Facility _Information

facility _id utility

_code legal_owner_nam e

legl_operator_name

legal_address_type

legal_address

legal_city legal_state legal_zip 2952 14063 Oklahoma Gas & Electric Co. Oklahoma Gas & Electric Co.

legal owner P.O. Box 321, MC 600 Oklahoma City

OK 73101-0321 6095 14063 Oklahoma Gas & Electric Co. Oklahoma Gas & Electric Co.

legal owner P.O. Box 321, MC 600 Oklahoma City

OK 73101-0321

Page 1Facility _Information

plant_nam e

physical_address

phyical_city

physical_state

physical_zip

ma iling_address

ma iling_city

ma iling_state

ma iling_zip Muskogee 5501 Three Forks Rd Fort Gibson

OK 74401-7309 P.O. Box 321, MC 600

Oklahoma City

OK 73101-0321 Sooner 10800 County Rd 230 Red Rock OK 73061 P.O. Box 321, MC 600 Oklahoma City

OK 73101-0321

Page 2Facility _Information

RFA_small_entity

ff_fired_coal

ff_fired_oil ff_fired_ngas ff_fired_petcoke

ff_fired_other

ff_permitted_coal

ff_permitted_oil

ff_permitted_ngas No TRUE FALSE TRUE FALSE TRUE TRUE FALSE TRUE No TRUE TRUE FALSE FALSE TRUE TRUE TRUE FALSE

Page 3Facility _Information

ff_permitted_petcoke

ff_permitted_other

deviation_reporting

continuous_emissions

cem_provided

facility _note FALSE TRUE Deviations in excess of permit limits are reported to the State as required OAC 252:100-9 No Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope FALSE TRUE Deviations in excess of permit limits are reported to the State as required OAC 252:100-9 No Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of typical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 4Facility _Information

Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 5Facility _Information

Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 6Facility _Information

Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 7Facility _Information

Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 8Facility _Information

Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of typical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 9Facility _Information

Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of typical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 10Facility _Information

Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of typical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 11Facility _Information

Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of typical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 12Facility _Information

Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of typical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 13Facility _Information

Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Original design gross efficiency [%, HHV] = Muskogee Units 4, 5 & 6 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Muskogee Units 4, 5 & 6.Operating steam pressure (psig) = value is representative of ty pical operation averaged over the past 3 years for Muskogee 4, 5 & 6.Design steam temperature (F) = 1005 for Muskogee Units 4, 5 & 6.Ope Part 1 - General Facility InformationFacility and Fuel Information, Other Fuel Material: In the absence of an existing Federal program aimed at regulating the combustion of de minimis quantities of solid wastes in utility boilers and the potential economic burden that could otherwise result if it were subject to such a program, OG&E would likely cease burning said wastes and seek other options insofar as their management is concerned.Boiler Information, Boiler Information:Present maximum heat input [mmbtu/hr] = this parameter is not currently measured for Sooner Units 1 & 2.Original design gross efficiency [%, HHV] = Sooner Units 1 & 2 are 86.5%, estimated 8800 HHV.Present operating gross efficiency [%, HHV] = this parameter is not currently measured for Sooner Units 1 & 2.Operating steam pressure (psig) = value is representative of typical operation averaged over the past 3 years forSooner Units 1 & 2.Design steam temperature (F) = 1005 for Sooner Units 1 & 2.Operating steam tempera

Page 14facility _contacts

facility _id contact_id contact_title contact_name

contact_phone1

contact_phone2

contact_email

contact_primary 2952 1 Alternate Designated Responsible Official Robert F. Benham

4055533221 benham rf@oge.com TRUE 2952 2 Air Quality Coordinator Laura Herron

4055533057 herronlk@oge.com FALSE 6095 4 Alternate Designated Responsible Official Robert F. Benham

4055533221 benham rf@oge.com TRUE 6095 5 Air Quality Coordinator Laura herron

4055533057 herronlk@oge.com FALSE

Page 15facility _coal_utilized

facility _id coal_type percentage_mass percentage_btu

synfuel_type

coal_note 2952 subbituminous 100 100 6095 subbituminous 100 100

Page 16facility _oil_utilized

facility _id oil_type percentage_volume percentage_btu

other_type 6095 No.2 Fuel Oil (distillate) 100 100

Page 17facility _other_materials

facility _id other_material

permitted_burn

actually _burn other_quantity

other_quantity

_units other_note rcra_utilize rcra_explain 2952 Activated Carbon

TRUE TRUE 200 num ber/year 200 cubic ft/ year - last burned in 2005. I

No see main note on Facility and Fuel Information 2952 Ash from oil combustion

TRUE FALSE 0 num ber/year No ash from oil combustion burned in the past five years

