Facility _Information

facility _id utility

_code legal_owner_nam e

legl_operator_name

legal_address_type

legal_address

legal_city legal_state legal_zip 1702 4254 Consumers Energy Co Consumers Energy

Co. legal ownerOne Energy Plaza Jackson MI 49201

Page 1Facility _Information

plant_name

physical_address

phyical_city

physical_state

physical_zip

mailing_address

mailing_city

mailing_state

mailing_zip D.E. Karn 2742 N. Weadock Hwy

. Essexville MI 48732 2742 N. Weadock Hwy

. Essexville MI 48732

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 TRUE TRUE FALSE FALSE TRUE TRUE TRUE

Page 3Facility _Information

ff_permitted_petcoke

ff_permitted_other

deviation_reporting

continuous_emissions

cem_provided

facility _note FALSE FALSE Prompt Reporting of Deviations, Semi-annual ROP deviation report No PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 4Facility _Information

PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 5Facility _Information

PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 6Facility _Information

PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 7Facility _Information

PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 8Facility _Information

PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 9Facility _Information

PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 10Facility _Information

PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 11Facility _Information

PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 12Facility _Information

PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 13Facility _Information

PART IFuel InformationUnit 1&2 :Oil Type fired: %Volume or %BTU not known: Oil burned for startup operation and flame stabilizationFuel Information: Unit 3&4:Oil Type fired: %Volume or %BTU fired not known and not constant. Boiler burns a blend of Natural Gas and No. 6 oilOriginal Design Fuel: Crude OILBoiler Information1) Consumers Energy intiated a fleet wide sulfur reduction strategy in the 1980s to comply with Michigan's Part 401 Rules. This strategy included introduciton of low sulfur coal in to the fuel mix.2) Original design fuel for units 3 & 4: crude oilTemperatures above 300F were not allowed by the software to be entered in the database. EPA guidance directed to enter "1" and put correct temp in to the Notes section.Unit 1:Original design gross efficiency (HHV) 10700 Btu/lbmPresent operating gross efficiency (HHV)9607 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 993FDesign reheat Temperature (F) 1050FOperating reheat temperatu

Page 14facility _contacts

facility _id contact_id contact_title contact_name

contact_phone1

contact_phone2

contact_email

contact_primary 1702 1 Sr. Environmental Planner Kathryn Cunningham

5177683462 kmcunningham@cmsenergy.com TRUE 1702 2 Project Engineer Corwin Holm es

5177881756 clholmes@cmsenergy.com FALSE

Page 15facility _coal_utilized

facility _id coal_type percentage_mass percentage_btu

synfuel_type

coal_note 1702 bitum inous 25 32.4 Applicabble to Unit 1 and Unit 2Assumed Bituminous coal btu/lb content :12650Assumed subbituminous coal btu/lb content:8800 1702 subbituminous 75 67.6 Applicabble to Unit 1 and Unit 2Assumed Bituminous coal btu/lb content :12650Assumed subbituminous coal btu/lb content:8800

Page 16facility _coal_utilized

Applicabble to Unit 1 and Unit 2Assumed Bituminous coal btu/lb content :12650Assumed subbituminous coal btu/lb content:8800 Applicabble to Unit 1 and Unit 2Assumed Bituminous coal btu/lb content :12650Assumed subbituminous coal btu/lb content:8800

Page 17facility _oil_utilized

facility _id oil_type percentage_volume percentage_btu

other_type 1702 No.2 Fuel Oil (distillate) 1702 No.6 Fuel Oil (residual or bunker C)

Page 18facility _other_materials

facility _id other_material

permitted_burn

actually _burn other_quantity

other_quantity

_units other_note rcra_utilize rcra_explain

Page 19facility _other_materials

rcra_explain

Page 20boiler_information

facility _id boiler_id boiler_type boiler_other bottom_design

design_fuelheat_input max_heat_input MWe_capacity 1702 1 Tangential firing Wet Bottom coal 2257 2445 275 1702 2 Wall firing - front firing Wet Bottom coal 2320 2587 281 1702 3 Wall firing - front firing Dry Bottom fuel oil 6023 6674 662 1702 4 Wall firing - front firing Dry Bottom fuel oil 6023 6674 662

Page 21boiler_information

MWe_net_capacity

design_gross_efficiency

operating_gross_efficiency

design_pressure

operating_pressure

design_temp

operating_temp

design_reheat_multiple

design_reheat_temp1 255 89.2 86.5 2400 2304 FALSE 260 88.9 85.4 2400 2349 FALSE 638 89.35 89.55 1800 1807 FALSE 638 89.35 89.55 1800 1809 FALSE

