5 mmbtu/h Nitrogen O P BOILER D13.12 WOOD WA 29.5 mmbtu/h Nitrogen O P BOILER D13.12 WOOD WA 64.3 MMBTU/H Nitrogen O P OVEN FIR13.12 WOOD WA 64.3 MMBTU/H Nitrogen O P OVEN FIR13.12 WOOD 19.4 MMBTU/H STACK S11Nitrogen O P GOOD COM13.12 WOOD 23.8 MMBTU/H STACK S21Nitrogen O P GOOD COM13.12 WOOD 19.4 MMBTU/H STACK S11Nitrogen O P GOOD COM13.12 WOOD 23.8 MMBTU/H STACK S21Nitrogen O P GOOD COM13.12 WOOD 19.4 MMBTU/H STACK S11Nitrogen O P GOOD COM13.12 WOOD 23.8 MMBTU/H STACK S21Nitrogen O P GOOD COM13.12 WOOD 98 MMBTU/H Particulate A MULTICYC

13.12 WOOD 98 MMBTU/H Particulate A MULTICYC13.12 WOOD 40 MMBTU/H FUEL: EI Particulate A ELECROST13.12 WOOD 40 MMBTU/H FUEL: EI Particulate A ELECROST13.12 WOOD 19.4 MMBTU/H STACK S11Particulate A ELECTRIFI13.12 WOOD 23.8 MMBTU/H STACK S21Particulate A ELECTRIFI13.12 WOOD 19.4 MMBTU/H STACK S11Particulate A ELECTRIFI13.12 WOOD 23.8 MMBTU/H STACK S21Particulate A ELECTRIFI13.12 WOOD 19.4 MMBTU/H STACK S11Particulate A ELECTRIFI13.12 WOOD 23.8 MMBTU/H STACK S21Particulate A ELECTRIFI13.12 WOODWAS 57.2 MMBTU/H Particulate A MULTICLO13.12 WOODWAS 57.2 MMBTU/H Particulate A MULTICLO13.12 WOOD 53.5 MMBTU/H Particulate P GOOD COM13.12 WOOD 53.5 MMBTU/H Particulate P GOOD COM13.12 WOOD 28.7 MMBTU/H Particulate A MULTICLO13.12 WOOD 28.7 MMBTU/H Particulate A MULTICLO13.12 WOOD 40 MMBTU/H FUEL: EI Particulate A ELECTROS13.12 WOOD 40 MMBTU/H FUEL: EI Particulate A ELECTROS13.12 WOOD WA 29.63 MMBTU/H WELLONS BParticulate A MULTICLO13.12 WOOD WA 29.63 MMBTU/H WELLONS BParticulate A MULTICLO13.12 WOOD WA 64.3 MMBTU/H Particulate A ESP13.12 WOOD WA 64.3 MMBTU/H Particulate A ESP13.12 WOOD 19.4 MMBTU/H STACK S11Particulate A ELECTRIFI13.12 WOOD 23.8 MMBTU/H STACK S21Particulate A ELECTRIFI13.12 WOOD 19.4 MMBTU/H STACK S11Particulate A ELECTRIFI13.12 WOOD 23.8 MMBTU/H STACK S21Particulate A ELECTRIFI13.12 WOOD 19.4 MMBTU/H STACK S11Particulate A ELECTRIFI13.12 WOOD 23.8 MMBTU/H STACK S21Particulate A ELECTRIFI13.12 WOOD 28.7 MMBTU/H Sulfur DioxN13.12 WOOD 28.7 MMBTU/H Sulfur DioxN13.12 WOOD 40 MMBTU/H FUEL: EI Sulfur DioxN NONE IND13.12 WOOD 40 MMBTU/H FUEL: EI Sulfur DioxN NONE IND13.12 WOOD 28.7 MMBTU/H Visible EmiA MULTICLO13.12 WOOD 28.7 MMBTU/H Visible EmiA MULTICLO13.12 WOOD 40 MMBTU/H FUEL: EI Visible EmiN13.12 WOOD 40 MMBTU/H FUEL: EI Visible EmiN13.12 WOODWAS 57.2 MMBTU/H Volatile O N13.12 WOODWAS 57.2 MMBTU/H Volatile O N13.12 WOOD 98 MMBTU/H Volatile O N MULTICYC13.12 WOOD 98 MMBTU/H Volatile O N MULTICYC13.12 WOOD 28.7 MMBTU/H Volatile O N13.12 WOOD 28.7 MMBTU/H Volatile O N13.12 WOOD 40 MMBTU/H FUEL: EI Volatile O N NONE IND13.12 WOOD 40 MMBTU/H FUEL: EI Volatile O N NONE IND13.12 WOOD 36 MMBTU/H Volatile O N GOOD COM13.12 WOOD 36 MMBTU/H Volatile O N GOOD COM13.12 WOOD WA 29.63 MMBTU/H WELLONS BVolatile O P GOOD COM13.12 WOOD WA 29.63 MMBTU/H WELLONS BVolatile O P GOOD COM13.12 WOOD WA 64.3 MMBTU/H Volatile O P GOOD COM

13.12 WOOD WA 64.3 MMBTU/H Volatile O P GOOD COM13.12 WOOD 19.4 MMBTU/H STACK S11Volatile O P GOOD COM13.12 WOOD 23.8 MMBTU/H STACK S21Volatile O P GOOD COM13.12 WOOD 19.4 MMBTU/H STACK S11Volatile O P GOOD COM13.12 WOOD 23.8 MMBTU/H STACK S21Volatile O P GOOD COM13.12 WOOD 19.4 MMBTU/H STACK S11Volatile O P GOOD COM13.12 WOOD 23.8 MMBTU/H STACK S21Volatile O P GOOD COM

EMISLIMITEMISLIMITEMISLIMI PCTEFFIC EMISLIMITEMISLIMITEMISLIMI STDEMISSL0.24 LB/MMBTU 104 T/YR 0.240.24 LB/MMBTU 104 T/YR 0.2423.6 LB/H 0 0 0.423.6 LB/H 0 0 0.4

0.5 LB/MMBTU 0 49 LB/H 0.50.5 LB/MMBTU 0 49 LB/H 0.50.5 LB/MMBTU214.6 T/YR ANNUAL LMT 0.50.5 LB/MMBTU214.6 T/YR ANNUAL LMT 0.50.3 LB/MMBTU 21.4 T/YR 0.30.3 LB/MMBTU 21.4 T/YR 0.3

186.8 LB/H 818.2 T/YR 4.67186.8 LB/H 818.2 T/YR 4.67105.5 LB/H EACH 462.2 T/YR EACH 1.81105.5 LB/H EACH 462.2 T/YR EACH 1.81


0.475 LB/MMBTU 0.4750.475 LB/MMBTU 0.475

52.5 LB/H COMBINED 1.3552.5 LB/H COMBINED 1.152.5 LB/H COMBINED 1.3552.5 LB/H COMBINED 1.152.5 LB/H COMBINED 1.3552.5 LB/H COMBINED 1.1

13.57 LB/H 31 0 0.2313.57 LB/H 31 0 0.230.604 LB/MMBTU 43.1 T/YR 0.6040.604 LB/MMBTU 43.1 T/YR 0.604

0.25 LB/MMBTU 107 T/YR 0.250.25 LB/MMBTU 107 T/YR 0.25

0.3 LB/MMBTU 0 29.4 LB/H 0.30.3 LB/MMBTU 0 29.4 LB/H 0.3

57.2 LB/H 250.5 T/YR 1.4357.2 LB/H 250.5 T/YR 1.43

0.3 LB/MMBTU 8.9 LB/H 0.30.3 LB/MMBTU 8.9 LB/H 0.30.5 LB/MMBTU3 HR TEST 14.75 LB/H 0.50.5 LB/MMBTU3 HR TEST 14.75 LB/H 0.50.3 LB/MMBTU 0.30.3 LB/MMBTU 0.38.9 LB/H COMBINED 0.23

16.2 LB/H COMBINED 0.348.9 LB/H COMBINED 0.23

16.2 LB/H COMBINED 0.348.9 LB/H COMBINED 0.23

16.2 LB/H COMBINED 0.340.1 LB/MMBTU 99 9.8 LB/H 0.1

0.1 LB/MMBTU 99 9.8 LB/H 0.111.6 LB/H 50.8 T/YR 0.2911.6 LB/H 50.8 T/YR 0.29

6.5 LB/H COMBINED 0.515 LB/H COMBINED 0.5



0.1 LB/MMBTU 29.6 T/YR 0.10.1 LB/MMBTU 29.6 T/YR 0.10.1 LB/MMBTU 0.10.1 LB/MMBTU 0.10.2 LB/MMBTU 14.26 T/YR 0.20.2 LB/MMBTU 14.26 T/YR 0.2

11.6 LB/H 50.8 T/YR 0.2911.6 LB/H 50.8 T/YR 0.290.24 LB/MMBTU 80 7.2 LB/H 0.240.24 LB/MMBTU 80 7.2 LB/H 0.240.08 LB/MMBTU 0.080.08 LB/MMBTU 0.08




0.01 LB/MMBTU 0.7 T/YR 0.010.01 LB/MMBTU 0.7 T/YR 0.010.09 LB/H 0.8 T/YR 0.0020.09 LB/H 0.8 T/YR 0.002

20 % OPACIT6 MINUTE AVERAGE 2020 % OPACIT6 MINUTE AVERAGE 2010 % OPACIT6 MIN AV 1010 % OPACIT6 MIN AV 10

0.007 LB/MMBTU 3.15 T/YR0.007 LB/MMBTU 3.15 T/YR

0.1 LB/MMBTU 0 9.8 LB/H 0.10.1 LB/MMBTU 0 9.8 LB/H 0.1

0.01 LB/MMBTU 0.71 T/YR0.01 LB/MMBTU 0.71 T/YR0.48 LB/H 2.1 T/YR0.48 LB/H 2.1 T/YR

0.017 LB/MMBTU 0.61 LB/H0.017 LB/MMBTU 0.61 LB/H

0.1 LB/MMBTU 3 LB/H0.1 LB/MMBTU 3 LB/H

0.07 LB/MMBTU

0.07 LB/MMBTU0.5 LB/H COMBINED

0.62 LB/H COMBINED0.5 LB/H COMBINED

0.62 LB/H COMBINED0.5 LB/H COMBINED

0.62 LB/H COMBINED

STDUNITLISTDLIMIT POLLUTANTCOMPLIANCENOTESLB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU PERMIT MODIFICATION IS FOR CHANGE TO BACT CO LIMIT FROM 0.24 LB/MMBTU TO 0.5 LB/MMBTU. LB/MMBTU PERMIT MODIFICATION IS FOR CHANGE TO BACT CO LIMIT FROM 0.24 LB/MMBTU TO 0.5 LB/MMBTU. LB/MMBTU The CO emission rate during the stack test was 0.16 LB/MMBTU LB/MMBTU The CO emission rate during the stack test was 0.16 LB/MMBTU LB/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT LB/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT LB/MMBTUEACH, CA THE UNITS THAT EMIT CO ARE NOT BEING PHYSICALLY MODIFIED, THEREFORE, NO BACT ANALYSIS IS REQUIRED. LB/MMBTUEACH, CA THE UNITS THAT EMIT CO ARE NOT BEING PHYSICALLY MODIFIED, THEREFORE, NO BACT ANALYSIS IS REQUIRED. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTU LB/MMBTU LB/MMBTU The NOX emission rate from the stack test was 0.45 LB/MMBTU LB/MMBTU The NOX emission rate from the stack test was 0.45 LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT LB/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTUCALCULATB) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). LB/MMBTU

LB/MMBTU LB/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT LB/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU FABRIC FILTERS ARE INFEASIBLE DUE TO FIRE POTENTIAL. THEREFORE THE NEXT MOST EFFECTIVE CONTROL FOR PM10 IS THE DRY ELECTROSTATIC PRECIPITATOR. LB/MMBTU FABRIC FILTERS ARE INFEASIBLE DUE TO FIRE POTENTIAL. THEREFORE THE NEXT MOST EFFECTIVE CONTROL FOR PM10 IS THE DRY ELECTROSTATIC PRECIPITATOR. LB/MMBTU LB/MMBTU LB/MMBTU The emission rate from the stack test was 0.004 LB PM-PM10/MMBTU LB/MMBTU The emission rate from the stack test was 0.004 LB PM-PM10/MMBTU LB/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT LB/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT LB/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT % OPACIT6 MINUTE % OPACIT6 MINUTE % OPACIT6 MIN AV % OPACIT6 MIN AV

VOC CONTROL IS NOT FEASIBLE DUE TO THE LOW POTENTIAL VOC EMISSION CONCENTRATION. VOC CONTROL IS NOT FEASIBLE DUE TO THE LOW POTENTIAL VOC EMISSION CONCENTRATION.

LB/MMBTU LB/MMBTU

B) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). B) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). B) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). B) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). B) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2). B) GOOD COMBUSTION PRACTICES FOR BURNING WOOD FUEL: I) THE TEMPERATURE OF THE EXHAUST GAS EXITING THE BOILER SHALL BE MAINTAINED AT A MINIMUM OF 1250 DEGREES FAHRENHEIT. II) THE RESIDENCE TIME OF THE BOILER SHALL BE A MINIMUM OF 1 SECOND. III) THE 8-HOUR AVERAGE CARBON MONOXIDE CONCENTRATION OF THE EXHAUST GAS EXITING THE BOILER MAY NOT EXCEED 600 PARTS PER MILLION DRY VOLUME (PPMDV), AT 7% OXYGEN (O2).

PERMIT MODIFICATION IS FOR CHANGE TO BACT CO LIMIT FROM 0.24 LB/MMBTU TO 0.5 LB/MMBTU. PERMIT MODIFICATION IS FOR CHANGE TO BACT CO LIMIT FROM 0.24 LB/MMBTU TO 0.5 LB/MMBTU.

STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT THE UNITS THAT EMIT CO ARE NOT BEING PHYSICALLY MODIFIED, THEREFORE, NO BACT ANALYSIS IS REQUIRED. THE UNITS THAT EMIT CO ARE NOT BEING PHYSICALLY MODIFIED, THEREFORE, NO BACT ANALYSIS IS REQUIRED.


STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT



FABRIC FILTERS ARE INFEASIBLE DUE TO FIRE POTENTIAL. THEREFORE THE NEXT MOST EFFECTIVE CONTROL FOR PM10 IS THE DRY ELECTROSTATIC PRECIPITATOR. FABRIC FILTERS ARE INFEASIBLE DUE TO FIRE POTENTIAL. THEREFORE THE NEXT MOST EFFECTIVE CONTROL FOR PM10 IS THE DRY ELECTROSTATIC PRECIPITATOR.

The emission rate from the stack test was 0.004 LB PM-PM10/MMBTU The emission rate from the stack test was 0.004 LB PM-PM10/MMBTU STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT STANDARD EMISSIONS CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT


VOC CONTROL IS NOT FEASIBLE DUE TO THE LOW POTENTIAL VOC EMISSION CONCENTRATION. VOC CONTROL IS NOT FEASIBLE DUE TO THE LOW POTENTIAL VOC EMISSION CONCENTRATION.

FABRIC FILTERS ARE INFEASIBLE DUE TO FIRE POTENTIAL. THEREFORE THE NEXT MOST EFFECTIVE CONTROL FOR PM10 IS THE DRY ELECTROSTATIC PRECIPITATOR. FABRIC FILTERS ARE INFEASIBLE DUE TO FIRE POTENTIAL. THEREFORE THE NEXT MOST EFFECTIVE CONTROL FOR PM10 IS THE DRY ELECTROSTATIC PRECIPITATOR.

RBLCID FACILITY CORPORAFACILITYSAGENCYNPERMITDAFACILITYDPROCESSID-0009 ID NAT'L DEPARTMEID IDAHO, O 6/26/2000 NUCLEAR (4) CPP-6ID-0013 IDAHO NUNATIONALID IDAHO DE 6/26/2000 NUCLEAR BOILERS, ID-0013 IDAHO NUNATIONALID IDAHO DE 6/26/2000 NUCLEAR BOILER, PNJ-0045 MERCK - MERCK NJ NEW JERS1/14/1997 CHEMICALBOILERS - MO-0051 PROCTOR Proctor & MO MISSOURI 1/1/1998 SANITARYBOILERS, #TN-0054 PROCTOR PROCTOR TN TENNESSE3/19/1998 BOILERND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, ME-0017 MCCAINE MCCAINE ME MAINE DE 3/12/1999 BOILER, *NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, N*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, NVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOAK-0059 USAF EARUSAF EARAK ALASKA D 9/29/2003 BOILERS, DMN-0053 FAIRBAULMN MUNICMN MINNESOT7/15/2004 LARGE COBOILER, DIMN-0053 FAIRBAULMN MUNICMN MINNESOT7/15/2004 LARGE COBOILER, DIVA-0299 UNITED S UNITED S VA VIRGINIA 6/19/2006 GYPSUM WBOILER, OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)VA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOMN-0053 FAIRBAULMN MUNICMN MINNESOT7/15/2004 LARGE COBOILER, DIMN-0053 FAIRBAULMN MUNICMN MINNESOT7/15/2004 LARGE COBOILER, DINJ-0045 MERCK - MERCK NJ NEW JERS1/14/1997 CHEMICALBOILERS - KY-0068 TOYOTA MTOYOTA MKY KENTUCKY 5/29/1997 MODIFICABOILER (FMO-0051 PROCTOR Proctor & MO MISSOURI 1/1/1998 SANITARYBOILERS, #ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, ME-0017 MCCAINE MCCAINE ME MAINE DE 3/12/1999 BOILER, AK-0033 COMINCO COMINCO AK ALASKA D ### HEATERS, ID-0009 ID NAT'L DEPARTMEID IDAHO, O 6/26/2000 NUCLEAR (4) CPP-6ID-0013 IDAHO NUNATIONALID IDAHO DE 6/26/2000 NUCLEAR BOILERS, ID-0013 IDAHO NUNATIONALID IDAHO DE 6/26/2000 NUCLEAR BOILER, P*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, N*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, NLA-0137 NORTH BECOLUMBIALA LOUISIAN 5/22/2002 CARBON BSTEAM BOOK-0092 VALERO ATPI PETR OK OKLAHOMA1/13/2003 PETROLEUCRUDE OILOK-0092 VALERO ATPI PETR OK OKLAHOMA1/13/2003 PETROLEUCRUDE OILMI-0355 ABBOTT LABBOTT L MI MICHIGAN9/16/2003 NUTRITIO BOILER, FMI-0355 ABBOTT LABBOTT L MI MICHIGAN9/16/2003 NUTRITIO BOILER, FAK-0060 DUTCH HAWESTWARDAK ALASKA D ### FISH PRO BOILER, FUWA-0313 HANFORDUNITED S WA WASHINGT ### RADIOACTBOILERS, *NE-0023 BEATRICENEBRASKANE NEBRASKA6/22/2004 PERMIT TOAUXILIARY

*NE-0023 BEATRICENEBRASKANE NEBRASKA6/22/2004 PERMIT TOAUXILIARYVA-0299 UNITED S UNITED S VA VIRGINIA 6/19/2006 GYPSUM WBOILER, OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)KY-0068 TOYOTA MTOYOTA MKY KENTUCKY 5/29/1997 MODIFICABOILER (FND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T GLYCOL SKAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T PORTABLE AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T MISCELLAAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T RIG BOILEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (DAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (DAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,ME-0017 MCCAINE MCCAINE ME MAINE DE 3/12/1999 BOILER, ID-0009 ID NAT'L DEPARTMEID IDAHO, O 6/26/2000 NUCLEAR (4) CPP-6AK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCBOILERS (AK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCBOILER (IDAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCBOILER (IDAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCHOT AIR DAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCHOT AIR D*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, N*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, NVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOWA-0313 HANFORDUNITED S WA WASHINGT ### RADIOACTBOILERS, MN-0053 FAIRBAULMN MUNICMN MINNESOT7/15/2004 LARGE COBOILER, DIMN-0053 FAIRBAULMN MUNICMN MINNESOT7/15/2004 LARGE COBOILER, DIOH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)MO-0051 PROCTOR Proctor & MO MISSOURI 1/1/1998 SANITARYBOILERS, #VT-0016 OMYA / V OMYA, INC.VT VERMONT ### PRODUCTIBOILER, FVT-0018 AGRIMARK/AGRIMARK/VT VERMONT 1/3/2000 CHEESE BOILER, (2AK-0058 NORTHSTABP EXPLORAK ALASKA D 8/16/2000 OIL AND HEATERSVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOAK-0060 DUTCH HAWESTWARDAK ALASKA D ### FISH PRO BOILER, FUWA-0313 HANFORDUNITED S WA WASHINGT ### RADIOACTBOILERS, OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)NJ-0045 MERCK - MERCK NJ NEW JERS1/14/1997 CHEMICALBOILERS - KY-0068 TOYOTA MTOYOTA MKY KENTUCKY 5/29/1997 MODIFICABOILER (FTN-0054 PROCTOR PROCTOR TN TENNESSE3/19/1998 BOILER

ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T GLYCOL SKAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T PORTABLE AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T MISCELLAAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T RIG BOILEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (DAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (DAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,ME-0017 MCCAINE MCCAINE ME MAINE DE 3/12/1999 BOILER, ID-0009 ID NAT'L DEPARTMEID IDAHO, O 6/26/2000 NUCLEAR (4) CPP-6ID-0013 IDAHO NUNATIONALID IDAHO DE 6/26/2000 NUCLEAR BOILERS, ID-0013 IDAHO NUNATIONALID IDAHO DE 6/26/2000 NUCLEAR BOILER, PAK-0058 NORTHSTABP EXPLORAK ALASKA D 8/16/2000 OIL AND HEATERSAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCBOILERS (AK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCBOILER (IDAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCBOILER (IDAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCHOT AIR DAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCHOT AIR D*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, N*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, NLA-0137 NORTH BECOLUMBIALA LOUISIAN 5/22/2002 CARBON BSTEAM BOVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOAK-0059 USAF EARUSAF EARAK ALASKA D 9/29/2003 BOILERS, DAK-0060 DUTCH HAWESTWARDAK ALASKA D ### FISH PRO BOILER, FUMN-0053 FAIRBAULMN MUNICMN MINNESOT7/15/2004 LARGE COBOILER, DIMN-0053 FAIRBAULMN MUNICMN MINNESOT7/15/2004 LARGE COBOILER, DIOH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)NJ-0045 MERCK - MERCK NJ NEW JERS1/14/1997 CHEMICALBOILERS - KY-0068 TOYOTA MTOYOTA MKY KENTUCKY 5/29/1997 MODIFICABOILER (FND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T GLYCOL SKAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T PORTABLE AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T MISCELLAAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T RIG BOILEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (DAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (DAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,AK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATERS,

AK-0033 COMINCO COMINCO AK ALASKA D ### HEATERS, AK-0033 COMINCO COMINCO AK ALASKA D ### HEATERS, ID-0009 ID NAT'L DEPARTMEID IDAHO, O 6/26/2000 NUCLEAR (4) CPP-6AK-0058 NORTHSTABP EXPLORAK ALASKA D 8/16/2000 OIL AND HEATERSAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCBOILERS (AK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCBOILER (IDAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCBOILER (IDAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCHOT AIR DAK-0050 DUTCH HAUNISEA INAK ALASKA D 3/28/2001 THE DUTCHOT AIR D*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, N*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, NAK-0060 DUTCH HAWESTWARDAK ALASKA D ### FISH PRO BOILER, FUOH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)NJ-0045 MERCK - MERCK NJ NEW JERS1/14/1997 CHEMICALBOILERS - MO-0051 PROCTOR Proctor & MO MISSOURI 1/1/1998 SANITARYBOILERS, #TN-0054 PROCTOR PROCTOR TN TENNESSE3/19/1998 BOILERME-0017 MCCAINE MCCAINE ME MAINE DE 3/12/1999 BOILER, *NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS ### ELECTRICAUXILIARY*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, N*OH-0251 CENTRAL CENTRAL OH OHIO ENV ### SOYBEAN BOILER, NVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOMN-0053 FAIRBAULMN MUNICMN MINNESOT7/15/2004 LARGE COBOILER, DIMN-0053 FAIRBAULMN MUNICMN MINNESOT7/15/2004 LARGE COBOILER, DIOH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2)

PROCTYPEFUEL THRUPUT THRUPUTUPROCESSPOLLUTANCONTROLCTRLDESC13.22 DISTILLAT 29976 GAL/D FOUR CPP-Beryllium N NONE IND13.22 DISTILLAT 36.4 MMBTU/H TOTAL FUEBeryllium P DISTILLA13.22 DISTILLAT 29.3 MMBTU/H TOTAL FUEBeryllium P DISTILLA13.22 NO. 2 OIL 99.5 MMBTU/H NO. 2 FUECarbon MoN NONE13.22 #2 FUEL O 265.7 KGAL/YR ADDITIONACarbon MoN13.22 NO. 2 FUE 0 STACK TECarbon MoN13.22 NO. 2 FUE 13 MMBTU/H Carbon MoN13.22 NATURAL 28 MMBTU/H This procesCarbon MoN13.21 RESIDUAL 656.7 GAL/H INSTALLA Carbon MoN13.22 DISTILLAT 99 MMBTU/H DISTILLATCarbon MoP GOOD COM13.22 DISTILLAT 99 MMBTU/H DISTILLATCarbon MoP GOOD COM13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Carbon MoN13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Carbon MoN13.22 DISTILLAT 43.2 MMBTU One of two Carbon MoB GOOD COM13.22 DISTILLAT 43.2 MMBTU One of two Carbon MoB GOOD COM13.22 DIESEL Boiler unit Carbon MoP GOOD COMBUSTION PRACTIC13.22 #2 FUEL O 40 MMBTU/H AUXILIARYCarbon MoP GOOD COM13.22 #2 FUEL O 40 MMBTU/H AUXILIARYCarbon MoP GOOD COM13.22 2.6 MMBTU/H Carbon MoN13.22 FUEL OIL 20.4 MMBTU/H TWO BOILECarbon MoN13.22 FUEL OIL 20.4 MMBTU/H TWO BOILECarbon MoN13.22 DISTILLAT 43.2 MMBTU One of two Nitrogen D B FLUE GAS13.22 DISTILLAT 43.2 MMBTU One of two Nitrogen D B FLUE GAS13.22 #2 FUEL O 40 MMBTU/H AUXILIARYNitrogen D P LOW NOX 13.22 #2 FUEL O 40 MMBTU/H AUXILIARYNitrogen D P LOW NOX 13.22 NO. 2 OIL 99.5 MMBTU/H NO. 2 FUENitrogen O P LNB13.22 NO.2 FUEL 96 MMBTU/H A SEPARATNitrogen O N N/A13.22 #2 FUEL O 265.7 KGAL/YR ADDITIONANitrogen O P LOW NOX 13.22 NO. 2 FUE 13 MMBTU/H Nitrogen O N13.22 NATURAL 28 MMBTU/H This procesNitrogen O N13.21 RESIDUAL 656.7 GAL/H INSTALLA Nitrogen O P LOW NOX 13.22 ARCTIC D 13.4 MMBTU/H 3 ABCO H Nitrogen O P LOW NOX 13.22 DISTILLAT 29976 GAL/D FOUR CPP-Nitrogen O A FLUE GAS13.22 DISTILLAT 36.4 MMBTU/H TOTAL FUENitrogen O P FLUE GAS13.22 DISTILLAT 29.3 MMBTU/H TOTAL FUENitrogen O P FLUE GAS13.22 DISTILLAT 99 MMBTU/H DISTILLATNitrogen O P LIMIT BOI13.22 DISTILLAT 99 MMBTU/H DISTILLATNitrogen O P LIMIT BOI13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Nitrogen O P USE OF L13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Nitrogen O P USE OF L13.29 FEEDSTOC 15 MMBTU/H Nitrogen O N13.21 FUEL OIL 145 MMBTU/H Nitrogen O P ULTRA LO13.21 FUEL OIL 135 MMBTU/H Nitrogen O P ULTRA LO13.22 #2 FUEL O 98.51 MMBTU/H FUEL OIL Nitrogen O P LOW NOX 13.22 #2 FUEL O 98.51 MMBTU/H FUEL OIL Nitrogen O P LOW NOX 13.29 DISTILLAT 29.3 MMBTU/H Throughput Nitrogen O P LOW NOX 13.21 #2 FUEL O 50.2 MMBTU/H SIX HORI Nitrogen O P LOW NOX 13.22 NATURAL 73.3 MMBTU/H THIS UNITNitrogen O N OPERATIO

13.22 NATURAL 73.3 MMBTU/H THIS UNITNitrogen O N OPERATIO13.22 2.6 MMBTU/H Nitrogen O N13.22 FUEL OIL 20.4 MMBTU/H TWO BOILENitrogen O P LOW NOX 13.22 FUEL OIL 20.4 MMBTU/H TWO BOILENitrogen O P LOW NOX 13.22 NO.2 FUEL 96 MMBTU/H A SEPARATParticulate A FABRIC FI13.22 NO. 2 FUE 13 MMBTU/H Particulate N13.22 NATURAL 28 MMBTU/H This procesParticulate N13.22 DIESEL 1.05 LB/MMBTUGLYCOL SKParticulate N NONE IND13.22 DIESEL 1 MMBTU/H TYPICAL Particulate P GOOD OPE13.22 DIESEL 13 MMBTU/H EQUIPMENParticulate P GOOD OPE13.22 DIESEL 6.3 MMBTU/H PERMIT LIParticulate P GOOD OPE13.22 DIESEL 3.5 MMBTU/H PERMIT L Particulate P GOOD OPE13.22 DIESEL 4.2 MMBTU/H DURING PParticulate P GOOD OPE13.22 DIESEL 4 MMBTU/H TYPICAL Particulate P GOOD OPE13.22 DIESEL 35 MMBTU/H TYPICAL Particulate P GOOD OPE13.22 DIESEL 2 MMBTU/H TYPICAL Particulate P GOOD OPE13.22 DIESEL 20 MMBTU/H TYPICAL Particulate P GOOD OPE13.21 RESIDUAL 656.7 GAL/H INSTALLA Particulate P 0.5 % SUL13.22 DISTILLAT 29976 GAL/D FOUR CPP-Particulate N NONE IND13.29 LIQUID FU 400 BHP, EAC THIS ENT Particulate P GOOD AIR13.29 LIQUID FU 400 BHP ONE JOHNParticulate N13.29 LIQUID FU 200 BHP, EAC FOR PURPParticulate N13.29 24.1 MMBTU/H,TWO STORDParticulate N13.29 6.3 MMBTU/H ONE ALFA-Particulate N13.22 DISTILLAT 99 MMBTU/H DISTILLATParticulate P LIMITED U13.22 DISTILLAT 99 MMBTU/H DISTILLATParticulate P LIMITED U13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Particulate N13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Particulate N13.22 DISTILLAT 43.2 MMBTU One of two Particulate P GOOD COM13.22 DISTILLAT 43.2 MMBTU One of two Particulate P GOOD COM13.21 #2 FUEL O 50.2 MMBTU/H SIX HORI Particulate P REDUCED 13.22 #2 FUEL O 40 MMBTU/H AUXILIARYParticulate P CLEAN FU13.22 #2 FUEL O 40 MMBTU/H AUXILIARYParticulate P CLEAN FU13.22 FUEL OIL 20.4 MMBTU/H TWO BOILEParticulate N13.22 FUEL OIL 20.4 MMBTU/H TWO BOILEParticulate N13.22 #2 FUEL O 265.7 KGAL/YR ADDITIONAParticulate P LOW NOX 13.22 # 2 FUEL O 24 MMBTU/H fire tube b Particulate P LOW SULF13.21 #6 FUEL O 27 MMBTU/H Throughpu Particulate P FUEL S <=13.22 DIESEL 10 MMBTU/H SOURCE ID:Particulate P GOOD COMBUSTION PRACTIC13.22 DISTILLAT 43.2 MMBTU One of two Particulate P GOOD COM13.22 DISTILLAT 43.2 MMBTU One of two Particulate P GOOD COM13.29 DISTILLAT 29.3 MMBTU/H Throughput Particulate P GOOD COMBUSTION MANAGEME13.21 #2 FUEL O 50.2 MMBTU/H SIX HORI Particulate P REDUCED 13.22 FUEL OIL 20.4 MMBTU/H TWO BOILEParticulate N13.22 FUEL OIL 20.4 MMBTU/H TWO BOILEParticulate N13.22 NO. 2 OIL 99.5 MMBTU/H NO. 2 FUESulfur DioxN NONE13.22 NO.2 FUEL 96 MMBTU/H A SEPARATSulfur DioxP THE SULF13.22 NO. 2 FUE 0 STACK TESulfur DioxN

13.22 NO. 2 FUE 13 MMBTU/H Sulfur DioxN13.22 DIESEL 1.05 LB/MMBTUGLYCOL SKSulfur DioxP SULFUR C13.22 DIESEL 1 MMBTU/H TYPICAL Sulfur DioxP ENSURE TH13.22 DIESEL 13 MMBTU/H EQUIPMENSulfur DioxP TO ENSUR13.22 DIESEL 6.3 MMBTU/H PERMIT LISulfur DioxP SULFUR C13.22 DIESEL 3.5 MMBTU/H PERMIT L Sulfur DioxP SULFUR C13.22 DIESEL 4.2 MMBTU/H DURING PSulfur DioxP SULFUR C13.22 DIESEL 4 MMBTU/H TYPICAL Sulfur DioxP SULFUR C13.22 DIESEL 35 MMBTU/H TYPICAL Sulfur DioxP SULFUR C13.22 DIESEL 2 MMBTU/H TYPICAL Sulfur DioxP SULFUR C13.22 DIESEL 20 MMBTU/H TYPICAL Sulfur DioxP SULFUR C13.21 RESIDUAL 656.7 GAL/H INSTALLA Sulfur DioxP 0.5 % SUL13.22 DISTILLAT 29976 GAL/D FOUR CPP-Sulfur DioxP FUEL CON13.22 DISTILLAT 36.4 MMBTU/H TOTAL FUESulfur DioxP LOW SULF13.22 DISTILLAT 29.3 MMBTU/H TOTAL FUESulfur DioxP LOW SULF13.22 DIESEL 10 MMBTU/H SOURCE ID:Sulfur DioxP FUEL SULFUR LIMITS: USED O13.29 LIQUID FU 400 BHP, EAC THIS ENT Sulfur DioxP ACCORDIN13.29 LIQUID FU 400 BHP ONE JOHNSulfur DioxP USE DIES13.29 LIQUID FU 200 BHP, EAC FOR PURPSulfur DioxP USE DIES13.29 24.1 MMBTU/H,TWO STORDSulfur DioxP USE DIES13.29 6.3 MMBTU/H ONE ALFA-Sulfur DioxP USE DIES13.22 DISTILLAT 99 MMBTU/H DISTILLATSulfur DioxP LOW SULF13.22 DISTILLAT 99 MMBTU/H DISTILLATSulfur DioxP LOW SULF13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Sulfur DioxN13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Sulfur DioxN13.29 FEEDSTOC 15 MMBTU/H Sulfur DioxP SULFUR C13.22 DISTILLAT 43.2 MMBTU One of two Sulfur DioxP GOOD COM13.22 DISTILLAT 43.2 MMBTU One of two Sulfur DioxP GOOD COM13.22 DIESEL Boiler unit Sulfur DioxP LOW SULFUR FUEL: < 0.3 % S 13.29 DISTILLAT 29.3 MMBTU/H Throughput Sulfur DioxP LOW SULFUR FUEL: SULFUR RE13.22 #2 FUEL O 40 MMBTU/H AUXILIARYSulfur DioxP LOW SULF13.22 #2 FUEL O 40 MMBTU/H AUXILIARYSulfur DioxP LOW SULF13.22 FUEL OIL 20.4 MMBTU/H TWO BOILESulfur DioxN13.22 FUEL OIL 20.4 MMBTU/H TWO BOILESulfur DioxN13.22 NO. 2 OIL 99.5 MMBTU/H NO. 2 FUETotal Susp N NONE13.22 NO.2 FUEL 96 MMBTU/H A SEPARATVisible EmiN N/A13.22 NO. 2 FUE 13 MMBTU/H Visible EmiN13.22 NATURAL 28 MMBTU/H This procesVisible EmiN13.22 DIESEL 1.05 LB/MMBTUGLYCOL SKVisible EmiN NONE IND13.22 DIESEL 1 MMBTU/H TYPICAL Visible EmiP GOOD OPERATIONS PRACTICES.13.22 DIESEL 13 MMBTU/H EQUIPMENVisible EmiP GOOD OPE13.22 DIESEL 6.3 MMBTU/H PERMIT LIVisible EmiP GOOD OPE13.22 DIESEL 3.5 MMBTU/H PERMIT L Visible EmiP GOOD OPE13.22 DIESEL 4.2 MMBTU/H DURING PVisible EmiP GOOD OPE13.22 DIESEL 4 MMBTU/H TYPICAL Visible EmiP GOOD OPE13.22 DIESEL 35 MMBTU/H TYPICAL Visible EmiP GOOD OPE13.22 DIESEL 2 MMBTU/H TYPICAL Visible EmiP GOOD OPE13.22 DIESEL 20 MMBTU/H TYPICAL Visible EmiP GOOD OPE

13.22 DIESEL THESE SMVisible EmiN13.22 ARCTIC D 13.4 MMBTU/H 3 ABCO H Visible EmiP LOW NOX 13.22 DISTILLAT 29976 GAL/D FOUR CPP-Visible EmiN13.22 DIESEL 10 MMBTU/H SOURCE ID:Visible EmiP GOOD COM13.29 LIQUID FU 400 BHP, EAC THIS ENT Visible EmiP GOOD AIR13.29 LIQUID FU 400 BHP ONE JOHNVisible EmiN13.29 LIQUID FU 200 BHP, EAC FOR PURPVisible EmiN13.29 24.1 MMBTU/H,TWO STORDVisible EmiN13.29 6.3 MMBTU/H ONE ALFA-Visible EmiN13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Visible EmiN13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Visible EmiN13.29 DISTILLAT 29.3 MMBTU/H Throughput Visible EmiP GOOD COM13.22 FUEL OIL 20.4 MMBTU/H TWO BOILEVisible EmiN13.22 FUEL OIL 20.4 MMBTU/H TWO BOILEVisible EmiN13.22 NO. 2 OIL 99.5 MMBTU/H NO. 2 FUEVolatile O N NONE13.22 #2 FUEL O 265.7 KGAL/YR ADDITIONAVolatile O P LOW NOX 13.22 NO. 2 FUE 0 STACK TEVolatile O N13.21 RESIDUAL 656.7 GAL/H INSTALLA Volatile O N13.22 DISTILLAT 99 MMBTU/H DISTILLATVolatile O P GOOD COM13.22 DISTILLAT 99 MMBTU/H DISTILLATVolatile O P GOOD COM13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Volatile O N13.22 NO 2 FUEL 91.2 MMBTU/H Restriction Volatile O N13.22 DISTILLAT 43.2 MMBTU One of two Volatile O P GOOD COM13.22 DISTILLAT 43.2 MMBTU One of two Volatile O P GOOD COM13.22 #2 FUEL O 40 MMBTU/H AUXILIARYVolatile O P GOOD COM13.22 #2 FUEL O 40 MMBTU/H AUXILIARYVolatile O P GOOD COM13.22 FUEL OIL 20.4 MMBTU/H TWO BOILEVolatile O N13.22 FUEL OIL 20.4 MMBTU/H TWO BOILEVolatile O N

EMISLIMITEMISLIMITEMISLIMI PCTEFFIC EMISLIMITEMISLIMITEMISLIMI STDEMISSL0.126 LB/D COMBINED 0.0023 T/YR COMBINED

0.0126 LB/D 0.0023 T/YR0.0126 LB/D 0.0023 T/YR

3.6 LB/H 0.036 LB/MMBTU 0.0360.15 LB/MMBTU 0.1529.3 LB/H 0 36 LB/H 0

0.5 LB/H 0.0381 LB/H 0.036

0.16 LB/MMBTU 0 15.8 LB/H 09.9 LB/H 3.564 T/YR 0.19.9 LB/H 3.564 T/YR 0.1

11.8 LB/H 53.4 T/YR 0.1411.8 LB/H 53.4 T/YR 0.143.56 LB/H each unit3.56 LB/H each unit

GOOD COMBUSTION PRACTIC see note0.036 LB/MMBTU3 HOUR AVERAGE 0.0360.036 LB/MMBTU3 HOUR AVERAGE 0.036

0.2 LB/H 0.0770.73 LB/H 7.5 T/YR 0.0360.73 LB/H 7.5 T/YR 0.0366.17 LB/H each unit 0.1428246.17 LB/H each unit 0.142824

0.058 LB/MMBTU3 HOUR AVERAGE 0.0580.058 LB/MMBTU3 HOUR AVERAGE 0.058

10 LB/H 0.1 LB/MMBTU 0.10.2 LB/MMBTU 0.2

0.17 LB/MMBTU 0.170.5 LB/H 0.0385.8 LB/H 0.210.3 LB/MMBTU 0 29.6 LB/H 0.3

0.084 LB/MMBTU 0.084599.5 LB/D COMBINED 98.6 T/YR COMBINE 0.14599.5 LB/D 44 98.6 T/YR 0.69599.5 LB/D 44 98.6 T/YR 0.85


9.21 LB/H 22.7 T/YR 0.1069.21 LB/H 22.7 T/YR 0.106

20.93 LB/H HOURLY MAXIMUM 1.40.045 LB/MMBTU 84 28.6 T/YR 0.0450.059 LB/MMBTU 79 34.9 T/YR 0.059

0.14 LB/MMBTU 0.140.14 LB/MMBTU 0.14

4.4 LB/H each 0.150.09 LB/MMBTU@ 3% O2 76 4.52 LB/H 0.09

0.1 LB/MMBTU3 HOUR TEST AVG 0.1

0.1 LB/MMBTU3 HOUR TEST AVG 0.10.3 LB/H 0.1151.5 LB/H 3.5 T/YR 0.0721.5 LB/H 3.5 T/YR 0.0720.1 LB/MMBTU 0.10.2 LB/H 0.0152.4 LB/H 0.1 LB/MMBTU 0.1

0.05 GR/DSCF AV OVER 3 H0.05 GR/DSCF AVERAGED OVER 3 H0.05 GR/DSCF AV OVER 3 H0.05 GR/DSCF AV OVER 3 H0.05 GR/DSCF AV OVER 3 H0.05 GR/DSCF AV OVER 3 H0.05 GR/DSCF AV OVER 3 H0.05 GR/DSCF AV OVER 3 H0.05 GR/DSCF AV OVER 3 H0.05 GR/DSCF AV OVER 3 H0.08 LB/MMBTU 0 7.9 LB/H 0.080.05 GR/DSCF @ 3% O20.05 GR/DSCF EACH0.05 GR/DSCF 3 H AV0.05 GR/DSCF 3 H AV, EACH0.05 GR/DSCF 3 H AV, EACH0.05 GR/DSCF 3 H AV3.96 LB/H 1.426 T/YR 0.043.96 LB/H 1.426 T/YR 0.040.47 LB/H 2.06 T/YR 0.00540.47 LB/H 2.06 T/YR 0.00540.62 LB/H each unit0.62 LB/H each unit0.02 LB/MMBTU 1 LB/H 0.02

0.024 LB/MMBTU3 HOUR AVERAGE 0.0240.024 LB/MMBTU3 HOUR AVERAGE 0.024

0.31 LB/H 0.27 T/YR 0.0150.31 LB/H 0.27 T/YR 0.0150.05 LB/MMBTU 0.050.35 LB/MMBTU 8.4 LB/H 0.350.31 LB/MMBTU 8.5 LB/H each 0.31

GOOD COMBUSTION PRACTIC see note0.32 LB/H each unit0.32 LB/H each unit

GOOD COMBUSTION MANAGEMEsee note0.02 LB/MMBTU 1 LB/H 0.02

0.5 LB/H 0.78 T/YR 0.0240.5 LB/H 0.78 T/YR 0.0245.1 LB/H 0.0510.3 LB/MMBTU 40 T/YR 0.3

37.96 LB/H 0 46.64 LB/H 0

4 LB/H 0.31500 PPM AVERAGED OVER A PERIOD OF 3 H 2.71500 PPM AVERAGED OVER 3 H 2.71500 PPM AVERAGED OVER 3 H 2.71500 PPM AV OVER 3 H 2.71500 PPM AV OVER 3 H 2.71500 PPM AV OVER 3 H 2.71500 PPM AV OVER 3 H 2.71500 PPM AVERAGED OVER 3 H 2.71500 PPM AV OVER 3 H 2.71500 PPM AV OVER 3 H 2.71

0.52 LB/MMBTU 0 51.2 LB/H 01295 LB/D COMBINED 213 T/YR COMBINE 0.311295 LB/D 213 T/YR 1.51295 LB/D 213 T/YR 1.8

FUEL SULFUR LIMITS: USED O see note500 PPM 3 H AV, EACH 2.7500 PPM 3 H AV 2.7500 PPM 3 H AV, EACH 2.7500 PPM 3 H AV, EACH 2.7500 PPM 3 H AV 2.7

5.021 LB/H 1.807 T/YR 0.05075.021 LB/H 1.807 T/YR 0.0507

18.2 LB/H 26.2 T/YR 0.2118.2 LB/H 26.2 T/YR 0.21

166.17 LB/H HOURLY MAXIMUM 11.12.19 LB/H each unit2.19 LB/H each unit

LOW SULFUR FUEL: < 0.3 % S see noteLOW SULFUR FUEL: SULFUR REsee note

0.051 LB/MMBTU 0.0510.051 LB/MMBTU 0.051

10.4 LB/H 3.64 T/YR 0.5110.4 LB/H 3.64 T/YR 0.51

1.4 LB/H 0.14 LB/MMBTU 0.1420 % OPACITY 2020 % OPACITY 2020 % OPACITY 2020 % OPACITFOR > 3 MIN IN ANY 1 H 20

GOOD OPERATIONS PRACTICES. 2020 % OPACITFOR > 3 MIN IN ANY 1 H 2020 % OPACITFOR > 3 MIN IN ANY 1 H 2020 % OPACITFOR > 3 MIN IN ANY 1 H 2020 % OPACITFOR >3 MIN IN ANY 1 H 2020 % OPACITFOR > 3 MIN IN ANY 1 H 2020 % OPACITFOR > 3 MIN IN ANY 1 H 2020 % OPACITFOR > 3 MIN IN ANY 1 H 2020 % OPACITFOR > 3 MIN IN ANY 1 H 20

20 % OPACITY 2020 % OPACITY 2020 % OPACIT6 MIN AV 27 % OPACITFOR 1 6 M 2020 % OPACITY 2020 % OPACITFOR NO MORE THAN 3 MIN/H, EACH 2020 % OPACITFOR NO MORE THAN 3 MIN/H 2020 % OPACITFOR NO MORE THAN 3 MIN/H, EACH 2020 % OPACITFOR NO MORE THAN 3 MIN/H, EACH 2020 % OPACITFOR NO MORE THAN 3 MIN/H 2020 % OPACIT6-minute average 2020 % OPACIT6-minute average 2020 % OPACIT6 min avg 20

5 % OPACITAS A 6-MINUTE AVERAGE 55 % OPACITAS A 6-MINUTE AVERAGE 5

0.36 LB/H 0.0036 LB/MMBTU 0.00360.052 LB/MMBTU 0.052

4.4 LB/H 0 5.4 LB/H 00.84 LB/H 0 0 0

0.495 LB/H 0.178 T/YR0.495 LB/H 0.178 T/YR

1.18 LB/H 5.17 T/YR 0.0141.18 LB/H 5.17 T/YR 0.0140.23 LB/H each unit0.23 LB/H each unit


0.03 LB/H 0.5 T/YR 0.00150.03 LB/H 0.5 T/YR 0.0015


LB/MMBTU ADDITIONAL CO LIMIT IS 50 PPMVD @7% O2. LB/MMBTU

LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTU LB/MMBTUcalculated Standardized limit calculated using manufacturer's emission factor of 150 lbs CO/1,000,000 lbs of air for both natural gas and fuel oil. LB/MMBTUcalculated Standardized limit calculated using manufacturer's emission factor of 150 lbs CO/1,000,000 lbs of air for both natural gas and fuel oil.