No see main note on Facility and Fuel Information 2952 boiler cleaning solution

TRUE TRUE 98596 num ber/year gallons/year - last burned in 2007

No see main note on Facility and Fuel Information 2952 Demineralizer Resin

TRUE TRUE 1.5 num ber/year cubic ft/year - last burned in 2008

No see main note on Facility and Fuel Information 2952 EH Fluid TRUE TRUE 40 num ber/year gallons/year - last burned in 2008

No see main note on Facility and Fuel Information 2952 Hazardous W aste Fuel

FALSE TRUE 230 num ber/year gallons/year - last burned in 2009

No see main note on Facility and Fuel Information 2952 Slop Oil TRUE FALSE 0 num ber/year No slop oil burned in the past five years

No see main note on Facility and Fuel Information 2952 Used Anti-freeze

TRUE TRUE 735 num ber/year gallons/year - last burned in 2007

No see main note on Facility and Fuel Information 2952 Used Oil TRUE TRUE 8149 num ber/year gallons/year - last burned in 2009

No see main note on Facility and Fuel Information 2952 Used Oil-dry TRUE TRUE 1.15 tons/year last burned in 2009 No see main note on Facility and Fuel Information 2952 Used Solvent TRUE TRUE 30 num ber/year gallons/year - last burned in 2006

No see main note on Facility and Fuel Information 2952 Wa stewater Treatment Sludge

TRUE TRUE 5364 num ber/year cubic yards/year - last burned in 2005

No see main note on Facility and Fuel Information 2952 Wa ter-Iron Contaminated

TRUE TRUE 17500 num ber/year gallons/year - last burned in 2006

No see main note on Facility and Fuel Information 2952 Wa ter-Oil Contaminated

TRUE TRUE 46000 num ber/year gallons/year - last burned in 2009

No see main note on Facility and Fuel Information 6095 Activated Carbon

TRUE FALSE 0 num ber/year No activated carbon has been burned in the past five years

No see main note on Facility and Fuel Information 6095 Ash from Oil Combustion

TRUE FALSE 0 num ber/year No ash from oil combustion has been burned in the past five years

No see main note on Facility and Fuel Information 6095 Boiler Cleaning Solution

TRUE TRUE 176850 num ber/year gallons/year - last burned in 2007

No see main note on Facility and Fuel Information 6095 Demineralizer Resin

TRUE TRUE 0.75 tons/year llast burned in 2008 No see main note on Facility and Fuel Information 6095 Slop Oil TRUE TRUE 4.87 tons/year last burned in 2005 No see main note on Facility and Fuel Information 6095 Used Anti-freeze

TRUE TRUE 3 num ber/year lbs/year - last burned in 2009

No see main note on Facility and Fuel Information 6095 Used Oil TRUE TRUE 55.34 tons/year last burned in 2009 No see main note on Facility and Fuel Information 6095 Used Oil Dry TRUE TRUE 0.39 tons/year last burned in 2009 No see main note on Facility and Fuel Information 6095 Used Solvent TRUE FALSE 0 num ber/year no used solvent has been burned in past five years

No see main note on Facility and Fuel Information

Page 18facility _other_materials

rcra_explain see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information see main note on Facility and Fuel Information

Page 19boiler_information

facility _id boiler_id boiler_type boiler_other bottom_design

design_fuel heat_input max_heat_input MW e_capacity 2952 4 Tangential firing Dry Bottom coal 5150 391 2952 5 Tangential firing Dry Bottom coal 5150 415 2952 6 Tangential firing Dry Bottom coal 5150 371 6095 1 Tangential firing Dry Bottom coal 5115 401 6095 2 Tangential firing Dry Bottom coal 5150 383

Page 20boiler_information

MW e_net_capacity

design_gross_efficiency

operating_gross_efficiency

design_pressure

operating_pressure

design_temp

operating_temp

design_reheat_multiple

design_reheat_temp1 359 86.5 2400 2350 1 1 FALSE 1 386 86.5 2400 2400 1 1 FALSE 1 343 86.5 2400 2350 1 1 FALSE 1 373 86.5 2400 2400 1 1 FALSE 1 358 86.5 2400 2400 1 1 FALSE 1

Page 21boiler_information

design_reheat_temp2

operating_reheat_multiple

operating_reheat_temp1

operating_reheat_temp2

hours_operated

vg_capacity

_factor applicable_NSPS

retirement_year

retirement_year_CBI FALSE 1 6830 65 Subpart D FALSE FALSE 1 6567 60 Subpart D FALSE FALSE 1 7794 70 Subpart D FALSE FALSE 1 7798 78 Subpart D FALSE FALSE 1 7341 69 Subpart D FALSE

