Facility _Information facility _id utility

_code legal_owner_nam e

legl_operator_name

legal_address_type

legal_address

legal_city legal_state legal_zip 6030 Great River Energy Great River Energy

legal owner 12300 Elm Creek Boulevard Maple Grove

MN 55369-4718

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 Coal Creek 2875 3rd Street SW Underwood ND 58576-8576 2875 3rd Street SW

Underwood ND 58576-8576

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 58576-8576 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 Quarterly excess emission, semi annual and annual monitoring report for SO2, Nox, PM only , no requirements for mercury , HAPS or trace metals. Yes 1. The design basis heat input for CCS has never been achieved as a higher than design dilution is experience due to a low strip ratio of the shallow lignite seams. W hen applying for the initial Title V permit the heat input was changed to reflect actual fuel heat input. 2. Steam and pressure are nominal turbine throttle pressure values, actual values will range above and below this setpoint. 3. DOE project "Lignite Fuel Enhancement" that was placed in service December 2009. Post operational performance testing will be conducted in the spring of 2010 and the results reported in the final DOE report in June of 2010.4. Stack velocity reported in stanard ft/second.5. Stack height and diameter are in a several year process of being modified for wet stack conditions. W hen finished both stacks will be 25.75 diameter and 675' in height.

Page 4Facility _Information 1. The design basis heat input for CCS has never been achieved as a higher than design dilution is experience due to a low strip ratio of the shallow lignite seams. W hen applying for the initial Title V permit the heat input was changed to reflect actual fuel heat input. 2. Steam and pressure are nominal turbine throttle pressure values, actual values will range above and below this setpoint. 3. DOE project "Lignite Fuel Enhancement" that was placed in service December 2009. Post operational performance testing will be conducted in the spring of 2010 and the results reported in the final DOE report in June of 2010.4. Stack velocity reported in stanard ft/second.5. Stack height and diameter are in a several year process of being modified for wet stack conditions. W hen finished both stacks will be 25.75 diameter and 675' in height.

Page 5Facility _Information 1. The design basis heat input for CCS has never been achieved as a higher than design dilution is experience due to a low strip ratio of the shallow lignite seams. W hen applying for the initial Title V permit the heat input was changed to reflect actual fuel heat input. 2. Steam and pressure are nominal turbine throttle pressure values, actual values will range above and below this setpoint. 3. DOE project "Lignite Fuel Enhancement" that was placed in service December 2009. Post operational performance testing will be conducted in the spring of 2010 and the results reported in the final DOE report in June of 2010.4. Stack velocity reported in stanard ft/second.5. Stack height and diameter are in a several year process of being modified for wet stack conditions. W hen finished both stacks will be 25.75 diameter and 675' in height.

Page 6Facility _Information 1. The design basis heat input for CCS has never been achieved as a higher than design dilution is experience due to a low strip ratio of the shallow lignite seams. W hen applying for the initial Title V permit the heat input was changed to reflect actual fuel heat input. 2. Steam and pressure are nominal turbine throttle pressure values, actual values will range above and below this setpoint. 3. DOE project "Lignite Fuel Enhancement" that was placed in service December 2009. Post operational performance testing will be conducted in the spring of 2010 and the results reported in the final DOE report in June of 2010.4. Stack velocity reported in stanard ft/second.5. Stack height and diameter are in a several year process of being modified for wet stack conditions. W hen finished both stacks will be 25.75 diameter and 675' in height.

Page 7Facility _Information 1. The design basis heat input for CCS has never been achieved as a higher than design dilution is experience due to a low strip ratio of the shallow lignite seams. W hen applying for the initial Title V permit the heat input was changed to reflect actual fuel heat input. 2. Steam and pressure are nominal turbine throttle pressure values, actual values will range above and below this setpoint. 3. DOE project "Lignite Fuel Enhancement" that was placed in service December 2009. Post operational performance testing will be conducted in the spring of 2010 and the results reported in the final DOE report in June of 2010.4. Stack velocity reported in stanard ft/second.5. Stack height and diameter are in a several year process of being modified for wet stack conditions. W hen finished both stacks will be 25.75 diameter and 675' in height.