NOT AVAI One of two units NOT AVAI One of two units

BACT is good combustion practices. No emission rate limits. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LIMITS ARE FOR EACH BOILER. LB/MMBTU LIMITS ARE FOR EACH BOILER. LB/MMBTUNOT AVAI one of two units LB/MMBTUNOT AVAI one of two units LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTUCOMBINE LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU Limits based on manufacturer's emission factors: .0352 lb/MMBtu for natural gas and 0.106 lb/MMBtu for fuel oil. LB/MMBTU Limits based on manufacturer's emission factors: .0352 lb/MMBtu for natural gas and 0.106 lb/MMBtu for fuel oil. LB/MMBTUCALCULAT*AS IMPOSED BY PSD-LA-580(M-4), ISSUED JULY 11, 2005. ANNUAL NOX LIMIT FOR THE DRYER STACK (59), STEAM BOILER (62), MAIN COMBUSTION STACK (81), DRYER STACK (84), AND NEW TAIL GAS FLARE (123) ESTABLISHED AT 4140.30 TPY (ANNUAL MAXIMUM). PSD-LA-580(M-3) SETLB/MMBTU LB/MMBTU LB/MMBTU Limit is based on combustion of #2 fuel oil. Limit for burning natural gas is 0.08 lb/MMbtu. LB/MMBTU Limit is based on combustion of #2 fuel oil. Limit for burning natural gas is 0.08 lb/MMbtu. LB/MMBTUcalculated LB/MMBTU@ 3% O2 LB/MMBTU3 HOUR T OPERATION LIMITED TO 500 HOURS PER YEAR. THIS UNIT CAN BURN UP TO 289,000 GAL/YR OF DISTILATE OIL. THE LIMITS INDICATED HERE ARE FOR BURNING OIL. SEE THE PROCEESS AUXILIARY BOILER (NG) FOR EMISSION LIMITS WHILE BURNING NATURAL GAS.

LB/MMBTU3 HOUR T OPERATION LIMITED TO 500 HOURS PER YEAR. THIS UNIT CAN BURN UP TO 289,000 GAL/YR OF DISTILATE OIL. THE LIMITS INDICATED HERE ARE FOR BURNING OIL. SEE THE PROCEESS AUXILIARY BOILER (NG) FOR EMISSION LIMITS WHILE BURNING NATURAL GAS. LB/MMBTU LB/MMBTU LIMITS ARE FOR EACH BOILER. LB/MMBTU LIMITS ARE FOR EACH BOILER. LB/MMBTU THE OUTLET PARTICULATE CONCENTRATION FROM EACH FABRIC FILTER CONTROL DEVICE SHALL NOT EXCEED 0.003 GR PER ACF. LB/MMBTU LB/MMBTU

BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055.

LB/MMBTU NOT AVAI NOT AVAI NOT AVAI NEED EMISSION LIMIT IN STANDARDIZED UNITS. NOT AVAI

NEED EMISSION LIMIT IN STANDARDIZED UNITS.

LB/MMBTU LB/MMBTU LB/MMBTU USING NATURAL GAS WITH BACKUP NO. 2 FUEL OIL. EMISSIONS BASED ON MFG. TESTED RATE FOR NATURAL GAS 0.005 LB/MMBTU AND 0.0054 LB/MMBTU WHEN BURNING #2 OIL. LB/MMBTU USING NATURAL GAS WITH BACKUP NO. 2 FUEL OIL. EMISSIONS BASED ON MFG. TESTED RATE FOR NATURAL GAS 0.005 LB/MMBTU AND 0.0054 LB/MMBTU WHEN BURNING #2 OIL.

NOT AVAI one of two units NOT AVAI one of two units

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LIMIT IS FOR EACH BOILER. LB/MMBTU LIMIT IS FOR EACH BOILER. LB/MMBTU LB/MMBTU regulatory basis: MSER - most stringent emission rate LB/MMBTU

GOOD COMBUSTION PRACTICES. VISIBLE EMISSION LIMIT AS SURROGATE FOR PARTICULATE MATTER EMISSION LIMIT. NOT AVAI one of two units NOT AVAI one of two units

Limit is opacity limit of 20% opacity, 6 min avg. Vendor specifications for these boilers are: 0.025 lb/mmbtu and 0.015 gr/dscf. LB/MMBTU LB/MMBTU LIMIT IS FOR EACH BOILER. LB/MMBTU LIMIT IS FOR EACH BOILER. LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTUCALCULATBACT: FUEL SULFUR LIMIT STATE: EMISSION LIMIT 1 LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULATBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND FUEL RESTRICTION LB/MMBTUCALCULATBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR RESTRICTION TO FUEL LB/MMBTUCALCULATBACT: FUEL SULFUR CONTENT LIMITS STATE: EMISSION LIMIT 1 AND SULFUR CONTENT LIMIT TO FUEL LB/MMBTUCONVERTEBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR CONTENT RESTRICTION TO THE FUEL LB/MMBTUCALCULATBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR CONTENT RESTRICTION TO THE FUEL. LB/MMBTUCALCULATBACT: FUEL SULFUR CONTENT LIMITS STATE: EMISSION LIMIT 1 AND SULFUR CONTENT RESTRICTION TO THE FUEL. LB/MMBTUCALCULATBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR CONTENT RESTRICTION TO THE FUEL.

LB/MMBTUCOMBINE ACCORDING TO NSPS THESE PROCESS UNITS SHALL NOT COMBUST DISTILLATE OIL THAT CONTAINS GREATER THAN 0.5 WEIGHT PERCENT FUEL IN THE CPP-606 BOILERS. ACCORDING TO THIS PERMIT, THE CPP-606 AND INTEC PORTABLE BOILERS SHALL NOT COMBUST FUEL WITH GREATER THAN 0.3LB/MMBTU LB/MMBTU

No emission rate limit -- fuel sulfer limit is BACT. APPLICABLE TO SOURCES ID NO. 217 AND 218 WHICH ARE CAPABLE OF OPERATING ON USED OIL OR FUEL BLENDED WITH USED OIL. LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTUCALCULAT LB/MMBTU LB/MMBTU LB/MMBTUcalculated Using AP-42 emission factor of 0.6 lb/million cubic feet and manufacturer's data 0.21 lb SO2/mmBtu on #2 fuel oil or may opt for burning oil with no greater than 0.5 weight % sulfur. For each shipment of oil, the supplier shall provide the sulfur content LB/MMBTUcalculated Using AP-42 emission factor of 0.6 lb/million cubic feet and manufacturer's data 0.21 lb SO2/mmBtu on #2 fuel oil or may opt for burning oil with no greater than 0.5 weight % sulfur. For each shipment of oil, the supplier shall provide the sulfur content LB/MMBTUCALCULAT*AS IMPOSED BY PSD-LA-580(M-4), ISSUED JULY 11, 2005. ANNUAL SO2 LIMIT FOR THE DRYER STACK (59), STEAM BOILER (62), MAIN COMBUSTION STACK (81), DRYER STACK (84), AND NEW TAIL GAS FLARE (123) ESTABLISHED AT 15,095.70 TPY (ANNUAL MAXIMUM). PSD-LA-580(M-3) S

NOT AVAI One of two units NOT AVAI One of two units

BACT is the use of low sulfur fuel. No emission rate limits. BACT is fuel sulfur limit. Mass balance calculations result in an estimated 122 ppmv.

LB/MMBTU EMISSION LIMIT 1 EQUALS TO 0.05% S BY WEIGHT. LB/MMBTU EMISSION LIMIT 1 EQUALS TO 0.05% S BY WEIGHT. LB/MMBTU LIMITS ARE FOR EACH BOILER. LB/MMBTU LIMITS ARE FOR EACH BOILER. LB/MMBTU % OPACITY % OPACITY % OPACITY % OPACITFOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055 % OPACITFOR > 3 M % OPACITFOR > 3 M % OPACITFOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. % OPACITFOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055 % OPACITFOR >3 MIBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. % OPACITFOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. % OPACITFOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. % OPACITFOR > 3 MTYPICAL OPERATION BEFORE AND DURING COMMISSIONING PERIOD, 2190 H. TYPICAL OPERATION AFTER COMMISSIONING PERIOD, 0 H/YR. % OPACITFOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055.

% OPACITY % OPACITY % OPACIT6 MIN AV % OPACITY VE used as surrogate for PM10 emissions % OPACITFOR NO M % OPACITFOR NO M % OPACITFOR NO M % OPACITFOR NO M % OPACITFOR NO M % OPACIT6-minute a % OPACIT6-minute a % OPACITY Basis is state rule, opacity used as limit for PM10 BACT. % OPACITAS A 6-M OPACITY AT ANY STACK FROM EITHER BOILER. % OPACITAS A 6-M OPACITY AT ANY STACK FROM EITHER BOILER. LB/MMBTU ADDITIONAL VOC LIMIT IS 50 PPMVD @ 7% O2. LB/MMBTU

ADDITIONAL EMISSION LIMIT: 0.005 LB/MMBTU. ADDITIONAL EMISSION LIMIT: 0.005 LB/MMBTU.

LB/MMBTU Using manufacturers test data factors: 8 lb VOC/1,000,000 lb air for natural gas, and 15 lb VOC/1,000,000 lb air for fuel oil. LB/MMBTU Using manufacturers test data factors: 8 lb VOC/1,000,000 lb air for natural gas, and 15 lb VOC/1,000,000 lb air for fuel oil.

One of two units One of two units

LB/MMBTU LIMITS ARE FOR EACH BOILER. LB/MMBTU LIMITS ARE FOR EACH BOILER.

Standardized limit calculated using manufacturer's emission factor of 150 lbs CO/1,000,000 lbs of air for both natural gas and fuel oil. Standardized limit calculated using manufacturer's emission factor of 150 lbs CO/1,000,000 lbs of air for both natural gas and fuel oil.

Limits based on manufacturer's emission factors: .0352 lb/MMBtu for natural gas and 0.106 lb/MMBtu for fuel oil. Limits based on manufacturer's emission factors: .0352 lb/MMBtu for natural gas and 0.106 lb/MMBtu for fuel oil. *AS IMPOSED BY PSD-LA-580(M-4), ISSUED JULY 11, 2005. ANNUAL NOX LIMIT FOR THE DRYER STACK (59), STEAM BOILER (62), MAIN COMBUSTION STACK (81), DRYER STACK (84), AND NEW TAIL GAS FLARE (123) ESTABLISHED AT 4140.30 TPY (ANNUAL MAXIMUM). PSD-LA-580(M-3) SET

Limit is based on combustion of #2 fuel oil. Limit for burning natural gas is 0.08 lb/MMbtu. Limit is based on combustion of #2 fuel oil. Limit for burning natural gas is 0.08 lb/MMbtu.

OPERATION LIMITED TO 500 HOURS PER YEAR. THIS UNIT CAN BURN UP TO 289,000 GAL/YR OF DISTILATE OIL. THE LIMITS INDICATED HERE ARE FOR BURNING OIL. SEE THE PROCEESS AUXILIARY BOILER (NG) FOR EMISSION LIMITS WHILE BURNING NATURAL GAS.


THE OUTLET PARTICULATE CONCENTRATION FROM EACH FABRIC FILTER CONTROL DEVICE SHALL NOT EXCEED 0.003 GR PER ACF.

BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055.

USING NATURAL GAS WITH BACKUP NO. 2 FUEL OIL. EMISSIONS BASED ON MFG. TESTED RATE FOR NATURAL GAS 0.005 LB/MMBTU AND 0.0054 LB/MMBTU WHEN BURNING #2 OIL. USING NATURAL GAS WITH BACKUP NO. 2 FUEL OIL. EMISSIONS BASED ON MFG. TESTED RATE FOR NATURAL GAS 0.005 LB/MMBTU AND 0.0054 LB/MMBTU WHEN BURNING #2 OIL.

GOOD COMBUSTION PRACTICES. VISIBLE EMISSION LIMIT AS SURROGATE FOR PARTICULATE MATTER EMISSION LIMIT.

Limit is opacity limit of 20% opacity, 6 min avg. Vendor specifications for these boilers are: 0.025 lb/mmbtu and 0.015 gr/dscf.

BACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND FUEL RESTRICTION BACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR RESTRICTION TO FUEL BACT: FUEL SULFUR CONTENT LIMITS STATE: EMISSION LIMIT 1 AND SULFUR CONTENT LIMIT TO FUEL BACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR CONTENT RESTRICTION TO THE FUEL BACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR CONTENT RESTRICTION TO THE FUEL. BACT: FUEL SULFUR CONTENT LIMITS STATE: EMISSION LIMIT 1 AND SULFUR CONTENT RESTRICTION TO THE FUEL. BACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR CONTENT RESTRICTION TO THE FUEL.

ACCORDING TO NSPS THESE PROCESS UNITS SHALL NOT COMBUST DISTILLATE OIL THAT CONTAINS GREATER THAN 0.5 WEIGHT PERCENT FUEL IN THE CPP-606 BOILERS. ACCORDING TO THIS PERMIT, THE CPP-606 AND INTEC PORTABLE BOILERS SHALL NOT COMBUST FUEL WITH GREATER THAN 0.3

No emission rate limit -- fuel sulfer limit is BACT. APPLICABLE TO SOURCES ID NO. 217 AND 218 WHICH ARE CAPABLE OF OPERATING ON USED OIL OR FUEL BLENDED WITH USED OIL.

Using AP-42 emission factor of 0.6 lb/million cubic feet and manufacturer's data 0.21 lb SO2/mmBtu on #2 fuel oil or may opt for burning oil with no greater than 0.5 weight % sulfur. For each shipment of oil, the supplier shall provide the sulfur content Using AP-42 emission factor of 0.6 lb/million cubic feet and manufacturer's data 0.21 lb SO2/mmBtu on #2 fuel oil or may opt for burning oil with no greater than 0.5 weight % sulfur. For each shipment of oil, the supplier shall provide the sulfur content *AS IMPOSED BY PSD-LA-580(M-4), ISSUED JULY 11, 2005. ANNUAL SO2 LIMIT FOR THE DRYER STACK (59), STEAM BOILER (62), MAIN COMBUSTION STACK (81), DRYER STACK (84), AND NEW TAIL GAS FLARE (123) ESTABLISHED AT 15,095.70 TPY (ANNUAL MAXIMUM). PSD-LA-580(M-3) S

BACT is fuel sulfur limit. Mass balance calculations result in an estimated 122 ppmv.

BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055

BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055 BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. TYPICAL OPERATION BEFORE AND DURING COMMISSIONING PERIOD, 2190 H. TYPICAL OPERATION AFTER COMMISSIONING PERIOD, 0 H/YR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055.

Using manufacturers test data factors: 8 lb VOC/1,000,000 lb air for natural gas, and 15 lb VOC/1,000,000 lb air for fuel oil. Using manufacturers test data factors: 8 lb VOC/1,000,000 lb air for natural gas, and 15 lb VOC/1,000,000 lb air for fuel oil.

*AS IMPOSED BY PSD-LA-580(M-4), ISSUED JULY 11, 2005. ANNUAL NOX LIMIT FOR THE DRYER STACK (59), STEAM BOILER (62), MAIN COMBUSTION STACK (81), DRYER STACK (84), AND NEW TAIL GAS FLARE (123) ESTABLISHED AT 4140.30 TPY (ANNUAL MAXIMUM). PSD-LA-580(M-3) SET



USING NATURAL GAS WITH BACKUP NO. 2 FUEL OIL. EMISSIONS BASED ON MFG. TESTED RATE FOR NATURAL GAS 0.005 LB/MMBTU AND 0.0054 LB/MMBTU WHEN BURNING #2 OIL. USING NATURAL GAS WITH BACKUP NO. 2 FUEL OIL. EMISSIONS BASED ON MFG. TESTED RATE FOR NATURAL GAS 0.005 LB/MMBTU AND 0.0054 LB/MMBTU WHEN BURNING #2 OIL.


No emission rate limit -- fuel sulfer limit is BACT. APPLICABLE TO SOURCES ID NO. 217 AND 218 WHICH ARE CAPABLE OF OPERATING ON USED OIL OR FUEL BLENDED WITH USED OIL.


TYPICAL OPERATION BEFORE AND DURING COMMISSIONING PERIOD, 2190 H. TYPICAL OPERATION AFTER COMMISSIONING PERIOD, 0 H/YR.

*AS IMPOSED BY PSD-LA-580(M-4), ISSUED JULY 11, 2005. ANNUAL NOX LIMIT FOR THE DRYER STACK (59), STEAM BOILER (62), MAIN COMBUSTION STACK (81), DRYER STACK (84), AND NEW TAIL GAS FLARE (123) ESTABLISHED AT 4140.30 TPY (ANNUAL MAXIMUM). PSD-LA-580(M-3) SET


RBLCID FACILITY CORPORAFACILITYSAGENCYNPERMITDATE FACILITYDPROCESSAL-0202 CORUS T CORUS T AL ALABAMA 6/3/2003 STEEL MILEQUALIZITX-0430 DIAMOND DIAMOND TX TEXAS CO 5/23/2000 LOCATED AHEATERS,AL-0202 CORUS T CORUS T AL ALABAMA 6/3/2003 STEEL MILEQUALIZIWI-0161 AARROW AARROW WI WISCONSI 10/1/1998 CORE WASAL-0202 CORUS T CORUS T AL ALABAMA 6/3/2003 STEEL MILEQUALIZITX-0430 DIAMOND DIAMOND TX TEXAS CO 5/23/2000 LOCATED AHEATERS,TX-0430 DIAMOND DIAMOND TX TEXAS CO 5/23/2000 LOCATED AHEATERS,WI-0161 AARROW AARROW WI WISCONSI 10/1/1998 CORE WASAL-0202 CORUS T CORUS T AL ALABAMA 6/3/2003 STEEL MILEQUALIZIOK-0050 ONETA GECALPINE OK OKLAHOMA 1/21/2000 ELECTRICDUCT BUROK-0050 ONETA GECALPINE OK OKLAHOMA 1/21/2000 ELECTRICDUCT BUROK-0050 ONETA GECALPINE OK OKLAHOMA 1/21/2000 ELECTRICDUCT BUROK-0050 ONETA GECALPINE OK OKLAHOMA 1/21/2000 ELECTRICDUCT BUROK-0050 ONETA GECALPINE OK OKLAHOMA 1/21/2000 ELECTRICDUCT BUROK-0050 ONETA GECALPINE OK OKLAHOMA 1/21/2000 ELECTRICDUCT BURTX-0309 FORMOSA FORMOSA TX TEXAS CO 2/10/2000 THIS PER WASTE HEAMA-0029 SITHE MY SITHE MY MA MASSACHU 9/29/1999 COMBINEDBOILER, ACA-0919 COCA COLCOCA COLCA SOUTH CO 11/23/1999 BOILER, FCA-0938 CHILDRENCHILDRENCA SOUTH CO 12/2/1999 BOILERS BOILER, (3CA-1021 DAMAPONGDAMAPONGCA SOUTH CO 12/7/1999 BOILER: 1TX-0309 FORMOSA FORMOSA TX TEXAS CO 2/10/2000 THIS PER WASTE HEACA-0946 LACORR PLACORR PCA SOUTH CO 7/12/2000 PROVIDE BOILERAR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, PAR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, H*AL-0231 NUCOR DENUCOR C AL ALABAMA 6/12/2007 THE FACI VACUUM D*NE-0043 NATUREWORKS, LL NE NEBRASKA 10/1/2007 POLYMER HOT OIL NJ-0045 MERCK - MERCK NJ NEW JERS 1/14/1997 CHEMICALBOILERS -AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0019 QUINCY S QUINCY S AR ARKANSAS 3/4/1997 BOILER, IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PREIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #3IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #2IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #1IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HYDROGENIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PREWI-0188 GOLDEN BGOLDEN BWI WISCONSI 6/24/1997 PRINTING SPACE HELA-0115 GEISMAR SHELL CHLA LOUISIAN 11/3/1997 PERMIT F HEATER, HPA-0149 BUCKNELLBUCKNELLPA PENNSYLV 11/26/1997 HEAT RECLA-0113 BASF CORBASF CORLA LOUISIAN 12/30/1997 DUCT BURLA-0112 GEISMAR AIR LIQU LA LOUISIAN 2/13/1998 AIR SEPA BOILER NOLA-0112 GEISMAR AIR LIQU LA LOUISIAN 2/13/1998 AIR SEPA REACTIVAMI-0283 WESTERN WESTERN MI MICHIGAN 4/27/1998 POWER P DUCT BURWY-0051 UNION PA UNION PA WY WYOMING 5/18/1998 HEATER, 2WY-0052 UNION PA UNION PA WY WYOMING 5/18/1998 HEATER, 2ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER,

IN-0104 CON AGRACON AGRAIN INDIANA D 8/14/1998 SOYBEAN BOILERS,TX-0300 SALT CREMOBIL EX TX TEXAS CO 10/13/1998 MOBIL EX HOT OIL HOH-0245 REPUBLICREPUBLICOH OHIO ENV 1/27/1999 STEEL MILECCENTRINJ-0042 ROCHE VI ROCHE VITNJ NEW JERS 2/5/1999 COGENERBOILER 1 CO-0040 AMERICAN SODA, LLCO COLORADO 5/6/1999 INDUSTRICO-0041 AMERICAN SODA, LLCO COLORADO 5/6/1999 BOILER NOCA-0917 SOUTHERNSOUTHERNCA SOUTH CO 8/17/1999 HOT OIL CA-0948 MARUCHANMARUCHANCA SOUTH CO 9/9/1999 PASTA ANBOILER, (2MA-0029 SITHE MY SITHE MY MA MASSACHU 9/29/1999 COMBINEDBOILER, AOK-0051 GREEN COCOGENTRIOK OKLAHOMA 10/1/1999 AUXILIARYCA-0923 ARAMARK ARAMARK CA SAN JOAQ 10/4/1999 FACILITY DRYER, NCA-0919 COCA COLCOCA COLCA SOUTH CO 11/23/1999 BOILER, FCA-0918 SCHI SAN SCHI SAN CA CALIFORN 12/2/1999 CLAYTON CA-0938 CHILDRENCHILDRENCA SOUTH CO 12/2/1999 BOILERS BOILER, (3CA-1021 DAMAPONGDAMAPONGCA SOUTH CO 12/7/1999 BOILER: 1CA-0939 HI-COUNTHI-COUNTCA SOUTH CO 12/16/1999 BOILER U BOILERCA-1006 HI-COUNTHI-COUNTCA SOUTH CO 12/16/1999 BOILER, 2CA-0941 SANTA MOSANTA MOCA SOUTH CO 1/28/2000 BOILER U BOILER, TX-0309 FORMOSA FORMOSA TX TEXAS CO 2/10/2000 THIS PER WASTE HEACA-0942 SAN BERNSAN BERNCA SOUTH CO 2/15/2000 BOILER U BOILER, CA-0942 SAN BERNSAN BERNCA SOUTH CO 2/15/2000 BOILER U BOILER, LPA-0165 PROCTER PROCTER PA PENNSYLV 2/24/2000 THIS LAT BOILERS, (CA-0944 BUMBLE BBUMBLE BCA SOUTH CO 3/10/2000 BOILER P BOILERCA-0940 NATION WNATION WCA SOUTH CO 3/15/2000 EMERGENCBOILER, CA-0947 RRR REALRRR REALCA SOUTH CO 3/15/2000 BOILER U BOILERCA-1005 COLLEGE COLLEGE CA SOUTH CO 3/16/2000 BOILER, 5CA-0945 LIBERTY LIBERTY CA SOUTH CO 3/17/2000 MANUFACTBOILERAK-0053 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0053 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HETX-0274 SOLAR GAAMERIPOLTX TEXAS CO 4/3/2000 AMERIPOLAUXILIARYCA-0943 L & N UNI L & N UNI CA SOUTH CO 4/6/2000 BOILER U BOILERMA-0027 CABOT P CABOT P MA MASSACHU 5/7/2000 COMBINEDAUXILIARYLA-0146 SHELL CHSHELL CHLA LOUISIAN 5/10/2000 SHELL CHEC15/C16 CA-0946 LACORR PLACORR PCA SOUTH CO 7/12/2000 PROVIDE BOILERCA-1100 LACORR PLACORR PCA SOUTH CO 7/12/2000 BOILER: 5WY-0056 LA LAND &LOUISIANAWY WYOMING 7/25/2000 NATURAL BOILER (AUWI-0181 CHARTER CHARTER WI WISCONSI 8/2/2000 STEEL MILBOILERWI-0181 CHARTER CHARTER WI WISCONSI 8/2/2000 STEEL MILSPACE HECA-1061 NELCO PRNELCO PRCA SOUTH CO 8/4/2000 HEATER: TX-0363 SAINT-GO VETROTEXTX TEXAS CO 11/13/2000 VETROTEXBOILER NOSC-0065 BROAD RI BROAD RI SC SOUTH CA 12/21/2000 ELECTRICHOT WATERAR-0040 DUKE ENEDUKE ENEAR ARKANSAS 12/29/2000 NATURAL BOILERS, NM-0042 DEMING EDUKE ENENM NEW MEXI 12/29/2000 THIS FAC AUX-1 AUXAR-0044 ARKANSASARKANSASAR ARKANSAS 1/5/2001 STEEL MILPREHEATERAL-0168 GENPOWERGENPOWERAL ALABAMA 1/12/2001 ELECTRICBOILERIN-0090 NUCOR STNUCOR STIN INDIANA D 1/19/2001 LADLE PRIN-0090 NUCOR STNUCOR STIN INDIANA D 1/19/2001 TUNDISH AL-0169 BLOUNT MBLOUNT CAL ALABAMA 2/5/2001 ELECTRICAUXILIARY

OH-0258 PRO TEC USS GALVAOH OHIO ENV 2/15/2001 STEEL FINBOILERS (OH-0255 PSEG WATPSEG WATOH OHIO ENV 3/29/2001 THREE 17 BOILER, OK-0074 KIAMICHI KIOWA POOK OKLAHOMA 5/1/2001 ENERGY PAUXILIARYIN-0086 MIRANT S MIRANT S IN INDIANA D 5/9/2001 AUXILARY NV-0039 CHUCK LENEVADA NV CLARK CO 6/1/2001 A NEW EL AUXILIARIN-0087 DUKE ENEDUKE ENEIN INDIANA D 6/6/2001 AUXILARY AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AL-0190 GE PLASTGE PLASTAL ALABAMA 7/13/2001 SYNTHETIFURNACE, AL-0190 GE PLASTGE PLASTAL ALABAMA 7/13/2001 SYNTHETIFURNACE, OH-0263 FREMONT CALPINE OH OHIO ENV 8/9/2001 TWO 180 AUXILIARYOK-0044 SMITH PO SMITH COOK OKLAHOMA 8/16/2001 ELEC. PO AUXILIARYOK-0054 QUAD GRAQUAD GRAOK OKLAHOMA 8/21/2001 PRINT SH BOILERSOK-0054 QUAD GRAQUAD GRAOK OKLAHOMA 8/21/2001 PRINT SH HEATERS/CA-1099 COSMETICCOSMETICCA SOUTH CO 9/4/2001 BOILER: 5CA-0903 DISNEYLADISNEYLACA SOUTH CO 9/27/2001 BOILER, MD-0033 KELSON RFREE STATMD MARYLAND 9/27/2001 FACILITY AUXILIARYAL-0179 TENASKA TENASKA AL ALABAMA 10/3/2001 NATURAL 30 MMBTUIN-0110 COGENTRICOGENTRIIN INDIANA D 10/5/2001 POWER P BOILER, AOH-0265 DRESDEN Dresden E OH OHIO ENV 10/16/2001 TWO 171.7BOILER, OK-0043 WEBERS FENERGETIOK OKLAHOMA 10/22/2001 AUXILIARYAL-0181 DUKE ENEDUKE ENEAL ALABAMA 10/23/2001 COMBINED31.4 MMB*WA-0292 SATSOP CGRAYS HAWA WASHINGT 10/23/2001 GE F7 TU AUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS 10/24/2001 ELECTRICFUEL GASOK-0071 MCCLAIN NRG MCCLOK OKLAHOMA 10/25/2001 AUXILIARYPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERALIMESTONCA-1109 SUPERIORSUPERIORCA SOUTH CO 10/30/2001 METAL HETX-0378 LA PORTEATOFINA TX TEXAS CO 11/5/2001 ATOFINA PACKAGE *OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN BOILER, *OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN DRYER, SIN-0095 ALLEGHENALLEGHENIN INDIANA D 12/7/2001 ELECTRICAUXILLIARAL-0180 DUKE ENEDUKE ENEAL ALABAMA 12/11/2001 NATURAL 35 MMBTU/AR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER EXAR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER EAR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER, *PA-0210 DART CONDART CONPA PENNSYLV 12/14/2001 NEW BOILEBOILER, (2OH-0257 JACKSON JACKSON OH OHIO ENV 12/27/2001 FOUR 305 AUXILIARYNC-0094 GENPOWERGENPOWERNC NORTH CA 1/9/2002 POWER GEBOILER, ALA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOOK-0055 MUSTANG MUSTANG OK OKLAHOMA 2/12/2002 AUXILIARYOK-0056 HORSESHMUSTANG OK OKLAHOMA 2/12/2002 POWER P AUXILIARTX-0388 SAND HIL AUSTIN ELTX TEXAS CO 2/12/2002 ELECTRICINLET AIRLA-0120 GEISMAR SHELL CHLA LOUISIAN 2/26/2002 RE-EVALUAREGENERALA-0120 GEISMAR SHELL CHLA LOUISIAN 2/26/2002 RE-EVALUASYLTHERMLA-0120 GEISMAR SHELL CHLA LOUISIAN 2/26/2002 RE-EVALUAHOT OIL FAR-0051 DUKE ENEDUKE EN AR ARKANSAS 4/1/2002 620 MW NABOILER, A

TN-0153 WILLIAMS WILLIAMS TN MEMPHIS 4/3/2002 PETROLEUBOILER, NTN-0153 WILLIAMS WILLIAMS TN MEMPHIS 4/3/2002 PETROLEUCCR STABIA-0058 GREATER MIDAMERIIA IOWA DEP 4/10/2002 AUXILIARYOK-0072 REDBUD PREDBUD EOK OKLAHOMA 5/6/2002 ELECTRICAUXILIARYOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 RECUPERAOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 FUEL SUPPOK-0070 GENOVA OGENOVA OOK OKLAHOMA 6/13/2002 COMBINEDAUXILIARYNM-0044 CLOVIS E DUKE ENENM NEW MEXI 6/27/2002 THIS IS AUXILIARYAL-0185 BARTON SBARTON SAL ALABAMA 7/12/2002 ELECTRICTWO (2) 4IA-0060 HAWKEYE ENTERGY IA IOWA DEP 7/23/2002 ENTERGY IAUXILIARYAR-0070 GENOVA AGENOVA AAR ARKANSAS 8/23/2002 COMBINEDAUXILIARYVA-0261 CPV CUNNCOMPETITVA VIRGINIA 9/6/2002 TURBINESAUXILIARYOH-0248 LAWRENCCALPINE OH OHIO ENV 9/24/2002 THREE 18 BOILERCA-1023 LA COUNTLA COUNTCA SOUTH CO 10/8/2002 BOILER, 3AL-0192 HONDA MAHONDA MAAL ALABAMA 10/18/2002 AUTOMOBIBOILERS, WI-0195 SENA NIA STORA ENWI WISCONSI 10/18/2002 PROCESS NJ-0062 CONSOLIDCONSOLIDNJ NEW JERS 10/22/2002 POWER GFUEL GAS GA-0101 MURRAY EDUKE ENEGA GEORGIA 10/23/2002 ELECTRICBOILER, AVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, AVA-0260 HENRY C Cogentrix VA VIRGINIA 11/21/2002 4 COMBINAUXILIARYTX-0408 INDIAN R INDIAN R TX TEXAS CO 11/22/2002 NATURAL AUXILIARYVA-0243 STANLEY FURNITURVA VIRGINIA 12/1/2002 WOOD HOUBOILER, NTX-0392 LUCITE B INEOS ACRTX TEXAS CO 12/9/2002 SULFURICNO.1 PRETX-0392 LUCITE B INEOS ACRTX TEXAS CO 12/9/2002 SULFURICNO. 2 PRTX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEINHEAT TRATX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEINHEAT TRATX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEIN(2) STEAMIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS GAS HEATEIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS AUXILIARYTX-0389 BAYTOWN DEGUSSA TX TEXAS CO 12/31/2002 BACK-UP WA-0291 WALLULA WALLULA WA WASHINGT 1/3/2003 WALLULA BOILER, APA-0216 J & L SPE J & L SPE PA PENNSYLV 1/13/2003 THIS PA/ BOILER, DOH-0295 GMC TRUCGENERAL OH OHIO ENV 1/14/2003 LIGHT DU NATURAL TX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHOT OIL HTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOGLYCOL RTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHOT OIL HTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHP TEG FLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRREGENERALA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRPEB RECOOR-0040 KLAMATH KLAMATH OR OREGON D 3/12/2003 POWER GEBOILER, AOK-0090 DUKE ENEDUKE EN OK OKLAHOMA 3/21/2003 MERCHANTBOILER, AGA-0098 RINCON PGENPOWERGA GEORGIA 3/24/2003 ELECTRICAUXILIARYVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOOH-0276 CHARTER CHARTER OH OHIO ENV 4/14/2003 NEW MELTBOILER FGA-0105 MCINTOSHSAVANNAHGA GEORGIA 4/17/2003 ELECTRICFUEL GASLA-0184 TITANIUM LOUISIAN LA LOUISIAN 5/13/2003 TITANIUM OXYGEN SULA-0184 TITANIUM LOUISIAN LA LOUISIAN 5/13/2003 TITANIUM TICL4 SUPLA-0184 TITANIUM LOUISIAN LA LOUISIAN 5/13/2003 TITANIUM SPRAY DRY

LA-0184 TITANIUM LOUISIAN LA LOUISIAN 5/13/2003 TITANIUM CALCINER GA-0107 TALBOT E OGLETHOGA GEORGIA 6/9/2003 ELECTRICFUEL GAS IA-0068 EMERY GEINTERSTAIA IOWA DEP 6/26/2003 IPL CHAN GAS HEATTX-0458 JACK COUDUKE ENETX TEXAS CO 7/22/2003 DUKE ENEAUXILIARYOH-0254 DUKE ENEDUKE ENEOH OHIO ENV 8/14/2003 TWO 170 BOILERAZ-0049 LA PAZ G ALLEGHENAZ ARIZONA 9/4/2003 NATURAL AUXILIARAZ-0049 LA PAZ G ALLEGHENAZ ARIZONA 9/4/2003 NATURAL AUXILIARIN-0108 NUCOR STNUCOR STIN INDIANA D 11/21/2003 STEEL MINBOILER, NMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDBOILER, OR-0039 COB ENERGPeoples EnOR OREGON D 12/30/2003 POWER GEBOILERS, WI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SAL-0191 HYUNDAI HYUNDAI AL ALABAMA 3/23/2004 AUTOMOBIBOILERS, NV-0037 COPPER SEMPRA NV CLARK CO 5/14/2004 A 600 MW AUXILIARYWV-0021 OHIO RIV CABOT COWV WEST VIR 6/9/2004 AN EXISTI BOILER, NAR-0086 NUCOR-YANUCOR-YAAR ARKANSAS 6/11/2004 VTD BOILCO-0058 CHEYENNECHEYENNECO COLORADO 6/12/2004 COMPRESSHEATERSWI-0223 LOUISIAN LOUISIAN WI WISCONSI 6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI 6/17/2004 OSB MILL THERMAL ONE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNII REHNE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNII BILEMN-0053 FAIRBAULMN MUNICMN MINNESOT 7/15/2004 LARGE COBOILER, NAR-0077 BLUEWATESTEELCORAR ARKANSAS 7/22/2004 THE FACI BOILERSWI-0226 WPS - WE WISCONSIWI WISCONSI 8/27/2004 ELECTRIC NATURAL WI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICNATURAL WI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICGAS HEATEWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAB63, S63;NV-0042 CAPITAL CAPITAL NV CLARK CO 11/5/2004 A WOOD CFUEL COMAZ-0047 WELLTON DOME VALAZ ARIZONA 12/1/2004 COMBINEDAUXILIARYOH-0252 DUKE ENEDUKE ENEOH OHIO ENV 12/28/2004 FOUR NATBOILERS (WA-0301 BP CHERRBRITISH WA WASHINGT 4/20/2005 BRITISH PROCESS LA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 FUEL GAS LA-0203 OAKDALE MARTCO LLA LOUISIAN 6/13/2005 PSD FOR AUXILIARLA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BCRACKINGMD-0035 DOMINIONDOMINION MD MARYLAND 8/12/2005 LNG FACILVAPORIZAAK-0062 BADAMI D BP EXPLOAK ALASKA D 8/19/2005 OIL AND NATCO PRAK-0062 BADAMI D BP EXPLOAK ALASKA D 8/19/2005 OIL AND NATCO MIAK-0062 BADAMI D BP EXPLOAK ALASKA D 8/19/2005 OIL AND NATCO TECA-1127 GENENTECGENENTECCA BAY AREA 9/27/2005 BOILER: >MD-0036 DOMINIONDOMINION MD MARYLAND 3/10/2006 LNG FACILFUEL GASCA-1128 COTTAGE COTTAGE CA SANTA BA 5/16/2006 BOILER: 5*NV-0046 GOODSPRIKERN RIV NV CLARK CO 5/16/2006 THE FACI COMMERCINV-0044 HARRAH'SHARRAH'SNV CLARK CO 1/4/2007 THE FACI COMMERCIOH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2*AL-0231 NUCOR DENUCOR C AL ALABAMA 6/12/2007 THE FACI GALVANIZIA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSINDIRECT

*AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CA3 NATURALMI-0301 ALCHEM AALCHEM AMI MICHIGAN 5/2/2000 SECONDARFLUESMI-0301 ALCHEM AALCHEM AMI MICHIGAN 5/2/2000 SECONDARREVERBEWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAB63, S63;MI-0301 ALCHEM AALCHEM AMI MICHIGAN 5/2/2000 SECONDARREVERBEMI-0301 ALCHEM AALCHEM AMI MICHIGAN 5/2/2000 SECONDARFLUESTX-0309 FORMOSA FORMOSA TX TEXAS CO 2/10/2000 THIS PER WASTE HEAMI-0301 ALCHEM AALCHEM AMI MICHIGAN 5/2/2000 SECONDARFLUESAK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAB63, S63;WI-0245 WPSC - W WPSC - W WI WISCONSI 6/1/2007 PROCESS WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAB63, S63;NM-0044 CLOVIS E DUKE ENENM NEW MEXI 6/27/2002 THIS IS AUXILIARYIA-0060 HAWKEYE ENTERGY IA IOWA DEP 7/23/2002 ENTERGY IAUXILIARYVA-0261 CPV CUNNCOMPETITVA VIRGINIA 9/6/2002 TURBINESAUXILIARYVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, AIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS GAS HEATEIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS AUXILIARYVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOMN-0053 FAIRBAULMN MUNICMN MINNESOT 7/15/2004 LARGE COBOILER, NMD-0036 DOMINIONDOMINION MD MARYLAND 3/10/2006 LNG FACILFUEL GASNJ-0045 MERCK - MERCK NJ NEW JERS 1/14/1997 CHEMICALBOILERS -CA-0775 CALIFORNCALIFORNCA SAN JOAQ 1/15/1997 CLAYTON CA-0802 KERN MEDKERN MEDCA SAN JOAQ 1/27/1997 PVI INDUSIN-0100 ROCKPORAK STEEL IN INDIANA D 2/13/1997 STEEL COIBOILERS (IN-0100 ROCKPORAK STEEL IN INDIANA D 2/13/1997 STEEL COIANNEALININ-0100 ROCKPORAK STEEL IN INDIANA D 2/13/1997 STEEL COIANNEALININ-0100 ROCKPORAK STEEL IN INDIANA D 2/13/1997 STEEL COIANNEALININ-0100 ROCKPORAK STEEL IN INDIANA D 2/13/1997 STEEL COIHYDROGENIN-0100 ROCKPORAK STEEL IN INDIANA D 2/13/1997 STEEL COIBOILERS (AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0019 QUINCY S QUINCY S AR ARKANSAS 3/4/1997 BOILER, IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PREIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #3IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #2IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #1IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HYDROGENIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PREKY-0068 TOYOTA MTOYOTA MKY KENTUCKY 5/29/1997 MODIFICABOILER (AL-0139 ANNISTONU.S. ARM AL ALABAMA 6/19/1997 BOILER, NAL-0140 ANNISTONU.S. ARM AL ALABAMA 6/19/1997 BOILER, NWI-0188 GOLDEN BGOLDEN BWI WISCONSI 6/24/1997 PRINTING SPACE HELA-0115 GEISMAR SHELL CHLA LOUISIAN 11/3/1997 PERMIT F HEATER, H

PA-0149 BUCKNELLBUCKNELLPA PENNSYLV 11/26/1997 HEAT RECLA-0113 BASF CORBASF CORLA LOUISIAN 12/30/1997 DUCT BURWY-0034 SOLVAY SSOLVAY SWY WYOMING 2/6/1998 BOILER, AK-0036 KUPARUK ARCO ALAAK ALASKA D 2/13/1998 PROCESS LA-0112 GEISMAR AIR LIQU LA LOUISIAN 2/13/1998 AIR SEPA BOILER NOLA-0112 GEISMAR AIR LIQU LA LOUISIAN 2/13/1998 AIR SEPA REACTIVAWY-0042 LOUISIAN LOUISIAN WY WYOMING 4/3/1998 BOILER, AMI-0283 WESTERN WESTERN MI MICHIGAN 4/27/1998 POWER P DUCT BURWY-0051 UNION PA UNION PA WY WYOMING 5/18/1998 HEATER, 2WY-0052 UNION PA UNION PA WY WYOMING 5/18/1998 HEATER, 2IA-0048 CARGILL I CARGILL I IA IOWA DEP 6/1/1998 SOYBEAN BOILER, ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, IN-0104 CON AGRACON AGRAIN INDIANA D 8/14/1998 SOYBEAN BOILERS,CA-0862 H&H HEATH&H HEATCA SOUTH CO 9/29/1998 FURNACE,TX-0300 SALT CREMOBIL EX TX TEXAS CO 10/13/1998 MOBIL EX HOT OIL HMS-0041 VICKSBURG CHEMI MS MISSISSIP 10/27/1998 BOILER, OH-0245 REPUBLICREPUBLICOH OHIO ENV 1/27/1999 STEEL MILECCENTRIAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T WASTE HENJ-0042 ROCHE VI ROCHE VITNJ NEW JERS 2/5/1999 COGENERBOILER 1 CO-0040 AMERICAN SODA, LLCO COLORADO 5/6/1999 INDUSTRICO-0041 AMERICAN SODA, LLCO COLORADO 5/6/1999 BOILER NOIN-0079 STEEL DYNSTEEL DYNIN INDIANA D 7/7/1999 DRYERS, IN-0080 STEEL DYNSTEEL DYNIN INDIANA D 7/7/1999 PREHEATECA-0917 SOUTHERNSOUTHERNCA SOUTH CO 8/17/1999 HOT OIL CA-0948 MARUCHANMARUCHANCA SOUTH CO 9/9/1999 PASTA ANBOILER, (2MA-0029 SITHE MY SITHE MY MA MASSACHU 9/29/1999 COMBINEDBOILER, AOK-0051 GREEN COCOGENTRIOK OKLAHOMA 10/1/1999 AUXILIARYCA-0923 ARAMARK ARAMARK CA SAN JOAQ 10/4/1999 FACILITY DRYER, NOK-0029 PSO NORTPUBLIC S OK OKLAHOMA 10/18/1999 ELECTRICDUCT BUCA-0929 FEDERAL FEDERAL CA SAN JOAQ 11/12/1999 GAS ABSOCA-0919 COCA COLCOCA COLCA SOUTH CO 11/23/1999 BOILER, FCA-0918 SCHI SAN SCHI SAN CA CALIFORN 12/2/1999 CLAYTON CA-0938 CHILDRENCHILDRENCA SOUTH CO 12/2/1999 BOILERS BOILER, (3CA-1021 DAMAPONGDAMAPONGCA SOUTH CO 12/7/1999 BOILER: 1CA-0939 HI-COUNTHI-COUNTCA SOUTH CO 12/16/1999 BOILER U BOILERCA-1006 HI-COUNTHI-COUNTCA SOUTH CO 12/16/1999 BOILER, 2OK-0041 MCCLAIN NRG MCCLOK OKLAHOMA 1/19/2000 POWER P AUXILIARYCA-0941 SANTA MOSANTA MOCA SOUTH CO 1/28/2000 BOILER U BOILER, TX-0309 FORMOSA FORMOSA TX TEXAS CO 2/10/2000 THIS PER WASTE HEACA-0942 SAN BERNSAN BERNCA SOUTH CO 2/15/2000 BOILER U BOILER, CA-0942 SAN BERNSAN BERNCA SOUTH CO 2/15/2000 BOILER U BOILER, LPA-0165 PROCTER PROCTER PA PENNSYLV 2/24/2000 THIS LAT BOILERS, (AL-0142 HONDA MAHONDA AL ALABAMA 2/29/2000 BOILERS,CA-0944 BUMBLE BBUMBLE BCA SOUTH CO 3/10/2000 BOILER P BOILERCA-0940 NATION WNATION WCA SOUTH CO 3/15/2000 EMERGENCBOILER, CA-0947 RRR REALRRR REALCA SOUTH CO 3/15/2000 BOILER U BOILERCA-1005 COLLEGE COLLEGE CA SOUTH CO 3/16/2000 BOILER, 5CA-0945 LIBERTY LIBERTY CA SOUTH CO 3/17/2000 MANUFACTBOILER

