Facility _Information facility _id utility

_code legal_owner_nam e

legl_operator_name

legal_address_type

legal_address

legal_city legal_state legal_zip 1710 4254 Consumers Energy Co, et.al Consumers Energy

Co legal ownerOne Energy Plaza Jackson MI 49201

Page 1Facility _Information plant_nam e

physical_address

phyical_city

physical_state

physical_zip

mailing_address

mailing_city

mailing_state

mailing_zip Consumers Energy

- J.H. Campbell 17000 Croswell

West Olive MI 49460 17000 Croswell West Olive MI 49460

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 FALSE FALSE FALSE TRUE TRUE FALSE

Page 3Facility _Information ff_permitted_petcoke

ff_permitted_other

deviation_reporting

continuous_emissions

cem_provided

facility _note FALSE FALSE Prompt reporting of deviaions, COMs Semi-annual report for monitor downtime, semi-annual ROP deviation reporting. No MDNRE Lansing, MI and EPA EDR submissions for SO2 and NOX CEMs PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 4Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 5Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 6Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 7Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 8Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 9Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 10Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 11Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 12Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 13Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 14Facility _Information PART ILegal Owner6.7% of the JHC3 Campbell Plant is owned by other parties.Facility and Fuel InformationOil Type fired: Oil burned for startup operation and flame stabilizationBoiler InformationTemperatures 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) 10,700 Btu/lbmPresent operating gross efficiency (HHV)8,961 Btu/lbmDesign steam temperature (F)1050FOperating steam temperature(F) 1,040FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 991FUnit2 :Original design gross efficiency(HHV) 11,600 Btu/lbmPresent operating gross efficiency (HHV)10,938Btu/lbmDesign steam temperature (F)1,000FOperating steam temperature(F) 983FDesign reheat Temperature (F) 1,000FOperating reheat temperature(F) 978FUnit 3 :Original design gross efficiency (HHV) 12,519 Btu/lbmPresent operating gross effic

Page 15facility _contacts facility _id contact_id contact_title contact_name

contact_phone1

contact_phone2

contact_email

contact_primary 1710 1 Sr. Environmental Planner Kathryn Cunningham

5177683462 kmcunningham@cmsenergy.com TRUE 1710 2 Project Engineer Corwin Holm es

5177881756 clholmes@cmsenergy.com FALSE

Page 16facility _coal_utilized facility _id coal_type percentage_mass percentage_btu

synfuel_type

coal_note 1710 bitum inous 29 26 Assumed Bituminous coal btu/lb content :12650Assumed subbituminous coal btu/lb content:8800Unit 1&Unit 3fuel utilized 100% subbituminous 1710 subbituminous 71 74 Assumed Bituminous coal btu/lb content :12650Assumed subbituminous coal btu/lb content:8800Unit 1&Unit 3fuel utilized 100% subbituminous

Page 17facility _coal_utilized
Assumed Bituminous coal btu/lb content :12650Assumed subbituminous coal btu/lb content:8800Unit 1&Unit 3fuel utilized 100% subbituminous Assumed Bituminous coal btu/lb content :12650Assumed subbituminous coal btu/lb content:8800Unit 1&Unit 3fuel utilized 100% subbituminous

Page 18facility _coal_utilized
Assumed Bituminous coal btu/lb content :12650Assumed subbituminous coal btu/lb content:8800Unit 1&Unit 3fuel utilized 100% subbituminous Assumed Bituminous coal btu/lb content :12650Assumed subbituminous coal btu/lb content:8800Unit 1&Unit 3fuel utilized 100% subbituminous

Page 19facility _oil_utilized facility _id oil_type percentage_volume percentage_btu

other_type 1710 No.2 Fuel Oil (distillate) 100 100

Page 20facility _other_materials facility _id other_material

permitted_burn

actually _burn other_quantity

other_quantity

_units other_note rcra_utilize rcra_explain

Page 21facility _other_materials rcra_explain

Page 22boiler_information

facility _id boiler_id boiler_type boiler_other bottom_design

design_fuelheat_input max_heat_input MWe_capacity 1710 Unit 1 Tangential firing Wet Bottom coal 2300 2561 274 1710 Unit 2 Wall firing - front firing Wet Bottom coal 3259 3392 374 1710 Unit 3 Wall firing - front firing Wet Bottom coal 7643 8199 869