Page 8Facility _Information 1. The design basis heat input for CCS has never been achieved as a higher than design dilution is experience due to a low strip ratio of the shallow lignite seams. W hen applying for the initial Title V permit the heat input was changed to reflect actual fuel heat input. 2. Steam and pressure are nominal turbine throttle pressure values, actual values will range above and below this setpoint. 3. DOE project "Lignite Fuel Enhancement" that was placed in service December 2009. Post operational performance testing will be conducted in the spring of 2010 and the results reported in the final DOE report in June of 2010.4. Stack velocity reported in stanard ft/second.5. Stack height and diameter are in a several year process of being modified for wet stack conditions. W hen finished both stacks will be 25.75 diameter and 675' in height.

Page 9Facility _Information 1. The design basis heat input for CCS has never been achieved as a higher than design dilution is experience due to a low strip ratio of the shallow lignite seams. W hen applying for the initial Title V permit the heat input was changed to reflect actual fuel heat input. 2. Steam and pressure are nominal turbine throttle pressure values, actual values will range above and below this setpoint. 3. DOE project "Lignite Fuel Enhancement" that was placed in service December 2009. Post operational performance testing will be conducted in the spring of 2010 and the results reported in the final DOE report in June of 2010.4. Stack velocity reported in stanard ft/second.5. Stack height and diameter are in a several year process of being modified for wet stack conditions. W hen finished both stacks will be 25.75 diameter and 675' in height.

Page 10Facility _Information 1. The design basis heat input for CCS has never been achieved as a higher than design dilution is experience due to a low strip ratio of the shallow lignite seams. W hen applying for the initial Title V permit the heat input was changed to reflect actual fuel heat input. 2. Steam and pressure are nominal turbine throttle pressure values, actual values will range above and below this setpoint. 3. DOE project "Lignite Fuel Enhancement" that was placed in service December 2009. Post operational performance testing will be conducted in the spring of 2010 and the results reported in the final DOE report in June of 2010.4. Stack velocity reported in stanard ft/second.5. Stack height and diameter are in a several year process of being modified for wet stack conditions. W hen finished both stacks will be 25.75 diameter and 675' in height.

Page 11Facility _Information 1. The design basis heat input for CCS has never been achieved as a higher than design dilution is experience due to a low strip ratio of the shallow lignite seams. W hen applying for the initial Title V permit the heat input was changed to reflect actual fuel heat input. 2. Steam and pressure are nominal turbine throttle pressure values, actual values will range above and below this setpoint. 3. DOE project "Lignite Fuel Enhancement" that was placed in service December 2009. Post operational performance testing will be conducted in the spring of 2010 and the results reported in the final DOE report in June of 2010.4. Stack velocity reported in stanard ft/second.5. Stack height and diameter are in a several year process of being modified for wet stack conditions. W hen finished both stacks will be 25.75 diameter and 675' in height.

Page 12facility _contacts facility _id contact_id contact_title contact_name

contact_phone1

contact_phone2

contact_email

contact_primary 6030 1 Leader, Environmental & Plant Services Diane Stockdill

7014427012 dstockdill@grenergy .com TRUE

Page 13facility _coal_utilized facility _id coal_type percentage_mass percentage_btu

synfuel_type

coal_note 6030 lignite 100 100

Page 14facility _oil_utilized facility _id oil_type percentage_volume percentage_btu

other_type 6030 No.2 Fuel Oil (distillate) 100 100

Page 15facility _other_materials facility _id other_material

permitted_burn

actually _burn other_quantity

other_quantity

_units other_note rcra_utilize rcra_explain

Page 16facility _other_materials rcra_explain

Page 17boiler_information

facility _id boiler_id boiler_type boiler_other bottom_design

design_fuel heat_input max_heat_input MW e_capacity 6030 1 Tangential firing Dry Bottom coal 5280 6015 619 6030 2 Tangential firing Dry Bottom coal 5280 6022 604

Page 18boiler_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 577 80.5 82.45 2520 2520 1000 1000 FALSE 1005 565 80.5 82.45 2520 2520 1000 1000 FALSE 1005

Page 19boiler_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 1005 8063 95.5 Subpart D FALSE FALSE 1005 7981 93.3 Subpart D FALSE