AK-0053 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0053 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HETX-0274 SOLAR GAAMERIPOLTX TEXAS CO 4/3/2000 AMERIPOLAUXILIARYCA-0943 L & N UNI L & N UNI CA SOUTH CO 4/6/2000 BOILER U BOILERCA-1020 MARGARETMARGARETCA SOUTH CO 5/1/2000 BOILER 4.CA-1060 COLOR AMCOLOR AMCA SOUTH CO 5/1/2000 DRYER ORMI-0301 ALCHEM AALCHEM AMI MICHIGAN 5/2/2000 SECONDARFLUESMA-0027 CABOT P CABOT P MA MASSACHU 5/7/2000 COMBINEDAUXILIARYLA-0146 SHELL CHSHELL CHLA LOUISIAN 5/10/2000 SHELL CHEC15/C16 CA-0946 LACORR PLACORR PCA SOUTH CO 7/12/2000 PROVIDE BOILERCA-1100 LACORR PLACORR PCA SOUTH CO 7/12/2000 BOILER: 5WY-0056 LA LAND &LOUISIANAWY WYOMING 7/25/2000 NATURAL BOILER (AUWI-0181 CHARTER CHARTER WI WISCONSI 8/2/2000 STEEL MILBOILERWI-0181 CHARTER CHARTER WI WISCONSI 8/2/2000 STEEL MILSPACE HECA-1061 NELCO PRNELCO PRCA SOUTH CO 8/4/2000 HEATER: AL-0217 BIRMINGHHOLCIM, I AL JEFFERSO 11/2/2000 THE PLANNATURAL TX-0363 SAINT-GO VETROTEXTX TEXAS CO 11/13/2000 VETROTEXBOILER NOSC-0065 BROAD RI BROAD RI SC SOUTH CA 12/21/2000 ELECTRICHOT WATERAR-0040 DUKE ENEDUKE ENEAR ARKANSAS 12/29/2000 NATURAL BOILERS, NM-0042 DEMING EDUKE ENENM NEW MEXI 12/29/2000 THIS FAC AUX-1 AUXAL-0178 ANNISTONUS ARMY -AL ALABAMA 1/5/2001 CHEMICALTWO (2) 1AL-0178 ANNISTONUS ARMY -AL ALABAMA 1/5/2001 CHEMICALTWO (2) 1AL-0168 GENPOWERGENPOWERAL ALABAMA 1/12/2001 ELECTRICBOILERIN-0090 NUCOR STNUCOR STIN INDIANA D 1/19/2001 LADLE PRIN-0090 NUCOR STNUCOR STIN INDIANA D 1/19/2001 TUNDISH CA-1108 INTERNATINTERNATCA SOUTH CO 1/22/2001 METAL HEAL-0169 BLOUNT MBLOUNT CAL ALABAMA 2/5/2001 ELECTRICAUXILIARYOH-0258 PRO TEC USS GALVAOH OHIO ENV 2/15/2001 STEEL FINBOILERS (OH-0255 PSEG WATPSEG WATOH OHIO ENV 3/29/2001 THREE 17 BOILER, MS-0045 NISSAN NONISSAN NOMS MISSISSIP 4/2/2001 AUTOMOBIBOILEROK-0074 KIAMICHI KIOWA POOK OKLAHOMA 5/1/2001 ENERGY PAUXILIARYIN-0086 MIRANT S MIRANT S IN INDIANA D 5/9/2001 AUXILARY OK-0046 THUNDERBTHUNDERBOK OKLAHOMA 5/17/2001 ELECTRICAUXILIARYNV-0039 CHUCK LENEVADA NV CLARK CO 6/1/2001 A NEW EL AUXILIARIN-0087 DUKE ENEDUKE ENEIN INDIANA D 6/6/2001 AUXILARY AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AL-0190 GE PLASTGE PLASTAL ALABAMA 7/13/2001 SYNTHETIFURNACE, AL-0190 GE PLASTGE PLASTAL ALABAMA 7/13/2001 SYNTHETIFURNACE, OH-0263 FREMONT CALPINE OH OHIO ENV 8/9/2001 TWO 180 AUXILIARYOK-0044 SMITH PO SMITH COOK OKLAHOMA 8/16/2001 ELEC. PO AUXILIARYOK-0054 QUAD GRAQUAD GRAOK OKLAHOMA 8/21/2001 PRINT SH BOILERSOK-0054 QUAD GRAQUAD GRAOK OKLAHOMA 8/21/2001 PRINT SH HEATERS/WV-0013 MARTINSBQuad/GraphWV WEST VIR 8/30/2001 COMPANY BOILERS, WV-0013 MARTINSBQuad/GraphWV WEST VIR 8/30/2001 COMPANY BOILERCA-1099 COSMETICCOSMETICCA SOUTH CO 9/4/2001 BOILER: 5

CA-0903 DISNEYLADISNEYLACA SOUTH CO 9/27/2001 BOILER, MD-0033 KELSON RFREE STATMD MARYLAND 9/27/2001 FACILITY AUXILIARYAL-0179 TENASKA TENASKA AL ALABAMA 10/3/2001 NATURAL 30 MMBTUIN-0110 COGENTRICOGENTRIIN INDIANA D 10/5/2001 POWER P BOILER, AOH-0265 DRESDEN Dresden E OH OHIO ENV 10/16/2001 TWO 171.7BOILER, OK-0043 WEBERS FENERGETIOK OKLAHOMA 10/22/2001 AUXILIARYAL-0181 DUKE ENEDUKE ENEAL ALABAMA 10/23/2001 COMBINED31.4 MMB*WA-0292 SATSOP CGRAYS HAWA WASHINGT 10/23/2001 GE F7 TU AUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS 10/24/2001 ELECTRICFUEL GASOK-0071 MCCLAIN NRG MCCLOK OKLAHOMA 10/25/2001 AUXILIARYCA-1101 ARAMARK ARAMARK CA SOUTH CO 10/27/2001 DRYER ORPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERALIMESTONCA-1109 SUPERIORSUPERIORCA SOUTH CO 10/30/2001 METAL HETX-0378 LA PORTEATOFINA TX TEXAS CO 11/5/2001 ATOFINA PACKAGE *OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN BOILER, *OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN DRYER, SCA-1103 NEWELLR NEWELLR CA SOUTH CO 12/7/2001 DRYER ORIN-0095 ALLEGHENALLEGHENIN INDIANA D 12/7/2001 ELECTRICAUXILLIARAL-0180 DUKE ENEDUKE ENEAL ALABAMA 12/11/2001 NATURAL 35 MMBTU/AR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER EXAR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER EAR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER, *PA-0210 DART CONDART CONPA PENNSYLV 12/14/2001 NEW BOILEBOILER, (2OH-0257 JACKSON JACKSON OH OHIO ENV 12/27/2001 FOUR 305 AUXILIARYNC-0094 GENPOWERGENPOWERNC NORTH CA 1/9/2002 POWER GEBOILER, ALA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOCA-1102 FLETCHERFLETCHERCA SOUTH CO 2/6/2002 DRYER OROK-0055 MUSTANG MUSTANG OK OKLAHOMA 2/12/2002 AUXILIARYOK-0056 HORSESHMUSTANG OK OKLAHOMA 2/12/2002 POWER P AUXILIARTX-0388 SAND HIL AUSTIN ELTX TEXAS CO 2/12/2002 ELECTRICINLET AIRLA-0120 GEISMAR SHELL CHLA LOUISIAN 2/26/2002 RE-EVALUAREGENERALA-0120 GEISMAR SHELL CHLA LOUISIAN 2/26/2002 RE-EVALUASYLTHERMLA-0120 GEISMAR SHELL CHLA LOUISIAN 2/26/2002 RE-EVALUAHOT OIL FAR-0051 DUKE ENEDUKE EN AR ARKANSAS 4/1/2002 620 MW NABOILER, ATN-0153 WILLIAMS WILLIAMS TN MEMPHIS 4/3/2002 PETROLEUBOILER, NTN-0153 WILLIAMS WILLIAMS TN MEMPHIS 4/3/2002 PETROLEUCCR STABIA-0058 GREATER MIDAMERIIA IOWA DEP 4/10/2002 AUXILIARYOK-0072 REDBUD PREDBUD EOK OKLAHOMA 5/6/2002 ELECTRICAUXILIARYOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 RECUPERAOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 FUEL SUPPOK-0070 GENOVA OGENOVA OOK OKLAHOMA 6/13/2002 COMBINEDAUXILIARYTX-0437 HARTBURGHARTBURGTX TEXAS CO 7/5/2002 LOCATED ABOILERS, AL-0185 BARTON SBARTON SAL ALABAMA 7/12/2002 ELECTRICTWO (2) 4AR-0070 GENOVA AGENOVA AAR ARKANSAS 8/23/2002 COMBINEDAUXILIARY*WA-0297 NORTHWESNORTHWESWA WASHINGT 8/30/2002 BOILEROH-0248 LAWRENCCALPINE OH OHIO ENV 9/24/2002 THREE 18 BOILERCA-1023 LA COUNTLA COUNTCA SOUTH CO 10/8/2002 BOILER, 3AL-0192 HONDA MAHONDA MAAL ALABAMA 10/18/2002 AUTOMOBIBOILERS,

WI-0195 SENA NIA STORA ENWI WISCONSI 10/18/2002 PROCESS NJ-0062 CONSOLIDCONSOLIDNJ NEW JERS 10/22/2002 POWER GFUEL GAS GA-0101 MURRAY EDUKE ENEGA GEORGIA 10/23/2002 ELECTRICBOILER, AVA-0260 HENRY C Cogentrix VA VIRGINIA 11/21/2002 4 COMBINAUXILIARYTX-0408 INDIAN R INDIAN R TX TEXAS CO 11/22/2002 NATURAL AUXILIARYVA-0243 STANLEY FURNITURVA VIRGINIA 12/1/2002 WOOD HOUBOILER, NTX-0392 LUCITE B INEOS ACRTX TEXAS CO 12/9/2002 SULFURICNO.1 PRETX-0392 LUCITE B INEOS ACRTX TEXAS CO 12/9/2002 SULFURICNO. 2 PRTX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEINHEAT TRATX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEINHEAT TRATX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEIN(2) STEAMIN-0116 PSEG LAWPSEG LAWIN INDIANA D 12/23/2002 POWER P HEATER, TX-0389 BAYTOWN DEGUSSA TX TEXAS CO 12/31/2002 BACK-UP WA-0291 WALLULA WALLULA WA WASHINGT 1/3/2003 WALLULA BOILER, APA-0216 J & L SPE J & L SPE PA PENNSYLV 1/13/2003 THIS PA/ BOILER, DOH-0295 GMC TRUCGENERAL OH OHIO ENV 1/14/2003 LIGHT DU NATURAL IA-0064 ROQUETTEROQUETTEIA IOWA DEP 1/31/2003 DEW POINTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHOT OIL HTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOGLYCOL RTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHOT OIL HTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHP TEG FIA-0063 WISDOM GCORN BELIA IOWA DEP 2/5/2003 HEATER ,OR-0040 KLAMATH KLAMATH OR OREGON D 3/12/2003 POWER GEBOILER, AOK-0090 DUKE ENEDUKE EN OK OKLAHOMA 3/21/2003 MERCHANTBOILER, AGA-0098 RINCON PGENPOWERGA GEORGIA 3/24/2003 ELECTRICAUXILIARYWA-0316 NORTHWESNORTHWESWA WASHINGT 3/27/2003 NATURAL BOILER, OH-0276 CHARTER CHARTER OH OHIO ENV 4/14/2003 NEW MELTBOILER FGA-0105 MCINTOSHSAVANNAHGA GEORGIA 4/17/2003 ELECTRICFUEL GASGA-0107 TALBOT E OGLETHOGA GEORGIA 6/9/2003 ELECTRICFUEL GAS IA-0068 EMERY GEINTERSTAIA IOWA DEP 6/26/2003 IPL CHAN GAS HEATTX-0458 JACK COUDUKE ENETX TEXAS CO 7/22/2003 DUKE ENEAUXILIARYOH-0254 DUKE ENEDUKE ENEOH OHIO ENV 8/14/2003 TWO 170 BOILERAZ-0049 LA PAZ G ALLEGHENAZ ARIZONA 9/4/2003 NATURAL AUXILIARAZ-0049 LA PAZ G ALLEGHENAZ ARIZONA 9/4/2003 NATURAL AUXILIARMI-0355 ABBOTT L ABBOTT L MI MICHIGAN 9/16/2003 NUTRITIO BOILER, GIN-0108 NUCOR STNUCOR STIN INDIANA D 11/21/2003 STEEL MINBOILER, NMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDBOILER, OR-0039 COB ENERGPeoples EnOR OREGON D 12/30/2003 POWER GEBOILERS, WI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SOK-0097 QUAD GRAQUAD GRAOK OKLAHOMA 2/3/2004 COMMERCIBOILERS,OK-0097 QUAD GRAQUAD GRAOK OKLAHOMA 2/3/2004 COMMERCIHEATERS/AR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, PAR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, HAR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, AL-0191 HYUNDAI HYUNDAI AL ALABAMA 3/23/2004 AUTOMOBIBOILERS,

ID-0015 J R SIMPL J R SIMP ID IDAHO DE 4/5/2004 THE DON SBOILER, 6NV-0037 COPPER SEMPRA NV CLARK CO 5/14/2004 A 600 MW AUXILIARYWV-0021 OHIO RIV CABOT COWV WEST VIR 6/9/2004 AN EXISTI BOILER, NCO-0058 CHEYENNECHEYENNECO COLORADO 6/12/2004 COMPRESSHEATERSWI-0223 LOUISIAN LOUISIAN WI WISCONSI 6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI 6/17/2004 OSB MILL THERMAL O*NE-0023 BEATRICENEBRASKANE NEBRASKA 6/22/2004 PERMIT TOAUXILIARYNE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNII REHNE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNII BILEAR-0077 BLUEWATESTEELCORAR ARKANSAS 7/22/2004 THE FACI BOILERSWI-0226 WPS - WE WISCONSIWI WISCONSI 8/27/2004 ELECTRIC NATURAL WI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICNATURAL WI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICGAS HEATEWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAB63, S63;NV-0042 CAPITAL CAPITAL NV CLARK CO 11/5/2004 A WOOD CFUEL COMAL-0212 HYUNDAI HYUNDAI AL ALABAMA 11/22/2004 AUTOMOBIBOILER, NAZ-0047 WELLTON DOME VALAZ ARIZONA 12/1/2004 COMBINEDAUXILIARYOH-0252 DUKE ENEDUKE ENEOH OHIO ENV 12/28/2004 FOUR NATBOILERS (WA-0301 BP CHERRBRITISH WA WASHINGT 4/20/2005 BRITISH PROCESS LA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 FUEL GAS LA-0203 OAKDALE MARTCO LLA LOUISIAN 6/13/2005 PSD FOR AUXILIARLA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BCRACKINGMD-0035 DOMINIONDOMINION MD MARYLAND 8/12/2005 LNG FACILVAPORIZAMD-0035 DOMINIONDOMINION MD MARYLAND 8/12/2005 LNG FACILEMERGENCAK-0062 BADAMI D BP EXPLOAK ALASKA D 8/19/2005 OIL AND NATCO PRAK-0062 BADAMI D BP EXPLOAK ALASKA D 8/19/2005 OIL AND NATCO TECA-1127 GENENTECGENENTECCA BAY AREA 9/27/2005 BOILER: >MD-0036 DOMINIONDOMINION MD MARYLAND 3/10/2006 LNG FACILFUEL GASCA-1128 COTTAGE COTTAGE CA SANTA BA 5/16/2006 BOILER: 5*NV-0046 GOODSPRIKERN RIV NV CLARK CO 5/16/2006 THE FACI COMMERCINV-0044 HARRAH'SHARRAH'SNV CLARK CO 1/4/2007 THE FACI COMMERCI*NC-0115 NC COMMUNICATIONNC NORTH CA 1/6/2007 DRYER OROH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2*AL-0231 NUCOR DENUCOR C AL ALABAMA 6/12/2007 THE FACI VACUUM D*AL-0231 NUCOR DENUCOR C AL ALABAMA 6/12/2007 THE FACI GALVANIZIA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSINDIRECT*AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CA3 NATURALAR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,KY-0068 TOYOTA MTOYOTA MKY KENTUCKY 5/29/1997 MODIFICABOILER (AL-0139 ANNISTONU.S. ARM AL ALABAMA 6/19/1997 BOILER, NAL-0140 ANNISTONU.S. ARM AL ALABAMA 6/19/1997 BOILER, NWI-0188 GOLDEN BGOLDEN BWI WISCONSI 6/24/1997 PRINTING SPACE HE

WY-0034 SOLVAY SSOLVAY SWY WYOMING 2/6/1998 BOILER, IA-0048 CARGILL I CARGILL I IA IOWA DEP 6/1/1998 SOYBEAN BOILER, ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, GA-0080 RAYONIERRAYONIERGA GEORGIA 11/5/1998 LUMBER MOIL HEATEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T WASTE HEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T GLYCOL REAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T GLYCOL SKAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T SPACE HEAAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T SPACE HEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T SPACE HEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T RIG BOILEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (NAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (NMA-0029 SITHE MY SITHE MY MA MASSACHU 9/29/1999 COMBINEDBOILER, ACA-0919 COCA COLCOCA COLCA SOUTH CO 11/23/1999 BOILER, FAK-0053 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0053 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HETX-0274 SOLAR GAAMERIPOLTX TEXAS CO 4/3/2000 AMERIPOLAUXILIARYMA-0027 CABOT P CABOT P MA MASSACHU 5/7/2000 COMBINEDAUXILIARYAK-0045 NORTH COPHILLIPS AK ALASKA D 6/6/2000 THIS PERMGLYCOL HEAK-0045 NORTH COPHILLIPS AK ALASKA D 6/6/2000 THIS PERMDRILLING WI-0181 CHARTER CHARTER WI WISCONSI 8/2/2000 STEEL MILBOILERWI-0181 CHARTER CHARTER WI WISCONSI 8/2/2000 STEEL MILSPACE HEMN-0039 MINNESO MINNESO MN MINNESOT 8/8/2000 WET CORNCARBON FAL-0217 BIRMINGHHOLCIM, I AL JEFFERSO 11/2/2000 THE PLANNATURAL AL-0178 ANNISTONUS ARMY -AL ALABAMA 1/5/2001 CHEMICALTWO (2) 1AL-0178 ANNISTONUS ARMY -AL ALABAMA 1/5/2001 CHEMICALTWO (2) 1SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICHOT WATEAK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (*NJ-0036 AES RED AES RED NJ NEW JERS 10/24/2001 ELECTRICFUEL GASPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERALIMESTONCA-1109 SUPERIORSUPERIORCA SOUTH CO 10/30/2001 METAL HE*OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN BOILER, *OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN DRYER, SIN-0097 CARGILL, CARGILL, IN INDIANA, 12/3/2001 GRAIN EL BOILERS 1IN-0095 ALLEGHENALLEGHENIN INDIANA D 12/7/2001 ELECTRICAUXILLIARAR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER EXAR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER EAR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER, LA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOKY-0087 QUEBECORQUEBECORKY KENTUCKY 7/12/2002 ROTOGRAVBOILER, NIA-0060 HAWKEYE ENTERGY IA IOWA DEP 7/23/2002 ENTERGY IAUXILIARYVA-0261 CPV CUNNCOMPETITVA VIRGINIA 9/6/2002 TURBINESAUXILIARYGA-0101 MURRAY EDUKE ENEGA GEORGIA 10/23/2002 ELECTRICBOILER, AVA-0243 STANLEY FURNITURVA VIRGINIA 12/1/2002 WOOD HOUBOILER, NTX-0392 LUCITE B INEOS ACRTX TEXAS CO 12/9/2002 SULFURICNO.1 PRE

IA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS GAS HEATEIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS AUXILIARYOH-0295 GMC TRUCGENERAL OH OHIO ENV 1/14/2003 LIGHT DU NATURAL IA-0064 ROQUETTEROQUETTEIA IOWA DEP 1/31/2003 DEW POINGA-0098 RINCON PGENPOWERGA GEORGIA 3/24/2003 ELECTRICAUXILIARYVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOIA-0068 EMERY GEINTERSTAIA IOWA DEP 6/26/2003 IPL CHAN GAS HEATMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDBOILER, WI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SOK-0097 QUAD GRAQUAD GRAOK OKLAHOMA 2/3/2004 COMMERCIHEATERS/WV-0021 OHIO RIV CABOT COWV WEST VIR 6/9/2004 AN EXISTI BOILER, NWI-0223 LOUISIAN LOUISIAN WI WISCONSI 6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI 6/17/2004 OSB MILL THERMAL OMN-0053 FAIRBAULMN MUNICMN MINNESOT 7/15/2004 LARGE COBOILER, NWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAB63, S63;MD-0035 DOMINIONDOMINION MD MARYLAND 8/12/2005 LNG FACILVAPORIZAOH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2*AL-0231 NUCOR DENUCOR C AL ALABAMA 6/12/2007 THE FACI VACUUM D*AL-0231 NUCOR DENUCOR C AL ALABAMA 6/12/2007 THE FACI GALVANIZIA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSINDIRECTIN-0108 NUCOR STNUCOR STIN INDIANA D 11/21/2003 STEEL MINBOILER, NIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PREIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #3IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #2IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #1IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HYDROGENIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PREWI-0188 GOLDEN BGOLDEN BWI WISCONSI 6/24/1997 PRINTING SPACE HELA-0113 BASF CORBASF CORLA LOUISIAN 12/30/1997 DUCT BURAK-0036 KUPARUK ARCO ALAAK ALASKA D 2/13/1998 PROCESS LA-0112 GEISMAR AIR LIQU LA LOUISIAN 2/13/1998 AIR SEPA BOILER NOLA-0112 GEISMAR AIR LIQU LA LOUISIAN 2/13/1998 AIR SEPA REACTIVAIA-0048 CARGILL I CARGILL I IA IOWA DEP 6/1/1998 SOYBEAN BOILER, TX-0300 SALT CREMOBIL EX TX TEXAS CO 10/13/1998 MOBIL EX HOT OIL HOH-0245 REPUBLICREPUBLICOH OHIO ENV 1/27/1999 STEEL MILECCENTRINJ-0042 ROCHE VI ROCHE VITNJ NEW JERS 2/5/1999 COGENERBOILER 1 CO-0041 AMERICAN SODA, LLCO COLORADO 5/6/1999 BOILER NOOK-0051 GREEN COCOGENTRIOK OKLAHOMA 10/1/1999 AUXILIARYOK-0075 GREEN COCOGENTRIOK OKLAHOMA 12/9/1999 TURBINESOK-0041 MCCLAIN NRG MCCLOK OKLAHOMA 1/19/2000 POWER P AUXILIARYTX-0309 FORMOSA FORMOSA TX TEXAS CO 2/10/2000 THIS PER WASTE HEAMI-0301 ALCHEM AALCHEM AMI MICHIGAN 5/2/2000 SECONDARREVERBEMI-0301 ALCHEM AALCHEM AMI MICHIGAN 5/2/2000 SECONDARFLUESLA-0146 SHELL CHSHELL CHLA LOUISIAN 5/10/2000 SHELL CHEC15/C16 MN-0039 MINNESO MINNESO MN MINNESOT 8/8/2000 WET CORNCARBON F

TX-0363 SAINT-GO VETROTEXTX TEXAS CO 11/13/2000 VETROTEXBOILER NOSC-0065 BROAD RI BROAD RI SC SOUTH CA 12/21/2000 ELECTRICHOT WATERAR-0040 DUKE ENEDUKE ENEAR ARKANSAS 12/29/2000 NATURAL BOILERS, NM-0042 DEMING EDUKE ENENM NEW MEXI 12/29/2000 THIS FAC AUX-1 AUXAR-0044 ARKANSASARKANSASAR ARKANSAS 1/5/2001 STEEL MILPREHEATERAL-0168 GENPOWERGENPOWERAL ALABAMA 1/12/2001 ELECTRICBOILERIN-0090 NUCOR STNUCOR STIN INDIANA D 1/19/2001 LADLE PRIN-0090 NUCOR STNUCOR STIN INDIANA D 1/19/2001 TUNDISH AL-0169 BLOUNT MBLOUNT CAL ALABAMA 2/5/2001 ELECTRICAUXILIARYOH-0258 PRO TEC USS GALVAOH OHIO ENV 2/15/2001 STEEL FINBOILERS (OH-0255 PSEG WATPSEG WATOH OHIO ENV 3/29/2001 THREE 17 BOILER, OK-0074 KIAMICHI KIOWA POOK OKLAHOMA 5/1/2001 ENERGY PAUXILIARYIN-0086 MIRANT S MIRANT S IN INDIANA D 5/9/2001 AUXILARY OK-0046 THUNDERBTHUNDERBOK OKLAHOMA 5/17/2001 ELECTRICAUXILIARYNV-0039 CHUCK LENEVADA NV CLARK CO 6/1/2001 A NEW EL AUXILIARIN-0087 DUKE ENEDUKE ENEIN INDIANA D 6/6/2001 AUXILARY AL-0190 GE PLASTGE PLASTAL ALABAMA 7/13/2001 SYNTHETIFURNACE, AL-0190 GE PLASTGE PLASTAL ALABAMA 7/13/2001 SYNTHETIFURNACE, OH-0263 FREMONT CALPINE OH OHIO ENV 8/9/2001 TWO 180 AUXILIARYOK-0044 SMITH PO SMITH COOK OKLAHOMA 8/16/2001 ELEC. PO AUXILIARYOK-0054 QUAD GRAQUAD GRAOK OKLAHOMA 8/21/2001 PRINT SH BOILERSOK-0054 QUAD GRAQUAD GRAOK OKLAHOMA 8/21/2001 PRINT SH HEATERS/MD-0033 KELSON RFREE STATMD MARYLAND 9/27/2001 FACILITY AUXILIARYAL-0179 TENASKA TENASKA AL ALABAMA 10/3/2001 NATURAL 30 MMBTUIN-0110 COGENTRICOGENTRIIN INDIANA D 10/5/2001 POWER P BOILER, AOH-0265 DRESDEN Dresden E OH OHIO ENV 10/16/2001 TWO 171.7BOILER, OK-0043 WEBERS FENERGETIOK OKLAHOMA 10/22/2001 AUXILIARYAL-0181 DUKE ENEDUKE ENEAL ALABAMA 10/23/2001 COMBINED31.4 MMB*WA-0292 SATSOP CGRAYS HAWA WASHINGT 10/23/2001 GE F7 TU AUXILIARYOK-0071 MCCLAIN NRG MCCLOK OKLAHOMA 10/25/2001 AUXILIARYTX-0378 LA PORTEATOFINA TX TEXAS CO 11/5/2001 ATOFINA PACKAGE IN-0097 CARGILL, CARGILL, IN INDIANA, 12/3/2001 GRAIN EL BOILERS 1AL-0180 DUKE ENEDUKE ENEAL ALABAMA 12/11/2001 NATURAL 35 MMBTU/*PA-0210 DART CONDART CONPA PENNSYLV 12/14/2001 NEW BOILEBOILER, (2OH-0257 JACKSON JACKSON OH OHIO ENV 12/27/2001 FOUR 305 AUXILIARYNC-0094 GENPOWERGENPOWERNC NORTH CA 1/9/2002 POWER GEBOILER, ALA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOOK-0056 HORSESHMUSTANG OK OKLAHOMA 2/12/2002 POWER P AUXILIARTX-0388 SAND HIL AUSTIN ELTX TEXAS CO 2/12/2002 ELECTRICINLET AIRLA-0120 GEISMAR SHELL CHLA LOUISIAN 2/26/2002 RE-EVALUAREGENERALA-0120 GEISMAR SHELL CHLA LOUISIAN 2/26/2002 RE-EVALUASYLTHERMLA-0120 GEISMAR SHELL CHLA LOUISIAN 2/26/2002 RE-EVALUAHOT OIL FAR-0051 DUKE ENEDUKE EN AR ARKANSAS 4/1/2002 620 MW NABOILER, ATN-0153 WILLIAMS WILLIAMS TN MEMPHIS 4/3/2002 PETROLEUBOILER, NTN-0153 WILLIAMS WILLIAMS TN MEMPHIS 4/3/2002 PETROLEUCCR STABIA-0058 GREATER MIDAMERIIA IOWA DEP 4/10/2002 AUXILIARYOK-0072 REDBUD PREDBUD EOK OKLAHOMA 5/6/2002 ELECTRICAUXILIARYOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 RECUPERA

OH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 FUEL SUPPOK-0070 GENOVA OGENOVA OOK OKLAHOMA 6/13/2002 COMBINEDAUXILIARYNM-0044 CLOVIS E DUKE ENENM NEW MEXI 6/27/2002 THIS IS AUXILIARYAL-0185 BARTON SBARTON SAL ALABAMA 7/12/2002 ELECTRICTWO (2) 4IA-0060 HAWKEYE ENTERGY IA IOWA DEP 7/23/2002 ENTERGY IAUXILIARYAR-0070 GENOVA AGENOVA AAR ARKANSAS 8/23/2002 COMBINEDAUXILIARYVA-0261 CPV CUNNCOMPETITVA VIRGINIA 9/6/2002 TURBINESAUXILIARYOH-0248 LAWRENCCALPINE OH OHIO ENV 9/24/2002 THREE 18 BOILERAL-0192 HONDA MAHONDA MAAL ALABAMA 10/18/2002 AUTOMOBIBOILERS, WI-0195 SENA NIA STORA ENWI WISCONSI 10/18/2002 PROCESS NJ-0062 CONSOLIDCONSOLIDNJ NEW JERS 10/22/2002 POWER GFUEL GAS VA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, ATX-0408 INDIAN R INDIAN R TX TEXAS CO 11/22/2002 NATURAL AUXILIARYVA-0243 STANLEY FURNITURVA VIRGINIA 12/1/2002 WOOD HOUBOILER, NTX-0392 LUCITE B INEOS ACRTX TEXAS CO 12/9/2002 SULFURICNO. 2 PRTX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEINHEAT TRATX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEINHEAT TRATX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEIN(2) STEAMIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS GAS HEATEIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS AUXILIARYTX-0389 BAYTOWN DEGUSSA TX TEXAS CO 12/31/2002 BACK-UP TX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHOT OIL HTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOGLYCOL RTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHOT OIL HTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHP TEG FLA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRREGENERALA-0193 STYRENE COS-MAR LA LOUISIAN 2/11/2003 PLANT PRPEB RECOOR-0040 KLAMATH KLAMATH OR OREGON D 3/12/2003 POWER GEBOILER, AOK-0090 DUKE ENEDUKE EN OK OKLAHOMA 3/21/2003 MERCHANTBOILER, AVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOOH-0276 CHARTER CHARTER OH OHIO ENV 4/14/2003 NEW MELTBOILER FIA-0068 EMERY GEINTERSTAIA IOWA DEP 6/26/2003 IPL CHAN GAS HEATTX-0458 JACK COUDUKE ENETX TEXAS CO 7/22/2003 DUKE ENEAUXILIARYOH-0254 DUKE ENEDUKE ENEOH OHIO ENV 8/14/2003 TWO 170 BOILERAZ-0049 LA PAZ G ALLEGHENAZ ARIZONA 9/4/2003 NATURAL AUXILIARAZ-0049 LA PAZ G ALLEGHENAZ ARIZONA 9/4/2003 NATURAL AUXILIARIN-0108 NUCOR STNUCOR STIN INDIANA D 11/21/2003 STEEL MINBOILER, NMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDBOILER, OK-0097 QUAD GRAQUAD GRAOK OKLAHOMA 2/3/2004 COMMERCIBOILERS,AR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, PAR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, HAR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, AL-0191 HYUNDAI HYUNDAI AL ALABAMA 3/23/2004 AUTOMOBIBOILERS, NV-0037 COPPER SEMPRA NV CLARK CO 5/14/2004 A 600 MW AUXILIARYAR-0086 NUCOR-YANUCOR-YAAR ARKANSAS 6/11/2004 VTD BOILAR-0077 BLUEWATESTEELCORAR ARKANSAS 7/22/2004 THE FACI BOILERSWI-0226 WPS - WE WISCONSIWI WISCONSI 8/27/2004 ELECTRIC NATURAL WI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICNATURAL

WI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICGAS HEATEWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAB63, S63;AZ-0047 WELLTON DOME VALAZ ARIZONA 12/1/2004 COMBINEDAUXILIARYOH-0252 DUKE ENEDUKE ENEOH OHIO ENV 12/28/2004 FOUR NATBOILERS (LA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 FUEL GAS LA-0203 OAKDALE MARTCO LLA LOUISIAN 6/13/2005 PSD FOR AUXILIARLA-0204 PLAQUEMISHINTECHLA LOUISIAN 7/27/2005 NEW 1.3 BCRACKINGMD-0036 DOMINIONDOMINION MD MARYLAND 3/10/2006 LNG FACILFUEL GAS*NV-0046 GOODSPRIKERN RIV NV CLARK CO 5/16/2006 THE FACI COMMERCINV-0044 HARRAH'SHARRAH'SNV CLARK CO 1/4/2007 THE FACI COMMERCIOH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2IA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSINDIRECT*AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CA3 NATURAL*NE-0043 NATUREWORKS, LL NE NEBRASKA 10/1/2007 POLYMER HOT OIL NJ-0045 MERCK - MERCK NJ NEW JERS 1/14/1997 CHEMICALBOILERS -AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PREIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #1IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HYDROGENKY-0068 TOYOTA MTOYOTA MKY KENTUCKY 5/29/1997 MODIFICABOILER (AL-0139 ANNISTONU.S. ARM AL ALABAMA 6/19/1997 BOILER, NAL-0140 ANNISTONU.S. ARM AL ALABAMA 6/19/1997 BOILER, NWI-0188 GOLDEN BGOLDEN BWI WISCONSI 6/24/1997 PRINTING SPACE HEAK-0036 KUPARUK ARCO ALAAK ALASKA D 2/13/1998 PROCESS TX-0300 SALT CREMOBIL EX TX TEXAS CO 10/13/1998 MOBIL EX HOT OIL HAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T WASTE HEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T GLYCOL REAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T GLYCOL SKAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T SPACE HEAAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T SPACE HEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T SPACE HEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T RIG BOILEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (NAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (NNJ-0042 ROCHE VI ROCHE VITNJ NEW JERS 2/5/1999 COGENERBOILER 1 MA-0029 SITHE MY SITHE MY MA MASSACHU 9/29/1999 COMBINEDBOILER, AOK-0051 GREEN COCOGENTRIOK OKLAHOMA 10/1/1999 AUXILIARYTX-0309 FORMOSA FORMOSA TX TEXAS CO 2/10/2000 THIS PER WASTE HEAAK-0053 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0053 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HETX-0274 SOLAR GAAMERIPOLTX TEXAS CO 4/3/2000 AMERIPOLAUXILIARYMI-0301 ALCHEM AALCHEM AMI MICHIGAN 5/2/2000 SECONDARFLUESMA-0027 CABOT P CABOT P MA MASSACHU 5/7/2000 COMBINEDAUXILIARY

AK-0045 NORTH COPHILLIPS AK ALASKA D 6/6/2000 THIS PERMGLYCOL HEAK-0045 NORTH COPHILLIPS AK ALASKA D 6/6/2000 THIS PERMDRILLING TX-0363 SAINT-GO VETROTEXTX TEXAS CO 11/13/2000 VETROTEXBOILER NOSC-0065 BROAD RI BROAD RI SC SOUTH CA 12/21/2000 ELECTRICHOT WATERAR-0040 DUKE ENEDUKE ENEAR ARKANSAS 12/29/2000 NATURAL BOILERS, AL-0168 GENPOWERGENPOWERAL ALABAMA 1/12/2001 ELECTRICBOILERIN-0090 NUCOR STNUCOR STIN INDIANA D 1/19/2001 LADLE PRAL-0169 BLOUNT MBLOUNT CAL ALABAMA 2/5/2001 ELECTRICAUXILIARYOH-0255 PSEG WATPSEG WATOH OHIO ENV 3/29/2001 THREE 17 BOILER, SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICHOT WATEIN-0086 MIRANT S MIRANT S IN INDIANA D 5/9/2001 AUXILARY NV-0039 CHUCK LENEVADA NV CLARK CO 6/1/2001 A NEW EL AUXILIARIN-0087 DUKE ENEDUKE ENEIN INDIANA D 6/6/2001 AUXILARY AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AL-0190 GE PLASTGE PLASTAL ALABAMA 7/13/2001 SYNTHETIFURNACE, AL-0190 GE PLASTGE PLASTAL ALABAMA 7/13/2001 SYNTHETIFURNACE, OH-0263 FREMONT CALPINE OH OHIO ENV 8/9/2001 TWO 180 AUXILIARYOK-0044 SMITH PO SMITH COOK OKLAHOMA 8/16/2001 ELEC. PO AUXILIARYIN-0110 COGENTRICOGENTRIIN INDIANA D 10/5/2001 POWER P BOILER, AOH-0265 DRESDEN Dresden E OH OHIO ENV 10/16/2001 TWO 171.7BOILER, OK-0043 WEBERS FENERGETIOK OKLAHOMA 10/22/2001 AUXILIARYAL-0181 DUKE ENEDUKE ENEAL ALABAMA 10/23/2001 COMBINED31.4 MMB*WA-0292 SATSOP CGRAYS HAWA WASHINGT 10/23/2001 GE F7 TU AUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS 10/24/2001 ELECTRICFUEL GASOK-0071 MCCLAIN NRG MCCLOK OKLAHOMA 10/25/2001 AUXILIARYPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERALIMESTONTX-0378 LA PORTEATOFINA TX TEXAS CO 11/5/2001 ATOFINA PACKAGE *OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN BOILER, *OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN DRYER, SIN-0095 ALLEGHENALLEGHENIN INDIANA D 12/7/2001 ELECTRICAUXILLIARAL-0180 DUKE ENEDUKE ENEAL ALABAMA 12/11/2001 NATURAL 35 MMBTU/OH-0257 JACKSON JACKSON OH OHIO ENV 12/27/2001 FOUR 305 AUXILIARYLA-0174 PORT HUDGEORGIA-LA LOUISIAN 1/25/2002 PULP MILLPOWER BOTX-0388 SAND HIL AUSTIN ELTX TEXAS CO 2/12/2002 ELECTRICINLET AIRAR-0051 DUKE ENEDUKE EN AR ARKANSAS 4/1/2002 620 MW NABOILER, AOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 RECUPERAOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 FUEL SUPPNM-0044 CLOVIS E DUKE ENENM NEW MEXI 6/27/2002 THIS IS AUXILIARYKY-0087 QUEBECORQUEBECORKY KENTUCKY 7/12/2002 ROTOGRAVBOILER, NOH-0248 LAWRENCCALPINE OH OHIO ENV 9/24/2002 THREE 18 BOILERWI-0195 SENA NIA STORA ENWI WISCONSI 10/18/2002 PROCESS NJ-0062 CONSOLIDCONSOLIDNJ NEW JERS 10/22/2002 POWER GFUEL GAS VA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, ATX-0408 INDIAN R INDIAN R TX TEXAS CO 11/22/2002 NATURAL AUXILIARYVA-0243 STANLEY FURNITURVA VIRGINIA 12/1/2002 WOOD HOUBOILER, NTX-0392 LUCITE B INEOS ACRTX TEXAS CO 12/9/2002 SULFURICNO.1 PRE

TX-0392 LUCITE B INEOS ACRTX TEXAS CO 12/9/2002 SULFURICNO. 2 PRTX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEINHEAT TRATX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEINHEAT TRATX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEIN(2) STEAMIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS GAS HEATEIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS AUXILIARYTX-0389 BAYTOWN DEGUSSA TX TEXAS CO 12/31/2002 BACK-UP VA-0279 CINCAP - Cinergy CapVA VIRGINIA 1/8/2003 POWER P HEATER, TX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHOT OIL HTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOGLYCOL RTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHOT OIL HTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHP TEG FOK-0090 DUKE ENEDUKE EN OK OKLAHOMA 3/21/2003 MERCHANTBOILER, AVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOOH-0276 CHARTER CHARTER OH OHIO ENV 4/14/2003 NEW MELTBOILER FIA-0068 EMERY GEINTERSTAIA IOWA DEP 6/26/2003 IPL CHAN GAS HEATTX-0458 JACK COUDUKE ENETX TEXAS CO 7/22/2003 DUKE ENEAUXILIARYOH-0254 DUKE ENEDUKE ENEOH OHIO ENV 8/14/2003 TWO 170 BOILERAZ-0049 LA PAZ G ALLEGHENAZ ARIZONA 9/4/2003 NATURAL AUXILIARAZ-0049 LA PAZ G ALLEGHENAZ ARIZONA 9/4/2003 NATURAL AUXILIARIN-0108 NUCOR STNUCOR STIN INDIANA D 11/21/2003 STEEL MINBOILER, NMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDBOILER, AR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, PAR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, HAR-0076 U.S. ARMYU.S. ARMYAR ARKANSAS 2/17/2004 PINE BLU BOILER, NV-0037 COPPER SEMPRA NV CLARK CO 5/14/2004 A 600 MW AUXILIARYAR-0086 NUCOR-YANUCOR-YAAR ARKANSAS 6/11/2004 VTD BOILNE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNII REHNE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNII BILEMN-0053 FAIRBAULMN MUNICMN MINNESOT 7/15/2004 LARGE COBOILER, NAR-0077 BLUEWATESTEELCORAR ARKANSAS 7/22/2004 THE FACI BOILERSWI-0226 WPS - WE WISCONSIWI WISCONSI 8/27/2004 ELECTRIC NATURAL WI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICNATURAL WI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICGAS HEATEWI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAB63, S63;AZ-0047 WELLTON DOME VALAZ ARIZONA 12/1/2004 COMBINEDAUXILIARYOH-0252 DUKE ENEDUKE ENEOH OHIO ENV 12/28/2004 FOUR NATBOILERS (LA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 FUEL GAS LA-0203 OAKDALE MARTCO LLA LOUISIAN 6/13/2005 PSD FOR AUXILIARAK-0062 BADAMI D BP EXPLOAK ALASKA D 8/19/2005 OIL AND NATCO PRAK-0062 BADAMI D BP EXPLOAK ALASKA D 8/19/2005 OIL AND NATCO MIAK-0062 BADAMI D BP EXPLOAK ALASKA D 8/19/2005 OIL AND NATCO TE*NV-0046 GOODSPRIKERN RIV NV CLARK CO 5/16/2006 THE FACI COMMERCIOH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2*AL-0231 NUCOR DENUCOR C AL ALABAMA 6/12/2007 THE FACI VACUUM D*AL-0231 NUCOR DENUCOR C AL ALABAMA 6/12/2007 THE FACI GALVANIZIA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSINDIRECT*AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL

*AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CA3 NATURALCA-0919 COCA COLCOCA COLCA SOUTH CO 11/23/1999 BOILER, FIN-0090 NUCOR STNUCOR STIN INDIANA D 1/19/2001 TUNDISH OK-0074 KIAMICHI KIOWA POOK OKLAHOMA 5/1/2001 ENERGY PAUXILIARY*PA-0210 DART CONDART CONPA PENNSYLV 12/14/2001 NEW BOILEBOILER, (2NV-0044 HARRAH'SHARRAH'SNV CLARK CO 1/4/2007 THE FACI COMMERCIWI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICNATURAL MN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDBOILER, WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAB63, S63;NJ-0045 MERCK - MERCK NJ NEW JERS 1/14/1997 CHEMICALBOILERS -IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PREIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #3IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #2IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #1IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HYDROGENIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PRENJ-0062 CONSOLIDCONSOLIDNJ NEW JERS 10/22/2002 POWER GFUEL GAS KY-0068 TOYOTA MTOYOTA MKY KENTUCKY 5/29/1997 MODIFICABOILER (AK-0036 KUPARUK ARCO ALAAK ALASKA D 2/13/1998 PROCESS ND-0018 ARCHER DARCHER DND NORTH DA 7/9/1998 VEGETABLBOILER, GA-0080 RAYONIERRAYONIERGA GEORGIA 11/5/1998 LUMBER MOIL HEATEOH-0245 REPUBLICREPUBLICOH OHIO ENV 1/27/1999 STEEL MILECCENTRIAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T WASTE HEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T GLYCOL REAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T GLYCOL SKAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T SPACE HEAAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T SPACE HEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T SPACE HEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T RIG BOILEAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (NAK-0038 NORTHSTABP EXPLOAK ALASKA D 2/5/1999 PERMIT T HEATER (NAK-0053 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0053 KENAI RE TESORO AAK ALASKA D 3/21/2000 THIS PER CRUDE HEAK-0045 NORTH COPHILLIPS AK ALASKA D 6/6/2000 THIS PERMGLYCOL HEAK-0045 NORTH COPHILLIPS AK ALASKA D 6/6/2000 THIS PERMDRILLING WI-0181 CHARTER CHARTER WI WISCONSI 8/2/2000 STEEL MILSPACE HETX-0363 SAINT-GO VETROTEXTX TEXAS CO 11/13/2000 VETROTEXBOILER NOSC-0065 BROAD RI BROAD RI SC SOUTH CA 12/21/2000 ELECTRICHOT WATEROH-0258 PRO TEC USS GALVAOH OHIO ENV 2/15/2001 STEEL FINBOILERS (OH-0255 PSEG WATPSEG WATOH OHIO ENV 3/29/2001 THREE 17 BOILER, SC-0061 COLUMBIACOLUMBIASC SOUTH CA 4/9/2001 ELECTRICHOT WATEAK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (AK-0047 MILNE PO BP EXPLORAK ALASKA D 7/13/2001 NATURAL HEATERS (OH-0263 FREMONT CALPINE OH OHIO ENV 8/9/2001 TWO 180 AUXILIARYIN-0110 COGENTRICOGENTRIIN INDIANA D 10/5/2001 POWER P BOILER, A