Page 23boiler_information

MWe_net_capacity

design_gross_efficiency

operating_gross_efficiency

design_pressure

operating_pressure

design_temp

operating_temp

design_reheat_multiple

design_reheat_temp1 260 90.26 86.3 2400 2398 1 1 FALSE 355 90.47 89.1 3500 3494.5 1 1 FALSE 825 89.74 84.5 2400 2430 1 1 FALSE

Page 24boiler_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 7705 74.86 N 2030 FALSE FALSE 7239 67.87 N 2030 FALSE FALSE 7171 77.51 Subpart D 2040 FALSE

Page 25boiler_information

NOx_control

SO2_control

combustion_additives Yes Yes No Yes Yes No Yes Yes No

Page 26boiler_fuels

facility _id boiler_id fuel_type fuel_year percentage_massvol percentage_btu

other_type 1710 Unit 1 coal - subbituminous 2009 100 100 1710 Unit 2 coal - bituminous2009 60.9 69.1 1710 Unit 2 coal - subbituminous 2009 39.1 30.9 1710 Unit 3 coal - subbituminous 2009 100 100

Page 27boiler_control_NOx

facility _id boiler_id NOx_type NOx_other NOx_online 1710 Unit 1 Low NOx Burner 4/1/2001 1710 Unit 2 Low NOx Burner 12/1/2000 1710 Unit 3 Low NOx Burner 3/1/2000

Page 28boiler_control_SO2

facility _id boiler_id SO2_type SO2_other SO2_online 1710 Unit 1 Low Sulfur Coal 12/1/1988 1710 Unit 2 Low Sulfur Coal 12/1/1988 1710 Unit 3 Low Sulfur Coal 12/1/1980

Page 29boiler_additives

facility _id boiler_id boiler_additive additive_other

additive_online

Page 30facility _units facility _id unit_id 1710 Unit 1 1710 Unit 2 1710 Unit 3

Page 31unit_boilers

facility _id unit_id boiler_id 1710 Unit 1 Unit 1 1710 Unit 2 Unit 2 1710 Unit 3 Unit 3

Page 32facility _controls facility _id control_id control_group control_type

control_other

legacy _control cntrol_online

control_offline

NOx_reagent 1710 JHC1-ESP PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 7/1/2001 1710 JHC2-ESP PM control Electrostatic precipitator, cold side, w/ flue gas conditioning FALSE 12/1/1978 1710 JHC3 - SCR

NOx control

Selective Cataly

tic Reduction FALSE 4/1/2007 Urea to Ammonia conversion 1710 JHC3-ESP PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 6/1/1980

Page 33facility _controls reagent_other

NOx_ammonia

SO2_sorbent

oher_sorbent

SO2_scrubber_additive Urea to Ammonia conversion

Page 34facility _sampling_ports facility _id sampling_port_id 1710 JHC12 Combined 1710 JHC3 - Comb 1710 JHC3 - Port A 1710 JHC3 - Port B

Page 35facility _stacks facility _id stack_id stack_height stack_diameter

sack_gas_velocity 1710 JHC 3 - Stack 642 27.25 1710 JHC Combined Stack 400 19

Page 36configurations

facility _id configuration_id 1710 JHC1-Conf 1710 JHC2-Conf 1710 JHC3-Conf

Page 37configuration_components

facility _id configuration_id

component_id

order component_type port_near 1710 JHC1-ConfJHC Combined Stack 3 Stack 1710 JHC1-ConfJHC12 Combined 4 Sam pling Port 1710 JHC1-ConfJHC1-ESP 2 PM control 1710 JHC1-Conf Unit 1 1 Unit 1710 JHC2-ConfJHC Combined Stack 3 Stack 1710 JHC2-ConfJHC12 Combined 4 Sam pling Port 1710 JHC2-ConfJHC2-ESP 2 PM control 1710 JHC2-Conf Unit 2 1 Unit 1710 JHC3-ConfJHC Combined Stack 6 Stack 1710 JHC3-ConfJHC3 - Comb 7 Sam pling Port 1710 JHC3-ConfJHC3 - Port A 4 Sam pling Port 1710 JHC3-ConfJHC3 - Port B 5 Sam pling Port 1710 JHC3-ConfJHC3 - SCR 2 NOx control 1710 JHC3-ConfJHC3-ESP 3 PM control 1710 JHC3-Conf Unit 3 1 Unit