Page 20boiler_information

NOx_control

SO2_control

combustion_additives Yes Yes No Yes Yes No

Page 21boiler_fuels

facility _id boiler_id fuel_type fuel_year percentage_massvol percentage_btu

other_type 6030 1 coal - lignite 2007 99.99 99.76 6030 1 coal - lignite 2008 99.98 99.59 6030 1 coal - lignite 2009 99.99 99.83 6030 1 oil - distillate 2007 0.01 0.24 6030 1 oil - distillate 2008 0.02 0.41 6030 1 oil - distillate 2009 0.01 0.17 6030 2 coal - lignite 2007 99.98 99.49 6030 2 coal - lignite 2008 99.98 99.65 6030 2 coal - lignite 2009 99.98 99.57 6030 2 oil - distillate 2007 0.02 0.51 6030 2 oil - distillate 2008 0.02 0.35 6030 2 oil - distillate 2009 0.02 0.43

Page 22boiler_control_NOx

facility _id boiler_id NOx_type NOx_other NOx_online 6030 1 Advanced Overfire Air 6/1/1998 6030 2 Advanced Overfire Air 6/1/2007

Page 23boiler_control_SO2

facility _id boiler_id SO2_type SO2_other SO2_online 6030 1 Other (specify) Dry Fining 12/1/2009 6030 2 Other (specify) Dry Fining 12/1/2009

Page 24boiler_additives

facility _id boiler_id boiler_additive additive_other

additive_online

Page 25facility _units facility _id unit_id 6030 1 6030 2

Page 26unit_boilers

facility _id unit_id boiler_id 6030 1 1 6030 2 2

Page 27facility _controls facility _id control_id control_group control_type

control_other

legacy _control cntrol_online

control_offline

NOx_reagent 6030 Unit 1 ESP PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 8/1/1979 6030 Unit 1FGD SO2 control Spray type FALSE 8/1/1979 6030 Unit 2 ESP PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 7/1/1981 6030 Unit 2 FGD SO2 control Spray type FALSE 7/1/1981

Page 28facility _controls reagent_other

NOx_ammonia

SO2_sorbent

oher_sorbent

SO2_scrubber_additive Other (specify)

Lim e/Dolom itic Lim e

No Other (specify)

Lim e/Dolom itic Lim e

No

Page 29facility _sampling_ports facility _id sampling_port_id 6030 U1 1 FGD Out 6030 U1 FGD In 6030 U1 Stack SP 6030 U2 Stack SP 6030 Unit 1 AH In

Page 30facility _stacks facility _id stack_id stack_height stack_diameter

sack_gas_velocity 6030 1stack 675 25.75 55 6030 2 stack 653 29 55

Page 31configurations

facility _id configuration_id 6030 Unit 1b 6030 Unit 2b

Page 32configuration_components

facility _id configuration_id

component_id

order component_type port_near 6030 Unit 1b 1 1 Unit 6030 Unit 1b 1stack 8 Stack 6030 Unit 1b U1 1 FGD Out 6 Sam pling Port pevious 6030 Unit 1b U1 FGD In 4 Sam pling Port next 6030 Unit 1b U1 Stack SP 7 Sam pling Port next 6030 Unit 1b Unit 1 AH In 2 Sam pling Port pevious 6030 Unit 1b Unit 1 ESP 3 PM control 6030 Unit 1b Unit 1FGD 5 SO2 control 6030 Unit 2b 2 1 Unit 6030 Unit 2b 2 stack 5 Stack 6030 Unit 2b U2 Stack SP 4 Sam pling Port next 6030 Unit 2b Unit 2 ESP 2 PM control 6030 Unit 2b Unit 2 FGD 3 SO2 control

Page 33configuration_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 6030 Unit 1b Nitrogen Oxide (NOx) State - State Operating Permit

5104 pound per hour (lb/hr) 0.4 pound per million British Thermal Unit (lb/MMBtu) 6030 Unit 1b Sulfur Dioxide (SO2) State - State Operating Permit

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

3 hours 6336 pound per hour (lb/hr) 6030 Unit 1b Total Suspended Particulates (TSP) State - State Operating Permit

528 pound per hour (lb/hr)

3 hours 0.1 pound per million British Thermal Unit (lb/MMBtu) 6030 Unit 2b Total Suspended Particulates (TSP) State - State Operating Permit

528 hours per day

(hr/day) 3 hours 0.1 pound per million British Thermal Unit (lb/MMBtu) 6030 Unit 2b Sulfur Dioxide (SO2) State - State Operating Permit

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

3 hours 6336 pound per hour (lb/hr) 6030 Unit 2b Nitrogen Oxide (NOx) State - State Operating Permit