Page 22boiler_information

NOx_control

SO2_control

combustion_additives Yes Yes No Yes Yes No Yes Yes No Yes Yes No Yes Yes No

Page 23boiler_fuels

facility _id boiler_id fuel_type fuel_year percentage_massvol percentage_btu

other_type 2952 4 coal - subbituminous 2007 0 99.88 2952 4 coal - subbituminous 2008 0 99.52 2952 4 coal - subbituminous 2009 0 99.6 2952 4 natural gas 2007 0 0.12 2952 4 natural gas 2008 0 0.48 2952 4 natural gas 2009 0 0.4 2952 5 coal - subbituminous 2007 0 98.68 2952 5 coal - subbituminous 2008 0 99.51 2952 5 coal - subbituminous 2009 0 99.81 2952 5 natural gas 2007 0 1.32 2952 5 natural gas 2008 0 0.49 2952 5 natural gas 2009 0 0.19 2952 6 coal - subbituminous 2007 0 99.92 2952 6 coal - subbituminous 2008 0 99.9 2952 6 coal - subbituminous 2009 0 99.57 2952 6 natural gas 2007 0 0.08 2952 6 natural gas 2008 0 0.1 2952 6 natural gas 2009 0 0.43 6095 1 coal - subbituminous 2007 0 99.74 6095 1 coal - subbituminous 2008 0 99.96 6095 1 coal - subbituminous 2009 0 99.92 6095 1 oil - distillate 2007 0 0.26 6095 1 oil - distillate 2008 0 0.04 6095 1 oil - distillate 2009 0 0.08 6095 2 coal - subbituminous 2007 0 99.19 6095 2 coal - subbituminous 2008 0 99.67 6095 2 coal - subbituminous 2009 0 99.91 6095 2 oil - distillate 2007 0 0.81 6095 2 oil - distillate 2008 0 0.33 6095 2 oil - distillate 2009 0 0.09

Page 24boiler_control_NOx

facility _id boiler_id NOx_type NOx_other NOx_online 2952 4 Overfire Air 12/1/1977 2952 5 Overfire Air 10/1/1978 2952 6 Overfire Air 6/1/1984 6095 1 Overfire Air 11/1/1979 6095 2 Overfire Air 12/1/1980

Page 25boiler_control_SO2

facility _id boiler_id SO2_type SO2_other SO2_online 2952 4 Low Sulfur Coal 12/1/1977 2952 5 Low Sulfur Coal 10/1/1978 2952 6 Low Sulfur Coal 6/1/1984 6095 1 Low Sulfur Coal 11/1/1979 6095 2 Low Sulfur Coal 12/1/1980

Page 26boiler_additives

facility _id boiler_id boiler_additive additive_other

additive_online

Page 27facility _units

facility _id unit_id 2952 4 2952 5 2952 6 6095 1 6095 2

Page 28unit_boilers

facility _id unit_id boiler_id 2952 4 4 2952 5 5 2952 6 6 6095 1 1 6095 2 2

Page 29facility _controls

facility _id control_id control_group control_type

control_other

legacy _control cntrol_online

control_offline

NOx_reagent 2952 MK4ESP PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 12/1/1977 2952 MK5ESP PM control Electrostatic precipitator, cold side, w/ flue gas conditioning FALSE 10/1/1978 2952 MK6ESP PM control Electrostatic precipitator, cold side, w/ flue gas conditioning FALSE 6/1/1984 6095 SO1 ESP PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 11/1/1979 6095 SO2 ESP PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 12/1/1980

Page 30facility _controls

reagent_other

NOx_ammonia

SO2_sorbent

oher_sorbent

SO2_scrubber_additive

Page 31facility _sampling_ports

facility _id sampling_port_id 2952 MK4STK PORTA 2952 MK4STK PORTB 2952 MK4STK PORTC 2952 MK4STK PORTD 2952 MK5STK PORTA 2952 MK5STK PORTB 2952 MK5STK PORTC 2952 MK5STK PORTD 2952 MK6STK PORTA 2952 MK6STK PORTB 2952 MK6STK PORTC 2952 MK6STK PORTD 6095 SO1STK PORTA 6095 SO1STK PORTB 6095 SO1STK PORTC 6095 SO1STK PORTD 6095 SO2STK PORTA 6095 SO2STK PORTB 6095 SO2STK PORTC 6095 SO2STK PORTD