Page 38configuration_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 1710 JHC3-Conf PM (Filterable) Fderal - Title V Operating Permit

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

1 hour 370 pound per hour (lb/hr) 1710 JHC3-Conf Sulfur Dioxide (SO2) Federal - Title V Operating Permit

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

3 hours 10500 pound per hour (lb/hr) 1710 JHC3-Conf Nitrogen Oxide (NOx) Federal - Title V Operating Permit

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

3 hours 6130 pound per hour (lb/hr) 1710 JHC1-Conf PM (Filterable) Fderal - Title V Operating Permit

0.16 1 hour 1710 JHC1-Conf Sulfur Dioxide (SO2) Federal - Title V Operating Permit

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

30 days 1710 JHC2-Conf PM (Filterable) Fderal - Title V Operating Permit

0.15 1 hour 1710 JHC2-Conf Sulfur Dioxide (SO2) Federal - Title V Operating Permit

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

30 days

Page 39configuration_pollutants1

avg_period_2

em lim it_details

test_method

em rate em rate_units guarantee_level

_explain

req_monitoring

eq_recordkeeping 1 hour PM, 1080 tons/yr based on 12 month rolling EPA Method 17 No not available Stack Testing, CAM

12 month rolling averages, CAM required recordkeeping 24 hours SO2 tons/year = 31,650 baserd on 12 month rolling No not available CEMS for flow rate and SO2

CEMs per Part 75, 3 hour rolling averages, daily averages, 12 month rolling average 24 hours Nox tons/year = 18,750 based on 12 month rolling average No not available CEMS for flow rate and Nox

CEMs per Part 75, 3 hour rolling averages, daily averages, 12 month rolling average lbs/1000 lbs exhaust gase

Method 17 No not available Stack Test (every

3 years), CAM Plan, COMs COMs 6 minute avearages No not available CEMs, fuel sulfur content

Maintain CEMS per Part 75 lbs/1000 lbs exhaust gas

Method 17 No not available Stack Test every

three years, COMs. COMs 6 minute averages, CAM plan requirements No not available CEMs, fuel sulfur content

Maintain CEMS per Part 75

Page 40configuration_pollutants1

req_reporting CAM required reporting, Stack Test Report, Deviation reporting, CAM reporting Quarterly

EERs, Semi-annual monitoring Deviation Reporting, ROP deviation reporting Quarterly

EERs, Semi-annual monitoring Deviation Reporting, ROP deviation reporting Subm ission of Stack Test Report. Deviation Reporting. Quarterly

EER, semi-annual deviation reporting. Subm ission of Stack Test Report. Deviation Reporting. Quarterly

EER, semi-annual deviation reporting.

Page 41control_technologies

facility _id configuration_id

component_id

control_id project_titleproject_type vendor_name

vndor_contact

vendor_phone

Page 42control_technologies

vendor_address

vndor_city

vendor_state

vendor_zip actual_start_date projected_start_date

end_date sorbent chemical_additive

Page 43control_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 44control_technologies feed_rate_units