Page 22boiler_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 5389 47.26 N 2030 FALSE FALSE 7291 74.81 N 2030 FALSE FALSE 627 Subpart D 2030 FALSE FALSE 627 Subpart D 2030 FALSE

Page 23boiler_information

NOx_control

SO2_control

combustion_additives No Yes No Yes Yes No Yes No No Yes

Page 24boiler_fuels

facility _id boiler_id fuel_type fuel_year percentage_massvol percentage_btu

other_type 1702 1 coal - bituminous2009 25 32.4 1702 1 coal - subbituminous 2009 75 67.6 1702 2 coal - bituminous2009 25 32.4 1702 2 coal - subbituminous 2009 75 67.6 1702 3 oil - other 2009 specification used oil 1702 3 oil - residual or bunker 2009 1702 4 oil - other 2009 specification used oil 1702 4 oil - residual or bunker 2009

Page 25boiler_control_NOx

facility _id boiler_id NOx_type NOx_other NOx_online 1702 2 Low NOx Burner 12/1/1998 1702 3 Low NOx Burner 12/1/2000 1702 4 Low NOx Burner 12/1/1993

Page 26boiler_control_SO2

facility _id boiler_id SO2_type SO2_other SO2_online 1702 1 Low Sulfur Coal 12/1/1980 1702 2 Low Sulfur Coal 12/1/1980

Page 27boiler_additives

facility _id boiler_id boiler_additive additive_other

additive_online

Page 28facility _units

facility _id unit_id 1702 Unit 1 1702 Unit 2 1702 Unit 3 1702 Unit 4

Page 29unit_boilers

facility _id unit_id boiler_id 1702 Unit 1 1 1702 Unit 2 2 1702 Unit 3 3 1702 Unit 4 4

Page 30facility _controls

facility _id control_id control_group control_type

control_other

legacy _control cntrol_online

control_offline

NOx_reagent 1702 DEK1-ESP1

PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 12/1/1959 1702 DEK1-ESP2

PM control Electrostatic precipitator, cold side, w/ flue gas conditioning FALSE 12/1/1976 1702 DEK1-SCRNOx control Selective Cataly

tic Reduction FALSE 12/1/2004 Urea to Ammonia conversion 1702 DEK2-ESP1

PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 12/1/1959 1702 DEK2-ESP2

PM control Electrostatic precipitator, cold side, w/ flue gas conditioning FALSE 12/1/1976 1702 DEK2-SCRNOx control Selective Cataly

tic Reduction FALSE 12/1/2003 Urea to Ammonia conversion

Page 31facility _controls

reagent_other

NOx_ammonia

SO2_sorbent

oher_sorbent

SO2_scrubber_additive

Urea to Ammonia conversion

Urea to Ammonia conversion

Page 32facility _sampling_ports

facility _id sampling_port_id 1702 DEK1-Port 1702 DEK2-Port 1702 DEK34-Port

Page 33facility _stacks

facility _id stack_id stack_height stack_diameter

sack_gas_velocity 1702 DEK1 - Stack 350 18 1702 DEK2-Stack 350 18 1702 DEK34-Combined Stack 450 34.5

Page 34configurations

facility _id configuration_id 1702 DEK1-Conf 1702 DEK2-Conf 1702 DEK3-Conf 1702 DEK4-Conf

Page 35configuration_components

facility _id configuration_id

component_id

order component_type port_near 1702 DEK1-ConfDEK1 - Stack 5 Stack 1702 DEK1-ConfDEK1-ESP1 3 PM control 1702 DEK1-ConfDEK1-ESP2 4 PM control 1702 DEK1-ConfDEK1-Port 6 Sam pling Port 1702 DEK1-ConfDEK1-SCR 2 NOx control 1702 DEK1-ConfUnit 1 1 Unit 1702 DEK2-ConfDEK2-ESP1 3 PM control 1702 DEK2-ConfDEK2-ESP2 4 PM control 1702 DEK2-ConfDEK2-Port 6 Sam pling Port 1702 DEK2-ConfDEK2-SCR 2 NOx control 1702 DEK2-ConfDEK2-Stack 5 Stack 1702 DEK2-ConfUnit 2 1 Unit 1702 DEK3-ConfDEK34-Combined Stack 2 Stack 1702 DEK3-ConfDEK34-Port 3 Sam pling Port 1702 DEK3-ConfUnit 3 1 Unit 1702 DEK4-ConfDEK34-Combined Stack 2 Stack 1702 DEK4-ConfDEK34-Port 3 Sam pling Port 1702 DEK4-ConfUnit 4 1 Unit

Page 36configuration_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 1702 DEK1-ConfPM (Filterable) Fderal - Title V Operating Permit

0.16 1 hour 1702 DEK1-ConfSulfur Dioxide (SO2) Federal - Title V Operating Permit