Page 32facility _stacks

facility _id stack_id stack_height stack_diameter

sack_gas_velocity 2952 MK4STK 350 24 56.173 2952 MK5STK 350 24 56.173 2952 MK6STK 500 24 81.53 6095 SO1 STK 500 22 106 6095 SO2 STK 499 23 106

Page 33configurations

facility _id configuration_id 2952 MK4 Config 2952 MK5 Config 2952 MK6 Config 6095 SO1 Config 6095 SO2 Config

Page 34configuration_components

facility _id configuration_id

component_id

order component_type port_near 2952 MK4 Config

4 1 Unit 2952 MK4 Config

MK4ESP 2 PM control 2952 MK4 Config

MK4STK 7 Stack 2952 MK4 Config

MK4STK PORTA 3 Sam pling Port next 2952 MK4 Config

MK4STK PORTB 4 Sam pling Port next 2952 MK4 Config

MK4STK PORTC 5 Sam pling Port next 2952 MK4 Config

MK4STK PORTD 6 Sam pling Port next 2952 MK5 Config

5 1 Unit 2952 MK5 Config

MK4STK PORTC 5 Sam pling Port next 2952 MK5 Config

MK5ESP 2 PM control 2952 MK5 Config

MK5STK 7 Stack 2952 MK5 Config

MK5STK PORTA 3 Sam pling Port next 2952 MK5 Config

MK5STK PORTB 4 Sam pling Port next 2952 MK5 Config

MK5STK PORTD 6 Sam pling Port next 2952 MK6 Config

6 1 Unit 2952 MK6 Config

MK6ESP 2 PM control 2952 MK6 Config

MK6STK 7 Stack 2952 MK6 Config

MK6STK PORTA 3 Sam pling Port next 2952 MK6 Config

MK6STK PORTB 4 Sam pling Port next 2952 MK6 Config

MK6STK PORTC 5 Sam pling Port next 2952 MK6 Config

MK6STK PORTD 6 Sam pling Port next 6095 SO1 Config 1 1 Unit 6095 SO1 ConfigSO1 ESP 2 PM control 6095 SO1 ConfigSO1 STK 7 Stack 6095 SO1 ConfigSO1STK PORTA 3 Sam pling Port next 6095 SO1 ConfigSO1STK PORTB 4 Sam pling Port next 6095 SO1 ConfigSO1STK PORTC 5 Sam pling Port next 6095 SO1 ConfigSO1STK PORTD 6 Sam pling Port next 6095 SO2 Config

2 1 Unit 6095 SO2 ConfigSO2 ESP 2 PM control 6095 SO2 ConfigSO2 STK 7 Stack 6095 SO2 ConfigSO2STK PORTA 3 Sam pling Port next 6095 SO2 ConfigSO2STK PORTB 4 Sam pling Port next 6095 SO2 ConfigSO2STK PORTC 5 Sam pling Port next 6095 SO2 ConfigSO2STK PORTD 6 Sam pling Port next

Page 35configuration_pollutants1

facility _id configuration_id

pollutant_nam e

permit_type_1

em lim it_1 em lim it_units_1 avg_period_1

em lim it_2 em lim it_units_2 2952 MK4 Config

PM (Condensable)

Federal - Title V Operating Permit

0.1 pound per million British Thermal Unit (lb/MMBtu)

24 hours 2952 MK4 Config

Nitrogen Oxide (NOx)

Federal - Title V Operating Permit

0.7 pound per million British Thermal Unit (lb/MMBtu)

3 hours 2952 MK4 Config

Sulfur Dioxide (SO2)

Federal - Title V Operating Permit

1.2 pound per million British Thermal Unit (lb/MMBtu)

3 hours 2952 MK5 Config

PM (Condensable)

Federal - Title V Operating Permit

0.1 pound per million British Thermal Unit (lb/MMBtu)

24 hours 2952 MK5 Config

Nitrogen Oxide (NOx)

Federal - Title V Operating Permit

0.7 pound per million British Thermal Unit (lb/MMBtu)

3 hours 2952 MK5 Config

Sulfur Dioxide (SO2)

Federal - Title V Operating Permit

1.2 pound per million British Thermal Unit (lb/MMBtu)

3 hours 2952 MK6 Config

PM (Condensable)

Federal - Title V Operating Permit

200.85 pound per hour (lb/hr)

1 hour 2952 MK6 Config

Sulfur Dioxide (SO2)

Federal - Title V Operating Permit

6180 pound per hour (lb/hr)

1 hour 1.2 pound per million British Thermal Unit (lb/MMBtu) 2952 MK6 Config

Nitrogen Oxide (NOx)

Federal - Title V Operating Permit

3605 pound per hour (lb/hr)