Page 45control_coal_ranks

facility _id configuration_id

component_id

control_id coal_type

Page 46control_pollutants1

facility _id configuration_id

component_id

control_id pollutant_nam e

Page 47control_costs

facility _id configuration_id

component_id

control_id boiler_retrofit boiler_new_install

total_capital_investm ent

total_operating_costs

base_year

Page 48control_costs

CBI

Page 49misc_controls

facility _id misc_control_id

control_description

Page 50misc_control_configurations

facility _id misc_control_id

configuration_id

Page 51fuel_shipments

facility _id shipment_id

shipment_date

amount_received

amount_units

fuel_type state_country other_country

county 1710 A 1/1/2009 40810.1 short tons (2000 lbs) coal WV 1710 AM 1/1/2009 318975.6 short tons (2000 lbs) coal WY 1710 AN 2/1/2009 331086.9 short tons (2000 lbs) coal WY 1710 AO 3/1/2009 298044.5 short tons (2000 lbs) coal WY 1710 AP 4/1/2009 287491.6 short tons (2000 lbs) coal WY 1710 AQ 5/1/2009 276980.8 short tons (2000 lbs) coal WY 1710 AR 6/1/2009 308713.4 short tons (2000 lbs) coal WY 1710 AS 7/1/2009 334882.7 short tons (2000 lbs) coal WY 1710 AT 8/1/2009 299840.7 short tons (2000 lbs) coal WY 1710 AU 9/1/2009 253078.1 short tons (2000 lbs) coal WY 1710 AugNo2 8/1/2009 2701 barrels oil MI 1710 AV 10/1/2009 310375.7 short tons (2000 lbs) coal WY 1710 AW 11/1/2009 265474.9 short tons (2000 lbs) coal WY 1710 AX 12/1/2009 302508.2 short tons (2000 lbs) coal WY 1710 B 2/1/2009 9943.44 short tons (2000 lbs) coal KY 1710 C 3/1/2009 10158.32 short tons (2000 lbs) coal WV 1710 D 5/1/2009 30359.74 short tons (2000 lbs) coal WV 1710 DecNo2 12/1/2009 2970 barrels oil MI 1710 E 6/1/2009 30765.96 short tons (2000 lbs) coal WV 1710 F 7/1/2009 64043.43 short tons (2000 lbs) coal WV 1710 FebNo2 2/1/2009 893 barrels oil MI 1710 G 8/1/2009 41608.73 short tons (2000 lbs) coal WV 1710 H 9/1/2009 51510.47 short tons (2000 lbs) coal WV 1710 I 10/1/2009 31793.84 short tons (2000 lbs) coal WV 1710 J 11/1/2009 43306.68 short tons (2000 lbs) coal WV 1710 JanNo.2 1/1/2009 894 barrels oil MI 1710 JulNo2 7/1/2009 2721 barrels oil MI 1710 JunNo2 6/1/2009 1786 barrels oil MI 1710 K 12/1/2009 11154.83 short tons (2000 lbs) coal WV 1710 MarNo2 3/1/2009 893 barrels oil MI 1710 MayNo2 5/1/2009 6033 barrels oil MI 1710 NovNo2 11/1/2009 2682 barrels oil MI 1710 OctNo2 10/1/2009 2683 barrels oil MI

Page 52fuel_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 Trucks Unit Train Unit Train Unit Train Unit Train Unit Train Unit Train Trucks Unit Train Unit Train Trucks Unit Train Unit Train Unit Train Unit Train Trucks Trucks Trucks Unit Train Trucks Trucks Trucks Trucks

Page 53fuel_shipment_configurations

facility _id shipment_id

configuration_id 1710 A JHC2-Conf 1710 AM JHC1-Conf 1710 AM JHC2-Conf 1710 AM JHC3-Conf 1710 AN JHC1-Conf 1710 AN JHC2-Conf 1710 AN JHC3-Conf 1710 AO JHC1-Conf 1710 AO JHC2-Conf 1710 AO JHC3-Conf 1710 AP JHC1-Conf 1710 AP JHC2-Conf 1710 AP JHC3-Conf 1710 AQ JHC1-Conf 1710 AQ JHC2-Conf 1710 AQ JHC3-Conf 1710 AR JHC1-Conf 1710 AR JHC2-Conf 1710 AR JHC3-Conf 1710 AS JHC1-Conf 1710 AS JHC2-Conf 1710 AS JHC3-Conf 1710 AT JHC1-Conf 1710 AT JHC2-Conf 1710 AT JHC3-Conf 1710 AU JHC1-Conf 1710 AU JHC2-Conf 1710 AU JHC3-Conf 1710 AugNo2 JHC1-Conf 1710 AugNo2 JHC2-Conf 1710 AugNo2 JHC3-Conf 1710 AV JHC1-Conf 1710 AV JHC2-Conf 1710 AV JHC3-Conf 1710 AW JHC1-Conf 1710 AW JHC2-Conf 1710 AW JHC3-Conf 1710 AX JHC1-Conf 1710 AX JHC2-Conf 1710 AX JHC3-Conf 1710 B JHC2-Conf 1710 C JHC2-Conf 1710 D JHC2-Conf 1710 DecNo2 JHC1-Conf 1710 DecNo2 JHC2-Conf 1710 DecNo2 JHC3-Conf 1710 E JHC2-Conf 1710 F JHC2-Conf 1710 FebNo2 JHC1-Conf 1710 FebNo2 JHC2-Conf 1710 FebNo2 JHC3-Conf Page 54fuel_shipment_configurations