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

30 days 1702 DEK2-ConfPM (Filterable) Fderal - Title V Operating Permit

0.16 1 hour 1702 DEK2-ConfSulfur Dioxide (SO2) Federal - Title V Operating Permit

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

30 days 1702 DEK3-ConfPM (Filterable) Fderal - Title V Operating Permit

0.1 1 hour 1702 DEK4-ConfPM (Filterable) Fderal - Title V Operating Permit

0.1 1 hour 1702 DEK4-ConfSulfur Dioxide (SO2) Federal - Title V Operating Permit

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

30 days 1702 DEK4-ConfNitrogen Oxide (NOx) Federal - Title V Operating Permit

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

24 hours 1702 DEK3-ConfNitrogen Oxide (NOx) Federal - Title V Operating Permit

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

24 hours 1702 DEK3-ConfSulfur Dioxide (SO2) Federal - Title V Operating Permit

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

30 days

Page 37configuration_pollutants1

avg_period_2

em lim it_details

test_method

em rate em rate_units guarantee_level

_explain

req_monitoring

eq_recordkeeping Lim it Units: lb/1000 lb exhaust gas, 50% excess air

17 No not available Stack Test, COMs, CAM compliance

COMs data, Stack Test Report, CAM compliance records No not available CEMs CEMs operation and maintenance per Part 75, monthly emission averages Lim it Units: lb/1000 lb exhaust gas, 50% excess air

17 No not available Stack Test, COMs, CAM compliance

COMs data, Stack Test Report, CAM compliance records No not available CEMs CEMs operation and maintenance per Part 75, monthly emission averages Lim it Units: lb/1000 lb exhaust gas, 50% Excess Air

17 No not available COMs COMs recordkeeping requirements Lim it units: lb/1000 lb exhaust gas

17 No not available COMs COMs recordkeeping requirements No not available CEMs CEMs data per Part 75 No not available CEMs CEMs data per Part 75 No not available CEMs CEMs data per Part 75 No not available CEMs CEMs data per Part 75

Page 38configuration_pollutants1

req_reporting Excursion Reporting, Prompt Deviation Reporting, Semi-annual ROP deviation reporting Quarterly

EER, EDR, Semi-annual monitoirng deviation reports, ROP deviation reporting. Excursion Reporting, Prompt Deviation Reporting, Semi-annual ROP deviation reporting Quarterly

EER, EDR, Semi-annual monitoirng deviation reports, ROP deviation reporting. Quarterly

COMs EER, Semi-annual ROP deviation reporting, Quarterly

COMs EER, Semi-annual ROP deviation reporting, Quarterly

CEMs EER, Semi-annual ROP deviation reporting, EDR Quarterly

CEMs EER, Semi-annual ROP deviation reporting, EDR Quarterly

CEMs EER, Semi-annual ROP deviation reporting, EDR Quarterly

CEMs EER, Semi-annual ROP deviation reporting, EDR

Page 39control_technologies

facility _id configuration_id

component_id

control_id project_titleproject_type vendor_name

vndor_contact

vendor_phone

Page 40control_technologies

vendor_address

vndor_city

vendor_state

vendor_zip actual_start_date projected_start_date

end_date sorbent chemical_additive

Page 41control_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 42control_technologies