OH-0265 DRESDEN Dresden E OH OHIO ENV 10/16/2001 TWO 171.7BOILER, PR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERALIMESTONTX-0378 LA PORTEATOFINA TX TEXAS CO 11/5/2001 ATOFINA PACKAGE *OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN BOILER, MS-0058 CHOCTAW CHOCTAW MS MISSISSIP 12/13/2001 POWER PLHEATER, OH-0257 JACKSON JACKSON OH OHIO ENV 12/27/2001 FOUR 305 AUXILIARYIA-0058 GREATER MIDAMERIIA IOWA DEP 4/10/2002 AUXILIARYOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 RECUPERAOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 FUEL SUPPKY-0087 QUEBECORQUEBECORKY KENTUCKY 7/12/2002 ROTOGRAVBOILER, NAL-0192 HONDA MAHONDA MAAL ALABAMA 10/18/2002 AUTOMOBIBOILERS, WI-0195 SENA NIA STORA ENWI WISCONSI 10/18/2002 PROCESS GA-0101 MURRAY EDUKE ENEGA GEORGIA 10/23/2002 ELECTRICBOILER, AIN-0116 PSEG LAWPSEG LAWIN INDIANA D 12/23/2002 POWER P HEATER, WA-0291 WALLULA WALLULA WA WASHINGT 1/3/2003 WALLULA BOILER, AGA-0098 RINCON PGENPOWERGA GEORGIA 3/24/2003 ELECTRICAUXILIARYOH-0276 CHARTER CHARTER OH OHIO ENV 4/14/2003 NEW MELTBOILER FMS-0057 SMEPA - SOUTH MIMS MISSISSIP 5/29/2003 POWER PLBOILERS, OH-0254 DUKE ENEDUKE ENEOH OHIO ENV 8/14/2003 TWO 170 BOILERAZ-0047 WELLTON DOME VALAZ ARIZONA 12/1/2004 COMBINEDAUXILIARYOH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2IA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSINDIRECTNJ-0045 MERCK - MERCK NJ NEW JERS 1/14/1997 CHEMICALBOILERS -AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,AR-0020 GEORGIA-GEORGIA-AR ARKANSAS 2/28/1997 BURNERS,IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PREIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #3IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #2IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN BOILER #1IA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HYDROGENIA-0054 BUNGE C BUNGE C IA IOWA DEP 5/20/1997 SOYBEAN HIGH PREWI-0188 GOLDEN BGOLDEN BWI WISCONSI 6/24/1997 PRINTING SPACE HETX-0300 SALT CREMOBIL EX TX TEXAS CO 10/13/1998 MOBIL EX HOT OIL HNJ-0042 ROCHE VI ROCHE VITNJ NEW JERS 2/5/1999 COGENERBOILER 1 MA-0029 SITHE MY SITHE MY MA MASSACHU 9/29/1999 COMBINEDBOILER, AOK-0051 GREEN COCOGENTRIOK OKLAHOMA 10/1/1999 AUXILIARYCA-0923 ARAMARK ARAMARK CA SAN JOAQ 10/4/1999 FACILITY DRYER, NCA-0919 COCA COLCOCA COLCA SOUTH CO 11/23/1999 BOILER, FOK-0041 MCCLAIN NRG MCCLOK OKLAHOMA 1/19/2000 POWER P AUXILIARYTX-0309 FORMOSA FORMOSA TX TEXAS CO 2/10/2000 THIS PER WASTE HEATX-0309 FORMOSA FORMOSA TX TEXAS CO 2/10/2000 THIS PER WASTE HEATX-0274 SOLAR GAAMERIPOLTX TEXAS CO 4/3/2000 AMERIPOLAUXILIARYMI-0301 ALCHEM AALCHEM AMI MICHIGAN 5/2/2000 SECONDARFLUESMA-0027 CABOT P CABOT P MA MASSACHU 5/7/2000 COMBINEDAUXILIARYWI-0181 CHARTER CHARTER WI WISCONSI 8/2/2000 STEEL MILBOILERWI-0181 CHARTER CHARTER WI WISCONSI 8/2/2000 STEEL MILSPACE HETX-0363 SAINT-GO VETROTEXTX TEXAS CO 11/13/2000 VETROTEXBOILER NO

AR-0040 DUKE ENEDUKE ENEAR ARKANSAS 12/29/2000 NATURAL BOILERS, NM-0042 DEMING EDUKE ENENM NEW MEXI 12/29/2000 THIS FAC AUX-1 AUXAL-0168 GENPOWERGENPOWERAL ALABAMA 1/12/2001 ELECTRICBOILERAL-0169 BLOUNT MBLOUNT CAL ALABAMA 2/5/2001 ELECTRICAUXILIARYOH-0258 PRO TEC USS GALVAOH OHIO ENV 2/15/2001 STEEL FINBOILERS (OH-0255 PSEG WATPSEG WATOH OHIO ENV 3/29/2001 THREE 17 BOILER, OK-0074 KIAMICHI KIOWA POOK OKLAHOMA 5/1/2001 ENERGY PAUXILIARYIN-0086 MIRANT S MIRANT S IN INDIANA D 5/9/2001 AUXILARY OK-0046 THUNDERBTHUNDERBOK OKLAHOMA 5/17/2001 ELECTRICAUXILIARYNV-0039 CHUCK LENEVADA NV CLARK CO 6/1/2001 A NEW EL AUXILIARIN-0087 DUKE ENEDUKE ENEIN INDIANA D 6/6/2001 AUXILARY AL-0190 GE PLASTGE PLASTAL ALABAMA 7/13/2001 SYNTHETIFURNACE, AL-0190 GE PLASTGE PLASTAL ALABAMA 7/13/2001 SYNTHETIFURNACE, OH-0263 FREMONT CALPINE OH OHIO ENV 8/9/2001 TWO 180 AUXILIARYOK-0044 SMITH PO SMITH COOK OKLAHOMA 8/16/2001 ELEC. PO AUXILIARYOK-0054 QUAD GRAQUAD GRAOK OKLAHOMA 8/21/2001 PRINT SH BOILERSMD-0033 KELSON RFREE STATMD MARYLAND 9/27/2001 FACILITY AUXILIARYAL-0179 TENASKA TENASKA AL ALABAMA 10/3/2001 NATURAL 30 MMBTUIN-0110 COGENTRICOGENTRIIN INDIANA D 10/5/2001 POWER P BOILER, AOH-0265 DRESDEN Dresden E OH OHIO ENV 10/16/2001 TWO 171.7BOILER, OK-0043 WEBERS FENERGETIOK OKLAHOMA 10/22/2001 AUXILIARYAL-0181 DUKE ENEDUKE ENEAL ALABAMA 10/23/2001 COMBINED31.4 MMB*WA-0292 SATSOP CGRAYS HAWA WASHINGT 10/23/2001 GE F7 TU AUXILIARY*NJ-0036 AES RED AES RED NJ NEW JERS 10/24/2001 ELECTRICFUEL GASPR-0007 COGENERAAES PUERPR PUERTO R 10/29/2001 COGENERALIMESTONTX-0378 LA PORTEATOFINA TX TEXAS CO 11/5/2001 ATOFINA PACKAGE *OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN BOILER, *OH-0251 CENTRAL CENTRAL OH OHIO ENV 11/29/2001 SOYBEAN DRYER, SIN-0095 ALLEGHENALLEGHENIN INDIANA D 12/7/2001 ELECTRICAUXILLIARAL-0180 DUKE ENEDUKE ENEAL ALABAMA 12/11/2001 NATURAL 35 MMBTU/AR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER EXAR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER EAR-0049 GEORGIA GEORGIA AR ARKANSAS 12/14/2001 KRAFT PAPBURNER, OH-0257 JACKSON JACKSON OH OHIO ENV 12/27/2001 FOUR 305 AUXILIARYNC-0094 GENPOWERGENPOWERNC NORTH CA 1/9/2002 POWER GEBOILER, ACA-1102 FLETCHERFLETCHERCA SOUTH CO 2/6/2002 DRYER OROK-0055 MUSTANG MUSTANG OK OKLAHOMA 2/12/2002 AUXILIARYOK-0056 HORSESHMUSTANG OK OKLAHOMA 2/12/2002 POWER P AUXILIARTX-0388 SAND HIL AUSTIN ELTX TEXAS CO 2/12/2002 ELECTRICINLET AIRAR-0051 DUKE ENEDUKE EN AR ARKANSAS 4/1/2002 620 MW NABOILER, AOK-0072 REDBUD PREDBUD EOK OKLAHOMA 5/6/2002 ELECTRICAUXILIARYOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 RECUPERAOH-0264 NORTON ENORTON OH OHIO ENV 5/23/2002 NINE 300 FUEL SUPPOK-0070 GENOVA OGENOVA OOK OKLAHOMA 6/13/2002 COMBINEDAUXILIARYNM-0044 CLOVIS E DUKE ENENM NEW MEXI 6/27/2002 THIS IS AUXILIARYTX-0437 HARTBURGHARTBURGTX TEXAS CO 7/5/2002 LOCATED ABOILERS, AL-0185 BARTON SBARTON SAL ALABAMA 7/12/2002 ELECTRICTWO (2) 4IA-0060 HAWKEYE ENTERGY IA IOWA DEP 7/23/2002 ENTERGY IAUXILIARY

AR-0070 GENOVA AGENOVA AAR ARKANSAS 8/23/2002 COMBINEDAUXILIARYVA-0261 CPV CUNNCOMPETITVA VIRGINIA 9/6/2002 TURBINESAUXILIARYOH-0248 LAWRENCCALPINE OH OHIO ENV 9/24/2002 THREE 18 BOILERWI-0195 SENA NIA STORA ENWI WISCONSI 10/18/2002 PROCESS NJ-0062 CONSOLIDCONSOLIDNJ NEW JERS 10/22/2002 POWER GFUEL GAS GA-0101 MURRAY EDUKE ENEGA GEORGIA 10/23/2002 ELECTRICBOILER, AVA-0255 VA POWERVirginia Po VA VIRGINIA 11/18/2002 THIE PER BOILER, ATX-0408 INDIAN R INDIAN R TX TEXAS CO 11/22/2002 NATURAL AUXILIARYTX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEINHEAT TRATX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEINHEAT TRATX-0354 ATOFINA ATOFINA TX TEXAS CO 12/19/2002 ACROLEIN(2) STEAMIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS GAS HEATEIA-0062 EMERY GEINTERSTATIA IOWA DEP 12/20/2002 PERMITS AUXILIARYTX-0389 BAYTOWN DEGUSSA TX TEXAS CO 12/31/2002 BACK-UP OH-0295 GMC TRUCGENERAL OH OHIO ENV 1/14/2003 LIGHT DU NATURAL TX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHOT OIL HTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOGLYCOL RTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHOT OIL HTX-0364 SALT CREEXXON MOTX TEXAS CO 1/31/2003 EXXON MOHP TEG FLA-0199 NORCO CHSHELL CHLA LOUISIAN 3/21/2003 UNIT MAN DEHYDROGOK-0090 DUKE ENEDUKE EN OK OKLAHOMA 3/21/2003 MERCHANTBOILER, AGA-0098 RINCON PGENPOWERGA GEORGIA 3/24/2003 ELECTRICAUXILIARYVA-0271 HARRISONCITY OF VA VIRGINIA 3/24/2003 BOILER NOOH-0276 CHARTER CHARTER OH OHIO ENV 4/14/2003 NEW MELTBOILER FIA-0068 EMERY GEINTERSTAIA IOWA DEP 6/26/2003 IPL CHAN GAS HEATTX-0458 JACK COUDUKE ENETX TEXAS CO 7/22/2003 DUKE ENEAUXILIARYOH-0254 DUKE ENEDUKE ENEOH OHIO ENV 8/14/2003 TWO 170 BOILERAZ-0049 LA PAZ G ALLEGHENAZ ARIZONA 9/4/2003 NATURAL AUXILIARAZ-0049 LA PAZ G ALLEGHENAZ ARIZONA 9/4/2003 NATURAL AUXILIARLA-0185 WEST MONGRAPHIC LA LOUISIAN 11/5/2003 FACILITY DRYER BURIN-0108 NUCOR STNUCOR STIN INDIANA D 11/21/2003 STEEL MINBOILER, NMN-0054 MANKATO ENERGY MN MINNESOT 12/4/2003 COMBINEDBOILER, WI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SWI-0207 ACE ETHAACE ETHAWI WISCONSI 1/21/2004 BOILER, SOK-0097 QUAD GRAQUAD GRAOK OKLAHOMA 2/3/2004 COMMERCIBOILERS,NV-0037 COPPER SEMPRA NV CLARK CO 5/14/2004 A 600 MW AUXILIARYCO-0058 CHEYENNECHEYENNECO COLORADO 6/12/2004 COMPRESSHEATERSWI-0223 LOUISIAN LOUISIAN WI WISCONSI 6/17/2004 OSB MILL THERMAL OWI-0223 LOUISIAN LOUISIAN WI WISCONSI 6/17/2004 OSB MILL THERMAL ONE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNII REHNE-0026 NUCOR STNUCOR STNE NEBRASKA 6/22/2004 NNII BILEMN-0053 FAIRBAULMN MUNICMN MINNESOT 7/15/2004 LARGE COBOILER, NAR-0077 BLUEWATESTEELCORAR ARKANSAS 7/22/2004 THE FACI BOILERSLA-0186 WEST MONGRAPHIC LA LOUISIAN 9/14/2004 FACILITY DRYER BURWI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICNATURAL WI-0227 PORT WASWE ENERGWI WISCONSI 10/13/2004 ELECTRICGAS HEATE

WI-0228 WPS - WE WISCONSIWI WISCONSI 10/19/2004 ELECTRICAB63, S63;AZ-0047 WELLTON DOME VALAZ ARIZONA 12/1/2004 COMBINEDAUXILIARYOK-0108 NOMACO ONOMACO IOK OKLAHOMA 12/3/2004 POLYETHYCOMBUSIOOH-0252 DUKE ENEDUKE ENEOH OHIO ENV 12/28/2004 FOUR NATBOILERS (LA-0192 CRESCENTCRESENT LA LOUISIAN 6/6/2005 NEW 600 FUEL GAS LA-0203 OAKDALE MARTCO LLA LOUISIAN 6/13/2005 PSD FOR AUXILIARMD-0035 DOMINIONDOMINION MD MARYLAND 8/12/2005 LNG FACILVAPORIZAMD-0035 DOMINIONDOMINION MD MARYLAND 8/12/2005 LNG FACILEMERGENCMD-0036 DOMINIONDOMINION MD MARYLAND 3/10/2006 LNG FACILFUEL GAS*NV-0046 GOODSPRIKERN RIV NV CLARK CO 5/16/2006 THE FACI COMMERCINV-0044 HARRAH'SHARRAH'SNV CLARK CO 1/4/2007 THE FACI COMMERCIMS-0085 DART CONDART CONMS MISSISSIP 1/31/2007 EPS CONTNATURAL OH-0309 TOLEDO SDAIMLER OH OHIO ENV 5/3/2007 THIS IS BOILER (2*AL-0231 NUCOR DENUCOR C AL ALABAMA 6/12/2007 THE FACI VACUUM D*AL-0231 NUCOR DENUCOR C AL ALABAMA 6/12/2007 THE FACI GALVANIZIA-0088 ADM CORNARCHER DIA IOWA DEP 6/29/2007 CONSISTSINDIRECT*AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CANATURAL *AL-0230 THYSSENKTHYSSENKAL ALABAMA 8/17/2007 A NEW CA3 NATURAL

PROCTYPEFUEL THRUPUT THRUPUTUPROCESSPOLLUTANCONTROLCTRLDESC13.3 NATURAL GAS 1.8 MMBTU/H Carbon MoN NATURAL 13.3 NATURAL GAS MULTIPLENitrogen O N13.3 NATURAL GAS 1.8 MMBTU/H Nitrogen O N NATURAL 13.3 NATURAL GAS 10 MMBTU/H Limit requi Particulate P BACT FOR13.3 NATURAL GAS 1.8 MMBTU/H Particulate N NATURAL 13.3 NATURAL GAS MULTIPLEParticulate P LOW SULFUR REFINERY FUEL13.3 NATURAL GAS MULTIPLESulfur DioxP LOW SULFUR REFINERY GAS 13.3 NATURAL GAS 10 MMBTU/H Limit requi Visible EmiP BACT FOR13.3 NATURAL GAS 1.8 MMBTU/H Volatile O N NATURAL

13.31 NATURAL GAS 328 MMBTU/H The emissio Combined CNitrogen O P13.31 NATURAL GAS 328 MMBTU/H The emissio Combined CCarbon MoP13.31 NATURAL GAS 328 MMBTU/H The emissio Combined CSulfur DioxP13.31 NATURAL GAS 328 MMBTU/H The emissio Combined CParticulate P13.31 NATURAL GAS 328 MMBTU/H The emissio Combined CVolatile O P13.31 NATURAL GAS 328 MMBTU/H The emissio Combined CSulfuric AciP13.31 NAT GAS SHALL BE Acrylonitril N NONE IND13.31 NATURAL GAS 96 MMBTU/H Ammonia ( A VAPOR TREATMENT SYSTEM. NO EMISSION RATE LIMITS PROVIDED.13.31 NATURAL GAS 31.5 MMBTU/H ARB RECORAmmonia ( N NO CONT13.31 NATURAL GAS 33.9 MMBTU/H 3 boilers, Ammonia ( P SCR STOI13.31 NATURAL GAS 16.5 MMBTU/H EQUIP: NAAmmonia ( N13.31 NAT GAS SHALL BE Ammonia ( N NONE IND13.31 NATURAL GAS 21 MMBTU/H CLEAVER Ammonia ( P SCR STOI13.31 NATURAL GAS 0.03 MMDSCF/ THROUGH Beryllium P NATURAL 13.31 NATURAL GAS 0.01 MMDSCF/ ADDITION Beryllium P NATURAL 13.31 NATURAL GAS 95 MMBTU/H Carbon DioN13.31 Carbon DioP GOOD COMBUSTION PRACTICES13.31 NATURAL GAS 99.5 MMBTU/H Carbon MoN NONE13.31 NATURAL GAS 50 MMBTU/H THE NUMBCarbon MoP GOOD COM13.31 NATURAL GAS 21 MMBTU/H THE BURNCarbon MoP GOOD COM13.31 NATURAL GAS 58.4 MMBTU/H THE BURNCarbon MoP GOOD COM13.31 NATURAL GAS 68 MMBTU/H TURBINE Carbon MoP GOOD COM13.31 FUEL OIL 0.3 MMBTU/H PERMIT NOCarbon MoP LOW NOX/13.31 NATURAL GAS 2.3 MMBTU/H BOILER BUCarbon MoP LOW NOX 13.31 NATURAL GAS 2.3 MMBTU/H 20% OPACICarbon MoP LOW NOX 13.31 NATURAL GAS 2.3 MMBTU/H FUEL IS N Carbon MoP LOW NOX 13.31 PERMIT N Carbon MoN13.31 NATURAL GAS 0.3 MMBTU/H FUELS ARECarbon MoN13.31 NATURAL GAS 93 MMBTU/H SECOND FCarbon MoN REGULATO13.31 NATURAL GAS 54.9 MMBTU/H Carbon MoP PROPER O13.31 NG SUPPLEME 24000 LB/HR ST COMPLIANCarbon MoN13.31 NATURAL GAS 0.4 MMLB/H STEAM Carbon MoP GOOD DES13.31 NATURAL GAS 95 MMBTU/H Carbon MoP GOOD DES13.31 9 MMBTU/H THROUGHPCarbon MoN13.31 NATURAL GAS 85 MMBTU/H THROUGHPCarbon MoN13.31 NATURAL GAS 45 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 45 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 28 MMBTU/H See separatCarbon MoN

13.31 NATURAL GAS 10 MMBTU/H 2 refinery Carbon MoP COMBUST13.31 NAT GAS 32.2 MMBTU/H Carbon MoN NONE IND13.31 NATURAL GAS 14 MMBTU/H Carbon MoN13.31 NATURAL GAS 84.4 MMBTU/H MFR. IS C Carbon MoN NONE LIS13.31 NATURAL GAS 80.8 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 51.08 MMBTU NATURAL Carbon MoP GOOD CO13.31 NATURAL GAS 6.5 MMBTU/H ARB RECOCarbon MoP POWER FL13.31 NATURAL GAS 8.18 MMBTU/H 2 BOILERSCarbon MoN13.31 NATURAL GAS 96 MMBTU/H Carbon MoA OXIDATIO13.31 NATURAL GAS Carbon MoP BOILER D13.31 NATURAL GAS 2.75 MMBTU/H ARB RECOCarbon MoP NATURAL 13.31 NATURAL GAS 31.5 MMBTU/H ARB RECORCarbon MoP GOOD COM13.31 NATURAL GAS 4.29 MMBTU/H ARB RECOCarbon MoP ULTRA LO13.31 NATURAL GAS 33.9 MMBTU/H 3 boilers, Carbon MoP GOOD COM13.31 NATURAL GAS 16.5 MMBTU/H EQUIP: NACarbon MoN13.31 NATURAL GAS 20.9 MMBTU/H Fire tube b Carbon MoP GOOD COM13.31 NATURAL GAS 20.9 MMBTU/H EQUIP: ALCarbon MoN13.31 NATURAL GAS 16.3 MMBTU/H CLEAVER BCarbon MoP FLUE GAS13.31 NAT GAS SHALL BE Carbon MoN NONE IND13.31 NATURAL GAS 6 MMBTU/H CLEAVER Carbon MoN13.31 LPG 6 MMBTU/H CLEAVER Carbon MoN13.31 NATURAL GAS 90 MMBTU/H INSTALLA Carbon MoP LOW NOX 13.31 NATURAL GAS 16.3 MMBTU/H SUPERIORCarbon MoN13.31 NATURAL GAS 28.8 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 7.5 MMBTU/H CLEAVER Carbon MoN13.31 NATURAL GAS 5.05 MMBTU/H EQUIP MFRCarbon MoN13.31 NATURAL GAS 16.3 MMBTU/H CLEAVER BCarbon MoN13.31 FUEL GAS 65.6 MMBTU/H PERMIT I Carbon MoP GOOD OPE13.31 FUEL GAS 65.6 MMBTU/H PERMIT I Carbon MoP GOOD OPE13.31 NATURAL GAS 54.01 MMBTU/H WILL BE Carbon MoN NONE IND13.31 NATURAL GAS 6.3 MMBTU/H SUPERIOR Carbon MoN13.31 NATURAL GAS 26.6 MMBTU/H PROCESS Carbon MoA OXIDATIO13.31 NATURAL GAS 20.75 MMBTU/H EMISSION Carbon MoP GOOD COM13.31 NATURAL GAS 21 MMBTU/H CLEAVER Carbon MoN13.31 NATURAL GAS 21 MMBTU/H EQUIP: , Carbon MoA SCR13.31 NATURAL GAS 76.7 MMBTU/H ONLY USEDCarbon MoN13.31 NATURAL GAS 10 MMBTU/H THIS BOILCarbon MoP BACT FOR CO IS DETERMINED TO BE GOOD COMBUSTION CONTROL AND THE USE OF NATURAL GAS TO13.31 5 MMBTU/H SPACE HECarbon MoP BACT FOR CO IS DETERMINED TO BE GOOD COMBUSTION CONTROL AND THE USE OF NATURAL GAS T13.31 NATURAL GAS 19 MMBTU/H EQUIP: , Carbon MoN13.31 NAT GAS Carbon MoN NONE IND13.31 NATURAL GAS 11 MMBTU/H (EACH) Carbon MoP GOOD CO13.31 NATURAL GAS 44.1 MMBTU/H THROUGHPCarbon MoP PROPER C13.31 NATURAL GAS 44.1 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 4 MMBTU/H Carbon MoP NATURAL 13.31 NATURAL GAS 83 MMBTU/H BOILER OPCarbon MoP EFFICIEN13.31 NATURAL GAS 15 MMBTU/HRTUNDISH Carbon MoP PERMIT LIMITATION IS NATURAL GAS OR PROPANE USAGE13.31 6 MMBTU/H THROUGHPCarbon MoP PERMIT LIMITATION IS USE OF NATURAL GAS.13.31 NATURAL GAS 40 MMBTU/H Carbon MoP GOOD COM

13.31 NATURAL GAS 20.9 MMBTU/H This permit Carbon MoN13.31 NATURAL GAS 85.2 MMBTU/H Carbon MoN13.31 NATURAL GAS 27.5 MMBTU/H Carbon MoP GOOD OPE13.31 NATURAL GAS 35 MMBTU/H AUXILARY Carbon MoP GOOD COMB13.31 NATURAL GAS 44.1 MMBTU/H THESE (T Carbon MoP GOOD CO13.31 NATURAL GAS 46 MMBTU/H NATURAL Carbon MoP GOOD COMB13.31 NATURAL GAS 35 MMBTU/H 35 MMBTUCarbon MoP LIMIT EX13.31 NAT GAS 14.4 MMBTU/H EACH Carbon MoP LIMIT EX13.31 NAT GAS 29 MMBTU/H 29 MMBTUCarbon MoP FOLLOW P13.31 NAT GAS 17.5 MMBTU/H 17.5 MMBTCarbon MoP BACT LIM13.31 NATURAL GAS 10 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 20 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 80 MMBTU/H Auxiliary b Carbon MoN13.31 NATURAL GAS 48 MMBTU/H THROUGHPCarbon MoP COMBUST13.31 NATURAL GAS 62.77 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 16 MMBTU/H THESE UNCarbon MoP FUEL LIM13.31 NATURAL GAS 21.46 MMBTU/H EQUIP: , Carbon MoA ULTRA LO13.31 NATURAL GAS 8.5 MMBTU/H ARB RECOCarbon MoP ALZETA U13.31 NATURAL GAS 40 MMBTU/H EMISSIONSCarbon MoB EXCLUSIVE USE OF NATURAL 13.31 NATURAL GAS 30 MMBTU/H Operation lCarbon MoP EFFICIEN13.31 NATURAL GAS 35 MMBTU/H Carbon MoP CLEAN FU13.31 NATURAL GAS 49 MMBTU/H Boiler is r Carbon MoN13.31 NATURAL GAS 30 MMBTU/H BOILER OPCarbon MoP BOILER D13.31 NATURAL GAS 31.4 MMBTU/H Operation lCarbon MoP EFFICIEN13.31 NAT GAS 29.3 MMBTU/H 29.3 MMBTCarbon MoN13.31 NATURAL GAS 16 MMBTU/H FUEL GASCarbon MoP GOOD COM13.31 NATURAL GAS 22 MMBTU/H Carbon MoP USE OF N13.31 PROPANE 13 MMBTU/H LIMESTONCarbon MoP GOOD CO13.31 NATURAL GAS 12.6 MMBTU/H EQUIP: NOCarbon MoN13.31 NAT GAS 60 MMBTU/H Carbon MoN NONE IND13.31 NATURAL GAS 91.2 MMBTU/H Restriction Carbon MoN13.31 NATURAL GAS 37 MMBTU/H Baghouse wiCarbon MoN13.31 NATURAL GAS 21 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 35 MMBTU/H Carbon MoP GOOD CO13.31 NATURAL GAS 90 MMBTU/H Source has Carbon MoP GOOD COM13.31 NATURAL GAS 50 MMBTU/H Source not Carbon MoP GOOD COM13.31 NATURAL GAS 21 MMBTU/H Source is nCarbon MoP GOOD COM13.31 NATURAL GAS 33.5 MMBTU/H CLEAVER BCarbon MoP GOOD COM13.31 NATURAL GAS 76 MMBTU/H Limited to Carbon MoN13.31 NATURAL GAS 83 MMBTU/H Auxiliary b Carbon MoP GOOD C O13.31 NAT GAS 65.5 MMBTU/H EMISSION Carbon MoP GOOD EQU13.31 NATURAL GAS 31 MMBTU/H Carbon MoP COMBUST13.31 NATURAL GAS 0 Carbon MoP GOOD COM13.31 Carbon MoN13.31 NATURAL GAS 3.3 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 53 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 20 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 33 MMBTU/H Carbon MoP GOOD OPE

13.31 NATURAL GAS 95 MMBTU/H Carbon MoN13.31 NATURAL GAS 54 MMBTU/H Carbon MoN13.31 NATURAL GAS 68 MMBTU/H Carbon MoN13.31 NATURAL GAS 93 MMBUT/H Carbon MoP BOILER D13.31 NATURAL GAS 12.84 MMBTU/H Each boilerCarbon MoN13.31 NATURAL GAS 11.45 MMBTU/H Each fuel sCarbon MoN13.31 NATURAL GAS 33 MMBTU/H Carbon MoP BOILER D13.31 NATURAL GAS 33 MMBTU/H Emission li Carbon MoP DRY LOW 13.31 NATURAL GAS 40 MMBTU/H Carbon MoP GOOD COM13.31 NATUAL GAS 48.69 MILLION CF/YR Carbon MoB GCP13.31 NATURAL GAS 33 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 80 MMBTU/H one auxiliarCarbon MoP GOOD COM13.31 NATURAL GAS 99 MMBTU/H Carbon MoN13.31 NATURAL GAS 39 MMBTU/H MFR: SPRICarbon MoN13.31 NATURAL GAS 30 MMBTU/H throughput Carbon MoP CLEAN FU13.31 NATURAL GAS 34.4 MMBTU/H Throughput Carbon MoP ANY NEW 13.31 NATURAL GAS 4.62 MMBTU/H INSTALLA Carbon MoN GOOD COM13.31 NATURAL GAS 31.4 MMBTU/H HOURS OFCarbon MoP GOOD COM13.31 NATURAL GAS 99 MMBTU/H 2 Auxiliary Carbon MoP GOOD COM13.31 NATURAL GAS 40 MMBTU/H Two Auxili Carbon MoP GOOD COM13.31 NATURAL GAS 6 MMBTU/H BOILERS Carbon MoN13.31 NATURAL GAS 26.5 MMBTU/H KEWANEE NCarbon MoN EMISSION 13.31 NATURAL GAS Carbon MoN13.31 NATURAL GAS Carbon MoN13.31 NATURAL GAS 31 MMBTU/H Carbon MoN NONE IND13.31 NATURAL GAS 31 MMBTU/H Carbon MoN NONE IND13.31 NATURAL GAS 15.8 MMBTU/H Carbon MoN NONE IND13.31 NATURAL GAS 16.4 MMBTU/H Natural GaCarbon MoN13.31 NATURAL GAS 68 MMBTU/H Limited to Carbon MoA CATALYTI13.31 NATURAL GAS 13.4 MMBUT/H Carbon MoN13.31 NATURAL GAS 55.3 MMBTU/H OperationalCarbon MoN13.31 NATURAL GAS 33.5 MMBTU/H Installatio Carbon MoN13.31 NATURAL GAS 1700 MMCF/rolli THE INCR Carbon MoN13.31 NAT GAS 12 MMBTU/H Carbon MoN NONE IND13.31 NAT GAS 2.5 MMBTU/H Carbon MoN NONE IND13.31 NAT GAS 32.5 MMBTU/H Carbon MoN NONE IND13.31 NAT GAS 3 MMBTU/H Carbon MoN NONE IND13.31 14.4 MMBTU/H Carbon MoP GOOD COM13.31 25.2 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 50000 LB/H Throughput Carbon MoN13.31 NATURAL GAS 33 MMBTU/H Carbon MoP BOILER D13.31 NATURAL GAS 83 MMBTU/H THE BOILECarbon MoN13.31 NATURAL GAS 43.2 MMBTU/H One of two Carbon MoB CONTINUO13.31 NATURAL GAS 25 MMBTU/H VACUUM OCarbon MoN13.31 NATURAL GAS 5 MMBTU/H Carbon MoN13.31 NATURAL GAS 5.61 MMBTU/H Carbon MoP GOOD EQU13.31 NATURAL GAS 10.2 MMBTU/H Carbon MoP GOOD EQU13.31 NATURAL GAS 13.31 MMBTU/H Carbon MoP GOOD EQU

13.31 NATURAL GAS 12.24 MMBTU/H Carbon MoP GOOD EQU13.31 NATURAL GAS 5 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 9 MMBTU/H One naturalCarbon MoP GOOD COM13.31 NATURAL GAS 36 mmbtu/h Carbon MoN13.31 NATURAL GAS 30.6 MMBTU/H THE MAXI Carbon MoN13.31 NATURAL GAS 41 MMBTU/H THIS BOILCarbon MoN13.31 NATURAL GAS 55.34 MMBTU/H THIS BOI Carbon MoN13.31 NATURAL GAS 34 MMBTU/H Throughput Carbon MoP GOOD COM13.31 NATURAL GAS 70 MMBTU/H NATURAL Carbon MoP GOOD CO13.31 NATURAL GAS 80 MMBTU/H Throughput Carbon MoP GOOD CO13.31 NATURAL GAS 60 MMBTU/H NATURAL Carbon MoP NATURAL 13.31 NATURAL GAS 80 MMBTU/H NAT. GAS Carbon MoP NAT. GAS13.31 NATURAL GAS 11 MMBTU/H Carbon MoP NATURAL 13.31 NATURAL GAS 34 MMBTU/H Carbon MoP NATURAL 13.31 NATURAL GAS 50 MMBTU/H BACT for Carbon MoP CLEAN FU13.31 NATURAL GAS 60 MMBTU/H Carbon MoP EFFECTIV13.31 NATURAL GAS 365 MMSCF/Y Boiler has Carbon MoN13.31 NATURAL GAS 50 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 45 MMBTU/H TWO HOT Carbon MoP GOOD COM13.31 NATURAL GAS 32 MMBTU/H STACK S31Carbon MoP USE OF NA13.31 NATURAL GAS 32 MMBTU/H STACK S32Carbon MoP USE OF NA13.31 NATURAL GAS 143 MMBTU/H Carbon MoN13.31 NATURAL GAS 6.8 MMBTU/H Carbon MoN13.31 NATURAL GAS 40 MMBTU/H AUXILIARYCarbon MoP GOOD COM13.31 NATURAL GAS 22 MMBTU/H ENTRY IN Carbon MoP GOOD COM13.31 NATURAL GAS 46.2 MMBTU/H NOT PSD Carbon MoP BOILER D13.31 NATURAL GAS 97.1 MMBTU/H Carbon MoP NATURAL 13.31 NATURAL GAS 10 MMBTU/H GAS CONDCarbon MoP NATURAL 13.31 NATURAL GAS 0.75 MMBTU/H EMISSION Carbon MoP NATURAL 13.31 NATURAL GAS 8.8 MMBTU/H THE PROCCarbon MoP USE OF N13.31 NATURAL GAS 38 MMBTU/H Carbon MoN13.31 NATURAL GAS 30.6 MMBTU/H LIMITS A Carbon MoN13.31 NATURAL GAS 13 MMBTU/H Isom hydrotCarbon MoP GOOD COM13.31 19 MMBTU/H Carbon MoP GOOD COM13.31 NATURAL GAS 66.5 MMBTU/H OPERATINGCarbon MoP USE OF N13.31 90 MMBTU/H EA. Carbon MoP GOOD COM13.31 NATURAL GAS SEVEN VAPCarbon MoP EACH VAP13.31 NATURAL GAS 34 MMBTU/H Carbon MoP GOOD OPE13.31 NATURAL GAS 14.87 MMBTU/H Carbon MoP GOOD OPE13.31 NATURAL GAS 1.34 MMBTU/H Carbon MoP GOOD OPE13.31 NATURAL GAS 97 MMBTU/H EQUIP: WACarbon MoP ULTRA LO13.31 NATURAL GAS ENGINEERICarbon MoP GOOD COM13.31 NATURAL GAS 25 MMBTU/H EQUIP: THCarbon MoA ULTRA-LO13.31 NATURAL GAS 3.85 MMBTU/H THE UNIT' Carbon MoP GOOD COM13.31 NATURAL GAS 35.4 MMBTU/H THE BACTCarbon MoP GOOD COM13.31 NATURAL GAS 20.4 MMBTU/H TWO BOILCarbon MoN13.31 NATURAL GAS 98.7 MMBTU/H Carbon MoN13.31 NATURAL GAS 93.7 MMBTU/H PROJECT Carbon MoA LOW NOX

13.31 NATURAL GAS 99 MMBTU/H THIS PRO Carbon MoN13.31 NATURAL GAS 27.2 MMBTU/H THIS PRO Carbon MoN13.31 NATURAL GAS 33.4 MMBTU eaTHIS PRO Carbon MoN13.31 NATURAL GAS 64.9 MMBtu eacTHIS PROCCarbon MoN13.31 NATURAL GAS 42000 LB/H HOLDING CChlorine / N COMBUSTI13.31 NATURAL GAS 42000 LB/H HOLDING CDioxins & P DIOXIN A13.31 NATURAL GAS 0.75 MMBTU/H EMISSION Fluorine P NATURAL 13.31 NATURAL GAS 42000 LB/H HOLDING CHydrochloriA LIME INJ13.31 NATURAL GAS 42000 LB/H HOLDING CHydrochloriN FLUES: D13.31 NAT GAS SHALL BE Hydrogen N NONE IND13.31 NATURAL GAS 42000 LB/H HOLDING CHydrogen FN COMBUSTI13.31 NAT GAS 17.5 MMBTU/H 17.5 MMBTHydrogen SP FUEL SULFUR CONTENT LIMIT13.31 NATURAL GAS 0.75 MMBTU/H EMISSION Lead (Pb) P NATURAL 13.31 NATURAL GAS Lead (Pb) P USE OF N13.31 NATURAL GAS 0.75 MMBTU/H EMISSION Mercury P NATURAL 13.31 NATURAL GAS 33 MMBTU/H Emission li Nitrogen D P CLEAN FU13.31 NATUAL GAS 48.69 MILLION CF/YR Nitrogen D B GCP13.31 NATURAL GAS 80 MMBTU/H one auxiliarNitrogen D P LOW NOX 13.31 NATURAL GAS 99 MMBTU/H 2 Auxiliary Nitrogen D P LOW NOX 13.31 NATURAL GAS 16.4 MMBTU/H Natural GaNitrogen D P DLN13.31 NATURAL GAS 68 MMBTU/H Limited to Nitrogen D P DLN13.31 NATURAL GAS 43.2 MMBTU/H One of two Nitrogen D B FLUE GAS13.31 NATURAL GAS 40 MMBTU/H AUXILIARYNitrogen D P LOW NOX 13.31 NATURAL GAS ENGINEERINitrogen D B DRY LNB 13.31 NATURAL GAS 99.5 MMBTU/H Nitrogen O P ULTRA LO13.31 NATURAL GAS 8.1 MMBTU/H ARB RECORNitrogen O P PREMIXED13.31 NATURAL GAS 2.8 MMBTU/H ARB RECORNitrogen O P OPERATIO13.31 NATURAL GAS 76 MMBTU/H LOCATED Nitrogen O P LOW NOX 13.31 NATURAL GAS 72.3 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 55.2 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 65.7 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 6.75 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 76 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 50 MMBTU/H THE NUMBNitrogen O P LOW NOX 13.31 NATURAL GAS 21 MMBTU/H THE BURNNitrogen O P LOW NOX 13.31 NATURAL GAS 58.4 MMBTU/H THE BURNNitrogen O P LOW NOX 13.31 NATURAL GAS 68 MMBTU/H TURBINE Nitrogen O P LOW NOX13.31 FUEL OIL 0.3 MMBTU/H PERMIT NONitrogen O P LOW NOX/13.31 NATURAL GAS 2.3 MMBTU/H BOILER BUNitrogen O P LOW NOX B13.31 NATURAL GAS 2.3 MMBTU/H 20% OPACINitrogen O P LOW NOX B13.31 NATURAL GAS 2.3 MMBTU/H FUEL IS N Nitrogen O P LOW NOX 13.31 PERMIT N Nitrogen O N13.31 NATURAL GAS 0.3 MMBTU/H FUELS ARENitrogen O N ADDITIONA13.31 NATURAL GAS 96 MMBTU/H A SEPARANitrogen O N N/A13.31 NATURAL GAS 13.4 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 11.7 MMBTU/H Nitrogen O P CLEAN FU13.31 NATURAL GAS 93 MMBTU/H SECOND FNitrogen O N REGULATO13.31 NATURAL GAS 54.9 MMBTU/H Nitrogen O P LOW NOX

13.31 NG SUPPLEME 24000 LB/HR ST COMPLIANNitrogen O N13.31 NATURAL GAS 0.4 MMLB/H STEAM Nitrogen O B LOW NOX 13.31 NATURAL GAS 100 MMBTU/H HEATING MNitrogen O P LOW NOX"13.31 NATURAL GAS 8 MMBTU/H OTHER COMNitrogen O P CZ LINER13.31 NATURAL GAS 95 MMBTU/H Nitrogen O P LOW NOX 13.31 9 MMBTU/H THROUGHPNitrogen O N13.31 22.89 MMBTU/H CLEAVER-Nitrogen O N13.31 NATURAL GAS 85 MMBTU/H THROUGHPNitrogen O P LOW NOX B13.31 NATURAL GAS 45 MMBTU/H Nitrogen O P ULTRA LO13.31 NATURAL GAS 45 MMBTU/H Nitrogen O P ULTRA LO13.31 77 MMBTU/H PERMIT NUNitrogen O N13.31 NATURAL GAS 28 MMBTU/H See separatNitrogen O N13.31 NATURAL GAS 10 MMBTU/H 2 refinery Nitrogen O P LOW NOX 13.31 NATURAL GAS 7 MMBTU/H ARB RECORNitrogen O P ELEVEN LO13.31 NAT GAS 32.2 MMBTU/H Nitrogen O N NONE IND13.31 NATURAL GAS 99 MMBTU/H NOX IS T Nitrogen O B LOW NOX B13.31 NATURAL GAS 14 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 52.8 MMBTU/H MAXIMUM Nitrogen O N NONE IND13.31 NATURAL GAS 84.4 MMBTU/H MFR. IS C Nitrogen O N13.31 NATURAL GAS 80.8 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 51.08 MMBTU NATURAL Nitrogen O P LOW NOX 13.31 NATURAL GAS 10 MMBTU/H THESE HENitrogen O P LOW NOX 13.31 NATURAL GAS 10 MMBTU/H THESE HENitrogen O P LOW NOX 13.31 NATURAL GAS 6.5 MMBTU/H ARB RECONitrogen O P POWER FL13.31 NATURAL GAS 8.18 MMBTU/H 2 BOILERSNitrogen O P LOW NOX 13.31 NATURAL GAS 96 MMBTU/H Nitrogen O A SCR13.31 NATURAL GAS Nitrogen O P LOW NOX 13.31 NATURAL GAS 2.75 MMBTU/H ARB RECONitrogen O P NATURAL 13.31 NATURAL GAS 99 MMBTU Nitrogen O P LOW NOX 13.31 NATURAL GAS 7.6 MMBTU/H ARB RECORNitrogen O P LOW-NOX13.31 NATURAL GAS 31.5 MMBTU/H ARB RECORNitrogen O B COEN LOW13.31 NATURAL GAS 4.29 MMBTU/H ARB RECONitrogen O P ULTRA LO13.31 NATURAL GAS 33.9 MMBTU/H 3 boilers, Nitrogen O A HONEYCOM13.31 NATURAL GAS 16.5 MMBTU/H EQUIP: NANitrogen O N SELCTIVE13.31 NATURAL GAS 20.9 MMBTU/H Fire tube b Nitrogen O P LOW NOX 13.31 NATURAL GAS 20.9 MMBTU/H EQUIP: ALNitrogen O A LOW NOX 13.31 NATURAL GAS 22 MMBTU/H See RBLC INitrogen O P COMBUST13.31 NATURAL GAS 16.3 MMBTU/H CLEAVER BNitrogen O P LOW NOX 13.31 NAT GAS SHALL BE Nitrogen O N NONE IND13.31 NATURAL GAS 6 MMBTU/H CLEAVER Nitrogen O P LOW NOX 13.31 LPG 6 MMBTU/H CLEAVER Nitrogen O P LOW NOX 13.31 NATURAL GAS 90 MMBTU/H INSTALLA Nitrogen O P LOW NOX 13.31 NATURAL GAS 10 MMBTU/H Nitrogen O P NATURAL 13.31 NATURAL GAS 16.3 MMBTU/H SUPERIORNitrogen O P LOW NOX 13.31 NATURAL GAS 28.8 MMBTU/H Nitrogen O P13.31 NATURAL GAS 7.5 MMBTU/H CLEAVER Nitrogen O P LOW NOX 13.31 NATURAL GAS 5.05 MMBTU/H EQUIP MFRNitrogen O P LOW NOX 13.31 NATURAL GAS 16.3 MMBTU/H CLEAVER BNitrogen O P ULTRA LO

13.31 FUEL GAS 65.6 MMBTU/H PERMIT I Nitrogen O P LOW NOX 13.31 FUEL GAS 65.6 MMBTU/H PERMIT I Nitrogen O P LOW NOX 13.31 NATURAL GAS 54.01 MMBTU/H WILL BE Nitrogen O N NONE IND13.31 NATURAL GAS 6.3 MMBTU/H SUPERIOR Nitrogen O P LOW NOX 13.31 NATURAL GAS 4.2 MMBTU/H MFR: KEWANitrogen O A SCONOX C13.31 NATURAL GAS 6 MMBTU/H EQUIP: , Nitrogen O A LOW NOX 13.31 NATURAL GAS 42000 LB/H HOLDING CNitrogen O N FLUES CA13.31 NATURAL GAS 26.6 MMBTU/H PROCESS Nitrogen O B SCR, DRY13.31 NATURAL GAS 20.75 MMBTU/H EMISSION Nitrogen O P LOW NOX 13.31 NATURAL GAS 21 MMBTU/H CLEAVER Nitrogen O A SELECTIV13.31 NATURAL GAS 21 MMBTU/H EQUIP: , Nitrogen O A SCR13.31 NATURAL GAS 76.7 MMBTU/H ONLY USEDNitrogen O P LOW NOX 13.31 NATURAL GAS 10 MMBTU/H THIS BOILNitrogen O P NATURAL 13.31 5 MMBTU/H SPACE HENitrogen O P BACT FOR13.31 NATURAL GAS 19 MMBTU/H EQUIP: , Nitrogen O A ULTRA-LO13.31 NATURAL GAS 80 MMBTU/H Nitrogen O N13.31 NAT GAS Nitrogen O N NONE IND13.31 NATURAL GAS 11 MMBTU/H (EACH) Nitrogen O P LOW NOX 13.31 NATURAL GAS 44.1 MMBTU/H THROUGHPNitrogen O P LOW NOX 13.31 NATURAL GAS 44.1 MMBTU/H Nitrogen O B DRY LOW 13.31 NATURAL GAS 13.4 MMBTU/H LP BackupNitrogen O P LOW NOX 13.31 NATURAL GAS 11.7 MMBTU/H LP BackupNitrogen O P LOW NOX 13.31 NATURAL GAS 83 MMBTU/H BOILER OPNitrogen O P LOW NOX 13.31 NATURAL GAS 15 MMBTU/HRTUNDISH Nitrogen O P LOW NOX 13.31 6 MMBTU/H THROUGHPNitrogen O P LOW NOX 13.31 NATURAL GAS 8.8 MMBTU/H, EQUIP: RENitrogen O A LOW-NOX13.31 NATURAL GAS 40 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 20.9 MMBTU/H This permit Nitrogen O P LOW NOX 13.31 NATURAL GAS 85.2 MMBTU/H Nitrogen O N13.31 NATURAL GAS 35 MMBTU For this pr Nitrogen O P LOW NOX 13.31 NATURAL GAS 27.5 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 35 MMBTU/H AUXILARY Nitrogen O P LOW NOX 13.31 NATURAL GAS 20 MMBTU/H CO limits aNitrogen O P LOW NOX 13.31 NATURAL GAS 44.1 MMBTU/H THESE (T Nitrogen O P GOOD CO13.31 NATURAL GAS 46 MMBTU/H NATURAL Nitrogen O P GOOD COM13.31 NATURAL GAS 35 MMBTU/H 35 MMBTUNitrogen O P LIMIT EX13.31 NAT GAS 14.4 MMBTU/H EACH Nitrogen O N LIMIT EX13.31 NAT GAS 29 MMBTU/H 29 MMBTUNitrogen O N BACT LIM13.31 NAT GAS 17.5 MMBTU/H 17.5 MMBTNitrogen O P BACT LIM13.31 NATURAL GAS 10 MMBTU/H Nitrogen O P GOOD COM13.31 NATURAL GAS 20 MMBTU/H Nitrogen O P GOOD COM13.31 NATURAL GAS 80 MMBTU/H Auxiliary b Nitrogen O P LOW NOX 13.31 NATURAL GAS 48 MMBTU/H THROUGHPNitrogen O P DRY LOW 13.31 NATURAL GAS 62.77 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 16 MMBTU/H THESE UNNitrogen O P FUEL LIM13.31 NATURAL GAS 65.78 MMBTU/H THREE IDENitrogen O B LOW-NOX 13.31 NATURAL GAS 54.4 MMBTU/H PROPANE Nitrogen O B LOW NOX 13.31 NATURAL GAS 21.46 MMBTU/H EQUIP: , Nitrogen O A ULTRA LO