1710 G JHC2-Conf 1710 H JHC2-Conf 1710 I JHC2-Conf 1710 J JHC2-Conf 1710 JanNo.2 JHC1-Conf 1710 JanNo.2 JHC2-Conf 1710 JanNo.2 JHC3-Conf 1710 JulNo2 JHC1-Conf 1710 JulNo2 JHC2-Conf 1710 JulNo2 JHC3-Conf 1710 JunNo2 JHC1-Conf 1710 JunNo2 JHC2-Conf 1710 JunNo2 JHC3-Conf 1710 K JHC2-Conf 1710 MarNo2 JHC1-Conf 1710 MarNo2 JHC2-Conf 1710 MarNo2 JHC3-Conf 1710 MayNo2 JHC1-Conf 1710 MayNo2 JHC2-Conf 1710 MayNo2 JHC3-Conf 1710 NovNo2 JHC1-Conf 1710 NovNo2 JHC2-Conf 1710 NovNo2 JHC3-Conf 1710 OctNo2 JHC1-Conf 1710 OctNo2 JHC2-Conf 1710 OctNo2 JHC3-Conf

Page 55fuel_shipment_samples

facility _id shipment_id

sample_id amount_fuel amount_fuel_units

total_sulfur ash_content heating_value

hating_units

Page 56fuel_shipment_samples

chlorine chlorine_units fluorine fluorine_units data_provided

data_other_specified

supplier_type

supplier_name

supplier_address

Page 57fuel_shipment_samples

supplier_city

supplier_state

supplier_zip

lab_nam e lab_address lab_city lab_state lab_zip analysis_copies

Page 58fuel_shipment_samples analysis_copies

Page 59fuel_sample_pollutants

facility _id shipment_id

sample_id fuel_pollutant pollutant_conc

pollutant_conc_units

pollutant_conc_ND

pollutant_conc_MDL

Page 60test_reports

facility _id report_id report_typeother_type report_description report_begin_date

report_end_date

before_control

during_deviation 1710 JHC12 - 2005 PM Compliance Testing

compliance Particulate Compliance Testing per ROP 9/21/2005 9/22/2005 No No 1710 JHC12 - Hg Internal Test

other Vendor Guarentee Testing RATA for Hg CEMs for engineering performance testing

12/2/2008 12/4/2008 No No 1710 JHC12-PM 2008 Compliance Testing

compliance PM Compliance testing required by ROP 10/7/2008 10/8/2008 No No 1710 JHC3 - 2005 Particulate Test

compliance Particulate testing requried by ROP 9/27/2005 9/28/2005 No No 1710 JHC3 - 2008 Particulate Test

compliance Particulate Testing per ROP requirement 9/23/2008 9/24/2008 No No 1710 JHC3A - Hg CEMs performance Test

other Vendor Guarentee Testing RATA for Hg CEMs for engineering performance testing

######## ######## No No 1710 JHC3B Hg CEMs Performance Test

other RATA for Hg CEMs Conducted for the vendor guarentee performance testing as part of engineering project.