1 hour 0.7 pound per million British Thermal Unit (lb/MMBtu) 2952 MK6 Config

Carbon Monoxide (CO)

Federal - Title V Operating Permit

180 pound per hour (lb/hr)

1 hour 2952 MK6 Config

PM10 (Filterable)

Fedral - Title V Operating Permit

0.039 pound per million British Thermal Unit (lb/MMBtu)

24 hours 6095 SO1 ConfigPM (Condensable) Federal - Title V Operating Permit

0.1 pound per million British Thermal Unit (lb/MMBtu)

24 hours 6095 SO1 ConfigSulfur Dioxide (SO2) Federal - Title V Operating Permit

1.2 pound per million British Thermal Unit (lb/MMBtu)

3 hours 6095 SO1 ConfigNitrogen Oxide (NOx) Federal - Title V Operating Permit

0.7 pound per million British Thermal Unit (lb/MMBtu)

3 hours 6095 SO2 ConfigPM (Condensable) Federal - Title V Operating Permit

0.1 pound per million British Thermal Unit (lb/MMBtu)

24 hours 6095 SO2 ConfigSulfur Dioxide (SO2) Federal - Title V Operating Permit

1.2 pound per million British Thermal Unit (lb/MMBtu)

3 hours 6095 SO2 ConfigNitrogen Oxide (NOx) Federal - Title V Operating Permit

0.7 pound per million British Thermal Unit (lb/MMBtu)

3 hours

Page 36configuration_pollutants1

avg_period_2

em lim it_details

test_method

em rate em rate_units guarantee_level

_explain

req_monitoring

eq_recordkeeping see note Stack test ma intain copy of test report Continuous Emission Monitoring

ma intain CEMS data for 5 years Continuous Emission Monitoring

ma intain CEMS data for 5 years Stack test ma intain copy of test report Continuous Emission Monitoring

ma intain CEMS data for 5 years Continuous Emission Monitoring

ma intain CEMS data for 5 years Stack test Maintain copy of test report 3 hours Continuous Emission Monitoring ma intain CEMS data for 5 year 3 hours Continuous Emission Monitoring ma intain CEMS data for 5 year Continuous Emission Monitoring

ma intain CEMS data for 5 year Stack test Maintain copy of test report see note Stack test ma intain copy of test report Continuous Emission Monitoring

ma intain CEMS data for 5 years Continuous Emission Monitoring

ma intain CEMS data for 5 years Stack test ma intain copy of test report Continuous Emission Monitoring

ma intain CEMS data for 5 years Continuous Emission Monitoring

ma intain CEMS data for 5 years

Page 37configuration_pollutants1

req_reporting Federal TVState Federal Acid Rain ProgramFederal TVState Federal Acid Rain ProgramFederal TVState Federal TVState Federal Acid Rain ProgramFederal TVState Federal Acid Rain ProgramFederal TVState Federal TVState Federal Acid Rain ProgramFederal TVState Federal Acid Rain ProgramFederal TVState Federal Acid Rain ProgramFederal TVState Federal TVState Federal TVState Federal Acid Rain ProgramFederal TVState Federal Acid Rain ProgramFederal TVState Federal TVState Federal Acid Rain ProgramFederal TVState Federal Acid Rain ProgramFederal TVState

Page 38control_technologies

facility _id configuration_id

component_id

control_id project_title project_type vendor_name

vndor_contact

vendor_phone

Page 39control_technologies

vendor_address

vndor_city

vendor_state

vendor_zip actual_start_date projected_start_date

end_date sorbent chemical_additive

Page 40control_technologies

injection_point

HAP_em ission_reduction

HAP_em ission_rate

HAP_em ission_rate_units

HAP_achieved_reduction

HAP_achieved_rate

HAP_achieved_rate_units

feed_rate feed_rate_units

Page 41control_technologies

feed_rate_units

Page 42control_coal_ranks

facility _id configuration_id

component_id

control_id coal_type

Page 43control_pollutants1

facility _id configuration_id

component_id

control_id pollutant_nam e

Page 44control_costs

facility _id configuration_id

component_id

control_id boiler_retrofit boiler_new_install

total_capital_investm ent

total_operating_costs

base_year

Page 45control_costs

CBI

Page 46mi sc_controls

facility _id mi sc_control_id

control_description 2952 1 Low sulfur coal 2952 2 over fire air 6095 1 Low Sulfur Coal 6095 2 overfire air

Page 47mi sc_control_configurations

facility _id mi sc_control_id

configuration_id 2952 1 MK4 Config 2952 1 MK5 Config 2952 1 MK6 Config 2952 2 MK4 Config 2952 2 MK5 Config 2952 2 MK6 Config 6095 1 SO1 Config 6095 1 SO2 Config 6095 2 SO1 Config 6095 2 SO2 Config