feed_rate_units

Page 43control_coal_ranks

facility _id configuration_id

component_id

control_id coal_type

Page 44control_pollutants1

facility _id configuration_id

component_id

control_id pollutant_nam e

Page 45control_costs

facility _id configuration_id

component_id

control_id boiler_retrofit boiler_new_install

total_capital_investment

total_operating_costs

base_year

Page 46control_costs

CBI

Page 47misc_controls

facility _id misc_control_id

control_description

Page 48misc_control_configurations

facility _id misc_control_id

configuration_id

Page 49fuel_shipments

facility _id shipment_id

shipment_date

amount_received

amount_units

fuel_type state_country other_country

county 1702 AA 9/1/2009 52624.52 short tons (2000 lbs) coal WV 1702 AB 10/1/2009 41414.42 short tons (2000 lbs) coal WV 1702 AC 12/1/2009 44295.72 short tons (2000 lbs) coal WV 1702 AprNo2 4/1/2009 2585.6 barrels oil MI 1702 AprNo6 4/1/2009 28695 barrels oil MI 1702 AugNo2 8/1/2009 642.8 barrels oil MI 1702 AugOSF 8/1/2009 6645 barrels oil MI 1702 CD 2/1/2009 19456.71 short tons (2000 lbs) coal WY 1702 CE 3/1/2009 79263.27 short tons (2000 lbs) coal WY 1702 CF 4/1/2009 57410.77 short tons (2000 lbs) coal WY 1702 CG 5/1/2009 97289.2 short tons (2000 lbs) coal WY 1702 CH 6/1/2009 80468.65 short tons (2000 lbs) coal WY 1702 CI 7/1/2009 69631.76 short tons (2000 lbs) coal WY 1702 CJ 8/1/2009 103894.9 short tons (2000 lbs) coal WY 1702 CK 9/1/2009 80517.97 short tons (2000 lbs) coal WY 1702 CL 10/1/2009 88839.55 short tons (2000 lbs) coal WY 1702 CM 11/1/2009 57718.42 short tons (2000 lbs) coal WY 1702 CN 12/1/2009 45405.99 short tons (2000 lbs) coal WY 1702 DecNo2 12/1/2009 1709.3 barrels oil MI 1702 DecOSF 12/1/2009 2049 barrels oil MI 1702 FebNo2 2/1/2009 1671.2 barrels oil MI 1702 FebOSF 2/1/2009 881 barrels oil MI 1702 JanNo2 1/1/2009 638 barrels oil MI 1702 JanOSF 1/1/2009 2035 barrels oil MI 1702 JulNo2 7/1/2009 2747.4 barrels oil MI 1702 JulNo6 7/1/2009 1463 barrels oil MI 1702 JulOSF 7/1/2009 7182 barrels oil MI 1702 JunNo2 6/1/2009 1428.7 barrels oil MI 1702 JunNo6 6/1/2009 22861 barrels oil MI 1702 JunOSF 6/1/2009 1158 barrels oil MI 1702 MarNo2 3/1/2009 2314 barrels oil MI 1702 MayNo2 5/1/2009 1033.3 barrels oil MI 1702 MayNo6 5/1/2009 1374 barrels oil MI 1702 NovNo2 11/1/2009 333.3 barrels oil MI 1702 NovOSF 11/1/2009 3775 barrels oil MI 1702 OctNo2 10/1/2009 1290.5 barrels oil MI 1702 OctOSF 10/1/2009 583 barrels oil MI 1702 S 1/1/2009 19688.9 short tons (2000 lbs) coal WV 1702 SepNo2 9/1/2009 676.1 barrels oil MI 1702 SepOSF 9/1/2009 2031 barrels oil MI 1702 T 2/1/2009 51246.33 short tons (2000 lbs) coal WV 1702 U 3/1/2009 50483.2 short tons (2000 lbs) coal WV 1702 V 4/1/2009 85200.5 short tons (2000 lbs) coal WV 1702 W 5/1/2009 53500.4 short tons (2000 lbs) coal WV 1702 X 6/1/2009 42956.23 short tons (2000 lbs) coal WV 1702 Y 7/1/2009 32593.26 short tons (2000 lbs) coal WV 1702 Z 8/1/2009 31592.38 short tons (2000 lbs) coal WV

Page 50fuel_shipments

coal_seam shipment_method

Unit Train Unit Train Unit Train Trucks Trucks Trucks Trucks Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Trucks Unit Train Trucks Trucks Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train

Page 51fuel_shipment_configurations

facility _id shipment_id

configuration_id 1702 AA DEK1-Conf 1702 AA DEK2-Conf 1702 AB DEK1-Conf 1702 AB DEK2-Conf 1702 AC DEK1-Conf 1702 AC DEK2-Conf 1702 AprNo2 DEK1-Conf 1702 AprNo2 DEK2-Conf 1702 AprNo6 DEK3-Conf 1702 AprNo6 DEK4-Conf 1702 AugNo2 DEK1-Conf 1702 AugNo2 DEK2-Conf 1702 AugOSF DEK3-Conf 1702 AugOSF DEK4-Conf 1702 CD DEK1-Conf 1702 CD DEK2-Conf 1702 CE DEK1-Conf 1702 CE DEK2-Conf 1702 CF DEK1-Conf 1702 CF DEK2-Conf 1702 CG DEK1-Conf 1702 CG DEK2-Conf 1702 CH DEK1-Conf 1702 CH DEK2-Conf 1702 CI DEK1-Conf 1702 CI DEK2-Conf 1702 CJ DEK1-Conf 1702 CJ DEK2-Conf 1702 CK DEK1-Conf 1702 CK DEK2-Conf 1702 CL DEK1-Conf 1702 CL DEK2-Conf 1702 CM DEK1-Conf 1702 CM DEK2-Conf 1702 CN DEK1-Conf 1702 CN DEK2-Conf 1702 DecNo2 DEK1-Conf 1702 DecNo2 DEK2-Conf 1702 DecOSF DEK3-Conf 1702 DecOSF DEK4-Conf 1702 FebNo2 DEK1-Conf 1702 FebNo2 DEK2-Conf 1702 FebOSF DEK3-Conf 1702 FebOSF DEK4-Conf 1702 JanNo2 DEK1-Conf 1702 JanNo2 DEK2-Conf 1702 JanOSF DEK3-Conf 1702 JanOSF DEK4-Conf 1702 JulNo2 DEK1-Conf 1702 JulNo2 DEK2-Conf 1702 JulNo6 DEK3-Conf