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

Page 61test_reports

deviation_reports No No No No No No No

Page 62test_report_configurations

facility _id report_id configuration_id 1710 JHC12 - 2005 PM Compliance Testing

JHC1-Conf 1710 JHC12 - 2005 PM Compliance Testing

JHC2-Conf 1710 JHC12 - Hg Internal Test

JHC1-Conf 1710 JHC12 - Hg Internal Test

JHC2-Conf 1710 JHC12-PM 2008 Compliance Testing

JHC1-Conf 1710 JHC12-PM 2008 Compliance Testing

JHC2-Conf 1710 JHC3 - 2005 Particulate Test

JHC3-Conf 1710 JHC3 - 2008 Particulate Test

JHC3-Conf 1710 JHC3A - Hg CEMs performance Test

JHC3-Conf 1710 JHC3B Hg CEMs Performance Test

JHC3-Conf

Page 63test_report_fuels

facility _id report_id fuel_id 1710 JHC12 - 2005 PM Compliance Testing

mix - sub/bit 1710 JHC12 - Hg Internal Test

mix - sub/bit 1710 JHC12-PM 2008 Compliance Testing

mix - sub/bit 1710 JHC3 - 2005 Particulate Test

coal 1710 JHC3 - 2008 Particulate Test

coal 1710 JHC3A - Hg CEMs performance Test

Coal 1710 JHC3B Hg CEMs Performance Test

coal

Page 64test_report_fuel_types

facility _id report_id fuel_id fuel_type percentage_massvol percentage_btu

other_type 1710 JHC12 - 2005 PM Compliance Testing

mix - sub/bit

coal - bituminous 1710 JHC12 - 2005 PM Compliance Testing

mix - sub/bit

coal - subbituminous 1710 JHC12 - Hg Internal Test

mix - sub/bit

coal - bituminous 1710 JHC12 - Hg Internal Test

mix - sub/bit

coal - subbituminous 1710 JHC12-PM 2008 Compliance Testing

mix - sub/bit

coal - bituminous 1710 JHC12-PM 2008 Compliance Testing

mix - sub/bit

coal - subbituminous 1710 JHC3 - 2008 Particulate Test

coal coal - subbituminous 100 100 1710 JHC3A - Hg CEMs performance Test

Coal coal - subbituminous 100 100 1710 JHC3B Hg CEMs Performance Test

coal coal - subbituminous 100 100

Page 65cem_data

facility _id tim e_period

cem_period_description 1710 2005-2009 The Hg CEMS are not requried and are not operated according to a Standard or QAQC plan

Page 66cem_data The Hg CEMS are not requried and are not operated according to a Standard or QAQC plan

Page 67cem_data_pollutants1

facility _id tim e_period

pollutant_nam e 1710 2005-2009 Nitrogen Oxide (NOx) 1710 2005-2009 Sulfur Dioxide (SO2)

Page 68test_report_sampling

facility _id report_id sampling_port_id point_differ point_description befre_SO2_device

point_orientation

normal_bypass_percent

testing_bypass_percent 1710 JHC12 - 2005 PM Compliance Testing

JHC12 Combined

No No 1710 JHC12 - Hg Internal Test

JHC12 Combined

No No 1710 JHC12-PM 2008 Compliance Testing

JHC12 Combined

No No 1710 JHC3 - 2005 Particulate Test

JHC3 - Comb

No No 1710 JHC3 - 2008 Particulate Test

JHC3 - Comb

No No 1710 JHC3A - Hg CEMs performance Test

JHC3 - Port A

No The ESP for JHC3 has two outlets, Duct A and Duct B, each of which have test ports prior to entering the main stack. The Hg CEMs are located in these test ports. No 1710 JHC3B Hg CEMs Performance Test

JHC3 - Port B

No The JHC Unit 3 ESP has two outlets, Duct A and Duct B, prior to entering the main exhaust stack. The Hg Test ports are located in each of these ducts. No

Page 69test_report_sampling

fg_fraction

Page 70sampling_runs

facility _id report_id sampling_port_id run_id start_datetime end_datetim e

unit_load net_generation fg_moisture_content 1710 JHC12 - 2005 PM Compliance Testing