Page 48fuel_shipments

facility _id shipment_id

shipment_date

am ount_received

am ount_units

fuel_type state_country other_country

county 2952 Apr 2009 4/1/2009 586952.8 short tons (2000 lbs) coal WY 2952 Aug 2009 8/1/2009 538953.2 short tons (2000 lbs) coal WY 2952 Dec 2009 12/1/2009 420955.4 short tons (2000 lbs) coal WY 2952 Feb 2009 2/1/2009 536539.4 short tons (2000 lbs) coal WY 2952 Jan 2010 1/1/2010 497067.4 short tons (2000 lbs) coal WY 2952 Jul 2009 7/1/2009 505933.7 short tons (2000 lbs) coal WY 2952 Jun 2009 6/1/2009 582699.9 short tons (2000 lbs) coal WY 2952 Mar 2009 3/1/2009 516600.4 short tons (2000 lbs) coal WY 2952 May

2009 5/1/2009 598290.9 short tons (2000 lbs) coal WY 2952 Nov 2009 11/1/2009 47366569 short tons (2000 lbs) coal WY 2952 Oct 2009 10/1/2009 456182.2 short tons (2000 lbs) coal WY 2952 Sep 2009 9/1/2009 159892.7 short tons (2000 lbs) coal WY 6095 Apr 2009 4/1/2009 358687.8 short tons (2000 lbs) coal WY 6095 Aug 2009 8/1/2009 326735.2 short tons (2000 lbs) coal WY 6095 Dec 2009 12/1/2009 301144.9 short tons (2000 lbs) coal WY 6095 Feb 2009 2/1/2009 417950.2 short tons (2000 lbs) coal WY 6095 Jan 2010 1/1/2010 356292 short tons (2000 lbs) coal WY 6095 Jul 2009 7/1/2009 392950.4 short tons (2000 lbs) coal WY 6095 Jun 2009 6/1/2009 216647.7 short tons (2000 lbs) coal WY 6095 Mar 2009 3/1/2009 408519.3 short tons (2000 lbs) coal WY 6095 May

2009 5/1/2009 251260.7 short tons (2000 lbs) coal WY 6095 Nov 2009 11/1/2009 339313.9 short tons (2000 lbs) coal WY 6095 Oct 2009 10/1/2009 215204.2 short tons (2000 lbs) coal WY 6095 Sep 2009 9/1/2009 541254.9 short tons (2000 lbs) coal WY

Page 49fuel_shipments

coal_seam shipment_method

Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train

Page 50fuel_shipment_configurations

facility _id shipment_id

configuration_id 2952 Apr 2009 MK4 Config 2952 Apr 2009 MK5 Config 2952 Apr 2009 MK6 Config 2952 Aug 2009 MK4 Config 2952 Aug 2009 MK5 Config 2952 Aug 2009 MK6 Config 2952 Dec 2009 MK4 Config 2952 Dec 2009 MK5 Config 2952 Dec 2009 MK6 Config 2952 Feb 2009 MK4 Config 2952 Feb 2009 MK5 Config 2952 Feb 2009 MK6 Config 2952 Jan 2010 MK4 Config 2952 Jan 2010 MK5 Config 2952 Jan 2010 MK6 Config 2952 Jul 2009 MK4 Config 2952 Jul 2009 MK5 Config 2952 Jul 2009 MK6 Config 2952 Jun 2009 MK4 Config 2952 Jun 2009 MK5 Config 2952 Jun 2009 MK6 Config 2952 Mar 2009 MK4 Config 2952 Mar 2009 MK5 Config 2952 Mar 2009 MK6 Config 2952 May

2009 MK4 Config 2952 May

2009 MK5 Config 2952 May

2009 MK6 Config 2952 Nov 2009 MK4 Config 2952 Nov 2009 MK5 Config 2952 Nov 2009 MK6 Config 2952 Oct 2009 MK4 Config 2952 Oct 2009 MK5 Config 2952 Oct 2009 MK6 Config 2952 Sep 2009 MK4 Config 2952 Sep 2009 MK5 Config 2952 Sep 2009 MK6 Config 6095 Apr 2009 SO1 Config 6095 Apr 2009 SO2 Config 6095 Aug 2009 SO1 Config 6095 Aug 2009 SO2 Config 6095 Dec 2009 SO1 Config 6095 Dec 2009 SO2 Config 6095 Feb 2009 SO1 Config 6095 Feb 2009 SO2 Config 6095 Jan 2010 SO1 Config 6095 Jan 2010 SO2 Config 6095 Jul 2009 SO1 Config 6095 Jul 2009 SO2 Config 6095 Jun 2009 SO1 Config 6095 Jun 2009 SO2 Config 6095 Mar 2009 SO1 Config