Page 52fuel_shipment_configurations

1702 JulNo6 DEK4-Conf 1702 JulOSF DEK3-Conf 1702 JulOSF DEK4-Conf 1702 JunNo2 DEK1-Conf 1702 JunNo2 DEK2-Conf 1702 JunNo6 DEK3-Conf 1702 JunNo6 DEK4-Conf 1702 JunOSF DEK3-Conf 1702 JunOSF DEK4-Conf 1702 MarNo2 DEK1-Conf 1702 MarNo2 DEK2-Conf 1702 MayNo2 DEK1-Conf 1702 MayNo2 DEK2-Conf 1702 MayNo6 DEK3-Conf 1702 MayNo6 DEK4-Conf 1702 NovNo2 DEK1-Conf 1702 NovNo2 DEK2-Conf 1702 NovOSF DEK3-Conf 1702 NovOSF DEK4-Conf 1702 OctNo2 DEK1-Conf 1702 OctNo2 DEK2-Conf 1702 OctOSF DEK3-Conf 1702 OctOSF DEK4-Conf 1702 S DEK1-Conf 1702 S DEK2-Conf 1702 SepNo2 DEK1-Conf 1702 SepNo2 DEK2-Conf 1702 SepOSF DEK3-Conf 1702 SepOSF DEK4-Conf 1702 T DEK1-Conf 1702 T DEK2-Conf 1702 U DEK1-Conf 1702 U DEK2-Conf 1702 V DEK1-Conf 1702 V DEK2-Conf 1702 W DEK1-Conf 1702 W DEK2-Conf 1702 X DEK1-Conf 1702 X DEK2-Conf 1702 Y DEK1-Conf 1702 Y DEK2-Conf 1702 Z DEK1-Conf 1702 Z DEK2-Conf

Page 53fuel_shipment_samples

facility _id shipment_id

sample_id amount_fuel amount_fuel_units

total_sulfur ash_content heating_value

hating_units 1702 FebOSF 35 24655 gallons 0.337 0.51 146243 Btu/gal 1702 JanOSF 34 12156 gallons 0.329 0.7 140341 Btu/gal 1702 JulOSF 39 84591 gallons 0.1638 0.1 139265 Btu/gal 1702 JunOSF 37 72753 gallons 0.1987 0.55 139708 Btu/gal 1702 JunOSF 38 47867 gallons 0.1673 0.1 47867 Btu/gal 1702 NovOSF 40 36337 gallons 0.1557 0.55 139287 Btu/gal 1702 OctOSF 40 24503 gallons 0.1557 0.55 139287 Btu/gal 1702 SepOSF 40 24370 gallons 0.1557 0.55 139287 Btu/gal

Page 54fuel_shipment_samples

chlorine chlorine_units fluorine fluorine_units data_provided

data_other_specified

supplier_type

supplier_name

supplier_address contractual obligations Fuel supplier contractual obligations Fuel supplier contractual obligations Fuel supplier contractual obligations Fuel supplier contractual obligations Fuel supplier contractual obligations Fuel supplier contractual obligations Fuel supplier

Page 55fuel_shipment_samples

supplier_city

supplier_state

supplier_zip

lab_nam e lab_address lab_city lab_state lab_zip analysis_copies No No No No No No No