JHC12 Combined

1 9/21/2005 9/21/2005 641 12.59 1710 JHC12 - 2005 PM Compliance Testing

JHC12 Combined

2 9/22/2005 9/22/2005 642 14.02 1710 JHC12 - 2005 PM Compliance Testing

JHC12 Combined

3 9/22/2005 9/22/2005 644 15.58 1710 JHC12 - 2005 PM Compliance Testing

JHC12 Combined

average 9/21/2005 9/22/2005 643 14.06 1710 JHC12 - Hg Internal Test

JHC12 Combined

average 12/2/2008 12/4/2008 1710 JHC12-PM 2008 Compliance Testing

JHC12 Combined

1 10/7/2008 10/7/2008 647 8.2 1710 JHC12-PM 2008 Compliance Testing

JHC12 Combined

2 10/7/2008 10/7/2008 638 9.4 1710 JHC12-PM 2008 Compliance Testing

JHC12 Combined

3 10/8/2008 10/8/2008 644 9.1 1710 JHC12-PM 2008 Compliance Testing

JHC12 Combined

average 10/7/2008 10/8/2008 643 9.1 1710 JHC3 - 2005 Particulate Test

JHC3 - Comb

1 9/27/2005 9/27/2005 5859 10.6 1710 JHC3 - 2005 Particulate Test

JHC3 - Comb

2 9/28/2005 9/28/2005 5941 10 1710 JHC3 - 2005 Particulate Test

JHC3 - Comb

3 9/28/2005 9/28/2005 6015 11 1710 JHC3 - 2005 Particulate Test

JHC3 - Comb

average 9/27/2005 9/28/2005 10.5 1710 JHC3 - 2008 Particulate Test

JHC3 - Comb

1 9/23/2008 9/23/2008 5676 10.08 1710 JHC3 - 2008 Particulate Test

JHC3 - Comb

2 9/23/2008 9/23/2008 5679 9.16 1710 JHC3 - 2008 Particulate Test

JHC3 - Comb

3 9/24/2008 9/24/2008 5686 9.16 1710 JHC3 - 2008 Particulate Test

JHC3 - Comb

average 9/23/2008 9/24/2008 10.1 1710 JHC3A - Hg CEMs performance Test

JHC3 - Port A

average ######## ######## 1710 JHC3B Hg CEMs Performance Test

JHC3 - Port B

average ######## ########

Page 71sampling_runs

fg_flow_rate

fg_flow_rate_units

standard_temperature

standard_pressure

normal_temperature

normal_pressure

fg_oxygen_content

fg_CO2_content

fg_temperature 1436898 dscfm 6.17 13.38 294.6 1445303 dscfm 6 13.02 290 1460878 dscfm 5.95 13.11 291 1447693 dscfm 6.04 13.17 292 1474447 dscfm 6.06 13.25 283.1 1443044 dscfm 6.04 13.17 285.8 1476900 dscfm 6.33 13.12 284.1 1464797 dscfm 6.14 13.12 284.3 1861380 dscfm 14.35 1 1911901 dscfm 14.94 1 1910766 dscfm 14.46 1 1895685 dscfm 14.58 1 1861380 dscfm 5.44 14.12 1 1909059 dscfm 5.74 14.07 1 1887350 dscfm 5.56 13.89 1 1885930 dscfm 5.58 14.03 1

Page 72sampling_runs

fg_pressure

Hg_loi test_method run_comments

fuel_id fuel_unit_load fuel_flow_rate

fuel_ash fuel_heating_value 17 mix - sub/bit 12105 17 mix - sub/bit 12034 17 mix - sub/bit 12034 Method 17 mix - sub/bit 643 12058 30B 17 mix 12447 17 mix 12447 17 mix 12897 EPA Method 17 mix 643 12597 17 load units are klb/hr steam flow, flue gas temp at port = 319.8 PRB 17 unit load units = klb/hr steam flow, flue gas temp at port= 318.5F PRB 12956 17 unit load - klb/hr steam flow, flue gas temp = 321.5 PRB 12956 Method 17 The Boiler Output was 5938klb/hr steam flow. Flue Gas Temp was 319.9F PRB 12956 17 unit load=klb/hr steam flow, flue gas temp=329.8 PRB 11871 17 unit load = klb/hr steam flow, flue gas temp=335.3 PRB 11871 17 unit load= klb/hr steam flow, flue gas temp=328F PRB 12161 Method 17 Unit load was 5680 klb/hr steam flow. Flue Gas Temp was 331F. PRB 11967.7 30B 30B

Page 73sampling_runs

fuel_sulfur

Page 74sampling_run_pollutants1

facility _id report_id sampling_port_id run_id pollutant_nam e conc conc_units conc_ND conc_MDL 1710 JHC3 - 2005 Particulate Test