13.31 NATURAL GAS 8.5 MMBTU/H ARB RECONitrogen O P ALZETA U13.31 NATURAL GAS 40 MMBTU/H EMISSIONSNitrogen O B EXCLUSIVE USE OF NATURAL 13.31 NATURAL GAS 30 MMBTU/H Operation lNitrogen O P LOW NOX 13.31 NATURAL GAS 35 MMBTU/H Nitrogen O P CLEAN FU13.31 NATURAL GAS 49 MMBTU/H Boiler is r Nitrogen O N13.31 NATURAL GAS 30 MMBTU/H BOILER OPNitrogen O P LOW NOX 13.31 NATURAL GAS 31.4 MMBTU/H Operation lNitrogen O P LOW NOX 13.31 NAT GAS 29.3 MMBTU/H 29.3 MMBTNitrogen O P FGR AND 13.31 NATURAL GAS 16 MMBTU/H FUEL GASNitrogen O N NONE- CO13.31 NATURAL GAS 22 MMBTU/H Nitrogen O P NATURAL 13.31 NATURAL GAS 3.5 MMBTU/H,EQUIP: , Nitrogen O A LOW NOX 13.31 PROPANE 13 MMBTU/H LIMESTONNitrogen O P COMBUST13.31 NATURAL GAS 12.6 MMBTU/H EQUIP: NONitrogen O A NEW FUR13.31 NAT GAS 60 MMBTU/H Nitrogen O P ULTRA LO13.31 NATURAL GAS 91.2 MMBTU/H Restriction Nitrogen O P USE OF L13.31 NATURAL GAS 37 MMBTU/H Baghouse wiNitrogen O N13.31 NATURAL GAS 5.4 MMBTU/H MFR: FERRNitrogen O A LOW NOX13.31 NATURAL GAS 21 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 35 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 90 MMBTU/H Source has Nitrogen O P LOW NOX B13.31 NATURAL GAS 50 MMBTU/H Source not Nitrogen O A LOW NOX 13.31 NATURAL GAS 21 MMBTU/H Source is nNitrogen O P LOW NOX 13.31 NATURAL GAS 33.5 MMBTU/H CLEAVER BNitrogen O P LO-NOX B13.31 NATURAL GAS 76 MMBTU/H Limited to Nitrogen O P LOW NOX 13.31 NATURAL GAS 83 MMBTU/H Auxiliary b Nitrogen O P LOW NOX 13.31 NAT GAS 65.5 MMBTU/H EMISSION Nitrogen O P LOW-NOX13.31 NATURAL GAS 5 MMBTU/H,EQUIP: , Nitrogen O A LOW-NOX13.31 NATURAL GAS 31 MMBTU/H Nitrogen O N COMBUST13.31 NATURAL GAS 0 Nitrogen O P GOOD COM13.31 Nitrogen O N13.31 NATURAL GAS 3.3 MMBTU/H Nitrogen O P PREMIX S13.31 NATURAL GAS 53 MMBTU/H Nitrogen O P ULTRA LO13.31 NATURAL GAS 20 MMBTU/H Nitrogen O P ULTRA LO13.31 NATURAL GAS 33 MMBTU/H Nitrogen O N13.31 NATURAL GAS 95 MMBTU/H Nitrogen O N13.31 NATURAL GAS 54 MMBTU/H Nitrogen O N13.31 NATURAL GAS 68 MMBTU/H Nitrogen O N13.31 NATURAL GAS 93 MMBUT/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 12.84 MMBTU/H Each boilerNitrogen O N13.31 NATURAL GAS 11.45 MMBTU/H Each fuel sNitrogen O N13.31 NATURAL GAS 33 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 40 mmbtu/h Nitrogen O P LOW NOX BURNERS, CLEAN FU13.31 NATURAL GAS 40 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 33 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 4.19 MMBTU/H PSD for NONitrogen O P GOOD COM13.31 NATURAL GAS 99 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 39 MMBTU/H MFR: SPRINitrogen O P ULTRA-LO13.31 NATURAL GAS 30 MMBTU/H throughput Nitrogen O P LOW NOX

13.31 NATURAL GAS 34.4 MMBTU/H Throughput Nitrogen O P ANY NEW 13.31 NATURAL GAS 4.62 MMBTU/H INSTALLA Nitrogen O N LOW NOX 13.31 NATURAL GAS 31.4 MMBTU/H HOURS OFNitrogen O P DRY LOW 13.31 NATURAL GAS 40 MMBTU/H Two Auxili Nitrogen O P LOW NOX 13.31 NATURAL GAS 6 MMBTU/H BOILERS Nitrogen O N13.31 NATURAL GAS 26.5 MMBTU/H KEWANEE NNitrogen O N EMISSION 13.31 NATURAL GAS Nitrogen O N13.31 NATURAL GAS Nitrogen O N13.31 NATURAL GAS 31 MMBTU/H Nitrogen O N NONE IND13.31 NATURAL GAS 31 MMBTU/H Nitrogen O N NONE IND13.31 NATURAL GAS 15.8 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 2.4 MMBTU/H Startup gasNitrogen O N13.31 NATURAL GAS 13.4 MMBUT/H Nitrogen O N13.31 NATURAL GAS 55.3 MMBTU/H OperationalNitrogen O N LNB PLUS13.31 NATURAL GAS 33.5 MMBTU/H Installatio Nitrogen O P ULTRA LO13.31 NATURAL GAS 1700 MMCF/rolli THE INCR Nitrogen O N13.31 NATURAL GAS 1.6 MMBTU/H natural gasNitrogen O P GOOD COM13.31 NAT GAS 12 MMBTU/H Nitrogen O N NONE IND13.31 NAT GAS 2.5 MMBTU/H Nitrogen O N NONE IND13.31 NAT GAS 32.5 MMBTU/H Nitrogen O N NONE IND13.31 NAT GAS 3 MMBTU/H Nitrogen O N NONE IND13.31 NATURAL GAS 5.38 MMBTU/H Nitrogen O P DLN13.31 NATURAL GAS 50000 LB/H Throughput Nitrogen O N13.31 NATURAL GAS 33 MMBTU/H Nitrogen O P LOW-NOX13.31 NATURAL GAS 83 MMBTU/H THE BOILENitrogen O N13.31 NATURAL GAS 4.19 MMBTU/H Sellers C10Nitrogen O P GOOD COM13.31 NATURAL GAS 25 MMBTU/H VACUUM ONitrogen O A LOW NOX 13.31 NATURAL GAS 5 MMBTU/H Nitrogen O N13.31 NATURAL GAS 5 MMBTU/H Nitrogen O P DRY LOW 13.31 NATURAL GAS 9 MMBTU/H One naturalNitrogen O A DLN13.31 NATURAL GAS 36 mmbtu/h Nitrogen O N13.31 NATURAL GAS 30.6 MMBTU/H THE MAXI Nitrogen O N13.31 NATURAL GAS 41 MMBTU/H THIS BOILNitrogen O P LOW NOX 13.31 NATURAL GAS 55.34 MMBTU/H THIS BOI Nitrogen O P LOW NOX 13.31 NATURAL GAS 98.51 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 34 MMBTU/H Throughput Nitrogen O P LOW NOX 13.31 NATURAL GAS 70 MMBTU/H NATURAL Nitrogen O P DRY LOW 13.31 NATURAL GAS 80 MMBTU/H Throughput Nitrogen O P LOW NOX 13.31 NATURAL GAS 60 MMBTU/H NATURAL Nitrogen O P LOW NOX 13.31 NATURAL GAS 80 MMBTU/H NAT. GAS Nitrogen O P NAT. GAS13.31 NATURAL GAS 11 MMBTU/H Nitrogen O P NATURAL 13.31 NATURAL GAS 34 MMBTU/H Nitrogen O P NATURAL 13.31 NATURAL GAS 600 HP Throughput Nitrogen O P LOW NOX 13.31 NATURAL GAS 16 MMBTU/H Nitrogen O P MAINTENA13.31 NATURAL GAS 0.03 MMDSCF/ THROUGH Nitrogen O P LOW-NOX 13.31 NATURAL GAS 0.01 MMDSCF/ ADDITION Nitrogen O P LOW-NOX 13.31 NATURAL GAS 1.4 mmbtu/h Nitrogen O P LOW-NOX 13.31 NATURAL GAS 50 MMBTU/H BACT for Nitrogen O P NATURAL

13.31 NATURAL GAS 64 MMBTU/H BABCOCK Nitrogen O P LOW-NOX13.31 NATURAL GAS 60 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 365 MMSCF/Y Boiler has Nitrogen O A LOW-NOX 13.31 NATURAL GAS 45 MMBTU/H TWO HOT Nitrogen O P LOW NOX 13.31 NATURAL GAS 32 MMBTU/H STACK S31Nitrogen O P USE OF NA13.31 NATURAL GAS 32 MMBTU/H STACK S32Nitrogen O P USE OF NA13.31 OIL/NG 73.3 MMBTU/H THIS UNITNitrogen O N OPERATIO13.31 NATURAL GAS 143 MMBTU/H Nitrogen O A ULTRA-LO13.31 NATURAL GAS 6.8 MMBTU/H Nitrogen O A ULTRA-LO13.31 NATURAL GAS 22 MMBTU/H ENTRY IN Nitrogen O A LOW NOX 13.31 NATURAL GAS 46.2 MMBTU/H NOT PSD Nitrogen O P BURNER D13.31 NATURAL GAS 97.1 MMBTU/H Nitrogen O P NATURAL 13.31 NATURAL GAS 10 MMBTU/H GAS CONDNitrogen O P NATURAL 13.31 NATURAL GAS 0.75 MMBTU/H EMISSION Nitrogen O P NATURAL 13.31 NATURAL GAS 8.8 MMBTU/H THE PROCNitrogen O P USE OF N13.31 NATURAL GAS 24.5 mmbtu/h THROUGHPUNitrogen O P LOW NOX 13.31 NATURAL GAS 38 MMBTU/H Nitrogen O A LOW NOX 13.31 NATURAL GAS 30.6 MMBTU/H LIMITS A Nitrogen O N13.31 NATURAL GAS 13 MMBTU/H Isom hydrotNitrogen O P ULTRA LO13.31 19 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 66.5 MMBTU/H OPERATINGNitrogen O P USE OF N13.31 90 MMBTU/H EA. Nitrogen O B LOW NOX 13.31 NATURAL GAS SEVEN VAPNitrogen O A ULNB13.31 NATURAL GAS ONE 1.3 Nitrogen O A LNB13.31 NATURAL GAS 34 MMBTU/H Nitrogen O P LOW NOX 13.31 NATURAL GAS 1.34 MMBTU/H Nitrogen O P CONVENTI13.31 NATURAL GAS 97 MMBTU/H EQUIP: WANitrogen O P ULTRA LO13.31 NATURAL GAS ENGINEERINitrogen O B GOOD COM13.31 NATURAL GAS 25 MMBTU/H EQUIP: THNitrogen O A ULTRA-LO13.31 NATURAL GAS 3.85 MMBTU/H THE UNIT' Nitrogen O P GOOD COM13.31 NATURAL GAS 35.4 MMBTU/H THE BACTNitrogen O B LOW-NOX 13.31 NATURAL GAS 5.4 MMBTU/H ANY OTHENitrogen O A LOW NOX 13.31 NATURAL GAS 20.4 MMBTU/H TWO BOILNitrogen O P LOW NOX 13.31 NATURAL GAS 95 MMBTU/H Nitrogen O P ULTRA LO13.31 NATURAL GAS 98.7 MMBTU/H Nitrogen O A SCR13.31 NATURAL GAS 93.7 MMBTU/H PROJECT Nitrogen O A LOW NOX 13.31 NATURAL GAS 99 MMBTU/H THIS PRO Nitrogen O P ULTRA LO13.31 NATURAL GAS 27.2 MMBTU/H THIS PRO Nitrogen O P ULTRA LO13.31 NATURAL GAS 27.2 MMBTU/H THIS PRO Nitrogen O P ULTRA LO13.31 NATURAL GAS 33.4 MMBTU eaTHIS PRO Nitrogen O P UNLB WIT13.31 NATURAL GAS 64.9 MMBtu eacTHIS PROCNitrogen O P ULNB & E13.31 NATURAL GAS 50 MMBTU/H THE NUMBParticulate P CLEAN FU13.31 NATURAL GAS 21 MMBTU/H THE BURNParticulate P CLEAN FU13.31 NATURAL GAS 58.4 MMBTU/H THE BURNParticulate P CLEAN FU13.31 NATURAL GAS 96 MMBTU/H A SEPARAParticulate A FABRIC FI13.31 NATURAL GAS 13.4 MMBTU/H Particulate P CLEAN FU13.31 NATURAL GAS 11.7 MMBTU/H Particulate P CLEAN FU13.31 NATURAL GAS 93 MMBTU/H SECOND FParticulate P SECTION N

13.31 NATURAL GAS 100 MMBTU/H HEATING MParticulate N MINIMAL 13.31 77 MMBTU/H PERMIT NUParticulate N13.31 NATURAL GAS 28 MMBTU/H See separatParticulate N13.31 NATURAL GAS 75 MMBTU/H HOT OIL HParticulate P FUEL LIMITATIONS, SEE POLL13.31 NATURAL GAS 52.8 MMBTU/H MAXIMUM Particulate P GOOD OPE13.31 NATURAL GAS 5 MMBTU/H MAXIMUM Particulate N13.31 NATURAL GAS 1.05 MMBTU/H SECOND FUParticulate N NONE IND13.31 NATURAL GAS 0.5 MMBTU/H MAXIMUM OParticulate P GOOD OPE13.31 NATURAL GAS 0.63 MMBTU/H MAXIMUM OParticulate P GOOD OPE13.31 NATURAL GAS 1.06 MMBTU/H MAXIMUM OParticulate P GOOD OPE13.31 NATURAL GAS 6.3 MMBTU/H PERMIT LIParticulate P GOOD OPE13.31 NATURAL GAS 3.5 MMBTU/H UNITS 208Particulate P GOOD OPE13.31 NATURAL GAS 4.2 MMBTU/H THE SOURParticulate P GOOD OPE13.31 NATURAL GAS 96 MMBTU/H Particulate P NATURAL 13.31 NATURAL GAS 31.5 MMBTU/H ARB RECORParticulate N NO BACT L13.31 FUEL GAS 65.6 MMBTU/H PERMIT I Particulate P GOOD OPE13.31 FUEL GAS 65.6 MMBTU/H PERMIT I Particulate P GOOD OPE13.31 NATURAL GAS 54.01 MMBTU/H WILL BE Particulate P FUEL SPE13.31 NATURAL GAS 26.6 MMBTU/H PROCESS Particulate P NATURAL 13.31 NATURAL GAS 8.36 MMBTU/H THREE PRParticulate N NONE IND13.31 NATURAL GAS 100 HP THE OWNEParticulate N NONE IND13.31 NATURAL GAS 10 MMBTU/H THIS BOILParticulate P BACT FOR13.31 5 MMBTU/H SPACE HEParticulate P BACT FOR13.31 NATURAL GAS 5.2 MMBTU/H COMPLIANCParticulate A VENTURI 13.31 NATURAL GAS 80 MMBTU/H Particulate A BAGHOUS13.31 NATURAL GAS 13.4 MMBTU/H LP BackupParticulate N13.31 NATURAL GAS 11.7 MMBTU/H LP BackupParticulate N13.31 NATURAL GAS 11 MMBTU/H USED FORParticulate P CLEAN BU13.31 NATURAL GAS 35 MMBTU/H 35 MMBTUParticulate N13.31 NAT GAS 14.4 MMBTU/H EACH Particulate N13.31 NAT GAS 29 MMBTU/H 29 MMBTUParticulate N13.31 NATURAL GAS 16 MMBTU/H FUEL GASParticulate N NONE- PM13.31 PROPANE 13 MMBTU/H LIMESTONParticulate A BAGHOUS13.31 NATURAL GAS 12.6 MMBTU/H EQUIP: NOParticulate N13.31 NATURAL GAS 91.2 MMBTU/H Restriction Particulate N13.31 NATURAL GAS 37 MMBTU/H Baghouse wiParticulate A BAGHOUSE13.31 NATURAL GAS 75 MMBTU/H CEMS, WHEParticulate N13.31 NATURAL GAS 21 MMBTU/H Particulate P NATURAL 13.31 NATURAL GAS 90 MMBTU/H Source has Particulate P USE OF N13.31 NATURAL GAS 50 MMBTU/H Source not Particulate P NATURAL 13.31 NATURAL GAS 21 MMBTU/H Source is nParticulate P NATURAL 13.31 NAT GAS 65.5 MMBTU/H EMISSION Particulate P FIRED BY13.31 NATURAL GAS 33.5 MMBTU/H Boiler is a Particulate N13.31 NATUAL GAS 48.69 MILLION CF/YR Particulate B GCP13.31 NATURAL GAS 80 MMBTU/H one auxiliarParticulate P GOOD COM13.31 NATURAL GAS 31.4 MMBTU/H HOURS OFParticulate P GOOD COM13.31 NATURAL GAS 26.5 MMBTU/H KEWANEE NParticulate N EMISSION 13.31 NATURAL GAS Particulate N

13.31 NATURAL GAS 16.4 MMBTU/H Natural GaParticulate P LOW ASH 13.31 NATURAL GAS 68 MMBTU/H Limited to Particulate P LOW ASH 13.31 NATURAL GAS 1700 MMCF/rolli THE INCR Particulate N13.31 NATURAL GAS 1.6 MMBTU/H natural gasParticulate P GOOD COM13.31 NATURAL GAS 83 MMBTU/H THE BOILEParticulate N13.31 NATURAL GAS 43.2 MMBTU/H One of two Particulate P GOOD COM13.31 NATURAL GAS 9 MMBTU/H One naturalParticulate P LOW ASH 13.31 NATURAL GAS 70 MMBTU/H NATURAL Particulate N CLEAN FU13.31 NATURAL GAS 60 MMBTU/H NATURAL Particulate P NATURAL 13.31 NATURAL GAS 80 MMBTU/H NAT. GAS Particulate P NATURAL 13.31 NATURAL GAS 11 MMBTU/H Particulate P NATURAL 13.31 NATURAL GAS 34 MMBTU/H Particulate P NATURAL 13.31 NATURAL GAS 16 MMBTU/H Particulate P EXCLUSIV13.31 NATURAL GAS 365 MMSCF/Y Boiler has Particulate N13.31 NATURAL GAS 32 MMBTU/H STACK S31Particulate P USE OF NA13.31 NATURAL GAS 32 MMBTU/H STACK S32Particulate P USE OF NA13.31 NATURAL GAS 40 MMBTU/H AUXILIARYParticulate P CLEAN FU13.31 NATURAL GAS 0.75 MMBTU/H EMISSION Particulate P NATURAL 13.31 NATURAL GAS SEVEN VAPParticulate Matter (PM)13.31 NATURAL GAS 20.4 MMBTU/H TWO BOILParticulate N13.31 NATURAL GAS 95 MMBTU/H Particulate N13.31 NATURAL GAS 98.7 MMBTU/H Particulate N13.31 NATURAL GAS 93.7 MMBTU/H PROJECT Particulate N13.31 NATURAL GAS 34 MMBTU/H Throughput Particulate P COMPLIAN13.31 FUEL OIL 0.3 MMBTU/H PERMIT NOParticulate P LOW NOX/13.31 NATURAL GAS 2.3 MMBTU/H BOILER BUParticulate P LOW NOX 13.31 NATURAL GAS 2.3 MMBTU/H 20% OPACIParticulate P LOW NOX 13.31 NATURAL GAS 2.3 MMBTU/H FUEL IS N Particulate P LOW NOX 13.31 PERMIT N Particulate N13.31 NATURAL GAS 0.3 MMBTU/H FUELS AREParticulate N13.31 NATURAL GAS 93 MMBTU/H SECOND FParticulate N REGULATO13.31 NATURAL GAS 0.4 MMLB/H STEAM Particulate P GOOD DES13.31 NATURAL GAS 8 MMBTU/H OTHER COMParticulate P NATURAL 13.31 NATURAL GAS 95 MMBTU/H Particulate P GOOD DES13.31 9 MMBTU/H THROUGHPParticulate N13.31 77 MMBTU/H PERMIT NUParticulate N13.31 NAT GAS 32.2 MMBTU/H Particulate P FUEL IS L13.31 NATURAL GAS 14 MMBTU/H Particulate N13.31 NATURAL GAS 84.4 MMBTU/H MFR. IS C Particulate N13.31 NATURAL GAS 51.08 MMBTU NATURAL Particulate P COMBUST13.31 NATURAL GAS Particulate P USE OF L13.31 NATURAL GAS 0 MANUFACTParticulate P LOW ASH 13.31 NATURAL GAS 22 MMBTU/H See RBLC IParticulate P CLEAN FU13.31 NAT GAS SHALL BE Particulate N NONE IND13.31 NATURAL GAS 42000 LB/H HOLDING CParticulate B BAGHOUSE13.31 NATURAL GAS 42000 LB/H HOLDING CParticulate N COMBUSTI13.31 NATURAL GAS 20.75 MMBTU/H EMISSION Particulate P GOOD COM13.31 NATURAL GAS 5.2 MMBTU/H COMPLIANCParticulate A VENTURI

13.31 NAT GAS Particulate N NONE IND13.31 NATURAL GAS 11 MMBTU/H (EACH) Particulate P CLEAN BU13.31 NATURAL GAS 44.1 MMBTU/H THROUGHPParticulate P CLEAN FU13.31 NATURAL GAS 44.1 MMBTU/H Particulate P NATURAL 13.31 NATURAL GAS 4 MMBTU/H Particulate P NATURAL 13.31 NATURAL GAS 83 MMBTU/H BOILER OPParticulate P EFFICIEN13.31 NATURAL GAS 15 MMBTU/HRTUNDISH Particulate P PERMIT LIMITATION IS USE OF NATURAL GAS OR PROPANE13.31 6 MMBTU/H THROUGHPParticulate P PERMIT LIMITATION IS USE OF NATURAL GAS.13.31 NATURAL GAS 40 MMBTU/H Particulate P GOOD COM13.31 NATURAL GAS 20.9 MMBTU/H This permit Particulate N13.31 NATURAL GAS 85.2 MMBTU/H Particulate N13.31 NATURAL GAS 27.5 MMBTU/H Particulate P GOOD COM13.31 NATURAL GAS 35 MMBTU/H AUXILARY Particulate P GOOD COMB13.31 NATURAL GAS 20 MMBTU/H CO limits aParticulate P USE OF L13.31 NATURAL GAS 44.1 MMBTU/H THESE (T Particulate P USE OF P13.31 NATURAL GAS 46 MMBTU/H NATURAL Particulate P GOOD COMB13.31 NATURAL GAS 10 MMBTU/H Particulate P GOOD COM13.31 NATURAL GAS 20 MMBTU/H Particulate P GOOD COM13.31 NATURAL GAS 80 MMBTU/H Auxiliary b Particulate N13.31 NATURAL GAS 48 MMBTU/H THROUGHPParticulate P USE OF L13.31 NATURAL GAS 62.77 MMBTU/H Particulate P NATURAL 13.31 NATURAL GAS 16 MMBTU/H THESE UNParticulate P FUEL LIM13.31 NATURAL GAS 40 MMBTU/H EMISSIONSParticulate B EXCLUSIVE USE OF NATURAL13.31 NATURAL GAS 30 MMBTU/H Operation lParticulate P NATURAL 13.31 NATURAL GAS 35 MMBTU/H Particulate P CLEAN FU13.31 NATURAL GAS 49 MMBTU/H Boiler is r Particulate N13.31 NATURAL GAS 30 MMBTU/H BOILER OPParticulate P USE OF L13.31 NATURAL GAS 31.4 MMBTU/H Operation lParticulate P NATURAL G13.31 NAT GAS 29.3 MMBTU/H 29.3 MMBTParticulate N13.31 NATURAL GAS 22 MMBTU/H Particulate P USE OF L13.31 NAT GAS 60 MMBTU/H Particulate N NONE IND13.31 NATURAL GAS 75 MMBTU/H CEMS, WHEParticulate N13.31 NATURAL GAS 35 MMBTU/H Particulate P NATURAL 13.31 NATURAL GAS 33.5 MMBTU/H CLEAVER BParticulate N13.31 NATURAL GAS 76 MMBTU/H Limited to Particulate N13.31 NATURAL GAS 83 MMBTU/H Auxiliary b Particulate P GOOD COM13.31 NAT GAS 65.5 MMBTU/H EMISSION Particulate P FIRED BY13.31 NATURAL GAS 0 Particulate P LOW ASH 13.31 Particulate N13.31 NATURAL GAS 3.3 MMBTU/H Particulate P GOOD COM13.31 NATURAL GAS 53 MMBTU/H Particulate P GOOD COM13.31 NATURAL GAS 20 MMBTU/H Particulate P GOOD COM13.31 NATURAL GAS 33 MMBTU/H Particulate P GOOD OPE13.31 NATURAL GAS 95 MMBTU/H Particulate N13.31 NATURAL GAS 54 MMBTU/H Particulate N13.31 NATURAL GAS 68 MMBTU/H Particulate N13.31 NATURAL GAS 93 MMBUT/H Particulate P USE OF N13.31 NATURAL GAS 12.84 MMBTU/H Each boilerParticulate N

13.31 NATURAL GAS 11.45 MMBTU/H Each fuel sParticulate N13.31 NATURAL GAS 33 MMBTU/H Particulate P LOW ASH 13.31 NATURAL GAS 33 MMBTU/H Emission li Particulate P NATURAL 13.31 NATURAL GAS 40 MMBTU/H Particulate P NATURAL 13.31 NATUAL GAS 48.69 MILLION CF/YR Particulate B GCP13.31 NATURAL GAS 33 MMBTU/H Particulate P GOOD COM13.31 NATURAL GAS 80 MMBTU/H one auxiliarParticulate P GOOD COM13.31 NATURAL GAS 99 MMBTU/H Particulate N13.31 NATURAL GAS 30 MMBTU/H throughput Particulate P CLEAN FU13.31 NATURAL GAS 34.4 MMBTU/H Throughput Particulate P NATURAL 13.31 NATURAL GAS 4.62 MMBTU/H INSTALLA Particulate N THE USE 13.31 NATURAL GAS 99 MMBTU/H 2 Auxiliary Particulate P CLEAN FU13.31 NATURAL GAS 6 MMBTU/H BOILERS Particulate N13.31 NATURAL GAS 26.5 MMBTU/H KEWANEE NParticulate N NO CONTRO13.31 NATURAL GAS Particulate N13.31 NATURAL GAS 31 MMBTU/H Particulate N NONE IND13.31 NATURAL GAS 31 MMBTU/H Particulate N NONE IND13.31 NATURAL GAS 15.8 MMBTU/H Particulate N NONE IND13.31 NATURAL GAS 16.4 MMBTU/H Natural GaParticulate P LOW ASH 13.31 NATURAL GAS 68 MMBTU/H Limited to Particulate P LOW ASH 13.31 NATURAL GAS 13.4 MMBUT/H Particulate N13.31 NAT GAS 12 MMBTU/H Particulate N NONE IND13.31 NAT GAS 2.5 MMBTU/H Particulate N NONE IND13.31 NAT GAS 32.5 MMBTU/H Particulate N NONE IND13.31 NAT GAS 3 MMBTU/H Particulate N NONE IND13.31 14.4 MMBTU/H Particulate P USE OF C13.31 25.2 MMBTU/H Particulate P USE OF C13.31 NATURAL GAS 50000 LB/H Throughput Particulate N13.31 NATURAL GAS 33 MMBTU/H Particulate P USE OF L13.31 NATURAL GAS 43.2 MMBTU/H One of two Particulate P GOOD COM13.31 NATURAL GAS 25 MMBTU/H VACUUM OParticulate N13.31 NATURAL GAS 9 MMBTU/H One naturalParticulate P LOW ASH 13.31 NATURAL GAS 36 mmbtu/h Particulate N13.31 NATURAL GAS 30.6 MMBTU/H THE MAXI Particulate N13.31 NATURAL GAS 41 MMBTU/H THIS BOILParticulate N13.31 NATURAL GAS 55.34 MMBTU/H THIS BOI Particulate N13.31 NATURAL GAS 34 MMBTU/H Throughput Particulate P COMPLIAN13.31 NATURAL GAS 70 MMBTU/H NATURAL Particulate N CLEAN FU13.31 NATURAL GAS 600 HP Throughput Particulate P CLEAN FU13.31 NATURAL GAS 0.03 MMDSCF/ THROUGH Particulate P NATURAL 13.31 NATURAL GAS 0.01 MMDSCF/ ADDITION Particulate P NATURAL 13.31 NATURAL GAS 1.4 mmbtu/h Particulate P NATURAL 13.31 NATURAL GAS 50 MMBTU/H BACT for Particulate P CLEAN FU13.31 NATURAL GAS 60 MMBTU/H Particulate P RESTRICT13.31 NATURAL GAS 50 MMBTU/H Particulate P GOOD COM13.31 NATURAL GAS 22 MMBTU/H ENTRY IN Particulate P NATURAL 13.31 NATURAL GAS 46.2 MMBTU/H NOT PSD Particulate P NATURAL 13.31 NATURAL GAS 97.1 MMBTU/H Particulate P NATURAL

13.31 NATURAL GAS 10 MMBTU/H GAS CONDParticulate P NATURAL 13.31 NATURAL GAS 0.75 MMBTU/H EMISSION Particulate P NATURAL 13.31 NATURAL GAS 38 MMBTU/H Particulate N13.31 NATURAL GAS 30.6 MMBTU/H LIMITS A Particulate N13.31 19 MMBTU/H Particulate P USE OF L13.31 NATURAL GAS 66.5 MMBTU/H OPERATINGParticulate P USE OF N13.31 90 MMBTU/H EA. Particulate P GOOD COM13.31 NATURAL GAS ENGINEERIParticulate P USE OF L13.31 NATURAL GAS 3.85 MMBTU/H THE UNIT' Particulate P GOOD COM13.31 NATURAL GAS 35.4 MMBTU/H THE BACTParticulate P USE OF N13.31 NATURAL GAS 20.4 MMBTU/H TWO BOILParticulate N13.31 NATURAL GAS 93.7 MMBTU/H PROJECT Particulate N13.31 NATURAL GAS 99 MMBTU/H THIS PRO Particulate N13.31 NATURAL GAS 27.2 MMBTU/H THIS PRO Particulate N13.31 NATURAL GAS 33.4 MMBTU eaTHIS PRO Particulate N13.31 NATURAL GAS 64.9 MMBtu eacTHIS PROCParticulate N13.31 Particulate N13.31 NATURAL GAS 99.5 MMBTU/H Sulfur DioxN NONE13.31 NATURAL GAS 50 MMBTU/H THE NUMBSulfur DioxP CLEAN FU13.31 NATURAL GAS 21 MMBTU/H THE BURNSulfur DioxP CLEAN FU13.31 NATURAL GAS 58.4 MMBTU/H THE BURNSulfur DioxP CLEAN FU13.31 FUEL OIL 0.3 MMBTU/H PERMIT NOSulfur DioxP LIMIT CH13.31 NATURAL GAS 2.3 MMBTU/H FUEL IS N Sulfur DioxN SO2 LIMIT13.31 PERMIT N Sulfur DioxN13.31 NATURAL GAS 96 MMBTU/H A SEPARASulfur DioxP THE SULF13.31 NATURAL GAS 13.4 MMBTU/H Sulfur DioxP CLEAN FU13.31 NATURAL GAS 11.7 MMBTU/H Sulfur DioxP CLEAN FU13.31 NATURAL GAS 93 MMBTU/H SECOND FSulfur DioxN REGULATO13.31 NATURAL GAS 8 MMBTU/H OTHER COMSulfur DioxP NATURAL GAS FUEL. PERMIT LI13.31 NAT GAS 32.2 MMBTU/H Sulfur DioxP FUEL IS L13.31 NATURAL GAS 52.8 MMBTU/H MAXIMUM Sulfur DioxP HYDROGEN13.31 NATURAL GAS 5 MMBTU/H MAXIMUM Sulfur DioxP HYDROGEN13.31 NATURAL GAS 1.05 MMBTU/H SECOND FUSulfur DioxP HYDROGEN13.31 NATURAL GAS 0.5 MMBTU/H MAXIMUM OSulfur DioxP HYDROGEN13.31 NATURAL GAS 0.63 MMBTU/H MAXIMUM OSulfur DioxP HYDROGEN13.31 NATURAL GAS 1.06 MMBTU/H MAXIMUM OSulfur DioxP HYDROGEN13.31 NATURAL GAS 6.3 MMBTU/H PERMIT LISulfur DioxP HYDROGEN13.31 NATURAL GAS 3.5 MMBTU/H UNITS 208Sulfur DioxP HYDROGEN13.31 NATURAL GAS 4.2 MMBTU/H THE SOURSulfur DioxP HYDROGEN13.31 NATURAL GAS 84.4 MMBTU/H MFR. IS C Sulfur DioxN NONE LIS13.31 NATURAL GAS 96 MMBTU/H Sulfur DioxP NATURAL G13.31 NATURAL GAS Sulfur DioxP USE OF N13.31 NAT GAS SHALL BE Sulfur DioxN NONE IND13.31 FUEL GAS 65.6 MMBTU/H PERMIT I Sulfur DioxP USE ONLY FUEL GAS WITH A 13.31 FUEL GAS 65.6 MMBTU/H PERMIT I Sulfur DioxP USE ONLY FUEL GAS WITH A 13.31 NATURAL GAS 54.01 MMBTU/H WILL BE Sulfur DioxP FUEL SPE13.31 NATURAL GAS 42000 LB/H HOLDING CSulfur DioxN COMBUSTI13.31 NATURAL GAS 26.6 MMBTU/H PROCESS Sulfur DioxP NATURAL G

13.31 NATURAL GAS 8.36 MMBTU/H THREE PRSulfur DioxP USE NATU13.31 NATURAL GAS 100 HP THE OWNESulfur DioxP USE NATU13.31 NAT GAS Sulfur DioxN NONE IND13.31 NATURAL GAS 11 MMBTU/H (EACH) Sulfur DioxP LOW SULF13.31 NATURAL GAS 44.1 MMBTU/H THROUGHPSulfur DioxP LOW SULF13.31 NATURAL GAS 83 MMBTU/H BOILER OPSulfur DioxN13.31 NATURAL GAS 15 MMBTU/HRTUNDISH Sulfur DioxP PERMIT LIMITATION IS NATURAL GAS OR PROPANE USAGE13.31 NATURAL GAS 40 MMBTU/H Sulfur DioxP GOOD COM13.31 NATURAL GAS 85.2 MMBTU/H Sulfur DioxP LOW S NAT13.31 NATURAL GAS 11 MMBTU/H USED FORSulfur DioxP CLEAN FU13.31 NATURAL GAS 35 MMBTU/H AUXILARY Sulfur DioxP LOW SULFU13.31 NATURAL GAS 44.1 MMBTU/H THESE (T Sulfur DioxP USE OF P13.31 NATURAL GAS 46 MMBTU/H NATURAL Sulfur DioxP NATURAL G13.31 NATURAL GAS 35 MMBTU/H 35 MMBTUSulfur DioxP BURN NAT13.31 NAT GAS 14.4 MMBTU/H EACH Sulfur DioxP USE FUEL13.31 NAT GAS 29 MMBTU/H 29 MMBTUSulfur DioxP BURN NAT13.31 NATURAL GAS 10 MMBTU/H Sulfur DioxP GOOD COM13.31 NATURAL GAS 20 MMBTU/H Sulfur DioxP GOOD COM13.31 NATURAL GAS 80 MMBTU/H Auxiliary b Sulfur DioxN13.31 NATURAL GAS 48 MMBTU/H THROUGHPSulfur DioxP USE OF P13.31 NATURAL GAS 35 MMBTU/H Sulfur DioxP GOOD COM13.31 NATURAL GAS 49 MMBTU/H Boiler is r Sulfur DioxP THE MAXI13.31 NATURAL GAS 30 MMBTU/H BOILER OPSulfur DioxP USE OF N13.31 NATURAL GAS 31.4 MMBTU/H Operation lSulfur DioxP NATURAL G13.31 NAT GAS 29.3 MMBTU/H 29.3 MMBTSulfur DioxN13.31 NATURAL GAS 16 MMBTU/H FUEL GASSulfur DioxP NATURAL 13.31 NATURAL GAS 22 MMBTU/H Sulfur DioxP USE OF P13.31 PROPANE 13 MMBTU/H LIMESTONSulfur DioxP USING PR13.31 NAT GAS 60 MMBTU/H Sulfur DioxN NONE IND13.31 NATURAL GAS 91.2 MMBTU/H Restriction Sulfur DioxN13.31 NATURAL GAS 37 MMBTU/H Baghouse wiSulfur DioxN13.31 NATURAL GAS 21 MMBTU/H Sulfur DioxP LOW SULF13.31 NATURAL GAS 35 MMBTU/H Sulfur DioxP NATURAL 13.31 NATURAL GAS 76 MMBTU/H Limited to Sulfur DioxN LOW SULFU13.31 NAT GAS 65.5 MMBTU/H EMISSION Sulfur DioxP FIRING N13.31 Sulfur DioxP FUEL REST13.31 NATURAL GAS 33 MMBTU/H Sulfur DioxP FUELS LIMIT: < 2 GR/100 DSCF13.31 NATURAL GAS 12.84 MMBTU/H Each boilerSulfur DioxP THE MAXI13.31 NATURAL GAS 11.45 MMBTU/H Each fuel sSulfur DioxP THE MAXI13.31 NATURAL GAS 33 MMBTU/H Emission li Sulfur DioxP NATURAL 13.31 NATURAL GAS 33.5 MMBTU/H Boiler is a Sulfur DioxP CLEAN FUE13.31 NATURAL GAS 99 MMBTU/H Sulfur DioxN13.31 NATURAL GAS 34.4 MMBTU/H Throughput Sulfur DioxP BACT IS USE OF NATURAL GA13.31 NATURAL GAS 4.62 MMBTU/H INSTALLA Sulfur DioxN LOW SULF13.31 NATURAL GAS 99 MMBTU/H 2 Auxiliary Sulfur DioxP LOW SULF13.31 NATURAL GAS 6 MMBTU/H BOILERS Sulfur DioxN13.31 NATURAL GAS 26.5 MMBTU/H KEWANEE NSulfur DioxN EMISSION 13.31 NATURAL GAS Sulfur DioxN

13.31 NATURAL GAS Sulfur DioxN13.31 NATURAL GAS 31 MMBTU/H Sulfur DioxP FUEL GAS13.31 NATURAL GAS 31 MMBTU/H Sulfur DioxP FUEL GAS13.31 NATURAL GAS 15.8 MMBTU/H Sulfur DioxP FUEL GAS13.31 NATURAL GAS 16.4 MMBTU/H Natural GaSulfur DioxP LOW SULF13.31 NATURAL GAS 68 MMBTU/H Limited to Sulfur DioxP LOW SULF13.31 NATURAL GAS 13.4 MMBUT/H Sulfur DioxN13.31 NATURAL GAS 5 MMBTU/H Sulfur DioxP FUEL SULFUR LIMIT: 0.8 GR/113.31 NAT GAS 12 MMBTU/H Sulfur DioxN NONE IND13.31 NAT GAS 2.5 MMBTU/H Sulfur DioxN NONE IND13.31 NAT GAS 32.5 MMBTU/H Sulfur DioxN NONE IND13.31 NAT GAS 3 MMBTU/H Sulfur DioxN NONE IND13.31 NATURAL GAS 33 MMBTU/H Sulfur DioxP BACT IS U13.31 NATURAL GAS 43.2 MMBTU/H One of two Sulfur DioxB CONTINUO13.31 NATURAL GAS 25 MMBTU/H VACUUM OSulfur DioxN13.31 NATURAL GAS 9 MMBTU/H One naturalSulfur DioxP LOW SULF13.31 NATURAL GAS 36 mmbtu/h Sulfur DioxN13.31 NATURAL GAS 30.6 MMBTU/H THE MAXI Sulfur DioxN13.31 NATURAL GAS 41 MMBTU/H THIS BOILSulfur DioxN13.31 NATURAL GAS 55.34 MMBTU/H THIS BOI Sulfur DioxN13.31 NATURAL GAS 34 MMBTU/H Throughput Sulfur DioxP COMPLIAN13.31 NATURAL GAS 70 MMBTU/H NATURAL Sulfur DioxP LOW SULF13.31 NATURAL GAS 0.03 MMDSCF/ THROUGH Sulfur DioxP LOW-SULF13.31 NATURAL GAS 0.01 MMDSCF/ ADDITION Sulfur DioxP LOW-SULF13.31 NATURAL GAS 1.4 mmbtu/h Sulfur DioxP LOW-SULF13.31 NATURAL GAS 60 MMBTU/H Sulfur DioxP USE OF L13.31 NATURAL GAS 50 MMBTU/H Sulfur DioxP GOOD COM13.31 NATURAL GAS 143 MMBTU/H Sulfur DioxN13.31 NATURAL GAS 6.8 MMBTU/H Sulfur DioxN13.31 NATURAL GAS 40 MMBTU/H AUXILIARYSulfur DioxP LOW SULFUR FUEL 0.8 GR/SC13.31 NATURAL GAS 22 MMBTU/H ENTRY IN Sulfur DioxP NATURAL 13.31 NATURAL GAS 46.2 MMBTU/H NOT PSD Sulfur DioxP NATURAL 13.31 NATURAL GAS 97.1 MMBTU/H Sulfur DioxP NATURAL 13.31 NATURAL GAS 10 MMBTU/H GAS CONDSulfur DioxP NATURAL 13.31 NATURAL GAS 0.75 MMBTU/H EMISSION Sulfur DioxP NATURAL 13.31 NATURAL GAS 38 MMBTU/H Sulfur DioxN13.31 NATURAL GAS 30.6 MMBTU/H LIMITS A Sulfur DioxP THE MAXI13.31 19 MMBTU/H Sulfur DioxP USE OF L13.31 NATURAL GAS 66.5 MMBTU/H OPERATINGSulfur DioxP USE OF N13.31 NATURAL GAS 34 MMBTU/H Sulfur DioxP LIMIT SU13.31 NATURAL GAS 14.87 MMBTU/H Sulfur DioxP LIMIT SU13.31 NATURAL GAS 1.34 MMBTU/H Sulfur DioxP LIMIT SU13.31 NATURAL GAS 3.85 MMBTU/H THE UNIT' Sulfur DioxP LOW-SULF13.31 NATURAL GAS 20.4 MMBTU/H TWO BOILSulfur DioxN13.31 NATURAL GAS 95 MMBTU/H Sulfur DioxN13.31 NATURAL GAS 98.7 MMBTU/H Sulfur DioxN13.31 NATURAL GAS 93.7 MMBTU/H PROJECT Sulfur DioxN13.31 NATURAL GAS 99 MMBTU/H THIS PRO Sulfur DioxN

13.31 NATURAL GAS 27.2 MMBTU/H THIS PRO Sulfur DioxN13.31 NATURAL GAS 33.4 MMBTU eaTHIS PRO Sulfur DioxN13.31 NATURAL GAS 64.9 MMBtu eacTHIS PROCSulfur DioxN13.31 NATURAL GAS 31.5 MMBTU/H ARB RECORSulfur Oxi N NO BACT L13.31 6 MMBTU/H THROUGHPSulfur Oxi P PERMIT LIMITATION IS USE OF NATURAL GAS.13.31 NATURAL GAS 27.5 MMBTU/H Sulfur Oxi P USE OF N13.31 NATURAL GAS 33.5 MMBTU/H CLEAVER BSulfur Oxi P LOW SULF13.31 NATURAL GAS 35.4 MMBTU/H THE BACTSulfur Oxi P USE OF N13.31 NATURAL GAS 97.1 MMBTU/H Sulfur Trio P NATURAL 13.31 NATURAL GAS 70 MMBTU/H NATURAL Sulfuric AciP LOW SULF13.31 NATURAL GAS 0.75 MMBTU/H EMISSION Sulfuric AciP NATURAL 13.31 NATURAL GAS 99.5 MMBTU/H Total Susp N13.31 FUEL OIL 0.3 MMBTU/H PERMIT NOTotal Susp P LOW NOX/13.31 NATURAL GAS 2.3 MMBTU/H BOILER BUTotal Susp P LOW NOX 13.31 NATURAL GAS 2.3 MMBTU/H 20% OPACITotal Susp P LOW NOX 13.31 NATURAL GAS 2.3 MMBTU/H FUEL IS N Total Susp P LOW NOX 13.31 PERMIT N Total Susp N13.31 NATURAL GAS 0.3 MMBTU/H FUELS ARETotal Susp N13.31 NATURAL GAS 4.62 MMBTU/H INSTALLA Total Susp N13.31 NATURAL GAS 96 MMBTU/H A SEPARAVisible EmiN N/A13.31 NATURAL GAS 8 MMBTU/H OTHER COMVisible EmiN13.31 NATURAL GAS 28 MMBTU/H See separatVisible EmiN13.31 NATURAL GAS 75 MMBTU/H HOT OIL HVisible EmiN13.31 NATURAL GAS 14 MMBTU/H Visible EmiN13.31 NATURAL GAS 52.8 MMBTU/H MAXIMUM Visible EmiN NONE IND13.31 NATURAL GAS 5 MMBTU/H MAXIMUM Visible EmiN NONE IND13.31 NATURAL GAS 1.05 MMBTU/H SECOND FUVisible EmiN NONE INDICATED.13.31 NATURAL GAS 0.5 MMBTU/H MAXIMUM OVisible EmiP GOOD OPE13.31 NATURAL GAS 0.63 MMBTU/H MAXIMUM OVisible EmiP GOOD OPE13.31 NATURAL GAS 1.06 MMBTU/H MAXIMUM OVisible EmiP GOOD OPERATIONS PRACTICES.13.31 NATURAL GAS 6.3 MMBTU/H PERMIT LIVisible EmiP GOOD OPE13.31 NATURAL GAS 3.5 MMBTU/H UNITS 208Visible EmiP GOOD OPE13.31 NATURAL GAS 4.2 MMBTU/H THE SOURVisible EmiP GOOD OPE13.31 FUEL GAS 65.6 MMBTU/H PERMIT I Visible EmiN NONE IND13.31 FUEL GAS 65.6 MMBTU/H PERMIT I Visible EmiN NONE IND13.31 NATURAL GAS 8.36 MMBTU/H THREE PRVisible EmiN NONE IND13.31 NATURAL GAS 100 HP THE OWNEVisible EmiN NONE IND13.31 5 MMBTU/H SPACE HEVisible EmiN13.31 NAT GAS Visible EmiN NONE IND13.31 NATURAL GAS 11 MMBTU/H (EACH) Visible EmiP GOOD COM13.31 NATURAL GAS 20.9 MMBTU/H This permit Visible EmiN13.31 NATURAL GAS 85.2 MMBTU/H Visible EmiN13.31 NATURAL GAS 11 MMBTU/H USED FORVisible EmiP CLEAN FU13.31 NATURAL GAS 35 MMBTU/H 35 MMBTUVisible EmiN13.31 NAT GAS 14.4 MMBTU/H EACH Visible EmiN13.31 NAT GAS 29 MMBTU/H 29 MMBTUVisible EmiN13.31 NATURAL GAS 80 MMBTU/H Auxiliary b Visible EmiN13.31 NATURAL GAS 35 MMBTU/H Visible EmiP CLEAN FU