Page 56fuel_shipment_samples

analysis_copies

Page 57fuel_sample_pollutants

facility _id shipment_id

sample_id fuel_pollutant pollutant_conc

pollutant_conc_units

pollutant_conc_ND

pollutant_conc_MDL 1702 FebOSF 35 Lead (Pb) 19 parts per million (dry) (ppm) FALSE 1702 FebOSF 35 Manganese (Mn) 2.1 parts per million (dry) (ppm) FALSE 1702 FebOSF 35 Nickel (Ni) 1 parts per million (dry) (ppm) FALSE 1702 JanOSF 34 Lead (Pb) 14 parts per million (dry) (ppm) FALSE 1702 JanOSF 34 Manganese (Mn) 1.9 parts per million (dry) (ppm) FALSE 1702 JanOSF 34 Nickel (Ni) 0.77 parts per million (dry) (ppm) FALSE 1702 JulOSF 39 Lead (Pb) 15 parts per million (dry) (ppm) FALSE 1702 JulOSF 39 Manganese (Mn) 2.3 parts per million (dry) (ppm) FALSE 1702 JulOSF 39 Nickel (Ni) 0.98 parts per million (dry) (ppm) FALSE 1702 JunOSF 37 Lead (Pb) 13 parts per million (dry) (ppm) FALSE 1702 JunOSF 37 Manganese (Mn) 1.8 parts per million (dry) (ppm) FALSE 1702 JunOSF 37 Nickel (Ni) 0.97 parts per million (dry) (ppm) FALSE 1702 JunOSF 38 Lead (Pb) 15 parts per million (dry) (ppm) FALSE 1702 JunOSF 38 Manganese (Mn) 1.9 parts per million (dry) (ppm) FALSE 1702 JunOSF 38 Nickel (Ni) 0.87 parts per million (dry) (ppm) FALSE 1702 NovOSF 40 Lead (Pb) 16 mi lligramper kilogram (dry) (mg/kg) FALSE 1702 NovOSF 40 Manganese (Mn) 2 mi lligramper kilogram (dry) (mg/kg) FALSE 1702 NovOSF 40 Nickel (Ni) 1.2 mi lligramper kilogram (dry) (mg/kg) FALSE 1702 OctOSF 40 Lead (Pb) 16 parts per million (dry) (ppm) FALSE 1702 OctOSF 40 Manganese (Mn) 2 parts per million (dry) (ppm) FALSE 1702 OctOSF 40 Nickel (Ni) 1.2 parts per million (dry) (ppm) FALSE 1702 SepOSF 40 Lead (Pb) 16 parts per million (dry) (ppm) FALSE 1702 SepOSF 40 Manganese (Mn) 2 parts per million (dry) (ppm) FALSE 1702 SepOSF 40 Nickel (Ni) 1.2 parts per million (dry) (ppm) FALSE

Page 58test_reports

facility _id report_id report_typeother_type report_description report_begin_date

report_end_date

before_control

during_deviation 1702 2005 DEK2-PM Testing

compliance Particulate testing required by ROP ######## No No 1702 DEK1 - 2005 PM Testing

compliance Particulate testing required by ROP ######## No No 1702 DEK1 - 2009 PM Testing

compliance Particulate testing required by ROP 3/11/2009 No No 1702 DEK1 - Hg Cems Performance Test

other Vendor Performance Guarentee RATA test for vendor performance guarentee for engineering project

######## ######## No No 1702 DEK2 - 2008 PM Testing

compliance Particulate testing required by ROP ######## No No 1702 DEK2 - Hg CEMs performance guarentee

other Vendor Performance Guarentee RATA for Hg CEMs for vendor performance guarentee for engineering project.

######## ######## No No

Page 59test_reports

deviation_reports No No No No No No

Page 60test_report_configurations

facility _id report_id configuration_id 1702 2005 DEK2-PM Testing

DEK2-Conf 1702 DEK1 - 2005 PM Testing

DEK1-Conf 1702 DEK1 - 2009 PM Testing

DEK1-Conf 1702 DEK1 - Hg Cems Performance Test

DEK1-Conf 1702 DEK2 - 2008 PM Testing

DEK2-Conf 1702 DEK2 - Hg CEMs performance guarentee

DEK2-Conf

Page 61test_report_fuels

facility _id report_id fuel_id 1702 2005 DEK2-PM Testing

Mix 1702 DEK1 - 2005 PM Testing

Mix 1702 DEK1 - 2009 PM Testing

mix 1702 DEK1 - Hg Cems Performance Test

Mix 1702 DEK2 - 2008 PM Testing

Mix 1702 DEK2 - Hg CEMs performance guarentee

mix

Page 62test_report_fuel_types

facility _id report_id fuel_id fuel_type percentage_massvol percentage_btu

other_type 1702 2005 DEK2-PM Testing

Mix coal - bituminous 1702 2005 DEK2-PM Testing

Mix coal - subbituminous 1702 DEK1 - 2005 PM Testing

Mix coal - bituminous 1702 DEK1 - 2005 PM Testing

Mix coal - subbituminous 1702 DEK1 - 2009 PM Testing

mix coal - bituminous 1702 DEK1 - 2009 PM Testing

mix coal - subbituminous 1702 DEK1 - Hg Cems Performance Test

Mix coal - bituminous 1702 DEK1 - Hg Cems Performance Test

Mix coal - subbituminous 1702 DEK2 - 2008 PM Testing

Mix coal - bituminous 1702 DEK2 - 2008 PM Testing

Mix coal - subbituminous 1702 DEK2 - Hg CEMs performance guarentee

mix coal - bituminous 1702 DEK2 - Hg CEMs performance guarentee

mix coal - subbituminous

Page 63cem_data

facility _id time_period

cem_period_description 1702 2005-2009

Page 64cem_data_pollutants1

facility _id time_period

pollutant_nam e 1702 2005-2009 Nitrogen Oxide (NOx) 1702 2005-2009 Sulfur Dioxide (SO2)