5104 pound per hour (lb/hr) 0.4 pound per million British Thermal Unit (lb/MMBtu)

Page 34configuration_pollutants1

avg_period_2

em lim it_3 em lim it_units_3 avg_period_3

em lim it_4 em lim it_units_4 avg_period_4

em lim it_details

test_method pound per million British Thermal Unit (lb/MMBtu) Nox annual compliance

3 hours 3 hours 3 hours 3 hours pound per million British Thermal Unit (lb/MMBtu) Annual compliance on both limits

Page 35configuration_pollutants1

em rate em rate_units guarantee_level

_explain

req_monitoring

eq_recordkeeping

req_reporting 0.35 pound per million British Thermal Unit (lb/MMBtu)

No Continuous Emission Monitoring CEMS Data

Quarterly

Excess EmissionSemi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emmission Inventory Quarterly EDR 6043 pound per hour (lb/hr)

No Continuous Emission Monitoring CEMS Data

Quarterly

Excess EmissionSemi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emmission Inventory Quarterly EDR 198 pound per hour (lb/hr)

No Compliance Assurance Monitoring (CAM)Emission Testing CAM DataEm ission Test Data

Sem i-Annual Monitoring ReportAnnual Com pliance CertificationAnnual Emissions Inventory 198 pound per hour (lb/hr)

No Complaince Assurance Monitoring (CAM)Emission Testing CAM DataEm ission Test Data

Sem i-Annual MonitoringAnnual Com pliance CertificationAnnual Emission Inventory 6043 pound per hour (lb/hr)

No Continuous Emission Monitoring CEMS Data

Quarterly

Excess EmissionSemi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emission MonitoringQuarterly EDR 0.17 pound per million British Thermal Unit (lb/MMBtu)

No Continuous Emission Monitoring CEMS Data

Quarterly

Excess Emission Semi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emission Inventory Quarterly EDR

Page 36configuration_pollutants1 Quarterly

Excess EmissionSemi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emmission Inventory Quarterly EDR Quarterly

Excess EmissionSemi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emmission Inventory Quarterly EDR Sem i-Annual Monitoring ReportAnnual Com pliance CertificationAnnual Emissions Inventory Sem i-Annual MonitoringAnnual Com pliance CertificationAnnual Emission Inventory Quarterly

Excess EmissionSemi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emission MonitoringQuarterly EDR Quarterly

Excess Emission Semi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emission Inventory Quarterly EDR

Page 37configuration_pollutants1 Quarterly

Excess EmissionSemi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emmission Inventory Quarterly EDR Quarterly

Excess EmissionSemi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emmission Inventory Quarterly EDR Quarterly

Excess EmissionSemi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emission MonitoringQuarterly EDR Quarterly

Excess Emission Semi-Annual Monitoring ReportAnnual Compliance CertificationAnnual Emission Inventory Quarterly EDR

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

Page 47mi sc_control_configurations

facility _id mi sc_control_id

configuration_id

Page 48fuel_shipments

facility _id shipment_id

shipment_date

am ount_received

am ount_units

fuel_type state_country other_country

county 6030 01 1/1/2009 432693 short tons (2000 lbs) coal ND ND - McLean 6030 02 2/1/2009 379876 short tons (2000 lbs) coal ND ND - McLean 6030 03 3/1/2009 449611 short tons (2000 lbs) coal ND ND - McLean 6030 04 4/1/2009 422477 short tons (2000 lbs) coal ND ND - McLean 6030 05 5/1/2009 298802 short tons (2000 lbs) coal ND ND - McLean 6030 06 6/1/2009 433170 short tons (2000 lbs) coal ND ND - McLean 6030 07 7/1/2009 445632 short tons (2000 lbs) coal ND ND - McLean 6030 08 8/1/2009 446058 coal ND ND - McLean 6030 09 9/1/2009 415138 short tons (2000 lbs) coal ND ND - McLean 6030 10 10/1/2009 445666 short tons (2000 lbs) coal ND ND - McLean 6030 11 11/1/2009 440794 short tons (2000 lbs) coal ND ND - McLean 6030 12 12/1/2009 446949 short tons (2000 lbs) coal ND ND - McLean