13.31 NATURAL GAS 49 MMBTU/H Boiler is r Visible EmiN13.31 PROPANE 13 MMBTU/H LIMESTONVisible EmiA ESP AND 13.31 NAT GAS 60 MMBTU/H Visible EmiN NONE IND13.31 NATURAL GAS 91.2 MMBTU/H Restriction Visible EmiN13.31 NATURAL GAS 5.6 MMBTU/H Limited to Visible EmiN13.31 NATURAL GAS 76 MMBTU/H Limited to Visible EmiN13.31 NATURAL GAS 68 MMBTU/H Visible EmiN13.31 NATURAL GAS 12.84 MMBTU/H Each boilerVisible EmiN13.31 NATURAL GAS 11.45 MMBTU/H Each fuel sVisible EmiN13.31 NATURAL GAS 33.5 MMBTU/H Boiler is a Visible EmiN13.31 NATURAL GAS 30 MMBTU/H throughput Visible EmiN13.31 NATURAL GAS 34.4 MMBTU/H Throughput Visible EmiP NATURAL 13.31 NATURAL GAS 31.4 MMBTU/H HOURS OFVisible EmiP GOOD COM13.31 NATURAL GAS 2.4 MMBTU/H Startup gasVisible EmiN13.31 NATURAL GAS 55.3 MMBTU/H OperationalVisible EmiN13.31 NATURAL GAS 83 MMBTU/H THE BOILEVisible EmiN13.31 NATURAL GAS 25 MMBTU/H VACUUM OVisible EmiN13.31 NATURAL GAS 5.4 MMBTU/H natural gasVisible EmiN13.31 NATURAL GAS 30.6 MMBTU/H THE MAXI Visible EmiN13.31 NATURAL GAS 38 MMBTU/H Visible EmiN13.31 NATURAL GAS 20.4 MMBTU/H TWO BOILVisible EmiN13.31 NATURAL GAS 93.7 MMBTU/H PROJECT Visible EmiN13.31 NATURAL GAS 99.5 MMBTU/H Volatile O N NONE13.31 NATURAL GAS 50 MMBTU/H THE NUMBVolatile O N13.31 NATURAL GAS 21 MMBTU/H THE BURNVolatile O N13.31 NATURAL GAS 58.4 MMBTU/H THE BURNVolatile O N13.31 FUEL OIL 0.3 MMBTU/H PERMIT NOVolatile O P LOW NOX/13.31 NATURAL GAS 2.3 MMBTU/H BOILER BUVolatile O P LOW NOX 13.31 NATURAL GAS 2.3 MMBTU/H 20% OPACIVolatile O P LOW NOX B13.31 NATURAL GAS 2.3 MMBTU/H FUEL IS N Volatile O P LOW NOX 13.31 PERMIT N Volatile O N13.31 NATURAL GAS 0.3 MMBTU/H FUELS AREVolatile O N13.31 NATURAL GAS 93 MMBTU/H SECOND FVolatile O N REGULATO13.31 NAT GAS 32.2 MMBTU/H Volatile O N NONE IND13.31 NATURAL GAS 84.4 MMBTU/H MFR. IS C Volatile O N NONE LIS13.31 NATURAL GAS 96 MMBTU/H Volatile O P EMISSION13.31 NATURAL GAS Volatile O P BOILER D13.31 NATURAL GAS 2.75 MMBTU/H ARB RECOVolatile O N13.31 NATURAL GAS 31.5 MMBTU/H ARB RECORVolatile O N NO BACT 13.31 NATURAL GAS 22 MMBTU/H See RBLC IVolatile O P COMBUST13.31 NAT GAS SHALL BE Volatile O A THE WAST13.31 NAT GAS SHALL BE Volatile O N NONE IND13.31 NATURAL GAS 54.01 MMBTU/H WILL BE Volatile O N NONE IND13.31 NATURAL GAS 42000 LB/H HOLDING CVolatile O N COMBUSTI13.31 NATURAL GAS 26.6 MMBTU/H PROCESS Volatile O P COMBUSTI13.31 NATURAL GAS 10 MMBTU/H THIS BOILVolatile O P BACT FOR VOC IS DETERMINED TO BE USE OF NATURAL GAS TO FUEL BOILER. NO EMISSION RATE LI13.31 5 MMBTU/H SPACE HEVolatile O P BACT FOR VOC IS DETERMINED TO BE GOOD COMBUSTION CONTROL AND THE USE OF NATURAL GAS 13.31 NAT GAS Volatile O N NONE IND

13.31 NATURAL GAS 44.1 MMBTU/H THROUGHPVolatile O P CLEAN FU13.31 NATURAL GAS 44.1 MMBTU/H Volatile O P GOOD COM13.31 NATURAL GAS 83 MMBTU/H BOILER OPVolatile O P EFFICIEN13.31 NATURAL GAS 40 MMBTU/H Volatile O P GOOD COM13.31 NATURAL GAS 20.9 MMBTU/H This permit Volatile O N13.31 NATURAL GAS 85.2 MMBTU/H Volatile O N13.31 NATURAL GAS 27.5 MMBTU/H Volatile O P GOOD COM13.31 NATURAL GAS 35 MMBTU/H AUXILARY Volatile O P GOOD COMB13.31 NATURAL GAS 20 MMBTU/H CO limits aVolatile O N13.31 NATURAL GAS 44.1 MMBTU/H THESE (T Volatile O P GOOD CO13.31 NATURAL GAS 46 MMBTU/H NATURAL Volatile O P GOOD COMB13.31 NATURAL GAS 10 MMBTU/H Volatile O P GOOD COM13.31 NATURAL GAS 20 MMBTU/H Volatile O P GOOD COM13.31 NATURAL GAS 80 MMBTU/H Auxiliary b Volatile O N13.31 NATURAL GAS 48 MMBTU/H THROUGHPVolatile O P COMBUST13.31 NATURAL GAS 62.77 MMBTU/H Volatile O P GOOD COM13.31 NATURAL GAS 40 MMBTU/H EMISSIONSVolatile O B EXCLUSIVE USE OF NATURAL 13.31 NATURAL GAS 30 MMBTU/H Operation lVolatile O P EFFICIEN13.31 NATURAL GAS 35 MMBTU/H Volatile O P CLEAN FU13.31 NATURAL GAS 49 MMBTU/H Boiler is r Volatile O N13.31 NATURAL GAS 30 MMBTU/H BOILER OPVolatile O N13.31 NATURAL GAS 31.4 MMBTU/H Operation lVolatile O P EFFICIEN13.31 NAT GAS 29.3 MMBTU/H 29.3 MMBTVolatile O N13.31 NATURAL GAS 16 MMBTU/H FUEL GASVolatile O P GOOD COM13.31 PROPANE 13 MMBTU/H LIMESTONVolatile O P COMBUST13.31 NAT GAS 60 MMBTU/H Volatile O N NONE IND13.31 NATURAL GAS 91.2 MMBTU/H Restriction Volatile O N13.31 NATURAL GAS 37 MMBTU/H Baghouse wiVolatile O N13.31 NATURAL GAS 21 MMBTU/H Volatile O P GOOD COM13.31 NATURAL GAS 35 MMBTU/H Volatile O P GOOD CO13.31 NATURAL GAS 90 MMBTU/H Source has Volatile O N13.31 NATURAL GAS 50 MMBTU/H Source not Volatile O N13.31 NATURAL GAS 21 MMBTU/H Source is nVolatile O N13.31 NATURAL GAS 76 MMBTU/H Limited to Volatile O N13.31 NATURAL GAS 83 MMBTU/H Auxiliary b Volatile O P GOOD COM13.31 NATURAL GAS 5 MMBTU/H,EQUIP: , Volatile O N13.31 NATURAL GAS 31 MMBTU/H Volatile O N COMBUST13.31 NATURAL GAS 0 Volatile O P GOOD COM13.31 Volatile O N13.31 NATURAL GAS 33 MMBTU/H Volatile O P GOOD OPE13.31 NATURAL GAS 93 MMBUT/H Volatile O P BOILER D13.31 NATURAL GAS 12.84 MMBTU/H Each boilerVolatile O N13.31 NATURAL GAS 11.45 MMBTU/H Each fuel sVolatile O N13.31 NATURAL GAS 33 MMBTU/H Volatile O P BOILER D13.31 NATURAL GAS 33 MMBTU/H Emission li Volatile O P CLEAN FU13.31 NATURAL GAS 40 mmbtu/h Volatile O P GOOD COM13.31 NATURAL GAS 40 MMBTU/H Volatile O P GOOD COM13.31 NATUAL GAS 48.69 MILLION CF/YR Volatile O B GCP

13.31 NATURAL GAS 33 MMBTU/H Volatile O P GOOD COM13.31 NATURAL GAS 80 MMBTU/H one auxiliarVolatile O P GOOD COM13.31 NATURAL GAS 99 MMBTU/H Volatile O N13.31 NATURAL GAS 34.4 MMBTU/H Throughput Volatile O P BACT FOR VOC EMISSIONS FR13.31 NATURAL GAS 4.62 MMBTU/H INSTALLA Volatile O N GOOD COM13.31 NATURAL GAS 31.4 MMBTU/H HOURS OFVolatile O P GOOD COM13.31 NATURAL GAS 99 MMBTU/H 2 Auxiliary Volatile O P GOOD COM13.31 NATURAL GAS 6 MMBTU/H BOILERS Volatile O N13.31 NATURAL GAS 31 MMBTU/H Volatile O N NONE IND13.31 NATURAL GAS 31 MMBTU/H Volatile O N NONE IND13.31 NATURAL GAS 15.8 MMBTU/H Volatile O N NONE IND13.31 NATURAL GAS 16.4 MMBTU/H Natural GaVolatile O N13.31 NATURAL GAS 68 MMBTU/H Limited to Volatile O A CATALYTI13.31 NATURAL GAS 13.4 MMBUT/H Volatile O N13.31 NATURAL GAS 1700 MMCF/rolli THE INCR Volatile O N13.31 NAT GAS 12 MMBTU/H Volatile O N NONE IND13.31 NAT GAS 2.5 MMBTU/H Volatile O N NONE IND13.31 NAT GAS 32.5 MMBTU/H Volatile O N NONE IND13.31 NAT GAS 3 MMBTU/H Volatile O N NONE IND13.31 NATURAL GAS 7.7 MMBTU/H Volatile O P GOOD COM13.31 NATURAL GAS 33 MMBTU/H Volatile O P BOILER D13.31 NATURAL GAS 83 MMBTU/H THE BOILEVolatile O N13.31 NATURAL GAS 43.2 MMBTU/H One of two Volatile O P GOOD COM13.31 NATURAL GAS 25 MMBTU/H VACUUM OVolatile O N13.31 NATURAL GAS 9 MMBTU/H One naturalVolatile O P GOOD COM13.31 NATURAL GAS 36 mmbtu/h Volatile O N13.31 NATURAL GAS 30.6 MMBTU/H THE MAXI Volatile O N13.31 NATURAL GAS 41 MMBTU/H THIS BOILVolatile O N13.31 NATURAL GAS 55.34 MMBTU/H THIS BOI Volatile O N13.31 9.6 MMBTU/H DRYER ASVolatile O P GOOD COM13.31 NATURAL GAS 34 MMBTU/H Throughput Volatile O P COMPLIAN13.31 NATURAL GAS 70 MMBTU/H NATURAL Volatile O P GOOD CO13.31 NATURAL GAS 60 MMBTU/H NATURAL Volatile O P NATURAL 13.31 NATURAL GAS 80 MMBTU/H NAT. GAS Volatile O P NAT. GAS13.31 NATURAL GAS 11 MMBTU/H Volatile O P NATURAL 13.31 NATURAL GAS 34 MMBTU/H Volatile O P NATURAL 13.31 NATURAL GAS 600 HP Throughput Volatile O P MAINTENA13.31 NATURAL GAS 60 MMBTU/H Volatile O B EFFECTIV13.31 NATURAL GAS 45 MMBTU/H TWO HOT Volatile O P GOOD COM13.31 NATURAL GAS 32 MMBTU/H STACK S31Volatile O P USE OF NA13.31 NATURAL GAS 32 MMBTU/H STACK S32Volatile O P USE OF NA13.31 NATURAL GAS 143 MMBTU/H Volatile O N13.31 NATURAL GAS 6.8 MMBTU/H Volatile O N13.31 NATURAL GAS 40 MMBTU/H AUXILIARYVolatile O P GOOD COM13.31 NATURAL GAS 22 MMBTU/H ENTRY IN Volatile O P NATURAL 13.31 NATURAL GAS 13.3 MMBTU/H DRYER ASVolatile O P GOOD COM13.31 NATURAL GAS 97.1 MMBTU/H Volatile O P NATURAL 13.31 NATURAL GAS 10 MMBTU/H GAS CONDVolatile O P NATURAL

13.31 NATURAL GAS 0.75 MMBTU/H EMISSION Volatile O P NATURAL 13.31 NATURAL GAS 38 MMBTU/H Volatile O N13.31 NATURAL GAS COMBUSTIVolatile O P GOOD COMBUSTION DESIGN F13.31 NATURAL GAS 30.6 MMBTU/H LIMITS A Volatile O N13.31 19 MMBTU/H Volatile O P GOOD COM13.31 NATURAL GAS 66.5 MMBTU/H OPERATINGVolatile O P USE OF N13.31 NATURAL GAS SEVEN VAPVolatile Organic Com NATURAL 13.31 NATURAL GAS ONE 1.3 Volatile O P BURN NAT13.31 NATURAL GAS ENGINEERIVolatile O P GOOD COM13.31 NATURAL GAS 3.85 MMBTU/H THE UNIT' Volatile O P GOOD CO13.31 NATURAL GAS 35.4 MMBTU/H THE BACTVolatile O P GOOD COM13.31 NATURAL GAS 33.5 MMBTU/h Volatile O N13.31 NATURAL GAS 20.4 MMBTU/H TWO BOILVolatile O N13.31 NATURAL GAS 95 MMBTU/H Volatile O N13.31 NATURAL GAS 98.7 MMBTU/H Volatile O N13.31 NATURAL GAS 93.7 MMBTU/H PROJECT Volatile O A ROUTE PR13.31 NATURAL GAS 99 MMBTU/H THIS PRO Volatile O N13.31 NATURAL GAS 27.2 MMBTU/H THIS PRO Volatile O N13.31 NATURAL GAS 33.4 MMBTU eaTHIS PRO Volatile O N13.31 NATURAL GAS 64.9 MMBtu eacTHIS PROCVolatile O N

EMISLIMITEMISLIMITEMISLIMI EMISLIMITEMISLIMITEMISLIMI STDEMISSLSTDUNITLI7.2 LB/H 40 LB/MMCF 4 LB/MMBTU

0.05 LB/MMBTU 0.05 LB/MMBTU36 LB/H 200 LB/MMCF 20 LB/MMBTU

0.15 LB/MMBTU 0.15 LB/MMBTU6.72 LB/H 37.33 LB/MMCF 3.73 LB/MMBTU

LOW SULFUR REFINERY FUEL SEE NOTELOW SULFUR REFINERY GAS SEE NOTE

20 % OPACITY 20 % OPACITY0.5 LB/H 3 LB/MMCF

LOW NOX 0.08 LB/MMBTU 0.08COMBUST 0.1 LB/MMBTU 0.1LOW SULF 0.0013 LB/MMBTU 0.0013LOW ASH 0.015 LB/MMBTU 0.015GOOD CO 0.02 LB/MMBTU 0.02LOW SULF 0.15 E-3 LB/M SEE POLLUTANT NOTES

0.12 LB/H 0.52 T/YRVAPOR TREATMENT SYSTEM. NO EMISSION RATE LIMITS PROVIDED.

5 PPMVD @ 3% O25 PPMVD at 3% O25 NH3PPMVD15-MIN

5.1 LB/H 22.34 T/YR5 PPMVD Corrected to 3% O2

3.41 E-7 LB/H EACH1.4 E-7 LB/H

0.061 LB/MMBTU 5.8 LB/HGOOD COMBUSTION PRACTICES

3.6 LB/H 0.036 LB/MMBTU 0.036 LB/MMBTU0.1139 LB/MMBTU 0 0.1139 LB/MMBTU0.2142 LB/MMBTU 0 0.2142 LB/MMBTU0.1139 LB/MMBTU 0 0.1139 LB/MMBTU

10.6 LB/H 0 0 LB/MMBTU1.3 LB/H 5.7 T/YR 4.3 LB/MMBTU9.9 LB/H 43.36 T/YR 4.3 LB/MMBTU9.9 LB/H 43.36 T/YR 4.3 LB/MMBTU9.9 LB/H 43.36 T/YR 4.3 LB/MMBTU

0.53 LB/H 2.3 T/YR 0.034 LB/MMBTU1.3 LB/H 5.7 T/YR 4.3 LB/MMBTU

3.19 LB/H 0.034 LB/MMBTU2.09 LB/H 8.24 T/YR 0

0.1 LB/MMBTU 5.03 LB/HR 0.1 LB/MMBTU83.93 LB/H

5.7 LB/H HOURLY 24.97 T/YR ANNUAL M 0.06 LB/MMBTU0.4 LB/H HOURLY 1.75 T/YR ANNUAL M 0.044 LB/MMBTU6.8 LB/H 29.9 T/YR, FRESH AIR M 0.08 LB/MMBTU

0.04 LB/MMBTU 0 00.04 LB/MMBTU 0 0

1 LB/H 0.036 LB/MMBTU

0.074 MMBTU/H 0.074 MMBTU/H35 LB/MMSCF 0.42 LB/H 0.013 LB/MMBTU

1.2 LB/H 5.3 T/YR 0.086 LB/MMBTU3 LB/H 37 PPMVD @ 7% O2 0.036 LB/MMBTU

0.09 LB/MMBTU 0.09 LB/MMBTU0.09 LB/MMBTU 0.2 T/YR 0.09 LB/MMBTU

50 PPMVD @ 3% O2 0.3 LB/MMBTU100 PPMVD Corrected to 3% O2 0.074 LB/MMBTU7.7 LB/H 100 PPM @ 15% O2 0.08 LB/MMBTU

0.082 LB/MMBTU 0.082 LB/MMBTU0.348 LB/MMBTU 0.348 LB/MMBTU

50 PPMVD @ 3% O2 0.037 LB/MMBTU100 PPMVD @ 3% O2 0.075 LB/MMBTU

50 PPMVD at 3% O2 0.037 LB/MMBTU50 PPMVD @ 15-MIN AVG10 PPMVD Corrected to 3% O2 0.074 LB/MMBTU

100 PPMVD @ 15 MIN AVG 0.07 LB/MMBTU50 PPMVD Corrected to 3% O2 0.037 LB/MMBTU81 LB/H 247 T/YR50 PPMVD Corrected to 3% O2 0.037 LB/MMBTU

400 PPMVD Corrected to 3% O2 0.3 LB/MMBTU0.173 LB/MMBTU 0.173 LB/MMBTU

100 PPMVD Corrected to 3% O2 0.074 LB/MMBTU50 PPMVD Corrected to 3% O2 0.037 LB/MMBTU

100 PPMVD Corrected to 3% O2 0.074 LB/MMBTU50 PPMV @ 315 MIN AVG 0.06 LB/MMBTU50 PPM @ 3%15 MINUT 322 LB/MO 0.037 LB/MMBTU

0.07 LB/MMBTU 0.07 LB/MMBTU0.07 LB/MMBTU 0.07 LB/MMBTU4.45 LB/H 0.39 T/YR 0.08 LB/MMBTU100 PPMVD Corrected to 3% O2 0.074 LB/MMBTU

4 LB/H 0.15 LB/MMBTU1.66 LB/H 5.82 T/YR 0.08 LB/MMBTU

50 PPMVD Corrected to 3% O2 0.037 LB/MMBTU50 PPMVD@315 MIN

13.4 T/YR 13 LB/H 0.17 LB/MMBTUBACT FOR CO IS DETERMINED TO BE GOOD COMBUSTION CONTROL AND THE USE OF NATURAL GAS TOBACT FOR CO IS DETERMINED TO BE GOOD COMBUSTION CONTROL AND THE USE OF NATURAL GAS T

50 PPMVD 3% O20.57 LB/H 2.5 T/YR1.04 LB/H EACH0.15 LB/MMBTU 6.7 LB/H 0.15 LB/MMBTU

6.6 LB/H 0.022 LB/MMBTU0.3 LB/H combined 1.2 T/YR combined

0.085 LB/MMBTU 7.02 LB/H 0.085 LB/MMBTUPERMIT LIMITATION IS NATURAL GAS OR PROPANE USAGEPERMIT LIMITATION IS USE OF NATURAL GAS.

0.08 LB/MMBTU 3.2 LB/H 0.08 LB/MMBTU

0.23 LB/H each 1.01 T/YR each 0.011 LB/MMBTU6.3 LB/H 27.6 T/YR 0.074 LB/MMBTU

0.084 LB/MMBTU 0.084 LB/MMBTU0.824 LB/MMBTU 2.88 LB/H 0.824 LB/MMBTU

100 PPMVD@31-HOUR A 1.6 LB/H 0.036 LB/MMBTU0.082 LB/MMBTU 3.8 LB/H 0.082 LB/MMBTU

0.2 LB/MMBTUFIRING NAT GAS 0.2 LB/MMBTU0.02 LB/MMBTUFIRING NAT GAS 0.02 LB/MMBTU

5 LB/1000 G EA, FIRING DIESEL 0.2 LB/MMBTU0.2 LB/MMBTUFIRING NAT GAS 0.2 LB/MMBTU0.8 LB/H 0.08 LB/MMBTU 0.08 LB/MMBTU0.6 LB/H 0.03 LB/MMBTU 0.03 LB/MMBTU

7.84 LB/H 34.3 T/YR 0.098 LB/MMBTU7.91 LB/H combined 34.64 T/YR combined 0.084 LB/MMBTU

10.81 T/YR 4.39 LB/H1.32 LB/H/UNIT 4.33 T/YR100 PPMD @ 315-MIN

50 PPMVD @ 3% O2 0.0375 LB/MMBTUEXCLUSIVE USE OF NATURAL SEE NOTE

0.073 LB/MMBTU 2.2 LB/H 0.073 LB/MMBTU0.082 LB/MMBTU 2.87 LB/H 0.082 LB/MMBTU

4.12 LB/H 1.65 T/YR 0.084 LB/MMBTU0.085 LB/MMBTU 0.085 LB/MMBTU0.135 LB/MMBTU 4.71 LB/H

50 PPM @ 3%1-H AV 1.07 LB/H 0.037 LB/MMBTU0.86 LB/H 3.181 T/YR 0.0538 LB/MMBTU0.37 LB/MMBTU 0.37 LB/MMBTU0.26 LB/H 0.02 LB/MMBTU2000 PPMVD @ 3% 024.84 LB/H 21.19 T/YR 0.08 LB/MMBTU12.2 LB/H 53.4 LB/H 0.13 LB/MMBTU1.24 LB/H 5.43 T/YR 0.035 LB/MMBTU

0.082 LB/MMBTU 0.082 LB/MMBTU0.135 LB/MMBTU 4.71 LB/H

0.18 LB/MMBTU 0.18 LB/MMBTU0.18 LB/MMBTU 0.18 LB/MMBTU0.18 LB/MMBTU 3.8 LB/H 0.18 LB/MMBTU400 PPMDV @ 3% O2 0.3 LB/MMBTU

6.86 LB/H 10.28 T/YR 0.082 LB/MMBTU6.84 LB/H 0.082 LB/MMBTU36.8 LB/H 24.28 T/YR 0.56 LB/MMBTU


0.44 LB/H 0.22 T/YR0.26 LB/H 0.77 T/YR 0.08 LB/MMBTU4.25 LB/H 14.89 T/YR 0.08 LB/MMBTU1.62 LB/H 5.68 T/YR 0.08 LB/MMBTU0.15 LB/MMBTU 0.15 LB/MMBTU


0.084 LB/MMBTU 25.1 T/YR 0.084 LB/MMBTU0.07 LB/MMBTU 0.07 LB/MMBTU

0.514 LB/H 0.03 T/YR 0.04 LB/MMBTU0.96 LB/H 2 T/YR 0.084 LB/MMBTU

0.037 LB/MMBTU 0.037 LB/MMBTU4.9 LB/H 0.07 LB/MMBTU

0.082 LB/MMBTU 3.3 LB/H0.073 LB/MMBTU 0.073 LB/MMBTU

0.04 LB/MMBTU 0.04 LB/MMBTU6.42 LB/H 9.63 T/YR 0.08 LB/MMBTU8.32 LB/H 0.084 LB/MMBTU 0.084 LB/MMBTU100 PPMVD @ 3% 02

2.52 LB/H 0.084 LB/MMBTU 0.084 LB/MMBTU0.06 LB/MMBTU 0.06 LB/MMBTU0.69 LB/H 0.15 LB/MMBTU 0.15 LB/MMBTU

0.037 LB/MMBTU 0.037 LB/MMBTU14.9 LB/H EACH UNI 74 T/YR UNITS CO 0.15 LB/MMBTU

2.9 LB/H each unit 4.38 T/YR each unit 0.073 LB/MMBTU0.5 LB/H EACH 2.16 T/YR EACH 0.083 LB/MMBTU9.4 T/YR1.6 LB/H 6.1 T/YR1.6 LB/H 6.1 T/YR

2.59 LB/H 11.32 T/YR 0.08 LB/MMBTU2.59 LB/H 11.32 T/YR 0.08 LB/MMBTU1.33 LB/H EACH 5.81 T/YR EACH 0.08 LB/MMBTU


1.11 LB/H 4.85 T/YR111 PPMDV @ 3 hr ave 4.6 LB/H 3 hr ave 0.083 LB/MMBTU

2.75 LB/H 12.08 T/H 0.08 LB/MMBTU71.4 T/YR1.19 LB/H 4.33 T/YR 0.0992 LB/MMBTU0.25 LB/H 0.9 T/YR 0.1 LB/MMBTU3.21 LB/H 11.73 T/YR 0.099 LB/MMBTU0.25 LB/H 1.08 T/YR 0.0833 LB/MMBTU

1.2 LB/H HOURLY MAXIMUM 0.08 LB/MMBTU2.1 LB/H HOURLY MAXIMUM 0.08 LB/MMBTU

0.035 LB/MMBTU3-h avg 0.035 LB/MMBTU0.085 LB/MMBTU 0.085 LB/MMBTU0.093 LB/MMBTU 0.093 LB/MMBTU

3.56 LB/H each unit 0.08 LB/MMBTU2.06 LB/H FROM NAT 9.02 T/YR FROM NATURAL GAS COMBUS

37 PPM @ 15% O2 0.083 LB/MMBTU0.508 LB/H HOURLY 2.03 T/YR ANNUAL M 0.091 LB/MMBTU0.924 LB/H HOURLY 3.68 T/YR ANNUAL M 0.091 LB/MMBTU

2.31 LB/H HOURLY 9.198 T/YR ANNUAL M 0.091 LB/MMBTU

1.109 LB/H HOURLY 4.415 T/YR ANNUAL M 0.091 LB/MMBTU0.022 LB/MMBTU 0.022 LB/MMBTU0.082 LB/MMBTU 3.25 T/YR 0.082 LB/MMBTU

1.4 LB/H 4.1 T/YR3.34 LB/H 7 T/ROLLING 12-MONT 0.109 LB/MMBTU0.09 LB/MMBTU 0.09 LB/MMBTU0.14 LB/MMBTU 0.14 LB/MMBTU


0.037 LB/MMBTU 0.037 LB/MMBTU0.08 LB/MMBTU 0.08 LB/MMBTU0.08 LB/MMBTU 0.08 LB/MMBTU0.08 LB/MMBTU 0.08 LB/MMBTU0.08 LB/MMBTU 0.08 LB/MMBTU

4.5 LB/H 0.09 LB/MMBTU 0.09 LB/MMBTU0.08 LB/MMBTU 4.8 LB/H 0.08 LB/MMBTU

3.5 PPH 15.34 T/YR 0.09 LB/MMBTU4.2 LB/H 18.1 T/YR 0.0824 LB/MMBTU

0.037 LB/MMBTU1-HR AVERAGE 0.037 LB/MMBTU2.7 LB/H 0.084 LB/MMBTU2.7 LB/H 0.084 LB/MMBTU


0.084 LB/MMBTU3 HOUR AVERAGE 0.084 LB/MMBTU0.84 LB/MMBTU 0.84 LB/MMBTU1.67 LB/H 0.036 LB/MMBTU7.77 LB/H 0.08 LB/MMBTU0.47 LB/H 0.047 LB/MMBTU0.06 LB/H0.41 T/MO PER CALE 3.2 T/YR PER ROLLING 12-MONTH PERIOD0.08 LB/MMBTUBASED ON HIGHER HEATING VALUE OF 0.08 LB/MMBTU1.13 LB/H EACH BOI 1.69 T/ROLLIN EACH BOI 0.037 LB/MMBTU

70 PPM 7% O2, 24 1.1 LB/H 24 hr ave 0.085 LB/MMBTU1.52 LB/H HOURLY 0.57 T/YR *SEE NOT 0.08 LB/MMBTU6.57 LB/H HOURLY MAXIMUM 0.099 LB/MMBTU

0.046 LB/MMBTU 0.046 LB/MMBTU0.03 LB/MMBTU

0.1 LB/MMBTU 0.1 LB/MMBTU0.12 LB/MMBTU 0.12 LB/MMBTU0.15 LB/MMBTU 0.15 LB/MMBTU

50 PPMVD @ THREE 30-MIN SAMP PERIODS AV143 PPMVD

50 PPMV AT 6-MIN AV0.083 LB/MMBTU 1.42 T/YR0.036 LB/MMBTU 49 PPMVD 3% OXYG 0.036 LB/MMBTU

1.7 LB/H 7.5 T/YR 0.083 LB/MMBTU0.084 LB/MMBTU 8.3 LB/H

0.1 LB/MMBTUAVERAGE OF 3 TEST RUNS

0.09 LB/MMBTU 8.91 LB/H0.09 LB/MMBTU 2.45 LB/H0.09 LB/MMBTU 3.01 LB/H0.04 LB/MMBTU 2.62 LB/H0.03 LB/H CHLORINE 0.12 T/YR CHLORINE GAS

0.0002 GRAIN/TON0.0002 LB/H

0.4 LB/T OF FEED0.08 LB/H 0.35 T/YR1.16 LB/H 0.51 T/YR0.37 LB/H 1.62 T/YR

FUEL SULFUR CONTENT LIMIT SEE CONTROL DESCRIPTION0 LB/H0 LB/H0 LB/H

1.2 LB/H each 0.036 LB/MMBTU0.034 LB/MMBTU 0.034 LB/MMBTU

3.82 LB/H 5.73 T/YR 0.05 LB/MMBTU0.036 LB/MMBTUEACH UNI 18 T/YR UNITS CO 0.036 LB/MMBTU0.049 LB/MMBTU 0.049 LB/MMBTU0.049 LB/MMBTU 0.049 LB/MMBTU

6.17 LB/H each unit 0.14 LB/MMBTU0.04 LB/MMBTU3 HOUR AVERAGE 0.04 LB/MMBTU

17 PPMVD 3-HOUR AVERAGE1.1 LB/H 0.011 LB/MMBTU 0.011 LB/MMBTU

0.012 MMBTU/HR 0 00 NO NUMERIC LIMIT 0 0

6.08 LB/H TOTAL 0.04 LB/MMBTU1.89 LB/H 0.04 LB/MMBTU2.21 LB/H 0.04 LB/MMBTU2.63 LB/H 0.04 LB/MMBTU9.45 LB/H 0.1 LB/MMBTU9.12 LB/H TOTAL 0.04 LB/MMBTU

0.0913 LB/MMBTU 0 0.0913 LB/MMBTU0.0193 LB/MMBTU 0 0.0193 LB/MMBTU0.0913 LB/MMBTU 0 0.0913 LB/MMBTU

25 PPM @ 15% O2 0 0 LB/MMBTU1.66 LB/H 5.69 T/YR 5.5 LB/MMBTU6.81 LB/H 11.79 T/YR 3 LB/MMBTU

6.8 LB/H 11.79 T/YR 3 LB/MMBTU6.81 LB/H 11.79 T/YR 3 LB/MMBTU


0.1 LB/MMBTU 0.1 LB/MMBTU0.03 LB/MMBTU 0.8 LB/H 0.03 LB/MMBTU0.03 LB/MMBTU 0.7 LB/H 0.03 LB/MMBTU18.8 LB/H 0.2 LB/MMBTU0.06 LB/MMBTU 0 0.06 LB/MMBTU

0.1 LB/MMBTU 5.03 LB/HR 0.1 LB/MMBTU8 PPMV NAT. GAS 25 PPM 80% H2 0.0295 LB/MMBTU

0.038 LB/MMBTU 0 0150 PPMVD 266 LB/H 33.25 LB/MMBTU

4.75 LB/H HOURLY 20.81 T/YR ANNUAL M 0.05 LB/MMBTU0.39 LB/H HOURLY 1.71 T/YR ANNUAL M 0.043 LB/MMBTU

2.3 LB/H 0 015.3 LB/H 44.7 T/YR 0.18 LB/MMBTU0.03 LB/MMBTU 0 00.03 LB/MMBTU 0 013.6 LB/H 0.18 LB/MMBTU

5.8 LB/H 0.21 LB/MMBTU0.0365 LB/MMBTU 0.0365 LB/MMBTU

0 0 07.27 T/YR 1.66 LB/H 0.06 LB/MMBTU

0.042 LB/MMBTU 0.042 LB/MMBTU1.25 LB/H 5.5 T/YR 0.089 LB/MMBTU0.12 LB/MMBTU 0.12 LB/MMBTU33.8 LB/H 0.4 LB/MMBTU 0.4 LB/MMBTU0.05 LB/MMBTU 0.05 LB/MMBTU0.05 LB/MMBTU 0.05 LB/MMBTU

0.1 LB/MMBTU 00.1 LB/MMBTU 0 0.1 LB/MMBTU20 PPMVD @ 3% O215 PPMVD Corrected to 3% O2 0.018 LB/MMBTU


49.3 PPMV 0.0608 LB/MMBTU0.009 LB/MMBTU 0.009 LB/MMBTU

20 PPMV @ 3% O2 0.024 LB/MMBTU7 PPMVD @ 3% O2 0.0085 LB/MMBTU

12 PPMVD @ 3% O2 0.015 LB/MMBTU7 PPMVD at 3% O2 0.0085 LB/MMBTU7 PPMVD@315-MIN AVG9 PPMVD Corrected to 3% O2 0.011 LB/MMBTU9 PPMVD@315 MIN AVG 0.01 LB/MMBTU

0.035 LB/MMBTU 0.035 LB/MMBTU15 PPMVD Corrected to 3% O2 0.018 LB/MMBTU

166 LB/H 170 T/YR 0.13 LB/MMBTU12 PPMVD Corrected to 3% O2 0.015 LB/MMBTU30 PPMVD Corrected to 3% O2 0.037 LB/MMBTU

0.1 LB/MMBTU 0.1 LB/MMBTU0.35 LB/H 0.035 LB/MMBTU 0.035 LB/MMBTU

12 PPMVD Corrected to 3% O2 0.015 LB/MMBTU9 PPMVD Corrected to 3% O2 0.011 LB/MMBTU

12 PPMVD Corrected to 3% O2 0.015 LB/MMBTU20 PPMV @ 315 MIN AVG 0.015 LB/MMBTU12 PPM @ 3%15 MINUT 127 LB/MO 0.015 LB/MMBTU


5.4 LB/H 0.47 T/YR 0.1 LB/MMBTU12 PPMVD Corrected to 3% O2 0.015 LB/MMBTU

2 PPMVD @ 15-MIN AVG60 PPMVD @ 3 % O2 60 PPM @ 15% O2

1.18 LB/H 3.28 T/YR LB/MMBTU1.1 LB/H 0.04 LB/MMBTU

0.83 LB/H 2.91 T/YR 0.04 LB/MMBTU7 PPMVD Corrercted to 3% O2 0.009 LB/MMBTU7 PPMVD@315MIN

9.5 T/YR 9.2 LB/HR 0.12 LB/MMBTU30 PPMVD AT 3% OXYG 0.035 LB/MMBTU 0.035 LB/MMBTU

0.12 LB/MMBTU 0.12 LB/MMBTU12 PPMVD 3% O2

8 LB/H 0.1 LB/MMBTU2.29 LB/H 10.01 T/YR1.72 LB/H EACH0.12 LB/MMBTU 5.3 LB/H 0.12 LB/MMBTU

1.5 LB/H 0.03 LB/MMBTU0.036 LB/MMBTU 0.75 LB/H0.036 LB/MMBTU 0.53 LB/H

0.05 LB/MMBTU 4.18 LB/H 0.05 LB/MMBTU0.1 LB/MMBTU

0.15 LB/MMBTU40 PPMVD @ 3% O2 40 PPMVD @ 3% O2

0.08 LB/MMBTU 3.2 LB/H 0.08 LB/MMBTU0.69 LB/H 3.02 T/YR 0.033 LB/MMBTU3.07 LB/H 13.4 T/YR 0.036 LB/MMBTU0.12 LB/MMBTU 0.12 LB/MMBTU

0.1 LB/MMBTU 0.1 LB/MMBTU0.049 LB/MMBTU 1.72 LB/H 0.049 LB/MMBTU0.049 LB/MMBTU 0.049 LB/MMBTU

30 PPMVD@3ONE-HOU 5.2 LB/H 0.118 LB/MMBTU0.049 LB/MMBTU 2.28 LB/H 0.049 LB/MMBTU

0.05 LB/MMBTUEACH 0.05 LB/MMBTU0.08 LB/MMBTUEACH 0.08 LB/MMBTU11.3 LB/H EA, BASED ON HHV, FIRING FUEL OIL 0.08 LB/MMBTU0.08 LB/MMBTUAT ANY TIME 0.08 LB/MMBTU

0.5 LB/H 0.05 LB/MMBTU 0.05 LB/MMBTU1.2 LB/H 0.06 LB/MMBTU 0.06 LB/MMBTU

2.72 LB/H 11.9 T/YR 0.034 LB/MMBTU9.41 LB/H combined 41.22 T/YR combined 0.1 LB/MMBTU

0.035 LB/MMBTU 2.48 LB/H See Pollut 0.035 LB/MMBTU2.48 LB/H See Pollut 5.23 T/YR See Pollutant Noes


9 PPMD @ 315-MIN

12 PPMVD @ 3% O2 0.015 LB/MMBTUEXCLUSIVE USE OF NATURAL SEE NOTE

0.096 LB/MMBTU 2.9 LB/H 0.096 LB/MMBTU0.08 LB/MMBTU 2.8 LB/H 0.08 LB/MMBTU

4.9 LB/H 1.96 T/YR 0.1 LB/MMBTU0.05 LB/MMBTU 0.05 LB/MMBTU

0.108 LB/MMBTU 3.77 LB/H1.03 LB/H 1-HR 30 PPM @ 3%1-HR0.12 LB/MMBTU 1.197 LB/H 0.12 LB/MMBTU

0.036 LB/MMBTU 0.036 LB/MMBTU30 PPM@3% O2

1.95 LB/H 0.15 LB/MMBTU43 PPMVD @ 3% O2

0.9 LB/H 3.94 T/YR 0.015 LB/MMBTU3.21 LB/H 22.7 T/YR 0.0352 LB/MMBTU1.88 LB/H 8.23 T/YR 0.053 LB/MMBTU

18 PPMVD @ 3% O20.049 LB/MMBTU 0.049 LB/MMBTU0.108 LB/MMBTU 3.77 LB/H


0.0913 LB/MMBTU 1.9 LB/H 0.0913 LB/MMBTU30 PPMDV @ 3% O2 0.036 LB/MMBTU

6.69 LB/H 10.03 T/YR 0.08 LB/MMBTU4.07 LB/H 0.049 LB/MMBTU

61.34 LB/H 40.47 T/YR 0.1 LB/MMBTU30 PPMVD @30 MIN


0.53 LB/H 0.27 T/YR0.4 LB/H 1.16 T/YR 0.12 LB/MMBTU



0.06 LB/MMBTU 0.06 LB/MMBTU0.05 LB/MMBTU 16.4 T/YR 0.05 LB/MMBTU

0.075 LB/MMBTU 0.075 LB/MMBTU1.207 LB/H 0.06 T/YR 0.094 LB/MMBTU1.076 LB/H 2.24 T/YR 0.094 LB/MMBTU0.035 LB/MMBTU 0.035 LB/MMBTU

LOW NOX BURNERS, CLEAN FUSEE NOTE0.05 LB/MMBTU 2 LB/H0.04 LB/MMBTU 0.04 LB/MMBTU

34 PPM @ 3%24 H AVG 4 LB/D4.95 LB/H 0.05 LB/MMBTU 0.05 LB/MMBTU

9 PPMVD @ 3% O21.05 LB/H 0.035 LB/MMBTU 0.035 LB/MMBTU

0.044 LB/MMBTU 0.044 LB/MMBTU0.17 LB/H 0.036 LB/MMBTU 0.036 LB/MMBTU

30 PPM @ 3% O2 0.037 LB/MMBTU3.2 LB/H each unit 4.8 T/YR each unit 0.08 LB/MMBTU

0.59 LB/H EACH 2.58 T/YR EACH 0.098 LB/MMBTU12.8 T/YR


3.08 LB/H 13.48 T/YR 0.1 LB/MMBTU3.08 LB/H 13.48 T/YR 0.1 LB/MMBTU2.05 LB/H EACH 9 T/YR EACH 0.13 LB/MMBTU0.14 LB/MMBTU 0.14 LB/MMBTU

1.4 LB/H 6.12 T/YR30 PPMDV @ 3 hr ave 12.7 LB/H 3 hr ave 0.23 LB/MMBTU30 PPM @ 3% O2 0.04 LB/MMBTU

135.58 T/YR0.15 LB/MMBTU 0.24 LB/H 0.15 LB/MMBTU1.41 LB/H 5.15 T/YR 0.118 LB/MMBTU0.29 LB/H 1.07 T/YR 0.116 LB/MMBTU1.95 LB/H 8.54 T/YR 0.06 LB/MMBTU0.29 LB/H 1.29 T/YR 0.0967 LB/MMBTU

0.095 LB/MMBTU 0.095 LB/MMBTU30 PPMVD @ 3-H AVG


34 PPMDV @ 24 h avg 4 LB/D 0.04 LB/MMBTU2.45 LB/H FROM NAT 10.7 T/YR FROM NATURAL GAS COMBUS

99 PPM @ 15% O2 0.37 LB/MMBTU30 PPM @ 15% O2 0.11 LB/MMBTU

0.049 LB/MMBTU 1.93 T/YR 0.049 LB/MMBTU1.3 LB/H 3.9 T/YR

1.08 LB/H 2.3 T/ROLLING 12-MONT 0.035 LB/MMBTU0.027 LB/MMBTU 0.027 LB/MMBTU0.036 LB/MMBTU 0.036 LB/MMBTU

0.08 LB/MMBTU 0.08 LB/MMBTU0.035 LB/MMBTU 0.035 LB/MMBTU0.036 LB/MMBTU 0.036 LB/MMBTU0.035 LB/MMBTU3-h avg 0.035 LB/MMBTU

0.04 LB/MMBTU 0.04 LB/MMBTU0.04 LB/MMBTU 0.04 LB/MMTU0.04 LB/MMBTU 0.04 LB/MMBTU0.04 LB/MMBTU 0.04 LB/MMBTU

0.035 LB/MMBTU 0.035 LB/MMBTU2.48 LB/H 5.23 T/YR 0.155 LB/MMBTU

1.5 LB/H EACH 0.0528 LB/MMBTU0.6 LB/H EACH 0.051 LB/MMBTU0.2 LB/H 0.143 LB/MMBTU

1.75 LB/H 0.035 LB/MMBTU 0.035 LB/MMBTU

2.88 LB/H 12.63 T/YR 0.045 LB/MMBTU0.035 LB/MMBTU 9.6 TONS/YR 0.035 LB/MMBTU

2.08 PPH 9.13 T/YR 0.05 LB/MMBTU0.035 LB/MMBTU1-HR AVERAGE 0.035 LB/MMBTU

4.24 LB/H 0.13 LB/MMBTU3.2 LB/H 0.1 LB/MMBTU

0.05 LB/MMBTU3 HOUR TEST AVG 0.05 LB/MMBTU0.064 LB/MMBTU0.147 LB/MMBTU

0.08 LB/MMBTU 0.08 LB/MMBTU1.67 LB/H 3,300 HR / ROLLING 12 MO. 0.036 LB/MMBTU13.7 LB/H 0.141 LB/MMBTU

0.1 LBS/MMBTU 0.36 LB/H 0.1 LBS/MMBTU0.073 LB/H

0.5 T/MO PER CALE 3.81 T/YR PER ROLLING 12-MONTH PERIOD.0.35 LB/MMBTU 0.35 LB/MMBTU0.37 LB/MMBTUBASED ON HIGHER HEATING VALUE OF 0.37 LB/MMBTU1.07 LB/H EACH BOI 1.6 T/ROLLIN EACH BOI 0.035 LB/MMBTU