Page 65test_report_sampling

facility _id report_id sampling_port_id point_differ point_description befre_SO2_device

point_orientation

normal_bypass_percent

testing_bypass_percent 1702 2005 DEK2-PM Testing

DEK2-Port No No 1702 DEK1 - 2005 PM Testing

DEK1-Port No No 1702 DEK1 - 2009 PM Testing

DEK1-Port No No 1702 DEK1 - Hg Cems Performance Test

DEK1-Port No No 1702 DEK2 - 2008 PM Testing

DEK2-Port No No 1702 DEK2 - Hg CEMs performance guarentee

DEK2-Port No No

Page 66test_report_sampling

fg_fraction

Page 67sampling_runs

facility _id report_id sampling_port_id run_id start_datetime end_datetim e

unit_load net_generation fg_moisture_content 1702 2005 DEK2-PM Testing

DEK2-Port 1 ######## ######## 283 9.3 1702 2005 DEK2-PM Testing

DEK2-Port 2 ######## ######## 282 9.2 1702 2005 DEK2-PM Testing

DEK2-Port 3 ######## ######## 279 9.2 1702 2005 DEK2-PM Testing

DEK2-Port average ######## ######## 281 9.2 1702 DEK1 - 2005 PM Testing

DEK1-Port 1 ######## ######## 263 11.2 1702 DEK1 - 2005 PM Testing

DEK1-Port 2 ######## ######## 270 10.1 1702 DEK1 - 2005 PM Testing

DEK1-Port 3 ######## ######## 269 10.6 1702 DEK1 - 2005 PM Testing

DEK1-Port average ######## ######## 267 10.7 1702 DEK1 - 2009 PM Testing

DEK1-Port 1 3/11/2009 3/11/2009 268 8.5 1702 DEK1 - 2009 PM Testing

DEK1-Port 2 3/11/2009 3/11/2009 268 8.9 1702 DEK1 - 2009 PM Testing

DEK1-Port 3 3/11/2009 3/11/2009 267 8.9 1702 DEK1 - 2009 PM Testing

DEK1-Port average 3/11/2009 3/11/2009 268 8.8 1702 DEK1 - Hg Cems Performance Test

DEK1-Port average ######## ######## 1702 DEK2 - 2008 PM Testing

DEK2-Port 1 ######## ######## 278 8.3 1702 DEK2 - 2008 PM Testing

DEK2-Port 2 ######## ######## 279 9 1702 DEK2 - 2008 PM Testing

DEK2-Port 3 ######## ######## 280 9.8 1702 DEK2 - 2008 PM Testing

DEK2-Port average ######## ######## 279 9 1702 DEK2 - Hg CEMs performance guarentee

DEK2-Port average ######## ########

Page 68sampling_runs

fg_flow_rate

fg_flow_rate_units

standard_temperature

standard_pressure

normal_temperature

normal_pressure

fg_oxygen_content

fg_CO2_content

fg_temperature 627285 dscfm 6.09 13.08 1 609330 dscfm 6.01 13.18 1 609499 dscfm 6.09 13.07 1 615371 dscfm 6.06 13.11 1 606789 dscfm 4.34 15.01 1 605931 dscfm 4.4 14.68 1 600915 dscfm 4.44 14.68 1 604545 dscfm 4.39 14.79 1 624640 dscfm 5.48 13.7 292 615877 dscfm 5.63 13.62 298 611350 dscfm 5.56 13.84 286 617289 dscfm 5.56 13.72 292

610917 dscfm 6.36 12.89 300 631409 dscfm 6.31 12.91 294 634102 dscfm 6.2 13.02 298 625476 dscfm 6.29 12.94 298

Page 69sampling_runs

fg_pressure

Hg_loi test_method run_comments

fuel_id fuel_unit_load fuel_flow_rate

fuel_ash fuel_heating_value 17 flue gas temp=324F Mix 12456 17 flue gas temp=328F 17 flue gas temp=327F Mix 12456 17 flue gas temp=327F Mix 12456 17 flue gas temp=312F Mix 12564 17 flue gas temp=304F Mix 12564 17 flue gas temp=305F Mix 12564 Method 17 Flue gas temp was 307F Mix 12564 17 mix 12863 17 mix 12863 17 mix 12863 Method 17 mix 12863 30B 17 Mix 12555 17 Mix 12555 17 Mix 12555 Method 17 Mix 12555 30B

Page 70sampling_runs

fuel_sulfur

Page 71sampling_run_pollutants1

facility _id report_id sampling_port_id run_id pollutant_nam e conc conc_units conc_ND conc_MDL 1702 2005 DEK2-PM Testing