Page 49fuel_shipments

coal_seam shipment_method ND - McLean Conveyor ND - McLean Conveyor ND - McLean Conveyor ND - McLean Conveyor ND - McLean Conveyor ND - McLean Conveyor ND - McLean Conveyor ND - McLean Conveyor ND - McLean Conveyor ND - McLean Conveyor ND - McLean Conveyor ND - McLean Conveyor

Page 50fuel_shipment_configurations

facility _id shipment_id

configuration_id 6030 01 Unit 1b 6030 01 Unit 2b 6030 02 Unit 1b 6030 03 Unit 1b 6030 04 Unit 1b 6030 05 Unit 1b 6030 06 Unit 1b 6030 07 Unit 1b 6030 08 Unit 1b 6030 09 Unit 1b 6030 10 Unit 1b 6030 11 Unit 1b 6030 12 Unit 1b

Page 51fuel_shipment_samples

facility _id shipment_id

sample_id am ount_fuel am ount_fuel_units

total_sulfur ash_content heating_value

hating_units 6030 01 01 432693 tons 0.99 16.6 10049 6030 02 02 379876 tons 1.02 17.17 9994 Btu/lb 6030 03 03 449611 tons 1.1 17.67 9989 Btu/lb 6030 04 04 422477 tons 1.07 16.73 10026 Btu/lb 6030 05 05 298802 tons 1.03 17.25 9936 Btu/lb 6030 06 06 433170 tons 1.08 18.21 9813 Btu/lb 6030 07 07 445632 tons 1.14 18.21 9640 Btu/lb 6030 08 08 446058 tons 1.05 17.95 9789 Btu/lb 6030 09 09 415138 tons 1.07 18.63 9767 Btu/lb 6030 10 10 445666 tons 1.08 17.02 9976 Btu/lb 6030 11 11 440794 tons 1.08 17.69 9925 Btu/lb 6030 12 12 446949 tons 1.12 19.17 9753 Btu/lb

Page 52fuel_shipment_samples

chlorine chlorine_units fluorine fluorine_units data_provided

data_other_specified

supplier_type

supplier_name

supplier_address standard operational procedures Other standard operational procedures Other standard operational procedures Other standard operational procedures Other standard operational procedures Other standard operational procedures Other standard operational procedures Other standard operational procedures Other standard operational procedures Other standard operational procedures Other standard operational procedures Other standard operational procedures Other

Page 53fuel_shipment_samples

supplier_city

supplier_state

supplier_zip

lab_nam e lab_address lab_city lab_state lab_zip analysis_copies Coal Creek Station Laboratory

2875 3rd St. SW

Underwood ND 58576 No Coal Creek Station Laboratory

2875 3rd St. SW

Underwood NC 58576 No Coal Creek Station Laboratory

2875 3rd St SW

Underwood ND 58576 No Coal Creek Station laboratory

2875 3rd St. SW

Underwood ND 58576 No Coal Creek Station Laboratory

2875 3rd St. SW

Underwood ND 58576 No Coal Creek Station Laboratory

2875 3rd St. SW

Underwood ND 58576 No Coal Creek Station laboratory

2875 3rd St. SW

Underwood ND 58576 No Coal Creek Station laboratory

2875 3rd St. SW

Underwood ND 58576 No Coal Creek Station Laboratory

2875 3rd St. SW

Underwood NC 58576 No Coal Creek Station Laboratory

2875 3rd St. SW

Underwood ND 58576 No Coal Creek Station Laboratory

2875 3rd St. SW

Underwood ND 58576 No Coal Creek Station laboraotry

2875 3rd St. SW

Underwood ND 58576 No

Page 54fuel_shipment_samples analysis_copies

Page 55fuel_sample_pollutants

facility _id shipment_id

sample_id fuel_pollutant pollutant_conc

pollutant_conc_units

pollutant_conc_ND

pollutant_conc_MDL 6030 01 01 Mercury (Hg) 0.085 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 02 02 Mercury (Hg) 0.097 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 03 03 Mercury (Hg) 0.0946 mi lligram per kilogram (dry) (mg/kg) TRUE 6030 04 04 Mercury (Hg) 0.0935 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 05 05 Mercury (Hg) 0.1025 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 06 06 Mercury (Hg) 0.084 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 07 07 Mercury (Hg) 0.096 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 08 08 Mercury (Hg) 0.0976 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 09 09 Mercury (Hg) 0.102 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 10 10 Mercury (Hg) 0.099 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 11 11 Mercury (Hg) 0.0946 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 12 12 Mercury (Hg) 0.099 mi lligram per kilogram (dry) (mg/kg) FALSE