0.1 LB/MMBTU7% O2, 24 0.455 LB/H 24 hr ave 0.1 LB/MMBTU1.81 LB/H HOURLY 0.68 T/YR *SEE NOT 0.095 LB/MMBTU7.82 LB/H HOURLY MAXIMUM 0.118 LB/MMBTU

0.009 LB/MMBTU 0.009 LB/MMBTU0.012 LB/MMBTU 9 PPMVD0.036 LB/MMBTU3-HOUR AVERAGE0.095 LB/MMBTU 0.095 LB/MMBTU

0.08 LB/MMBTU 0.08 LB/MMBTU9 PPMVD @ THREE 30-MIN SAMP PERIODS AV

17 PPMVD 3-HOUR AVERAGE9 PPMV AT 6-MIN AV

0.101 LB/MMBTU 1.69 T/YR 0.101 LB/MMBTU0.035 LB/MMBTU 29 PPMVD 3% OXYG 0.035 LB/MMBTU

18 PPMVD@3%O20.72 LB/H 3.5 T/YR 0.035 LB/MMBTU


0.04 LB/MMBTUAVERAGE OF 3 TEST RUNS0.11 LB/MMBTU 10.89 LB/H0.11 LB/MMBTU 2.99 LB/H0.11 LB/MMBTU 2.99 LB/H0.11 LB/MMBTU 3.68 LB/H

0.035 LB/MMBTU 2.27 LB/H0.164 LB/MMBTU 0 0.164 LB/MMBTU

0.0164 LB/MMBTU 0 0.0164 LB/MMBTU0.0164 LB/MMBTU 0 0.0164 LB/MMBTU

0.1 LB/MMBTU 0.1 LB/MMBTU0.0076 LB/MMBTU 0.0076 LB/MMBTU0.0076 LB/MMBTU 0.0076 LB/MMBTU

1.25 LB/H 0.013 LB/MMBTU

5 LB/MMBTU 0 5 LB/MMBTU0.7 LB/H 3 LB/MMCF 0.009 LB/MMBTU2.4 LB/H 0.1 LB/MMBTU 0.1 LB/MMBTU

FUEL LIMITATIONS, SEE POLL SEE POLLUTANT NOTES0.05 GR/DSCF AVERAGED OVER 3 HOURS 0.0072 LB/MMBTU0.05 GR/DSCF AV OVER 3 H 0.0072 LB/MMBTU0.05 GR/DSCF 0.0072 LB/MMBTU0.05 GR/DSCF 0.0072 LB/MMBTU0.05 GR/DSCF 0.0072 LB/MMBTU0.05 GR/DSCF AVERAGED OVER 3 H 0.0072 LB/MMBTU0.05 GR/DSCF AV OVER 3 H 0.0072 LB/MMBTU0.05 GR/DSCF AVERAGED OVER 3 H 0.0072 LB/MMBTU0.05 GR/DSCF AV OVER 3 H 0.0072 LB/MMBTU


14 LB/MMSCF 20 % OPACITFOR NO MO 10 % OPACIT14 LB/MMSCF 20 % OPACITFOR NO MO 10 % OPACIT


0.05 GR/DSCF 3 H AV, E 0.06 LB/H 0.0071 LB/MMBTU0.05 GR/DSCF 3 H AV 0.034 LB/H 0.0071 LB/MMBTU


0.7 LB/H 0.13 LB/MMBTU4.03 LB/H 0.05 LB/MMBTU


0.6 LB/MMBTU 0.6 LB/MMBTU0.05 GR/DSCF 3 H AVERAGE, STANDARD CONDITIONS 0.0071 LB/MMBTU0.05 GR/DSCF 3 H AV, STANDARD CONDITIONS 0.0071 LB/MMBTU0.05 GR/DSCF 3 H AV, STANDARD CONDITIONS 0.0071 LB/MMBTU0.12 LB/H 0.433 T/YR 0.0271 LB/MMBTU1.24 LB/H 0.095 LB/MMBTU

0.1 GR/SCF 0.1 GR/SCF0.46 LB/H 2.06 T/YR 0.005 LB/MMBTU0.11 LB/H 0.48 T/YR 0.003 LB/MMBTU

7.6 LB/MMSCFPM AND PM10, FROM AP-42 0.007 LB/MMBTU0.0075 LB/MMBTU 0.0075 LB/MMBTU0.0217 LB/MMBTU 0.0217 LB/MMBTU0.0217 LB/MMBTU 0.0217 LB/MMBTU0.0164 LB/MMBTU 1.5 T/YR 0.0164 LB/MMBTU

3.33 LB/H 2.2 T/YR 0.05 LB/MMBTU0.308 LB/MMBTU 0.308 LB/MMBTU0.007 LB/MMBTU 0.007 LB/MMBTU


1.1 T/YR0.04 LB/H 0.18 T/YR


20 LB/MMCF 17 T/YR 0.02 LB/MMBTU0.008 LB/MMBTU 0.012 LB/H 0.008 LB/MMBTU

0.0084 LB/MMBTU 0.0084 LB/MMBTU0.62 LB/H each unit 0.014 LB/MMBTU


0.0075 LB/MMBTU 0.45 LB/H 0.0075 LB/MMBTU0.0075 LB/MMBTU 0.6 LB/H 0.0075 LB/MMBTU0.0075 LB/MMBTU 0.08 LB/H 0.0075 LB/MMBTU0.0075 LB/MMBTU 0.26 LB/H 0.0075 LB/MMBTU

0.12 LB/H 0.39 T/YR 0.0075 LB/MMBTU0.32 PPH 1.39 T/YR 0.008 LB/MMBTU0.84 LB/H 0.15 LB/MMBTU

1 LB/H 0.15 LB/MMBTU0.008 LB/MMBTU3 HOUR AVERAGE 0.008 LB/MMBTU

0.01 LB/H0.001 LB/MMBTU

0.04 LB/H 0.27 LB/YR 0.0019 LB/MMBTU0.0076 LB/MMBTU 0.72 LB/H0.0076 LB/MMBTU 0.75 LB/H

0.015 GR/DSCF AVERAGE OF 3 TEST RUNS0.0019 LB/MMBTU 0.0019 LB/MMBTU

0.18 LB/H 0.8 T/YR 0.6 LB/MMBTU1.39 LB/H 6.07 T/YR 0.6 LB/MMBTU1.39 LB/H 6.07 T/YR 0.6 LB/MMBTU1.39 LB/H 6.07 T/YR 0.6 LB/MMBTU0.21 LB/H 0.9 T/YR 0.014 LB/MMBTU0.18 LB/H 0.8 T/YR 0.6 LB/MMBTU1.25 LB/H 0.013 LB/MMBTU

5.4 LB/H0.05 GR/DSCF0.95 LB/H HOURLY 4.16 T/YR ANNUAL M 0.01 LB/MMBTU0.11 LB/H HOURLY 0.48 T/YR ANNUAL M 0.012 LB/MMBTU

0.7 LB/H 0.009 LB/MMBTU0.06 LB/H 0.26 T/YR 0.0019 LB/MMBTU



0.012 LB/MMBTU 0.012 LB/MMBTU0.1 T/YR

1.13 LB/H 3.4 T/YR0.61 LB/T2.11 LB/H 9.25 T/YR LB/MMBTU0.15 LB/H 0.53 T/YR 0.01 LB/MMBTU


0.08 LB/H 0.36 T/YR0.06 LB/H EACH0.01 LB/MMBTU 0.5 LB/H 0.01 LB/MMBTU

0.4 LB/H 0.01 LB/MM BTU0.2 LB/H combined 0.7 T/YR combined

0.01 LB/MMBTU 0.63 LB/H 0.01 LB/MMBTUPERMIT LIMITATION IS USE OF NATURAL GAS OR PROPANEPERMIT LIMITATION IS USE OF NATURAL GAS.

0.02 LB/MMBTU 0.8 LB/H 0.02 LB/MMBTU0.04 LB/H each 0.18 T/YR each 0.02 LB/MMBTU0.43 LB/H 1.87 T/YR 0.005 LB/MMBTU

0.0076 LB/MMBTU 0.0076 LB/MMBTU0.008 LB/MMBTU 0.28 LB/H 0.008 LB/MMBTU


0.0075 LB/MMBTU 0.35 LB/H 0.0075 LB/MMBTU0.1 LB/H 0.01 LB/MMBTU 0.01 LB/MMBTU0.1 LB/H 0.005 LB/MMBTU 0.005 LB/MMBTU

0.41 LB/H 1.8 T/YR 0.0051 LB / MMBTU0.72 LB/H combined 3.13 T/YR combined 0.0076 LB/MMBTU0.63 LB/H 2.76 T/YR0.12 LB/H per Unit 0.39 T/YR per Unit

EXCLUSIVE USE OF NATURAL SEE NOTE0.005 LB/MMBTU 0.2 LB/H 0.005 LB/MMBTU

0.02 LB/MMBTU 0.7 LB/H 0.02 LB/MMBTU0.38 LB/H 0.15 T/YR 0.0077 LB/MMBTU0.01 LB/MMBTU 0.01 LB/MMBTU

0.009 LB/MMBTU 0.31 LB/H7 LB/D FILTERABLE + CONDENSIBLE, ANNUAL AVG

0.009 LB/MMBTU 0.009 LB/MMBTU0.48 LB/H 2.11 T/YR 0.008 LB/MMBTU

794.13 LB/MMCF NG0.009 LB/MMBTU 0.31 LB/H

0.4 LB/MMBTU 0.4 LB/MMBTU1.52 LB/H 2.28 T/YR 0.02 LB/MMBTU0.62 LB/H 0.0075 LB/MMBTU3.33 LB/H 2.2 T/YR 0.05 LB/MMBTU

0.0076 LB/MMBTU 0.0076 LB/MMBTU0.04 LB/H 0.02 T/YR0.02 LB/H 0.07 T/YR 0.01 LB/MMBTU0.38 LB/H 1.35 T/YR 0.01 LB/MMBTU0.15 LB/H 0.51 T/YR 0.01 LB/MMBTU0.01 LB/MMBTU 0.01 LB/MMBTU



0.098 LB/H 0.005 T/YR 0.008 LB/MMBTU


0.3 LB/H 0.009 LB/MMBTU0.0075 LB/MMBTU 0.3 LB/H

0.007 LB/MMBTU0.012 LB/MMBTU 0.012 LB/MMBTU

0.58 LB/H 0.87 T/YR 0.007 LB/MMBTU0.76 LB/H 0.0076 LB/MMBTU 0.0076 LB/MMBTU

0.228 LB/H 0.0076 LB/MMBTU 0.0076 LB/MMBTU0.023 LB/MMBTU 0.023 LB/MMBTU

0.05 LB/H 0.011 LB/MMBTU0.7 LB/H EACH UNI 3.7 T/YR COMBINED 0.007 LB/MMBTU

0.05 LB/H EACH 0.2 T/YR EACH 0.0083 LB/MMBTU0.9 T/YR

0.04 LB/H 0.18 T/YR0.23 LB/H 1.02 T/YR 0.01 LB/MMBTU0.23 LB/H 1.02 T/YR 0.007 LB/MMBTU0.12 LB/H EACH 0.53 T/YR EACH 0.008 LB/MMBTU


0.1 LB/H 0.44 T/YR0.11 LB/H 0.4 T/YR 0.0092 LB/MMBTU0.02 LB/H 0.08 T/YR 0.008 LB/MMBTU0.29 LB/H 1.06 T/YR 0.009 LB/MMBTU0.02 LB/H 0.1 T/YR 0.006 LB/MMBTU0.11 LB/H HOURLY MAXIMUM 0.01 LB/MMBTU0.19 LB/H HOURLY MAXIMUM 0.01 LB/MMBTU

0.0042 LB/MMBTU 0.0042 LB/MMBTU0.01 LB/MMBTU 0.01 LB/MMBTU0.32 LB/H each unit 0.007 LB/MMBTU0.19 LB/H FROM NAT 0.83 T/YR FROM NATURAL GAS COMBUS


0.31 LB/H 0.64 T/ROLLING 12-MONT 0.01 LB/MMBTU0.015 LB/MMBTU 0.015 LB/MMBTU0.015 LB/MMBTU 0.015 LB/MMBTU


0.63 LB/H 2.76 T/YR 0.023 LB/MMBTU0.3 LB/H EACH 0.0106 LB/MMBTU0.1 LB/H EACH 0.0085 LB/MMBTU0.1 LB/H 0.071 LB/MMBTU

0.38 LB/H 0.0075 LB/MMBTU 0.0075 LB/MMBTU0.5 LB/H0.4 LB/H 1.7 T/YR 0.0075 LB/MMBTU

0.0076 LB/MMBTU 0.0076 LB/MMBTU0.8 LB/H


0.08 LB/H 0.008 LB/MMBTU0.006 LB/H

0.0033 LB/MMBTUBASED ON HIGHER HEATING VALUE OF 0.0033 LB/MMBTU0.31 LB/H EACH BOI 0.46 T/ROLLIN EACH BOI 0.01 LB/MMBTU0.14 LB/H HOURLY 0.05 T/YR *SEE NOT 0.007 LB/MMBTU0.59 LB/H HOURLY MAXIMUM 0.009 LB/MMBTU

0.007 LB/MMBTU 0.007 LB/MMBTU0.0074 LB/MMBTU3-HOUR AVERAGE0.0078 LB/MMBTU 0.13 T/YR 0.0078 LB/MMBTU0.0075 LB/MMBTU 0.26 LB/H 0.0075 LB/MMBTU

0.15 LB/H 0.78 T/YR 0.0075 LB/MMBTU0.015 GR/DSCF AVERAGE OF 3 TEST RUNS

0.0076 LB/MMBTU 0.75 LB/H0.0076 LB/MMBTU 0.21 LB/H0.0076 LB/MMBTU 6.25 LB/H0.0076 LB/MMBTU 0.5 LB/H

0.1 LB/H 0.001 LB/MMBTU0.0007 LB/MMBTU 0 0.0007 LB/MMBTU0.0007 LB/MMBTU 0 0.0007 LB/MMBTU0.0007 LB/MMBTU 0 0.0007 LB/MMBTU

1.26 T/YR 2.5 LB/MMBTU 2.5 LB/MMBTU9.46 T/YR 0.9 LB/MMBTU0.04 T/YR 0.0006 LB/MMBTU

0.3 LB/MMBTU 40 T/YR 0.3 LB/MMBTU0.016 LB/H 0.0012 LB/MMBTU0.014 LB/H 0.0012 LB/MMBTU

0.99 LB/H 0.011 LB/MMBTUNATURAL GAS FUEL. PERMIT LISEE NOTE

0.01 LB/H 0.04 T/YR 0.0003 LB/MMBTU500 PPM AVERAGED OVER 3 HOURS 2.55 LB/MMBTU500 PPM AV OVER A PERIOD OF 3 H 2.55 LB/MMBTU500 PPM AVERAGED OVER 3 H 2.55 LB/MMBTU500 PPM 2.55 LB/MMBTU500 PPM AV OVER A PERIOD OF 3 H 2.55 LB/MMBTU500 PPM AVERAGED OVER 3 H 2.55 LB/MMBTU500 PPM AV OVER 3 H 2.55 LB/MMBTU500 PPM AV OVER 3 H 2.55 LB/MMBTU500 PPM AV OVER 3 H 2.55 LB/MMBTU0.1 LB/H 0.001 LB/MMBTU0.3 LB/H 0.0029 LB/MMBTU

0.006 LB/MMBTU 0.006 LB/MMBTU0.26 LB/H 0.23 T/YR

USE ONLY FUEL GAS WITH A SEE CONTROL DESCRIPTION AND NOTESUSE ONLY FUEL GAS WITH A SEE CONTROL DESCRIPTION AND NOTES

0.77 LB/H 0.07 T/YR 0.014 LB/MMBTU0.12 LB/H 0.54 T/YR LB/MMBTU0.06 LB/H 0.0022 LB/MMBTU

500 PPM EACH, 3 H 0.28 LB/H 0.033 LB/MMBTU500 PPM 3 H AV 0.15 LB/H 0.033 LB/MMBTU

0.03 LB/H 0.12 T/YR0.0065 LB/H EACH

2 GR/DSCF 0.006 LB/MMBTU0.001 LB/MMBTU 0.13 LB/H 0.001 LB/MMBTU

PERMIT LIMITATION IS NATURAL GAS OR PROPANE USAGE0.006 LB/MMBTU 0.24 LB/H 0.006 LB/MMBTU


0.0006 LB/MMBTU 0.021 LB/H 0.0006 LB/MMBTU0.4 LB/H 0.009 LB/MMBTU

0.0006 LB/MMBTU 0.028 LB/H 0.0006 LB/MMBTU500 PPM 3 H AVERAGE 2.55 LB/MMBTU500 PPM 3 H AV 2.55 LB/MMBTU500 PPM 3 H AV 2.55 LB/MMBTU

0.01 LB/H 0.001 LB/MMBTU 0.001 LB/MMBTU0.01 LB/H 0.0005 LB/MMBTU 0.0005 LB/MMBTU0.48 LB/H 2.1 T/YR 0.006 LB/MMBTU0.57 LB/H combined 2.47 T/YR combined 0.2 LB/MMBTU

0.006 LB/MMBTU 0.21 LB/H 0.006 LB/MMBTU0.05 LB/H 0.02 T/YR 0.001 LB/MMBTU150 PPM

0.0057 LB/MMBTU 0.2 LB/H0.07 LB/H ANNUAL A 1 PPM @ 3%3-H AVERAGE


0.26 LB/H 0.02 LB/MMBTU0.95 LB/H 4.17 T/YR 0.02 LB/MMBTU

0.055 LB/H 0.6 LB/MMCF 0.0006 LB/MMBTU0.021 LB/H 0.09 T/YR 0.0006 LB/MMBTU

0.0006 LB/MMBTU 0.0006 LB/MMBTU0.0057 LB/MMBTU 0.2 LB/H


0.003 LB/H 0.0015 T/YRFUELS LIMIT: < 2 GR/100 DSCF see notes



0.56 LB/H 0.0057 LB/MMBTU 0.0057 LB/MMBTUBACT IS USE OF NATURAL GA see notes

0.014 LB/H 0.003 LB/MMBTU0.1 LB/H EACH UNI 0.44 T/YR UNITS CO 0.001 LB/MMBTU

0.01 LB/H EACH 0.02 T/YR EACH 0.0017 LB/MMBTU16 T/YR

0.1 LB/H 0.55 T/YR

0.1 LB/H 0.55 T/YR0.02 LB/H 0.08 T/YR 0.0006 LB/MMBTU0.02 LB/H 0.08 T/YR 0.0006 LB/MMBTU0.01 LB/H EACH 0.04 T/YR EACH 0.0006 LB/MMBTU


0.01 LB/H 0.05 T/YRFUEL SULFUR LIMIT: 0.8 GR/1 see note

0.01 LB/H 0.03 T/YR 0.0008 LB/MMBTU0.02 LB/H 0.01 T/YR 0.008 LB/MMBTU0.02 LB/H 0.08 T/YR 0.0006 LB/MMBTU0.01 LB/H 0.01 T/YR 0.003 LB/MMBTU

0.2 LB/H 0.006 LB/MMBTU2.19 LB/H each unit 0.05 LB/MMBTU0.01 LB/H FROM NAT 0.06 T/YR FROM NATURAL GAS COMBUS


0.031 LB/H 0.07 T/ROLLING 12-MONT 0.001 LB/MMBTU0.0025 LB/MMBTU 0.0025 LB/MMBTU0.0025 LB/MMBTU 0.0025 LB/MMBTU0.0006 LB/MMBTU 0.0006 LB/MMBTU

0.001 LB/MMBTU 0.001 LB/MMBTU0.1 LB/H EACH 0.0035 LB/MMBTU0.1 LB/H EACH 0.0085 LB/MMBTU0.1 LB/H 0.071 LB/MMBTU

0.04 LB/H0.1 LB/H 0.2 T/YR 0.0006 LB/MMBTU


LOW SULFUR FUEL 0.8 GR/SC see note0.0006 LB/MMBTU 0.0006 LB/MMBTU

0.05 LB/H0.06 LB/H 0.006 LB/MMBTU0.02 LB/H 0.002 LB/MMBTU

0.0004 LB/H0.0023 LB/MMBTUBASED ON HIGHER HEATING VALUE OF 0.0023 LB/MMBTU

0.031 LB/H EACH BOI 0.046 T/ROLLIN EACH BOI 0.001 LB/MMBTU0.008 LB/H HOURLY 0.003 T/YR *SEE NOT 0.0004 LB/MMBTU

0.05 LB/H HOURLY MAXIMUM 0.001 LB/MMBTU250 PPMV H2S CONTENT OF NATURAL GAS250 PPMV H2S CONTENT OF NATURAL GAS 1.28 *LB/MMBT250 PPMV H2S CONTENT OF NATURAL GAS 1.28 LB/MMBTU

0.0026 LB/MMBTU 0.01 T/YR 0.0026 LB/MMBTU0.01 LB/H 3.64 T/YR 0.0006 LB/MMBTU


6 PPMVD AVERAGE OF 3 TEST RUNS0.0006 LB/MMBTU 0.06 LB/H

0.0006 LB/MMBTU 0.016 LB/H0.0006 LB/MMBTU 0.02 LB/H0.0006 LB/MMBTU 0.04 LB/H0.0008 LB/MMBTU 0.0008 LB/MMBTU

PERMIT LIMITATION IS USE OF NATURAL GAS.2 GR/100 SCF4 LB/MMBTU 4 LB/MMBTU

0.001 LB/MMBTU 0.04 LB/H 0.001 LB/MMBTU0.09 LB/H SULFURIC ACID 0.0009 LB/MMBTU

0.8 GR/100 SCF0.0001 LB/H SULFURIC ACID MIST

0.33 LB/H 0.0033 LB/MMBTU 0.0033 LB/MMBTU0.18 LB/H 0.8 T/YR 0.6 LB/MMBTU1.39 LB/H 6.07 T/YR 0.6 LB/MMBTU1.39 LB/H 6.07 T/YR 0.6 LB/MMBTU1.39 LB/H 6.07 T/YR 0.6 LB/MMBTU0.21 LB/H 0.9 T/YR 0.014 LB/MMBTU0.18 LB/H 0.8 T/YR 0.6 LB/MMBTU0.05 LB/H 0.011 LB/MMBTU

20 % OPACITY 20 % OPACITY20 % OPACITY 20 % OPACITY20 % OPACITY 20 % OPACITY20 % OPACIT6 MIN AV 20 % OPACIT

5 % OPACIT6 minute average 5 % OPACIT20 % OPACITFOR > 3 MIN/ANY 1 HOUR 20 % OPACIT20 % OPACITFOR > 3 MIN IN ANY 1 H 20 % OPACIT

NONE INDICATED. 20 % OPACIT20 % OPACITFOR > 3 MIN IN ANY 1 H 20 % OPACIT20 % OPACITFOR > 3 MIN IN ANY 1 H 20 % OPACIT

GOOD OPERATIONS PRACTICES. 20 % OPACIT20 % OPACITFOR > 3 MIN IN ANY 1 H 20 % OPACIT20 % OPACITFOR > 3 MIN IN ANY 1 H 20 % OPACIT20 % OPACITFOR > 3 MIN IN ANY 1 H 20 % OPACIT20 % OPACITFOR NO MORE THAN 3 MIN/H 20 % OPACIT20 % OPACITFOR NO MORE THAN 3 MIN/H 20 % OPACIT20 % OPACITEACH, EXCEPT FOR 3 MIN IN ANY 1 H 20 % OPACIT20 % OPACITEXCEPT FOR 3 MIN IN ANY 1 H 20 % OPACIT20 % OPACITY 20 % OPACITY

5 % OPACIT6 MIN AV 5 % OPACIT20 % OPACITMETHOD 9 20 % OPACITY20 % OPACIT6 min avg 20 % OPACIT20 % OPACIT6 MINUTE AVERAGE 20 % OPACIT20 % OPACITY 20 % OPACITY20 % OPACIT3 MIN/H 20 % OPACIT20 % OPACIT3 MIN/H 20 % OPACIT20 % OPACIT3 MIN/H 20 % OPACIT10 % OPACITas a 6 minute average 10 % OPACIT20 % OPACITY 20 % OPACITY

20 % OPACITas a six minute average 20 % OPACIT20 % OPACIT6 MIN AV 27 % OPACIT1 6 MIN S 20 % OPACIT

5 % OPACIT6 MIN AV 5 % OPACIT20 % OPACIT6-minute average 20 % OPACIT40 % OPACITY 40 % OPACITY20 % OPACIT6 minute average 20 % OPACIT

0 % OPACITY 0 % OPACITY10 % OPACITas a six minute average 10 % OPACIT10 % OPACITas a six minute average 10 % OPACIT20 % OPACITY 20 % OPACITY10 % OPACITY 10 % OPACITY20 % OPACITY 20 % OPACITY10 % OPACITY 10 % OPACITY20 % OPACIT6-min avg 27 % OPACITone 6-min p 20 % OPACITY10 % OPACIT6 min ave 10 % OPACITY10 % OPACITY 10 % OPACITY20 % OPACIT6 M AV 20 % OPACIT40 % OPACITY 40 % OPACITY20 % OPACIT6 min avg 20 % OPACITY10 % OPACIT6-MINUTE AVERAGE 10 % OPACITY

5 % OPACITAS A 6-MINUTE AVERAGE 5 % OPACIT0 % SIX-MINUTE AVERAGE

0.33 LB/H 0.0033 LB/MMBTU 0.0033 LB/MMBTU0.0192 LB/MMBTU 0 0.0192 LB/MMBTU0.0564 LB/MMBTU 0 0.0564 LB/MMBTU0.0192 LB/MMBTU 0 0.0192 LB/MMBTU

0.25 LB/H 1.1 T/YR 0.8 LB/MMBTU2.37 LB/H 4.11 T/YR 1 LB/MMBTU2.37 LB/H 4.11 T/YR 1 LB/MMBTU2.37 LB/H 411 T/YR 1 LB/MMBTU

0.025 LB/H 0.11 T/YR 0.002 LB/MMBTU0.25 LB/H 1.1 T/YR 0.8 LB/MMBTU0.49 LB/H 0.005 LB/MMBTU

2.8 LB/MMSCF 0.03 LB/H0.2 LB/H 4.4 PPMVD @ 7% O2 0.002 LB/MMBTU0.8 LB/H 0.08 LB/MMBTU

0.0054 LB/MMBTU 0.0054 LB/MMBTU0.0055 LB/MMBTU 0.0055 LB/MMBTU0.0067 LB/MMBTUREACTIVE ORGANIC GASES 0.0067 LB/MMBTU

0.2 T/YR1.2 LB/H 3.84 T/YR

5.47 LB/H 14.32 T/YR0.29 LB/H 0.03 T/YR0.69 LB/H 3.04 T/YR LB/MMBTU

0.4 LB/H 0.016 LB/MMBTUBACT FOR VOC IS DETERMINED TO BE USE OF NATURAL GAS TO FUEL BOILER. NO EMISSION RATE LIBACT FOR VOC IS DETERMINED TO BE GOOD COMBUSTION CONTROL AND THE USE OF NATURAL GAS

0.05 LB/H 0.2 T/YR

0.016 LB/MMBTU 0.8 LB/H 0.016 LB/MMBTU0.7 LB/H 0.016 LB/MM BTU

0.006 LB/MMBTU 0.46 LB/H 0.006 LB/MMBTU0.02 LB/MMBTU 0.8 LB/H 0.02 LB/MMBTU0.11 LB/H 0.005 LB/MMBTU 0.005 LB/MMBTU0.35 LB/H 0.0041 LB/MMBTU 0.0041 LB/MMBTU

0.0055 LB/MMBTU0.0054 LB/MMBTU 0.19 LB/H 0.0054 LB/MMBTU


0.0054 LB/MMBTU 0.25 LB/H 0.0054 LB/MMBTU0.1 LB/H 0.01 LB/MMBTU 0.01 LB/MMBTU0.1 LB/H 0.005 LB/MMBTU 0.005 LB/MMBTU

0.44 LB/H 1.9 T/YR0.52 LB/H combined 2.27 T/YR combined 0.0055 LB/MMBTU4.38 T/YR

EXCLUSIVE USE OF NATURAL SEE NOTE0.004 LB/MMBTU 0.1 LB/H 0.004 LB/MMBTU0.011 LB/MMBTU 0.39 LB/H


0.0104 LB/MMBTU 0.5 LB/H0.16 LB/H 1-H AV, CARBON EQUIVALENT0.11 LB/H 0.407 T/YR0.01 LB/MMBTU 0.13 LB/H0.35 LB/H 1.53 T/YR0.65 LB/H 5.17 T/YR

0.1 LB/H 0.44 T/YR0.0054 LB/MMBTU 0.0054 LB/MMBTU

0.014 LB/MMBTU 0.5 LB/H0.045 LB/MMBTU0.045 LB/MMBTU

0.4 LB/H 0.0192 LB/MMBTU0.92 LB/H 1.37 T/YR 0.011 LB/MMBTU0.45 LB/H 0.0054 LB/MMBTU780 LB/MO FACILITYWIDE

0.0055 LB/MMBTU0.0055 LB/MMBTU 0.0055 LB/MMBTU

0.003 LB/H 0.015 T/YR0.016 LB/MMBTU 0.016 LB/MMBTU

0.0075 LB/MMBTU0.071 LB/H 0.004 T/YR 0.006 LB/MMBTU0.063 LB/H 0.13 T/YR 0.006 LB/MMBTU0.016 LB/MMBTU

0.5 LB/H0.02 LB/MMBTU

0.0054 LB/MMBTU 0.2 LB/H0.005 LB/MMBTU

0.018 LB/MMBTU0.42 LB/H 0.63 T/YR

0.545 LB/H 0.0055 LB/MMBTU 0.0055 LB/MMBTUBACT FOR VOC EMISSIONS FRsee notes

0.22 LB/H 0.05 LB/MMBTU 50 PPMVD@3%O20.0127 LB/MMBTU

0.4 LB/H EACH UNI 2 T/YR UNITS CO 0.004 LB/MMBTU0.01 LB/H EACH 0.05 T/YR EACH0.17 LB/H 0.74 T/YR0.17 LB/H 0.74 T/YR0.09 LB/H EACH 0.38 T/YR EACH

0.0054 LB/MMBTU 0.0054 LB/MMBTU0.0054 LB/MMBTU

0.08 LB/H 0.35 T/YR4.68 T/YR0.08 LB/H 0.28 T/YR0.02 LB/H 0.06 T/YR0.21 LB/H 0.77 T/YR0.02 LB/H 0.07 T/YR0.04 LB/H HOURLY 0.18 T/YR ANNUAL M 0.005 LB/MMBTU

0.016 LB/MMBTU0.004 LB/MMBTUAS METHANE

0.23 LB/H each unit0.13 LB/H FROM NAT 0.59 T/YR FROM NATURAL GAS COMBUSTION


0.49 LB/H 1.1 T/ROLLING 12-MONT 0.016 LB/MMBTU0.01 LB/MMBTU0.01 LB/MMBTU 0.01 LB/MMBTU

0.069 LB/H HOURLY 0.231 T/YR ANNUAL M 0.007 LB/MMBTU0.0026 LB/MMBTU 0.0026 LB/MMBTU

0.007 LB/MMBTU0.0054 LB/MMBTU0.0054 LB/MMBTU0.0054 LB/MMBTU0.0054 LB/MMBTU

0.52 LB/H NONMETH 1.722 T/YR NONMETHANE HYDROCARBONS0.4 LB/H

0.016 LB/MMBTU1-HR AVERAGE 0.016 LB/MMBTU0.18 LB/H0.18 LB/H


0.006 LB/MMBTU3 HOUR AVERAGE0.0055 LB/MMBTU

0.095 LB/H HOURLY 0.32 T/YR ANNUAL M 0.007 LB/MMBTU0.53 LB/H 0.0055 LB/MMBTU0.06 LB/H 0.006 LB/MMBTU

0.004 LB/H0.0033 LB/MMBTUBASED ON HIGHER HEATING VALUE OF FUEL

GOOD COMBUSTION DESIGN FSEE NOTE0.49 LB/H EACH BOI 0.74 T/ROLLIN EACH BOI 0.016 LB/MMBTU

0.1 LB/H HOURLY 0.04 T/YR *SEE NOT 0.005 LB/MMBTU0.43 LB/H HOURLY MAXIMUM

0.002 LB/MMBTU0.0054 LB/MMBTU3-HOUR AVERAGE

143 PPMVD 3-HOUR AVERAGE0.0052 LB/MMBTU 0.09 T/YR

0.005 LB/MMBTU 0.18 LB/H 0.005 LB/MMBTU0.81 TONS/YR 0.19 LB/H 0.0055 LB/MMBTU0.11 LB/H 0.5 T/YR 0.0054 LB/MMBTU


98 % REDUCTAVERAGE 3.16 LB/H AVERAGE OF 3 TEST RUNS0.0055 LB/MMBTU 0.55 LB/H0.0055 LB/MMBTU 0.15 LB/H0.0055 LB/MMBTU 0.18 LB/H0.0055 LB/MMBTU 0.36 LB/H

STDLIMIT POLLUTANTCOMPLIANCENOTESLB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

calculated BACT IS CLEAN FUEL, NO EMISSION RATE LIMITS. BACT IS CLEAN FUEL, NO EMISSION RATE LIMIT.

% OPACITY

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

REGULATED POLLUTANT IS SULFURIC ACID MIST. EMISSION LIMIT IS 0.00015 LB/MMBTU Limit is dry, averaged over 15 minutes and corrected to 3% O2. NH3 15 MIN @ 3% O2 BACT FOR PM WILL BE CONSIDERED AS BACT FOR BE.

LB/MMBTU ADDITIONAL CO LIMIT IS 50 PPMVD @ 7% O2. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI LB/MMBTU

NOT AVAI THREE ON CALCULAT

LB/MMBTU THESE LIMITS APPLY TO DUCT BURNERS OPERATING IN THE FRESH AIR MODE.

LB/MMBTU

MMBTU/H CALCULATADDITIONAL EMISSION LIMITS: 1.84 T/YR


Calculated CO 15 MIN @ 3% O2 LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

Calculated NOT AVAI Calculated CO 15 MIN @ 3% O2 CALCULAT Calculated CO 15 MIN @ 3% O2 NOT AVAI ADDITIONAL EMISSION LIMITS: 100 PPM @ 7% O2 24 H AV. THE CO EMISSION LIMITS APPLY WHENEVER HAZARDOUS WASTE IS BEING BURNED IN THE BOILER. HAZARDOUS WASTE MAY NOT BE BURNED IN THE WASTE HEAT BOILER UNTIL AND UNLESS APPROPRIATE AUTHORITY IS OBTAINED UNDER RCRA. Calculated CO 15 MIN @ 3% O2 Calculated

LB/MMBTU Calculated CO 15 MIN @ 3% O2 Calculated CO 15 MIN @ 3% O2 Calculated CO 15 MIN @ 3% O2 CALCULAT CALCULATCO 15 MIN @ 3% O2

LB/MMBTU LB/MMBTU

CONVERTEADDITIONAL CO LIMIT OF 100 PPMVD WHEN CORRECTED TO 3 % O2 (ONE-HOUR AVERAGE). Calculated CO 15 MIN @ 3% O2

LB/MMBTU LB/MMBTU

Calculated CO 15 MIN @ 3% O2 NOT AVAI

LB/MMBTU BACT FOR CO IS DETERMINED TO BE GOOD COMBUSTION CONTROL AND THE USE OF NATURAL GAS TO BACT FOR CO IS DETERMINED TO BE GOOD COMBUSTION CONTROL AND THE USE OF NATURAL GAS T

NOT AVAI

LB/MMBTU

CALCULAT

LB/MMBTU

LB/MMBTU

LB/MMBTU Limit is for each unit. Only 2 of the 4 boilers modified in this permit. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU EMISSION LIMITS 1 & 2 TAKE EFFECT ON JANUARY 1, 2006, PER SECTION 49 OF THE AIR QUALITY REGULATIONS. EMISSION LIMIT 2 APPLIES TO EACH AUXILIARY BOILER. LB/MMBTU

FIRING NA FIRING NA FIRING N FIRING NA

LB/MMBTU LB/MMBTU

Calculated LB/MMBTU

Not AvailabStandard Emissions for CO not available Not Availab NOT AVAI

LB/MMBTU HEAT INPUT TO THE AUXILIARY BOILERS (2) SHALL BE LIMITED TO 210,240 MMBTU FOR ANY CONSECUTIVE 12-MONTH PERIOD

LB/MMBTU LB/MMBTU LB/MMBTU Boiler is restricted to 800 hours or operation per a rolling 12 months. LB/MMBTU

CALCULAT


NOT AVAI CALCULATADDITIONAL EMISSION LIMIT OF 100 PPM @ 15% O2. calculated USING MANUFACTURER'S EMISSION FACTORS OF 150 LBS CO/1,000,000 POUNDS OF AIR for both NG and #2 fuel oil.

LB/MMBTU Emissions from natural gas combustion, using 0.035 lb CO/mmBtu LB/MMBTU

LB/MMBTU Limit for combined Burner A and Burner B: 25.2 lb/h LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

calculated LB/MMBTU LB/MMBTU LB/MMBTU


LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU Limits are for each boiler. Each boiler is retricted to 100 hours of operation. LB/MMBTU Limits are for each heater. LB/MMBTU

(LHV)

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU Limits are for each boiler.

NOT AVAI LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

EACH UNI each unit

LB/MMBTU UNCONTROLLED BECAUSE BOILER IS LESS THAN 40 MMBTU/H. NOT AVAI

CALCULAT CALCULAT EACH, CA

LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTU

NOT AVAI LB/MMBTU STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT.

SEE NOTESTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. SEE NOTESTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. SEE NOTESTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. ANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL AANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU one of two units

NOT AVAI LB/MMBTU

ANNUAL A ANNUAL A ANNUAL A

ANNUAL A LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

CALCULAT CALCULAT

LB/MMBTU LB/MMBTU LB/MMBTU NATURAL GAS FIRED 46.2 MMBTU/HR BOILER

CALCULAT CALCULAT NOT AVAI (LIMIT IS FOR EACH UNIT)

PER ROLLING 12-MONTH PERIOD THESE ARE FACILITY-WIDE EMISSION LIMITS. FOR COMBUSTION UNITS B03, B04, AND B08, EACH HAS AN ANNUAL EMISSION LIMIT OF 0.94 TONS PER YEAR. LB/MMBTU LB/MMBTU LIMITS ARE FOR EACH BOILER

calculated ANNUAL A*TPY LIMIT FOR ALL 3 HEATERS. AGGREGATE HEAT INPUT IS LIMITED TO 14,250 MM BTU/YR. ONLY 2 OF THE 3 HEATERS ARE ALLOWED TO OPERATE AT ANY GIVEN TIME. CALCULAT THREE ON

*SEE NOT GOOD OPERATIONAL PRACTICES *SEE NOT GOOD OPERATIONAL PRACTICES SEE NOTEGOOD OPERATIONAL PRACTICES

143 PPMVD (CORRECTED TO 3% O2)

LB/MMBTU THE DATA PERTAIN TO EITHER ONE OF THE HURST BOILERS, WHICH RATED HEAT INPUT IS 35.4 MMBTU/H. LB/MMBTU LIMITS ARE FOR EACH BOILER.

FLUORIDES (LIMIT IS FOR EACH UNIT) LIMIT IS COMBINED, FOR TWO REVERBS, SIDEWELLS AND FLUES. BURNING OF HCN SHALL BE LIMITED TO 12250 LB/H. (LIMIT IS FOR EACH UNIT) (LIMIT IS FOR EACH UNIT)

calculated LB/MMBTU LB/MMBTU

EACH UNI LB/MMBTU SCR cost $35k LB/MMBTU Boiler came with DLN therefore a cost/ton was not done. LB/MMBTU one of two units LB/MMBTU

17 PPMVD (CORRECTED TO 3% O2) LB/MMBTU BASIS OF LIMIT IS STATE EMISSION OFFSET RULE. NOX LIMIT IS AS NO2""

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTU

CALCULAT THREE ON CALCULAT

LB/MMBTU

LB/MMBTU Synthetic minor. PROJECT NOT SIGNIFICANT FOR NOX - NO BACT DETERMINATI0N REQUIRED. LB/MMBTU LB/MMBTU


LB/MMBTU

Not AvailabPERMIT LIMITS SET IN PPM, STANDARD UNITS NOT AVAILABLE. Calculated NOX 15 MIN @ 3% O2


Calculated NOT AVAI Calculated NOX 15 MIN @ 3% O2 CALCULAT

LB/MMBTU Calculated NOX 15 MIN @ 3% O2

LB/MMBTU ADDITIONAL EMISSION LIMITS: 150 PPM AT 24 H AV. Calculated NOX 15 MIN @ 3% O2 Calculated

LB/MMBTU LB/MMBTU

Calculated NOX 15 MIN @ 3% O2 Calculated NOX 15 MIN @ 3% O2 Calculated NOX 15 MIN @ 3% O2 CALCULAT CALCULATNOX 15 MIN @ 3% O2

LB/MMBTU LB/MMBTU LB/MMBTU EMISSIONS REGULATED UNDER PSD-TX-957 PERMIT AUTHORIZATION

Calculated NOX 15 MIN @ 3% O2 NOT AVAI

PPM @ 15% O2 SOURCE TEST RESULTS: O2, % (DRY) 19.66 NOX, PPMVD 3.02 (43.6 PPMVD@3%O2) CO2, % (DRY) 0.463 CO, PPMVD 15.01 FLUE GAS FLOW RATE, DSCFM 8,138 AQMD'S MONITORING AND SOURCE TEST ENGINEERING GROUP APPROVED THIS SOURCE TEST AS SHOWING THE NOX TO BE LESS THAN 60 PPMVD@3%O2. LB/MMBTU LB/MMBTU LB/MMBTU

Calculated NOX 15 MIN @ 3% O2 NOT AVAI


THE APPLICANT PROPOSED TO USE THE ALZETA ULNB. ALTHOUGH THE MODEL CBS BURNER HAS NOT BEEN DEMONSTRATED IN A PROCESS HEATER, IT HAS BEEN SUCCESSFULLY DEMONSTRATED IN A VARIETY OF WATER-TUBE AND FIRED-TUBE BOILERS. WHILE THIS APPLICATION HAS NOT YET BEEN SOURCE TESTED, IT IS HIGHLY PROBABLE THAT IT WILL PROVE SUCCESSFUL AND WILL BECOME ACHIEVED-IN-PRACTICE TECHNOLOGY FOR SMALL PROCESS HEATERS OF THIS TYPE. THE LEVEL WAS SUGGESTED BY THE APPLICANT. LB/MMBTU

NOT AVAI

LB/MMBTU CALCULAT

LB/MMBTU

PPMVD @ 3% O2 THIS IS A RECLAIM FACILITY. THE FACILITY REQUESTED A PERMIT MODIFICATION TO APPLY A RECLAIM CONCENTRATION LIMIT OF 40 PPMVD (CORRECTED TO 3% O2) TO THIS FURNACE. THIS LOW-NOX BURNER IS CONSIDERED ACHIEVED IN PRACTICE. ALTHOUGH THIS BURNER IS CAPABLE OF MEETING A NOX LIMIT OF 40 PPM IN THIS FURNACE WHEN OPERATED ON NATURAL GAS, NOX EMISSIONS MAY BE DIFFERENT IN OTHER FURNACES WITH OTHER BURNER/FURNACE CONFIGURATIONS, OPERATING TEMPERATURES OR OTHER OPERATING CONDITIONS. IT IS SUGGESTED THE THE NOX EMISSION GUARANTEE OR 50 PPM, THE BACT PART D GUIDELINE, BE USED AS A STARTING POINT IN PERMITTING A NEW OR MODIFIED FURNACE, I.E., IN THE PERMIT TO CONSTRUCT, AND THAT THE FINAL NOX LIMIT IN THE PERMIT TO OPERATE BE DETERMINED AFTER SOURCE TESTING IS COMPLETED. SOURCE TESTING SHOULD INCLUDE THE HIGHEST-NOX OPERATING MODE LB/MMBTU LB/MMBTU Limits are for each boiler. Only 2 of the 4 boilers modified in this permit. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU EMISSION LIMIT 1 IS AN EMISSION STANDARD PER SECTION 49 OF THE AIR QUALITY REGULATIONS. EMISSION LIMIT 2 APPLIES TO EACH AUXILIARY BOILER. LB/MMBTU

EACH EACH EA, FIRIN AT ANY TI

LB/MMBTU LB/MMBTU

Calculated LB/MMBTU LB/MMBTU Emission limit 2 is the maximum emission rate per heater / oxidizer combination. In addition, an annual emission limit of 5.23 T/YR applies to the same combination.

Not AvailabLimits are for heater / oxidizer combination. LB/MMBTU LB/MMBTU

NOT AVAI

LB/MMBTU HEAT INPUT TO THE AUXILIARY BOILERS (2) SHALL BE LIMITED TO 210,240 MMBTU FOR ANY CONSECUTIVE 12-MONTH PERIOD

LB/MMBTU LB/MMBTU LB/MMBTU Boiler is restricted to 800 hours or operation per a rolling 12 months. LB/MMBTU

NOT AVAI

LB/MMBTU LB/MMBTU

NOT AVAI LB/MMBTU

NOT AVAI LB/MMBTU LB/MMBTU EMISSION LIMITS BASED ON MANUFACTER'S TEST DATA. Additional limit: 9.6 ppm @ 15% O2 as 6-monute average. LB/MMBTU Emissions from natural gas combustion, using 0.053 lb NOx/mmBtu

LB/MMBTU

LB/MMBTU limit for burners A and B combined: 12.8 lb/h LB/MMBTU LB/MMBTU

CALCULAT LB/MMBTU

calculated LB/MMBTU


LB/MMBTU

SEE POLL THIS HEATER IS PERMITTED TO USE ULTRA LOW NOX BURNERS AS CONTROL WITH AN EMISSION LIMIT OF 0.04 LB/MMBTU OR COMBINATION BURNERS AS CONTROL WITH AN EMISSION LIMIT OF 0.06 LB/MMBTU. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU Limits are for each boiler. Each boiler is retricted to 100 hours of operation. LB/MMBTU Limits are for each heater. LB/MMBTU

BACT IS POLLUTION PREVENTION

LB/MMBTU NOT AVAI PERMIT LIMIT IS IN PPM, AND LB/DAY. A LIMIT IN LB/MMBTU WAS NOT PROVIDED.