JHC3 - Comb

1 PM (Filterable) 0.0053 FALSE 1710 JHC3 - 2005 Particulate Test

JHC3 - Comb

2 PM (Filterable) 0.0058 FALSE 1710 JHC3 - 2005 Particulate Test

JHC3 - Comb

3 PM (Filterable) 0.0047 FALSE 1710 JHC3 - 2008 Particulate Test

JHC3 - Comb

1 PM (Filterable) 0.0014 FALSE 1710 JHC3 - 2008 Particulate Test

JHC3 - Comb

2 PM (Filterable) 0.002 FALSE 1710 JHC3 - 2008 Particulate Test

JHC3 - Comb

3 PM (Filterable) 0.0023 FALSE 1710 JHC12 - 2005 PM Compliance Testing

JHC12 Combined

average PM (Filterable) 0.0093 FALSE 1710 JHC12-PM 2008 Compliance Testing

JHC12 Combined

average PM (Filterable) 0.0016 FALSE 1710 JHC12 - Hg Internal Test

JHC12 Combined

average Total Mercury (Hgt) 0.938 FALSE 1710 JHC3A - Hg CEMs performance Test

JHC3 - Port A

average Total Mercury (Hgt) 7.856 FALSE 1710 JHC3B Hg CEMs Performance Test

JHC3 - Port B

average Total Mercury (Hgt) 7.35 FALSE 1710 JHC3 - 2005 Particulate Test

JHC3 - Comb

average PM (Filterable) 0.0053 FALSE 1710 JHC3 - 2008 Particulate Test

JHC3 - Comb

average PM (Filterable) 0.0019 FALSE 1710 JHC12 - 2005 PM Compliance Testing

JHC12 Combined

1 PM (Filterable) 0.0121 FALSE 1710 JHC12 - 2005 PM Compliance Testing

JHC12 Combined

2 PM (Filterable) 0.0088 FALSE 1710 JHC12 - 2005 PM Compliance Testing

JHC12 Combined

3 PM (Filterable) 0.0071 FALSE 1710 JHC12-PM 2008 Compliance Testing

JHC12 Combined

1 PM (Filterable) 0.0014 FALSE 1710 JHC12-PM 2008 Compliance Testing

JHC12 Combined

2 PM (Filterable) 0.0018 FALSE 1710 JHC12-PM 2008 Compliance Testing

JHC12 Combined

3 PM (Filterable) 0.0016 FALSE

Page 75sampling_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 41.78 pound per hour (lb/hr)

FALSE 0.0094 pound per million British Thermal Unit (lb/MMBtu) FALSE gr/dscf 95.61 pound per hour (lb/hr)

FALSE 0.0104 pound per million British Thermal Unit (lb/MMBtu) FALSE gr/dscf 77.26 pound per hour (lb/hr)

FALSE 0.0084 pound per million British Thermal Unit (lb/MMBtu) FALSE gr/dscf 21.9 pound per hour (lb/hr)

FALSE 0.0026 pound per million British Thermal Unit (lb/MMBtu) FALSE gr/dscf 33.42 pound per hour (lb/hr)

FALSE 0.0038 pound per million British Thermal Unit (lb/MMBtu) FALSE gr/dscf 37.74 pound per hour (lb/hr)

FALSE 0.0044 pound per million British Thermal Unit (lb/MMBtu) FALSE gr/dscf 73.16 pound per hour (lb/hr)

FALSE 0.0115 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas 12.48 pound per hour (lb/hr)

FALSE 0.002 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas FALSE FALSE ug/wscm FALSE FALSE ug/wscm FALSE FALSE ug/wscm 71.55 pound per hour (lb/hr)

FALSE 0.0094 pound per million British Thermal Unit (lb/MMBtu) FALSE gr/dscf 31.03 pound per hour (lb/hr)

FALSE 0.0036 pound per million British Thermal Unit (lb/MMBtu) FALSE gr/dscf 93.41 pound per hour (lb/hr)

FALSE 0.0146 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas 69.32 pound per hour (lb/hr)

FALSE 0.0111 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas 56.75 pound per hour (lb/hr)

FALSE 0.0089 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas 10.73 pound per hour (lb/hr)

FALSE 0.0016 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas 14.05 pound per hour (lb/hr)

FALSE 0.0022 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000 lbs exhaust gas 12.65 pound per hour (lb/hr)

FALSE 0.002 pound per million British Thermal Unit (lb/MMBtu) FALSE lbs/1000lbs exhaust gas

Page 76sampling_run_pollutants1 run_pollutant_comment

lbs/1000 lbs exhaust gas lbs/1000 lbs exhaust gas

lbs/1000 lbs exhaust gas lbs/1000 lbs exhaust gas lbs/1000 lbs exhaust gas lbs/1000 lbs exhaust gas lbs/1000 lbs exhaust gas lbs/1000lbs exhaust gas

Page 77sampling_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 78sampling_run_fuel fuel_conc_MDL

Page 79