Page 51fuel_shipment_configurations

6095 Mar 2009 SO2 Config 6095 May

2009 SO1 Config 6095 May

2009 SO2 Config 6095 Nov 2009 SO1 Config 6095 Nov 2009 SO2 Config 6095 Oct 2009 SO1 Config 6095 Oct 2009 SO2 Config 6095 Sep 2009 SO1 Config 6095 Sep 2009 SO2 Config

Page 52fuel_shipment_samples

facility _id shipment_id

sample_id am ount_fuel am ount_fuel_units

total_sulfur ash_content heating_value

hating_units

Page 53fuel_shipment_samples

chlorine chlorine_units fluorine fluorine_units data_provided

data_other_specified

supplier_type

supplier_name

supplier_address

Page 54fuel_shipment_samples

supplier_city

supplier_state

supplier_zip

lab_nam e lab_address lab_city lab_state lab_zip analysis_copies

Page 55fuel_shipment_samples

analysis_copies

Page 56fuel_sample_pollutants

facility _id shipment_id

sample_id fuel_pollutant pollutant_conc

pollutant_conc_units

pollutant_conc_ND

pollutant_conc_MDL

Page 57test_reports

facility _id report_id report_type other_type report_description report_begin_date

report_end_date

before_control

during_deviation 2952 Stack Sampling Report\ Muskogee 4

compliance Muskogee Unit 4 particulate matter emission rate test 4/19/2006 4/20/2006 No No 2952 Stack Sampling Report\ Muskogee 5

compliance Muskogee Unit 5 particulate matter emission rate test 4/18/2006 4/19/2006 No No 2952 Stack Sampling Report\ Muskogee 6

compliance Muskogee Unit 6 particulate mater emission rate test 6/13/2006 6/14/2006 No No 6095 Stack Sampling Report\Sooner 1

compliance Sooner Unit 1 particulate matter emission rate test 3/5/2007 3/6/2007 No No 6095 Stack Sampling Report\Sooner 2

compliance Sooner Unit 2 particulate matter emission rate test 3/19/2007 3/20/2007 No No

Page 58test_reports

deviation_reports No No No No No

Page 59test_report_configurations

facility _id report_id configuration_id 2952 Stack Sampling Report\ Muskogee 4

MK4 Config 2952 Stack Sampling Report\ Muskogee 5

MK5 Config 2952 Stack Sampling Report\ Muskogee 6

MK6 Config 6095 Stack Sampling Report\Sooner 1

SO1 Config 6095 Stack Sampling Report\Sooner 2

SO2 Config

Page 60test_report_fuels

facility _id report_id fuel_id 2952 Stack Sampling Report\ Muskogee 4

coal 2952 Stack Sampling Report\ Muskogee 5

coal 2952 Stack Sampling Report\ Muskogee 6

coal 6095 Stack Sampling Report\Sooner 1

coal 6095 Stack Sampling Report\Sooner 2

coal

Page 61test_report_fuel_types

facility _id report_id fuel_id fuel_type percentage_massvol percentage_btu

other_type 2952 Stack Sampling Report\ Muskogee 4

coal coal - subbituminous 100 100 2952 Stack Sampling Report\ Muskogee 5

coal coal - subbituminous 100 100 2952 Stack Sampling Report\ Muskogee 6

coal coal - subbituminous 100 100 6095 Stack Sampling Report\Sooner 1

coal coal - subbituminous 100 100 6095 Stack Sampling Report\Sooner 2

coal coal - subbituminous 100 100

Page 62cem_data

facility _id tim e_period

cem_period_description

Page 63cem_data_pollutants1

facility _id tim e_period

pollutant_nam e

Page 64test_report_sampling

facility _id report_id sampling_port_id point_differ point_description befre_SO2_device

point_orientation

normal_bypass_percent

testing_bypass_percent 2952 Stack Sampling Report\ Muskogee 4

MK4STK No No 2952 Stack Sampling Report\ Muskogee 5

MK5STK No No 2952 Stack Sampling Report\ Muskogee 6

MK6STK No No 6095 Stack Sampling Report\Sooner 1

SO1 STK No No 6095 Stack Sampling Report\Sooner 2

SO2 STK No No

Page 65test_report_sampling

fg_fraction

Page 66sampling_runs

facility _id report_id sampling_port_id run_id start_datetime end_datetim e

unit_load net_generation fg_moisture_content 2952 Stack Sampling Report\ Muskogee 4