Page 56test_reports

facility _id report_id report_type other_type report_description report_begin_date

report_end_date

before_control

during_deviation 6030 DryFining Baseline\01

other Mercury and metals testing was performed on run of mine lignite prior to installing coal drying system. 9/16/2009 9/17/2009 Yes No

Page 57test_reports

deviation_reports No

Page 58test_report_configurations

facility _id report_id configuration_id 6030 DryFining Baseline\01

Unit 1b

Page 59test_report_fuels

facility _id report_id fuel_id 6030 DryFining Baseline\01

Run of Mine Lignite

Page 60test_report_fuel_types

facility _id report_id fuel_id fuel_type percentage_massvol percentage_btu

other_type 6030 DryFining Baseline\01

Run of Mine Lignite

coal - lignite 100 100

Page 61cem_data

facility _id tim e_period

cem_period_description 6030 9/16/2009 through 9/17/2009

Som e hours of mercury data at air heater inlet and FDG inlet and FGD outlet. EPA was contacted and due to the short duration of the CEMS data EPA responded that this data did not need to be submitted.

Page 62cem_data
Som e hours of mercury data at air heater inlet and FDG inlet and FGD outlet. EPA was contacted and due to the short duration of the CEMS data EPA responded that this data did not need to be submitted.

Page 63cem_data
Som e hours of mercury data at air heater inlet and FDG inlet and FGD outlet. EPA was contacted and due to the short duration of the CEMS data EPA responded that this data did not need to be submitted.

Page 64cem_data_pollutants1

facility _id tim e_period

pollutant_nam e 6030 9/16/2009 through 9/17/2009

Elem ental Mercury

(Hg0) 6030 9/16/2009 through 9/17/2009

Total Mercury

(Hgt)

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 6030 DryFining Baseline\01

1stack No No 6030 DryFining Baseline\01

U1 1 FGD Out

No No 6030 DryFining Baseline\01

U1 FGD In No Yes B 75 70 6030 DryFining Baseline\01

Unit 1 AH In Air Heater Inlet Sample Yes B 75 70

Page 66test_report_sampling

fg_fraction 100% gas flow 25% testing perfomred on absorber outlet duct - scrubber has 4 absorbers Flue Gas split into two ducts - sample represents one duct 50% 50% flow two air heaters per unit

Page 67sampling_runs

facility _id report_id sampling_port_id run_id start_datetime end_datetim e

unit_load net_generation fg_moisture_content 6030 DryFining Baseline\01

1stack average 9/17/2009 9/17/2009 600 559 17.42 6030 DryFining Baseline\01

U1 1 FGD Out

average 9/16/2009 9/17/2009 600 559 17.42 6030 DryFining Baseline\01

U1 FGD In average 9/16/2009 9/17/2009 600 559 17.42 6030 DryFining Baseline\01

Unit 1 AH In

average 9/16/2009 9/17/2009 600 559 17.42

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 1250618 dscfm 4.49 9.7 187 1250618 dscfm 4.49 9.7 138 1250618 dscfm 4.49 9.7 1250618 dscfm 4.49 9.7

Page 69sampling_runs

fg_pressure

Hg_loi test_method run_comments

fuel_id fuel_unit_load fuel_flow_rate

fuel_ash fuel_heating_value 27.64 M29 for metalsSorbent trap for Hg

Hg - CEMSTrace Metals M29

Load and Operating Conditions were held constant during the individual 3 hour test periods - Values are average of tests

Run of Mine Lignite

600 592895 16.54 10008 FGD Inlet temp 327 Air Heater Inlet Temp 2166 Degrees F

Page 70sampling_runs

fuel_sulfur 0.91

Page 71sampling_run_pollutants1

facility _id report_id sampling_port_id run_id pollutant_nam e conc conc_units conc_ND conc_MDL 6030 DryFining Baseline\01

U1 1 FGD Out

average Total Mercury (Hgt) 13.1 mi crogram per normal cubic meter (

FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Elem ental Mercury (Hg0) 12.31 mi crogram per normal cubic meter (

FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Oxidized Mercury (Hg++) 5 percent concentration (%)