LB/MMBTU Limits are for each boiler. NOT AVAI

LB/MMBTU

LB/MMBTU LB/MMBTU

CALCULAT each unit


LB/MMBTU LB/MMBTU

CALCULAT CALCULAT

LB/MMBTU LB/MMBTU

LB/MMBTU

Calculated NOT AVAI

LB/MMBTU SEE NOTESTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. SEE NOTESTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. CALCULATEMISSION LIMIT IN STANDARDIZED UNITS WAS CALCULATED BY DIVIDING THE HOURLY LIMIT BY THE THROUGHPUT. SEE NOTESTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT.

LB/MMBTU NOT AVAI

LB/MMBTU LB/MMBTU

calculated Additional limit: .66 t/yr NOT AVAI CALCULAT CALCULAT

LB/MMBTU

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU Limit is based on combustion of natural gas. Limit for burning #2 fuel oil is 0.14 lb/MMBtu LB/MMBTU LB/MMBTU LB/MMBTU Limit does not apply during startup and shut down. LB/MMBTU

LB/MMBTU LB/MMBTU LB/MMBTU Limit while burning propane: 0.15 lb/mmbtu (propane limited to < 336 h/yr each)

calculated CALCULATESTIMATED CAPITAL COSTS RANGE FROM $ 7500 TO $ 25000 FOR EACH BOILER. CALCULATESTIMATED CAPITAL COSTS RANGE FROM $ 7500 TO $ 25000 FOR EACH BOILER. CALCULATESTIMATED CAPITAL COSTS RANGE FROM $ 7500 TO $ 25000 FOR EACH BOILER.

LB/MMBTU

CALCULATNATURAL GAS USAGE LIMITED TO 559 MMCF/YR LB/MMBTU LB/MMBTU LB/MMBTU

CALCULAT CALCULAT 3 HOUR T OPERATION LIMITED TO 500 HOURS PER YEAR. THIS UNIT CAN BURN UP TO 289,000 GAL/YR OF DISTILATE OIL. SEE THE PROCEESS AUXILIARY BOILER (OIL) FOR EMISSION LIMITS WHILE BURNING DISTILATE OIL.

LB/MMBTU LB/MMBTU NATURAL GAS FIRED, 46.2 MMBTU/HR BOILER 1.22 LBS NOX / HR @ 37.1 MMBTU/HR (0.033 LBS/MMBTU)

CALCULATIF CAPACITY FACTOR DURING THE OZONE SEASON EXCEEDS 20%, THE FACILITY SHALL CONDUCT A COMBUSTION OPTIIMIZATION (IN ACCORDANCE WITH CH. NR 439, NOX RACT). NOT SUBJECT TO PSD BACT, AS THE INCREASE WAS OFFSET BY ADDITIONAL REDUCTIONS FROM THE COMBUSTION TURBINES / DUCT BURNERS. LBS/MMBTU

NOT AVAI (LIMIT IS FOR EACH UNIT) PER ROLLING 12-MONTH PERIOD. THESE ARE FACILITY-WIDE EMISSION LIMITS. FOR COMBUSTION UNITS B03, B04, AND B08, EACH HAS AN ANNUAL EMISSION LIMIT OF 1.12 TONS PER YEAR.

LB/MMBTU LB/MMBTU LB/MMBTU LIMITS ARE FOR EACH BOILER. LB/MMBTU

ANNUAL A*TPY LIMIT FOR ALL 3 HEATERS. AGGREGATE HEAT INPUT IS LIMITED TO 14,250 MM BTU/YR. ONLY 2 OF THE 3 HEATERS ARE ALLOWED TO OPERATE AT ANY GIVEN TIME. CALCULAT THREE ON

*SEE NOT LOW NOX BURNERS / FLUE GAS RECIRCULATION *SEE NOT CONVENTIONAL BURNER TECHNOLOGY


LB/MMBTU LB/MMBTU PPMVD" S WHICH RATED HEAT INPUT IS 35.4 MMBTU/H."

LB/MMBTU LIMITS ARE FOR EACH BOILER.

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU THE OUTLET PARTICULATE CONCENTRATION FROM EACH FABRIC FILTER CONTROL DEVICE SHALL NOT EXCEED 0.003 GR PER ACF. LB/MMBTU LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTU 500 H/YR RESTRICTION - THE ONLY REVISION MADE TO THE EXISTING PERMIT. LB/MMBTU

NOT TO EMIT GASES WITH PARTICULATE CONTENT EXCEEDING RATE CALCULATED THUS: E=0.5*(10/R) ^0.5, WHERE E=ALLOWABLE EMISSION RATE IN LB/MMBTU, AND R= HEAT INPUT IN MMBTU/H CALCULATBACT IS TO COMPLY WITH STATE STANDARDS 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU AND 1 GR = .000143 LB. CALCULATBACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1000 BTU = 1 DSCF NATURAL GAS AND 0.000143 LB = 1 GR. CALCULATBACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU CONVERTED USING FOLLOWING CONVERSION FACTORS; 1 DSCF NATURAL GAS = 1000 BTU, AND 1 GR = 0.000143 LB. CALCULATBACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. CALCULATBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. CALCULATBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS; 1 DSCF NATURAL GAS = 1000 BTU, AND 1 GR = 0.000143. CONVERTEEMISSIONS IN LB/MMBTU WERE CONVERTED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. CALCULATEMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055 CALCULATEMISSIONS IN LB/MMBTU CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 1 GR = 0.000143 LB. BACT IS CONSIDRED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055.

LB/MMBTU LB/MMBTU

FOR NO M FOR NO M CONVERTEPOLLUTANT DESCRIBED AS PM/PM10. OPACITY LIMIT OF 5%, AVERAGED OVER A 6-MINUTE PERIOD.

LB/MMBTU EACH, CA BASIS OF DETERMINATION IS 18 AAC 50.055(B)(1). THE OWNER REQUESTED TO LIMIT THE SULFUR CONTENT OF GASEOUS AND LIQUID FUELS TO 200-PPM HYDROGEN SULFIDE AND 0.25% SULFUR BY WEIGHT TO AVOID A PSD PRE-CONSTRUCTION REVIEW OF EXISTING EQUIPMENT. THE OWNER WILL ALSO LIMIT NATURAL GAS CONSUMPTION FOR GLYCOL HEATERS NO. 1, 2, AND 3 TO A COMBINED USE NOT TO EXCEED 63 MMSCF/12-MO PERIOD. THE EMISSION LLIMIT IN LB/MMBTU WAS CALCULATED BY DIVIDING THE HOURLY EMISSION LIMIT BY THE THROUGHPUT. CALCULATBASIS OF DETERMINATION - 18 AAC 50.055(B)(1). THE HOURLY EMISSION LIMIT WAS CONVERTED INTO STANDARDIZED UNITS BY DIVIDING IT BY THE THROUGHPUT.


LB/MMBTU CALCULATEMISSIONS PROVIDED IN LB/MMBTU WERE CALCULATED BY CONVERTING GR TO LB USING THE CONVERSION FACTOR OF 0.00014285714 AND BY CONVERTING DSCF TO MMBTU USING THE NATURAL GAS EQUIVALENT CONVERSION FACTOR OF 0.001. CALCULATEMISSIONS PROVIDED IN LB/MMBTU WERE CALCULATED BY CONVERTING GR TO LB USING THE CONVERSION FACTOR OF 0.00014285714 AND BY CONVERTING DSCF TO MMBTU USING THE NATURAL GAS HEAT VALUE (CONVERSION FACTOR) OF 0.001. CALCULATEMISSIONS PROVIDED IN LB/MMBTU WERE CALCULATED BY CONVERTING GR TO LB USING THE CONVERSION FACTOR OF 0.00014285714 AND BY CONVERTING DSCF TO MMBTU USING THE NATURAL GAS EQUIVALENT CONVERSION FACTOR OF 0.001.

LB/MMBTU LB/MMBTU

LB/MMBTU USING NATURAL GAS WITH BACKUP NO.2 FUEL OIL. EMISSIONS BASED ON MFG. TESTED RATE FOR NATURAL GAS 0.005 LB PE/MMBTU. LB/MMBTU BAGHOUSE WITH MANUFACTURER'S GUARANTEED GRAIN LOADING OF 0.0025 GRAIN/DSCF AND AIR FLOW RATE USED TO DEMONSTRATE COMPLIANCE. IF REQUIRED BY REGULATING AGENCY, METHOD 5 AND/OR 9 MAY BE USED TO DEMONSTRATE COMPLIANCE.

7.6 LB/MMPM EMISSIONS ARE FROM THE STANDARD IN AP-42. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU one of two boilers LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

calculated LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI PM (INCL. M202 BACKHALF CATCH) (LIMIT IS FOR EACH UNIT)

LB/MMBTU LIMITS ARE FOR EACH BOILER. PM LIMIT INCLUDES BOTH FILTERABLE AND CONDENSABLE FRACTIONS.

LB/MMBTU Filterable fraction only LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI NOT AVAI THREE ON CALCULAT

LB/MMBTU 500 H/YR RESTRICTION - THE ONLY REVISION MADE TO THE EXISTING PERMIT. CALCULATSTANDARD EMISSION LIMITS CALCULATED FROM HOURLY EMISSION LIITS AND HEATERS RATED CAPACITY.


Not Availab NOT AVAI

TOTAL PM10 EMISIONS FROM THE TWO FURNACES SHALL NOT EXCEED 0.61 LB/TON OF FEED/CHARGE. LB/MMBTU LB/MMBTU LB/MMBTU

NOT AVAI

LB/MMBTU LB/MM BTU

NOT AVAI LB/MMBTU

LB/MMBTU LB/MMBTU Limits are for each boiler. Only 2 of the 4 boilers modified in this permit. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU EMISSION LIMIT 1 APPLIES TO EACH AUXILIARY BOILER. LB/MMBTU LB/MMBTU LB/MMBTU LB / MMBTU LB/MMBTU

Not Availab

HEAT INPUT TO THE AUXILIARY BOILERS (2) SHALL BE LIMITED TO 210,240 MMBTU FOR ANY CONSECUTIVE 12-MONTH PERIOD LB/MMBTU LB/MMBTU

calculated Boiler is restricted to 800 hours or operation per a rolling 12 months. LB/MMBTU

NOT AVAI

LB/MMBTU CALCULAT NOT AVAI

LB/MMBTU LB/MMBTU

calculated LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU Limits are for each boiler. Each boiler is retricted to 100 hours of operation.

LB/MMBTU Limits are for each heater. LB/MMBTU

calculated

LB/MMBTU LB/MMBTU LB/MMBTU Limits are for each boiler. Additional limit: 10% Opacity as a 6 minute average. LB/MMBTU LB/MMBTU

EACH UNI



LB/MMBTU LB/MMBTU

CALCULATSTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT.

LB/MMBTU STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. SEE NOTESTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT.

LB/MMBTU STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. ANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL AANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

LB/MMBTU LB/MMBTU LB/MMBTU one of two units.

NOT AVAI LB/MMBTU


calculated CALCULAT CALCULAT CALCULAT

LB/MMBTU NOT AVAI

LB/MMBTU LB/MMBTU

BOTH PM / PM10 EMISSIONS OF 0.132 LBS/HR @ 37.1 MMBTU/HR (0.0036 LBS/MMBTU) CALCULATBOTH PM / PM10

CALCULATBOTH PM / PM10 NOT AVAI (LIMIT IS FOR EACH UNIT)

LB/MMBTU LB/MMBTU LIMITS ARE FOR EACH BOILER

ANNUAL A*TPY LIMIT FOR ALL 3 HEATERS. AGGREGATE HEAT INPUT IS LIMITED TO 14,250 MM BTU/YR. ONLY 2 OF THE 3 HEATERS ARE ALLOWED TO OPERATE AT ANY GIVEN TIME. CALCULAT THREE ON

PM10 - FILERABLE AND CONDENSIBLE LB/MMBTU LB/MMBTU THE DATA PERTAIN TO EITHER ONE OF THE HURST BOILERS, WHICH RATED HEAT INPUT IS 35.4 MMBTU/H. LB/MMBTU LIMITS ARE FOR EACH BOILER.

BECAUSE OF UNIT SIZE (62.4 MMBTU/HR) AND FUEL TYPE (NATURAL GAS), CONTROL IS COST PROHIBITIVE.

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

PERMIT LIMIT IS USE OF FUEL WITH H2S < 200 PPMV H2S. CALCULATSTANDARD EMISSION LIMITS CALCULATED FROM HOURLY EMISSION LIITS AND HEATERS RATED CAPACITY. CONVERTE CONVERTEBACT: FUEL SULFUR CONTENT LIMIT. STATE: EMISSION LIMIT 1 CALCULATBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 CALCULATBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 CALCULATBACT: FUEL SULFUR CONTENT LIMITS STATE: EMISSION LIMIT NO. 1 CALCULATBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 CALCULATBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 PLUS FUEL RESTRICTIONS CALCULATBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR RESTRICTION TO THE FUEL CALCULATBACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR CONTENT RESTRICTION TO FUEL


NOT AVAI 18 AAC 50.055(C) LIMIT IS 500 PPM, 3 H AVER NOT AVAI 18 AAC 50.055(C) LIMIT IS 500 PPM, 3 HR AVER CONVERTE

LB/MMBTU LB/MMBTU

EACH, CA BASIS OF DETERMINATION IS 18 AAC 50.055(C). THE HOURLY EMISSION LIMIT WAS CONVERTED INTO STANDARDIZED UNITS BY DIVIDING IT BY THE THROUGHPUT. THE OWNER REQUESTED TO LIMIT THE SULFUR CONTENT OF GASEOUS AND LIQUID FUELS TO 200-PPM HYDROGEN SULFIDE AND 0.25% SULFUR BY WEIGHT TO AVOID A PSD PRE-CONSTRUCTION REVIEW OF EXISTING EQUIPMENT. THE OWNER WILL ALSO LIMIT NATURAL GAS CONSUMPTION FOR GLYCOL HEATERS NO. 1, 2, AND 3 TO A COMBINED USE NOT TO EXCEED 63 MMSCF/12-MO PERIOD. CALCULATBASIS OF DETERMINATION- 18 AAC 50.055(C). THE HOURLY EMISSION LIMIT WAS CONVERTED INTO STANDARDIZED UNITS BY DIVIDING IT BY THE THROUGHPUT. NOT AVAI

STATE BACT PERFORMED LB/MMBTU LB/MMBTU

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU EMISSION LIMIT 1 APPLIES TO EACH AUXILIARY BOILER. LB/MMBTU

CALCULATEMISSIONS IN LB/MMBTU WERE CALCULATED USING THE ASSUMPTION THAT EMISSIONS IN PPM ARE AT 15% O2 AND THE FUEL IS NATURAL GAS. CALCULATEMISSIONS IN LB/MMBTU WERE CALCULATED USING THE ASSUMPTION THAT EMISSIONS IN PPM ARE AT 15% O2 AND THE FUEL IS NATURAL GAS. CALCULATEMISSIONS IN LB/MMBTU WERE CALCULATED USING THE ASSUMPTION THAT EMISSIONS IN PPM ARE AT 15% O2 AND THE FUEL IS NATURAL GAS.

LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU Boiler is restricted to 800 hours or operation per a rolling 12 months.

NOT AVAI

NOT AVAI THE ORIGINAL PERMIT LIMITED SO2 EMISSIONS TO 0.03 LB/HR AND 0.001 LB/MMBTU. LB/MMBTU LB/MMBTU LB/MMBTU

CALCULAT LB/MMBTU Using AP-42 emission factor of 0.6 lb/million cubic feet LB/MMBTU Emissions from natural gas combustion, using 0.0006 lb SO2/mmBtu LB/MMBTU

LB/MMBTU Additional limit: 2 grains/100 scf natural gas LB/MMBTU

no emission rate limit, fuels limit.

LB/MMBTU Limits are for each boiler. Each boiler is retricted to 100 hours of operation. LB/MMBTU Limits are for each heater.

calculated LB/MMBTU LB/MMBTU Limits are for each boiler.

No emission rate limits, BACT is pollution prevention

EACH UNI LB/MMBTU UNCONTROLLED BECAUSE BOILER IS LESS THAN 40 MMBTU/H.

NOT AVAI


LB/MMBTU LB/MMBTU

limit is fuel sulfur limit, no emission rate limit.

SEE NOTESTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. SEE NOTESTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. SEE NOTESTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. CALCULATSTANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. calculated

LB/MMBTU One of two units. NOT AVAI

LB/MMBTU


CALCULAT CALCULAT CALCULAT

LB/MMBTU

BACT is fuel sulfur limit.

LB/MMBTU

CALCULAT CALCULAT NOT AVAI (LIMIT IS FOR EACH UNIT)

LB/MMBTU LB/MMBTU LIMITS ARE FOR EACH BOILER.

ANNUAL A*TPY LIMIT FOR ALL 3 HEATERS. AGGREGATE HEAT INPUT IS LIMITED TO 14,250 MM BTU/YR. ONLY 2 OF THE 3 HEATERS ARE ALLOWED TO OPERATE AT ANY GIVEN TIME. CALCULAT

LIMIT SULFUR CONTENT IN FUEL COMBUSTED * EMISSION UNITS AND NUMERIC LIMITS ARE REQUIRED FOR SO2 USING APPENDIX E. PROCESS CODE 13.110 *SEE NOT * LIMIT SULFUR CONTENT OF FUEL COMBUSTED *SEE NOT LIMIT SULFUR CONTENT OF FUEL COMBUSTED

LB/MMBTU LB/MMBTU LIMITS ARE FOR EACH BOILER.

LB/MMBTU

NOT AVAI LB/MMBTU LB/MMBTU THE DATA PERTAIN TO EITHER ONE OF THE HURST BOILERS, WHICH RATED HEAT INPUT IS 35.4 MMBTU/H.

CALCULAT(LISTED AS SULFURIC ACID EMISSIONS) (LIMIT IS FOR EACH UNIT)


% OPACITY % OPACITY % OPACITY

6 MIN AV 6 minute a FOR > 3 MBACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055 FOR FUEL BURNING EQUIPMENT. FOR > 3 MBACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. FOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH THE STATE STANDARD 18 AAC 50.055. FOR > 3 MBACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. FOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. FOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055 FOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. FOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. FOR > 3 MBACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. FOR NO MBASIS OF DETERMINATION IS 18 AAC 50.055(A)(1) FOR NO MBASIS OF DETERMINATION IS 18 AAC 50.055(A)(1) EACH, EXCBASIS OF DETERMINATION- 18 AAC 50.055(A)(1) EXCEPT FODETERMINATION BASED ON 18 AAC 50.055(A)(1)

% OPACITY 6 MIN AV

% OPACITY STATE REG 6 min avg 6 MINUTE

% OPACITY 3 MIN/H 3 MIN/H 3 MIN/H as a 6 min

% OPACITY

as a six mi Boiler is restricted to 800 hours or operation per a rolling 12 months. 6 MIN AV 6 MIN AV 6-minute a

% OPACITY 6 minute a

% OPACITY as a six mi Limits are for each boiler. Each boiler is retricted to 100 hours of operation. as a six mi Limits are for each heater.

% OPACITY VE limited to 40% opacity when cleaning firebox or blowing soot, and for no more than 6 min/h % OPACITY % OPACITY State reg is regulatory basis. % OPACITY % OPACITY % OPACITY % OPACITY

AS A 6-M VE MAY EXCEED 20% OPACITY, AS A 6-MINUTE AV, FOR NOT MORE THAN 6 CONSECUTIVE MINUTES IN ANY 60 MINUTES, BUT SHALL NOT EXCEED 60% OPACITY AS A 6-MINUTE AV AT ANY TIME. % OPACITY % OPACITY % OPACITY

AS A 6-M OPACITY AT ANY STACK FROM EITHER BOILER.

LB/MMBTU ADDITIONAL VOC LIMIT IS 50 PPMVD @7% O2. LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

VOC ADDITIONAL EMISSION LIMITS: 0.13 T/YR LB/MMBTU LB/MMBTU LB/MMBTU LB/MMBTU

REACTIVELIMITS ARE FOR REACTIVE ORGANIC GASES. Not Availab

POLLUTANT IS A MIXTURE OF PROPYLENE AND PROPANE.

LB/MMBTU LB/MMBTU

BACT FOR VOC IS DETERMINED TO BE USE OF NATURAL GAS TO FUEL BOILER. NO EMISSION RATE LI BACT FOR VOC IS DETERMINED TO BE GOOD COMBUSTION CONTROL AND THE USE OF NATURAL GAS

LB/MMBTU LB/MM BTU LB/MMBTU LB/MMBTU LB/MMBTU Limit is for each boiler. Only 2 of the 4 boilers modified in this permit. Additional limit: 0.48 T/YR LB/MMBTU

LB/MMBTU LB/MMBTU LB/MMBTU EMISSION LIMIT 1 APPLIES TO EACH AUXILIARY BOILER. LB/MMBTU LB/MMBTU LB/MMBTU

LB/MMBTU

HEAT INPUT TO THE AUXILIARY BOILERS (2) SHALL BE LIMITED TO 210,240 MMBTU FOR ANY CONSECUTIVE 12-MONTH PERIOD

LB/MMBTU

LB/MMBTU Boiler is restricted to 800 hours or operation per a rolling 12 months. LB/MMBTU

NOT AVAI THE ORIGINAL PERMIT LIMITED VOC EMISSIONS TO 0.469 LB/HR.

Using Manufacturer's guaranteed emission rate: 8 lbs VOC/1,000,000 lbs air on natural gas. Emissions are from natural gas combustion, using 0.003 lb VOC/mmBtu

LB/MMBTU limit for burners A and B combined: 2.3 lb/h

LB/MMBTU calculated

LB/MMBTU

LB/MMBTU

LB/MMBTU Limits are for each boiler. Each boiler is retricted to 100 hours of operation. LB/MMBTU Limits are for each heater.

Additional limit: .005 lb/mmBtu

LB/MMBTU Limits are for each boiler. No emission rate limit, BACT is pollution prevention.

PPMVD@3%O2

EACH UNI UNCONTROLLED BECAUSE BOILER IS LESS THAN 40 MMBTU/H.

LB/MMBTU Cat. Ox. primarily controlling CO

ANNUAL A one of two units

FROM NATURAL GAS COMBUSTION LB/MMBTU

LB/MMBTU

LB/MMBTU

ANNUAL A LB/MMBTU

NONMETHANE HYDROCARBONS LIMITS ARE FOR NONMETHANE HYDROCARBONS.

LB/MMBTU

ANNUAL A *SEE NOT * CACULATED STANDARD NUMERIC LIMIT CALCULAT

(LIMIT IS FOR EACH UNIT) BACT IS GOOD DESIGN. NO EMISSION RATE LIMITS.

LB/MMBTU LIMITS ARE FOR EACH BOILER ANNUAL A*TPY LIMIT FOR ALL 3 HEATERS. AGGREGATE HEAT INPUT IS LIMITED TO 14,250 MM BTU/YR. ONLY 2 OF THE 3 HEATERS ARE ALLOWED TO OPERATE AT ANY GIVEN TIME.


LB/MMBTU THE DATA PERTAIN TO EITHER ONE OF THE HURST BOILERS, WHICH RATED HEAT INPUT IS 35.4 MMBTU/H. LB/MMBTU LB/MMBTU LIMITS ARE FOR EACH BOILER.

THE LIMITS ARE WRITTEN AS 98% REDUCTION ACROSS THE DRYER COMBUSTION CHAMBER AND 3.16 LB/HR AT THE OUTLET OF THE DRYER. THE POUND PER HOUR LIMIT IS MEASURED AS THE SUM OF THE METHOD 18 OR METHOD 320 RESULTS.

REGULATED POLLUTANT IS SULFURIC ACID MIST. EMISSION LIMIT IS 0.00015 LB/MMBTU

THESE LIMITS APPLY TO DUCT BURNERS OPERATING IN THE FRESH AIR MODE.

ADDITIONAL EMISSION LIMITS: 100 PPM @ 7% O2 24 H AV. THE CO EMISSION LIMITS APPLY WHENEVER HAZARDOUS WASTE IS BEING BURNED IN THE BOILER. HAZARDOUS WASTE MAY NOT BE BURNED IN THE WASTE HEAT BOILER UNTIL AND UNLESS APPROPRIATE AUTHORITY IS OBTAINED UNDER RCRA.

ADDITIONAL CO LIMIT OF 100 PPMVD WHEN CORRECTED TO 3 % O2 (ONE-HOUR AVERAGE).

EMISSION LIMITS 1 & 2 TAKE EFFECT ON JANUARY 1, 2006, PER SECTION 49 OF THE AIR QUALITY REGULATIONS. EMISSION LIMIT 2 APPLIES TO EACH AUXILIARY BOILER.


USING MANUFACTURER'S EMISSION FACTORS OF 150 LBS CO/1,000,000 POUNDS OF AIR for both NG and #2 fuel oil.

STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

THESE ARE FACILITY-WIDE EMISSION LIMITS. FOR COMBUSTION UNITS B03, B04, AND B08, EACH HAS AN ANNUAL EMISSION LIMIT OF 0.94 TONS PER YEAR.

*TPY LIMIT FOR ALL 3 HEATERS. AGGREGATE HEAT INPUT IS LIMITED TO 14,250 MM BTU/YR. ONLY 2 OF THE 3 HEATERS ARE ALLOWED TO OPERATE AT ANY GIVEN TIME.

THE DATA PERTAIN TO EITHER ONE OF THE HURST BOILERS, WHICH RATED HEAT INPUT IS 35.4 MMBTU/H.

BASIS OF LIMIT IS STATE EMISSION OFFSET RULE. NOX LIMIT IS AS NO2""

Synthetic minor. PROJECT NOT SIGNIFICANT FOR NOX - NO BACT DETERMINATI0N REQUIRED.

EMISSIONS REGULATED UNDER PSD-TX-957 PERMIT AUTHORIZATION

SOURCE TEST RESULTS: O2, % (DRY) 19.66 NOX, PPMVD 3.02 (43.6 PPMVD@3%O2) CO2, % (DRY) 0.463 CO, PPMVD 15.01 FLUE GAS FLOW RATE, DSCFM 8,138 AQMD'S MONITORING AND SOURCE TEST ENGINEERING GROUP APPROVED THIS SOURCE TEST AS SHOWING THE NOX TO BE LESS THAN 60 PPMVD@3%O2.

THE APPLICANT PROPOSED TO USE THE ALZETA ULNB. ALTHOUGH THE MODEL CBS BURNER HAS NOT BEEN DEMONSTRATED IN A PROCESS HEATER, IT HAS BEEN SUCCESSFULLY DEMONSTRATED IN A VARIETY OF WATER-TUBE AND FIRED-TUBE BOILERS. WHILE THIS APPLICATION HAS NOT YET BEEN SOURCE TESTED, IT IS HIGHLY PROBABLE THAT IT WILL PROVE SUCCESSFUL AND WILL BECOME ACHIEVED-IN-PRACTICE TECHNOLOGY FOR SMALL PROCESS HEATERS OF THIS TYPE. THE LEVEL WAS SUGGESTED BY THE APPLICANT.

THIS IS A RECLAIM FACILITY. THE FACILITY REQUESTED A PERMIT MODIFICATION TO APPLY A RECLAIM CONCENTRATION LIMIT OF 40 PPMVD (CORRECTED TO 3% O2) TO THIS FURNACE. THIS LOW-NOX BURNER IS CONSIDERED ACHIEVED IN PRACTICE. ALTHOUGH THIS BURNER IS CAPABLE OF MEETING A NOX LIMIT OF 40 PPM IN THIS FURNACE WHEN OPERATED ON NATURAL GAS, NOX EMISSIONS MAY BE DIFFERENT IN OTHER FURNACES WITH OTHER BURNER/FURNACE CONFIGURATIONS, OPERATING TEMPERATURES OR OTHER OPERATING CONDITIONS. IT IS SUGGESTED THE THE NOX EMISSION GUARANTEE OR 50 PPM, THE BACT PART D GUIDELINE, BE USED AS A STARTING POINT IN PERMITTING A NEW OR MODIFIED FURNACE, I.E., IN THE PERMIT TO CONSTRUCT, AND THAT THE FINAL NOX LIMIT IN THE PERMIT TO OPERATE BE DETERMINED AFTER SOURCE TESTING IS COMPLETED. SOURCE TESTING SHOULD INCLUDE THE HIGHEST-NOX OPERATING MODE

EMISSION LIMIT 1 IS AN EMISSION STANDARD PER SECTION 49 OF THE AIR QUALITY REGULATIONS. EMISSION LIMIT 2 APPLIES TO EACH AUXILIARY BOILER.

Emission limit 2 is the maximum emission rate per heater / oxidizer combination. In addition, an annual emission limit of 5.23 T/YR applies to the same combination.


EMISSION LIMITS BASED ON MANUFACTER'S TEST DATA. Additional limit: 9.6 ppm @ 15% O2 as 6-monute average.

THIS HEATER IS PERMITTED TO USE ULTRA LOW NOX BURNERS AS CONTROL WITH AN EMISSION LIMIT OF 0.04 LB/MMBTU OR COMBINATION BURNERS AS CONTROL WITH AN EMISSION LIMIT OF 0.06 LB/MMBTU.

PERMIT LIMIT IS IN PPM, AND LB/DAY. A LIMIT IN LB/MMBTU WAS NOT PROVIDED.

STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. EMISSION LIMIT IN STANDARDIZED UNITS WAS CALCULATED BY DIVIDING THE HOURLY LIMIT BY THE THROUGHPUT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT.

Limit is based on combustion of natural gas. Limit for burning #2 fuel oil is 0.14 lb/MMBtu

Limit while burning propane: 0.15 lb/mmbtu (propane limited to < 336 h/yr each)

ESTIMATED CAPITAL COSTS RANGE FROM $ 7500 TO $ 25000 FOR EACH BOILER. ESTIMATED CAPITAL COSTS RANGE FROM $ 7500 TO $ 25000 FOR EACH BOILER. ESTIMATED CAPITAL COSTS RANGE FROM $ 7500 TO $ 25000 FOR EACH BOILER.

OPERATION LIMITED TO 500 HOURS PER YEAR. THIS UNIT CAN BURN UP TO 289,000 GAL/YR OF DISTILATE OIL. SEE THE PROCEESS AUXILIARY BOILER (OIL) FOR EMISSION LIMITS WHILE BURNING DISTILATE OIL.

NATURAL GAS FIRED, 46.2 MMBTU/HR BOILER 1.22 LBS NOX / HR @ 37.1 MMBTU/HR (0.033 LBS/MMBTU) IF CAPACITY FACTOR DURING THE OZONE SEASON EXCEEDS 20%, THE FACILITY SHALL CONDUCT A COMBUSTION OPTIIMIZATION (IN ACCORDANCE WITH CH. NR 439, NOX RACT). NOT SUBJECT TO PSD BACT, AS THE INCREASE WAS OFFSET BY ADDITIONAL REDUCTIONS FROM THE COMBUSTION TURBINES / DUCT BURNERS.



THE OUTLET PARTICULATE CONCENTRATION FROM EACH FABRIC FILTER CONTROL DEVICE SHALL NOT EXCEED 0.003 GR PER ACF.

500 H/YR RESTRICTION - THE ONLY REVISION MADE TO THE EXISTING PERMIT.

NOT TO EMIT GASES WITH PARTICULATE CONTENT EXCEEDING RATE CALCULATED THUS: E=0.5*(10/R) ^0.5, WHERE E=ALLOWABLE EMISSION RATE IN LB/MMBTU, AND R= HEAT INPUT IN MMBTU/H BACT IS TO COMPLY WITH STATE STANDARDS 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU AND 1 GR = .000143 LB. BACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1000 BTU = 1 DSCF NATURAL GAS AND 0.000143 LB = 1 GR. BACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU CONVERTED USING FOLLOWING CONVERSION FACTORS; 1 DSCF NATURAL GAS = 1000 BTU, AND 1 GR = 0.000143 LB. BACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS; 1 DSCF NATURAL GAS = 1000 BTU, AND 1 GR = 0.000143. EMISSIONS IN LB/MMBTU WERE CONVERTED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055 EMISSIONS IN LB/MMBTU CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 1 GR = 0.000143 LB. BACT IS CONSIDRED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055.

POLLUTANT DESCRIBED AS PM/PM10. OPACITY LIMIT OF 5%, AVERAGED OVER A 6-MINUTE PERIOD.

BASIS OF DETERMINATION IS 18 AAC 50.055(B)(1). THE OWNER REQUESTED TO LIMIT THE SULFUR CONTENT OF GASEOUS AND LIQUID FUELS TO 200-PPM HYDROGEN SULFIDE AND 0.25% SULFUR BY WEIGHT TO AVOID A PSD PRE-CONSTRUCTION REVIEW OF EXISTING EQUIPMENT. THE OWNER WILL ALSO LIMIT NATURAL GAS CONSUMPTION FOR GLYCOL HEATERS NO. 1, 2, AND 3 TO A COMBINED USE NOT TO EXCEED 63 MMSCF/12-MO PERIOD. THE EMISSION LLIMIT IN LB/MMBTU WAS CALCULATED BY DIVIDING THE HOURLY EMISSION LIMIT BY THE THROUGHPUT. BASIS OF DETERMINATION - 18 AAC 50.055(B)(1). THE HOURLY EMISSION LIMIT WAS CONVERTED INTO STANDARDIZED UNITS BY DIVIDING IT BY THE THROUGHPUT.

EMISSIONS PROVIDED IN LB/MMBTU WERE CALCULATED BY CONVERTING GR TO LB USING THE CONVERSION FACTOR OF 0.00014285714 AND BY CONVERTING DSCF TO MMBTU USING THE NATURAL GAS EQUIVALENT CONVERSION FACTOR OF 0.001. EMISSIONS PROVIDED IN LB/MMBTU WERE CALCULATED BY CONVERTING GR TO LB USING THE CONVERSION FACTOR OF 0.00014285714 AND BY CONVERTING DSCF TO MMBTU USING THE NATURAL GAS HEAT VALUE (CONVERSION FACTOR) OF 0.001. EMISSIONS PROVIDED IN LB/MMBTU WERE CALCULATED BY CONVERTING GR TO LB USING THE CONVERSION FACTOR OF 0.00014285714 AND BY CONVERTING DSCF TO MMBTU USING THE NATURAL GAS EQUIVALENT CONVERSION FACTOR OF 0.001.

USING NATURAL GAS WITH BACKUP NO.2 FUEL OIL. EMISSIONS BASED ON MFG. TESTED RATE FOR NATURAL GAS 0.005 LB PE/MMBTU. BAGHOUSE WITH MANUFACTURER'S GUARANTEED GRAIN LOADING OF 0.0025 GRAIN/DSCF AND AIR FLOW RATE USED TO DEMONSTRATE COMPLIANCE. IF REQUIRED BY REGULATING AGENCY, METHOD 5 AND/OR 9 MAY BE USED TO DEMONSTRATE COMPLIANCE.

PM LIMIT INCLUDES BOTH FILTERABLE AND CONDENSABLE FRACTIONS.

500 H/YR RESTRICTION - THE ONLY REVISION MADE TO THE EXISTING PERMIT. STANDARD EMISSION LIMITS CALCULATED FROM HOURLY EMISSION LIITS AND HEATERS RATED CAPACITY.

TOTAL PM10 EMISIONS FROM THE TWO FURNACES SHALL NOT EXCEED 0.61 LB/TON OF FEED/CHARGE.

Limits are for each boiler. Additional limit: 10% Opacity as a 6 minute average.

STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

BOTH PM / PM10 EMISSIONS OF 0.132 LBS/HR @ 37.1 MMBTU/HR (0.0036 LBS/MMBTU)



BECAUSE OF UNIT SIZE (62.4 MMBTU/HR) AND FUEL TYPE (NATURAL GAS), CONTROL IS COST PROHIBITIVE.

STANDARD EMISSION LIMITS CALCULATED FROM HOURLY EMISSION LIITS AND HEATERS RATED CAPACITY.

BACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 PLUS FUEL RESTRICTIONS BACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR RESTRICTION TO THE FUEL BACT: FUEL SULFUR CONTENT LIMIT STATE: EMISSION LIMIT 1 AND SULFUR CONTENT RESTRICTION TO FUEL

BASIS OF DETERMINATION IS 18 AAC 50.055(C). THE HOURLY EMISSION LIMIT WAS CONVERTED INTO STANDARDIZED UNITS BY DIVIDING IT BY THE THROUGHPUT. THE OWNER REQUESTED TO LIMIT THE SULFUR CONTENT OF GASEOUS AND LIQUID FUELS TO 200-PPM HYDROGEN SULFIDE AND 0.25% SULFUR BY WEIGHT TO AVOID A PSD PRE-CONSTRUCTION REVIEW OF EXISTING EQUIPMENT. THE OWNER WILL ALSO LIMIT NATURAL GAS CONSUMPTION FOR GLYCOL HEATERS NO. 1, 2, AND 3 TO A COMBINED USE NOT TO EXCEED 63 MMSCF/12-MO PERIOD. BASIS OF DETERMINATION- 18 AAC 50.055(C). THE HOURLY EMISSION LIMIT WAS CONVERTED INTO STANDARDIZED UNITS BY DIVIDING IT BY THE THROUGHPUT.

EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE ASSUMPTION THAT EMISSIONS IN PPM ARE AT 15% O2 AND THE FUEL IS NATURAL GAS. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE ASSUMPTION THAT EMISSIONS IN PPM ARE AT 15% O2 AND THE FUEL IS NATURAL GAS. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE ASSUMPTION THAT EMISSIONS IN PPM ARE AT 15% O2 AND THE FUEL IS NATURAL GAS.

THE ORIGINAL PERMIT LIMITED SO2 EMISSIONS TO 0.03 LB/HR AND 0.001 LB/MMBTU.

STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT. STANDARDIZED EMISSION LIMIT CALCULATED FROM HEAT RATING AND HOURLY EMISSION LIMIT.


LIMIT SULFUR CONTENT IN FUEL COMBUSTED * EMISSION UNITS AND NUMERIC LIMITS ARE REQUIRED FOR SO2 USING APPENDIX E. PROCESS CODE 13.110


BACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055 FOR FUEL BURNING EQUIPMENT.

BACT IS CONSIDERED COMPLIANCE WITH THE STATE STANDARD 18 AAC 50.055.

BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055 BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055.

VE limited to 40% opacity when cleaning firebox or blowing soot, and for no more than 6 min/h

VE MAY EXCEED 20% OPACITY, AS A 6-MINUTE AV, FOR NOT MORE THAN 6 CONSECUTIVE MINUTES IN ANY 60 MINUTES, BUT SHALL NOT EXCEED 60% OPACITY AS A 6-MINUTE AV AT ANY TIME.

Limit is for each boiler. Only 2 of the 4 boilers modified in this permit. Additional limit: 0.48 T/YR


Using Manufacturer's guaranteed emission rate: 8 lbs VOC/1,000,000 lbs air on natural gas.

EMISSION LIMITS 1 & 2 TAKE EFFECT ON JANUARY 1, 2006, PER SECTION 49 OF THE AIR QUALITY REGULATIONS. EMISSION LIMIT 2 APPLIES TO EACH AUXILIARY BOILER.

ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.




EMISSION LIMIT 1 IS AN EMISSION STANDARD PER SECTION 49 OF THE AIR QUALITY REGULATIONS. EMISSION LIMIT 2 APPLIES TO EACH AUXILIARY BOILER.

THIS HEATER IS PERMITTED TO USE ULTRA LOW NOX BURNERS AS CONTROL WITH AN EMISSION LIMIT OF 0.04 LB/MMBTU OR COMBINATION BURNERS AS CONTROL WITH AN EMISSION LIMIT OF 0.06 LB/MMBTU.

OPERATION LIMITED TO 500 HOURS PER YEAR. THIS UNIT CAN BURN UP TO 289,000 GAL/YR OF DISTILATE OIL. SEE THE PROCEESS AUXILIARY BOILER (OIL) FOR EMISSION LIMITS WHILE BURNING DISTILATE OIL.

IF CAPACITY FACTOR DURING THE OZONE SEASON EXCEEDS 20%, THE FACILITY SHALL CONDUCT A COMBUSTION OPTIIMIZATION (IN ACCORDANCE WITH CH. NR 439, NOX RACT). NOT SUBJECT TO PSD BACT, AS THE INCREASE WAS OFFSET BY ADDITIONAL REDUCTIONS FROM THE COMBUSTION TURBINES / DUCT BURNERS.



NOT TO EMIT GASES WITH PARTICULATE CONTENT EXCEEDING RATE CALCULATED THUS: E=0.5*(10/R) ^0.5, WHERE E=ALLOWABLE EMISSION RATE IN LB/MMBTU, AND R= HEAT INPUT IN MMBTU/H BACT IS TO COMPLY WITH STATE STANDARDS 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU AND 1 GR = .000143 LB. BACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1000 BTU = 1 DSCF NATURAL GAS AND 0.000143 LB = 1 GR. BACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU CONVERTED USING FOLLOWING CONVERSION FACTORS; 1 DSCF NATURAL GAS = 1000 BTU, AND 1 GR = 0.000143 LB. BACT IS TO COMPLY WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS; 1 DSCF NATURAL GAS = 1000 BTU, AND 1 GR = 0.000143. EMISSIONS IN LB/MMBTU WERE CONVERTED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055. EMISSIONS IN LB/MMBTU WERE CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 0.000143 LB = 1 GR. BACT IS CONSIDERED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055 EMISSIONS IN LB/MMBTU CALCULATED USING THE FOLLOWING CONVERSION FACTORS: 1 DSCF NATURAL GAS = 1000 BTU, AND 1 GR = 0.000143 LB. BACT IS CONSIDRED COMPLIANCE WITH STATE STANDARD 18 AAC 50.055.

BASIS OF DETERMINATION IS 18 AAC 50.055(B)(1). THE OWNER REQUESTED TO LIMIT THE SULFUR CONTENT OF GASEOUS AND LIQUID FUELS TO 200-PPM HYDROGEN SULFIDE AND 0.25% SULFUR BY WEIGHT TO AVOID A PSD PRE-CONSTRUCTION REVIEW OF EXISTING EQUIPMENT. THE OWNER WILL ALSO LIMIT NATURAL GAS CONSUMPTION FOR GLYCOL HEATERS NO. 1, 2, AND 3 TO A COMBINED USE NOT TO EXCEED 63 MMSCF/12-MO PERIOD. THE EMISSION LLIMIT IN LB/MMBTU WAS CALCULATED BY DIVIDING THE HOURLY EMISSION LIMIT BY THE THROUGHPUT. BASIS OF DETERMINATION - 18 AAC 50.055(B)(1). THE HOURLY EMISSION LIMIT WAS CONVERTED INTO STANDARDIZED UNITS BY DIVIDING IT BY THE THROUGHPUT.


BAGHOUSE WITH MANUFACTURER'S GUARANTEED GRAIN LOADING OF 0.0025 GRAIN/DSCF AND AIR FLOW RATE USED TO DEMONSTRATE COMPLIANCE. IF REQUIRED BY REGULATING AGENCY, METHOD 5 AND/OR 9 MAY BE USED TO DEMONSTRATE COMPLIANCE.

ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

BASIS OF DETERMINATION IS 18 AAC 50.055(C). THE HOURLY EMISSION LIMIT WAS CONVERTED INTO STANDARDIZED UNITS BY DIVIDING IT BY THE THROUGHPUT. THE OWNER REQUESTED TO LIMIT THE SULFUR CONTENT OF GASEOUS AND LIQUID FUELS TO 200-PPM HYDROGEN SULFIDE AND 0.25% SULFUR BY WEIGHT TO AVOID A PSD PRE-CONSTRUCTION REVIEW OF EXISTING EQUIPMENT. THE OWNER WILL ALSO LIMIT NATURAL GAS CONSUMPTION FOR GLYCOL HEATERS NO. 1, 2, AND 3 TO A COMBINED USE NOT TO EXCEED 63 MMSCF/12-MO PERIOD. BASIS OF DETERMINATION- 18 AAC 50.055(C). THE HOURLY EMISSION LIMIT WAS CONVERTED INTO STANDARDIZED UNITS BY DIVIDING IT BY THE THROUGHPUT.


LIMIT SULFUR CONTENT IN FUEL COMBUSTED * EMISSION UNITS AND NUMERIC LIMITS ARE REQUIRED FOR SO2 USING APPENDIX E. PROCESS CODE 13.110

VE MAY EXCEED 20% OPACITY, AS A 6-MINUTE AV, FOR NOT MORE THAN 6 CONSECUTIVE MINUTES IN ANY 60 MINUTES, BUT SHALL NOT EXCEED 60% OPACITY AS A 6-MINUTE AV AT ANY TIME.

ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL CO EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 953.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

BASIS OF DETERMINATION IS 18 AAC 50.055(B)(1). THE OWNER REQUESTED TO LIMIT THE SULFUR CONTENT OF GASEOUS AND LIQUID FUELS TO 200-PPM HYDROGEN SULFIDE AND 0.25% SULFUR BY WEIGHT TO AVOID A PSD PRE-CONSTRUCTION REVIEW OF EXISTING EQUIPMENT. THE OWNER WILL ALSO LIMIT NATURAL GAS CONSUMPTION FOR GLYCOL HEATERS NO. 1, 2, AND 3 TO A COMBINED USE NOT TO EXCEED 63 MMSCF/12-MO PERIOD. THE EMISSION LLIMIT IN LB/MMBTU WAS CALCULATED BY DIVIDING THE HOURLY EMISSION LIMIT BY THE THROUGHPUT.


BAGHOUSE WITH MANUFACTURER'S GUARANTEED GRAIN LOADING OF 0.0025 GRAIN/DSCF AND AIR FLOW RATE USED TO DEMONSTRATE COMPLIANCE. IF REQUIRED BY REGULATING AGENCY, METHOD 5 AND/OR 9 MAY BE USED TO DEMONSTRATE COMPLIANCE.

ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P. ANNUAL PM10 EMISSIONS FROM THE FOLLOWING SOURCES ARE CAPPED AT 108.3 TPY: 145-02-A, 145-02-B, 145-02-C, 145-02-D, 145-02-E, 145-02-F, 145-02-G, 145-02-H, 145-02-I, 145-02-J, 145-02-K, 145-02-L, 145-02-M, 145-02-N, 145-02-O, & 145-02-P.

BASIS OF DETERMINATION IS 18 AAC 50.055(C). THE HOURLY EMISSION LIMIT WAS CONVERTED INTO STANDARDIZED UNITS BY DIVIDING IT BY THE THROUGHPUT. THE OWNER REQUESTED TO LIMIT THE SULFUR CONTENT OF GASEOUS AND LIQUID FUELS TO 200-PPM HYDROGEN SULFIDE AND 0.25% SULFUR BY WEIGHT TO AVOID A PSD PRE-CONSTRUCTION REVIEW OF EXISTING EQUIPMENT. THE OWNER WILL ALSO LIMIT NATURAL GAS CONSUMPTION FOR GLYCOL HEATERS NO. 1, 2, AND 3 TO A COMBINED USE NOT TO EXCEED 63 MMSCF/12-MO PERIOD.

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