MK4STK average 4/20/2006 4/20/2006 544 10.98 2952 Stack Sampling Report\ Muskogee 5

MK5STK average 4/19/2006 4/19/2006 546 10.77 2952 Stack Sampling Report\ Muskogee 6

MK6STK average 6/14/2006 6/14/2006 539.3 12.52 6095 Stack Sampling Report\Sooner 1

SO1 STK average 3/6/2007 3/6/2007 554 10.52 6095 Stack Sampling Report\Sooner 2

SO2 STK average 3/20/2007 3/20/2007 560 11.72

Page 67sampling_runs

fg_flow_rate

fg_flow_rate_units

standard_temperature

standard_pressure

normal_temperature

normal_pressure

fg_oxygen_content

fg_CO2_content

fg_temperature 1207818 dscfm 67 0.97 6 13.5 283 1246783 dscfm 65 0.98 6.4 13 282 1274478 dscfm 77 0.99 7.2 12.3 298 1318870 dscfm 60 0.98 6.7 12.6 1 1275799 dscfm 57 0.97 7.2 11.9 289

Page 68sampling_runs

fg_pressure

Hg_loi test_method run_comments

fuel_id fuel_unit_load fuel_flow_rate

fuel_ash fuel_heating_value 202 coal 202 coal 202 coal 202 202

Page 69sampling_runs

fuel_sulfur

Page 70sampling_run_pollutants1

facility _id report_id sampling_port_id run_id pollutant_nam e conc conc_units conc_ND conc_MDL 2952 Stack Sampling Report\ Muskogee 5

MK5STK average PM (Filterable) FALSE 2952 Stack Sampling Report\ Muskogee 5

MK5STK average PM (Condensable) FALSE 2952 Stack Sampling Report\ Muskogee 6

MK6STK average PM (Filterable) FALSE 2952 Stack Sampling Report\ Muskogee 6

MK6STK average PM (Condensable) FALSE 6095 Stack Sampling Report\Sooner 1

SO1 STK average PM (Filterable) FALSE 6095 Stack Sampling Report\Sooner 1

SO1 STK average PM (Condensable) FALSE 6095 Stack Sampling Report\Sooner 2

SO2 STK average PM (Filterable) FALSE 6095 Stack Sampling Report\Sooner 2

SO2 STK average PM (Condensable) FALSE 2952 Stack Sampling Report\ Muskogee 4

MK4STK average PM (Filterable) FALSE 2952 Stack Sampling Report\ Muskogee 4

MK4STK average PM (Condensable) FALSE

Page 71sampling_run_pollutants1

em ission_rate

em ission_rate_units

em ission_rate_ND

em ission_rate_MDL

em ission_factor

em ission_factor_units

em ission_factor_ND

em ission_factor_MDL

run_pollutant_comment 0.19 FALSE FALSE see main note on Part 2 Fuel Analysis and Emission Data 0.026 FALSE FALSE see main note on Part 2 Fuel Analysis and Emission Data 0.009 FALSE FALSE see main note on Part 2 Fuel Analysis and Emission Data 0.019 FALSE FALSE see main note on Part 2 Fuel Analysis and Emission Data 0.016 FALSE FALSE see main note on Part 2 Fuel Analysis and Emission Data 0.033 FALSE FALSE see main note on Part 2 Fuel Analysis and Emission Data 0.015 FALSE FALSE see main note on Part 2 Fuel Analysis and Emission Data 0.022 FALSE FALSE see main note on Part 2 Fuel Analysis and Emission Data 0.019 FALSE FALSE see main note on Part 2 Fuel Analysis and Emission Data 0.027 FALSE FALSE see main note on Part 2 Fuel Analysis and Emission Data

Page 72sampling_run_pollutants1

run_pollutant_comment see main note on Part 2 Fuel Analysis and Emission Data see main note on Part 2 Fuel Analysis and Emission Data see main note on Part 2 Fuel Analysis and Emission Data see main note on Part 2 Fuel Analysis and Emission Data see main note on Part 2 Fuel Analysis and Emission Data see main note on Part 2 Fuel Analysis and Emission Data see main note on Part 2 Fuel Analysis and Emission Data see main note on Part 2 Fuel Analysis and Emission Data see main note on Part 2 Fuel Analysis and Emission Data see main note on Part 2 Fuel Analysis and Emission Data

Page 73sampling_run_fuel

facility _id report_id sampling_port_id run_id fuel_pollutant fuel_conc fuel_conc_units fuel_conc_ND

fuel_conc_MDL

Page 74sampling_run_fuel

fuel_conc_MDL

Page 75