FALSE 6030 DryFining Baseline\01

Unit 1 AH In

average Total Mercury (Hgt) 19.18 mi crogram per normal cubic meter (

FALSE 6030 DryFining Baseline\01

Unit 1 AH In

average Elem ental Mercury (Hg0) 17.98 mi crogram per normal cubic meter (

FALSE 6030 DryFining Baseline\01

Unit 1 AH In

average Oxidized Mercury (Hg++) 23 percent concentration (%)

FALSE 6030 DryFining Baseline\01

U1 FGD In average Total Mercury (Hgt) 15.99 mi crogram per normal cubic meter (

FALSE 6030 DryFining Baseline\01

U1 FGD In average Elem ental Mercury (Hg0) 11.61 mi crogram per normal cubic meter (

FALSE 6030 DryFining Baseline\01

U1 FGD In average Oxidized Mercury (Hg++) 28 percent concentration (%)

FALSE 6030 DryFining Baseline\01

1stack average Arsenic (As) FALSE 6030 DryFining Baseline\01

1stack average Barium (Ba) FALSE 6030 DryFining Baseline\01

1stack average Beryllium (Be) FALSE 6030 DryFining Baseline\01

1stack average Cadmium (Cd) FALSE 6030 DryFining Baseline\01

1stack average Cobalt (Co) FALSE 6030 DryFining Baseline\01

1stack average Chromium (Cr) FALSE 6030 DryFining Baseline\01

1stack average Copper (Cu) FALSE 6030 DryFining Baseline\01

1stack average Manganese (Mn) FALSE 6030 DryFining Baseline\01

1stack average Nickel (Ni) FALSE 6030 DryFining Baseline\01

1stack average Lead (Pb) FALSE 6030 DryFining Baseline\01

1stack average Antim ony (Sb) FALSE 6030 DryFining Baseline\01

1stack average Vanadium (V) FALSE 6030 DryFining Baseline\01

1stack average Total Mercury (Hgt) 11.8 mi crogram per dry standard cubic meter ( 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 FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE 1.9 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 99.8% coal to stack reduction FALSE 241.6 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 99.7% coal to stack reduction FALSE 0.1 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 99.9% coal to stack reduction FALSE 0.2 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 99.7% coal to stack reduction FALSE 0.9 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 99.8% coal to stack reduction FALSE 5.4 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 99.5% coal to stack reduction FALSE 2.9 pound per trillion British Thermal Unit (lb/1012Btu) FALSE FALSE 14.5 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 99.8% reduction coal to stack FALSE 6.6 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 99.4% coal to stack reduction FALSE 5.1 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 98.9 % coal to stack reduction FALSE 0.4 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 99.5% coal to stack reduction FALSE 6.2 pound per trillion British Thermal Unit (lb/1012Btu) FALSE 99.7% coal to stack reduction FALSE FALSE Value at 3% Oxygen

Page 73sampling_run_pollutants1 run_pollutant_comment

99.8% coal to stack reduction 99.7% coal to stack reduction 99.9% coal to stack reduction 99.7% coal to stack reduction 99.8% coal to stack reduction 99.5% coal to stack reduction 99.8% reduction coal to stack 99.4% coal to stack reduction 98.9 % coal to stack reduction 99.5% coal to stack reduction 99.7% coal to stack reduction Value at 3% Oxygen

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 6030 DryFining Baseline\01

U1 1 FGD Out

average Antim ony

(Sb) 0.847 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Arsenic (As) 11.9 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Barium (Ba) 691 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Beryllium (Be) 1.09 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Cadmium (Cd) 0.116 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Chromium (Cr) 9.88 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Cobalt (Co) 3.667 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Copper (Cu) 9.5 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Lead (Pb) 4.5 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Manganese (Mn) 81.3 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Mercury

(Hg) 0.109 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Molybdenum (Mo) 2.74 mi lligram per kilogram (dry) (mg/kg)

FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Nickel (Ni) 11.6 mi lligram per kilogram (dry) (mg/kg) FALSE 6030 DryFining Baseline\01

U1 1 FGD Out

average Selenium (Se) parts per million (dry) (ppm) TRUE 0.811 6030 DryFining Baseline\01

U1 1 FGD Out

average Vanadium (V) 19.9 mi lligram per kilogram (dry) (mg/kg) FALSE

Page 75sampling_run_fuel fuel_conc_MDL

Page 76