DEK2-Port 2 PM (Filterable) 0.0368 FALSE 1702 2005 DEK2-PM Testing

DEK2-Port 3 PM (Filterable) 0.0343 FALSE 1702 2005 DEK2-PM Testing

DEK2-Port average PM (Filterable) 0.0344 FALSE 1702 DEK1 - 2005 PM Testing

DEK1-Port average PM (Filterable) 0.0149 FALSE 1702 DEK1 - 2009 PM Testing

DEK1-Port average PM (Filterable) 0.0217 FALSE 1702 DEK2 - 2008 PM Testing

DEK2-Port average PM (Filterable) 0.0101 FALSE 1702 DEK1 - Hg Cems Performance Test

DEK1-Port average Total Mercury (Hgt) 4.211 FALSE 1702 DEK2 - Hg CEMs performance guarentee

DEK2-Port average Total Mercury (Hgt) 1.449 FALSE 1702 DEK1 - 2005 PM Testing

DEK1-Port 1 PM (Filterable) 0.011 FALSE 1702 DEK1 - 2005 PM Testing

DEK1-Port 2 PM (Filterable) 0.016 FALSE 1702 DEK1 - 2005 PM Testing

DEK1-Port 3 PM (Filterable) 0.0177 FALSE 1702 DEK1 - 2009 PM Testing

DEK1-Port 1 PM (Filterable) 0.0178 FALSE 1702 DEK1 - 2009 PM Testing

DEK1-Port 2 PM (Filterable) 0.0242 FALSE 1702 DEK1 - 2009 PM Testing

DEK1-Port 3 PM (Filterable) 0.0231 FALSE 1702 DEK2 - 2008 PM Testing

DEK2-Port 1 PM (Filterable) 0.0103 FALSE 1702 DEK2 - 2008 PM Testing

DEK2-Port 2 PM (Filterable) 0.0087 FALSE 1702 DEK2 - 2008 PM Testing

DEK2-Port 3 PM (Filterable) 0.0113 FALSE 1702 2005 DEK2-PM Testing

DEK2-Port 1 PM (Filterable) 0.0321 FALSE

Page 72sampling_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 120.95 pound per hour (lb/hr)

FALSE 0.0452 pound per million British Thermal Unit (lb/MMBtu) FALSE lb/1000 lb exhaust gas 112.36 pound per hour (lb/hr)

FALSE 0.0423 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000lbs exhuast gas 113.8 pound per hour (lb/hr)

FALSE 0.0423 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000lbs exhaust gas 54.54 pound per hour (lb/hr)

FALSE 0.0183 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhuast gas, 50% air 74.29 pound per hour (lb/hr)

FALSE 0.0263 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas, 50% AIR 33.43 pound per hour (lb/hr)

FALSE 0.0127 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000lbs exhaust gas, 50% air FALSE FALSE ug/wscm FALSE FALSE ug/wscm 41 pound per hour (lb/hr)

FALSE 0.0135 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas 58.41 pound per hour (lb/hr)

FALSE 0.0197 pound per million British Thermal Unit (lb/MMBtu) FALSE bs/1000 lbs exhaust 64.21 pound per hour (lb/hr)

FALSE 0.0218 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000lbs exhaust gas 61.98 pound per hour (lb/hr)

FALSE 0.0217 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000lbs exhaust gas 82.32 pound per hour (lb/hr)

FALSE 0.0294 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas 78.55 pound per hour (lb/hr)

FALSE 0.0278 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000lbs exhuast gas 32.89 pound per hour (lb/hr)

FALSE 0.0128 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas 29.11 pound per hour (lb/hr)

FALSE 0.011 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000lbsexhaust gas 38.29 pound per hour (lb/hr)

FALSE 0.0142 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000lbs exhuast gas 108.08 pound per hour (lb/hr)

FALSE 0.0395 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000lbs exhaust gas

Page 73sampling_run_pollutants1

run_pollutant_comment lb/1000 lb exhaust gas lbs/1000lbs exhuast gas lbs/1000lbs exhaust gas lbs/1000 lbs exhuast gas, 50% air lbs/1000 lbs exhaust gas, 50% AIR lbs/1000lbs exhaust gas, 50% air

lbs/1000 lbs exhaust gas bs/1000 lbs exhaust lbs/1000lbs exhaust gas lbs/1000lbs exhaust gas lbs/1000 lbs exhaust gas lbs/1000lbs exhuast gas lbs/1000 lbs exhaust gas lbs/1000lbsexhaust gas lbs/1000lbs exhuast gas lbs/1000lbs exhaust gas

Page 74sampling_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 75sampling_run_fuel

fuel_conc_MDL

Page 76