Facility _Information facility _id utility

_code legal_owner_nam e

legl_operator_name

legal_address_type

legal_address

legal_city legal_state legal_zip 6077 13337 Nebraska Public Power District Nebraska Public Power District

legal owner1414 15th Street Colum bus NE 68601

Page 1Facility _Information plant_nam e

physical_address

phyical_city

physical_state

physical_zip

mailing_address

mailing_city

mailing_state

mailing_zip Gerald Gentleman

6089 South Highway

25 Sutherland NE 69165 PO Box 68 Sutherland NE 69165

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 None No Under Part I Facility and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 4Facility _Information Under Part I Facility

and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 5Facility _Information Under Part I Facility

and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 6Facility _Information Under Part I Facility

and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 7Facility _Information Under Part I Facility

and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 8Facility _Information Under Part I Facility

and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 9Facility _Information Under Part I Facility

and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 10Facility _Information Under Part I Facility

and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 11Facility _Information Under Part I Facility

and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 12Facility _Information Under Part I Facility

and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 13Facility _Information Under Part I Facility

and Fuel Information/Fuel Information Continued. This facility is permitted to burn oil but none was utilized during the 12 months prior to receiving this ICR. Thus this field was left blank.2 - Under Part I Boiler Information/Boiler Information the design steam temperature and design steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.1 - Under Part I Boiler Information/Boiler Information the operating steam temperature and operating steam reheat temperature for both Unit's 1 and 2 is 1005 Deg. F.3 - Under Part I Boiler Information/Boiler Information the present operating efficiency is not calculated on either Unit 1 or 2 due to not performing an analysis of the coal as it enters the boiler. Thus we do not know the HHV of the coal being fired and cannot calculate efficiency.Under Part I Boiler Information/Boiler Information the operating steam pressure for both Unit's 1 and 2 is the 2009 hourly average throttle pressure for hourly average loads greater than 5

Page 14facility _contacts facility _id contact_id contact_title contact_name

contact_phone1

contact_phone2

contact_email

contact_primary 6077 1 Corporate Environmental Manager Joe Citta, Jr.

4025635355 jlcitta@nppd.com TRUE

Page 15facility _coal_utilized facility _id coal_type percentage_mass percentage_btu

synfuel_type

coal_note 6077 subbituminous 100 100

Page 16facility _oil_utilized facility _id oil_type percentage_volume percentage_btu

other_type

Page 17facility _other_materials facility _id other_material

permitted_burn

actually _burn other_quantity

other_quantity

_units other_note rcra_utilize rcra_explain

Page 18facility _other_materials rcra_explain

Page 19boiler_information

facility _id boiler_id boiler_type boiler_other bottom_design

design_fuelheat_input max_heat_input MWe_capacity 6077 1 Wall firing - opposed firing Dry Bottom coal 7538 7538 715 6077 2 Wall firing - opposed firing Dry Bottom coal 7538 7538 750

Page 20boiler_information

MWe_net_capacity

design_gross_efficiency

operating_gross_efficiency

design_pressure

operating_pressure

design_temp

operating_temp

design_reheat_multiple

design_reheat_temp1 665 85.17 3 2620 2420 2 1 FALSE 2 700 85.35 3 2620 2360 2 1 FALSE 2

Page 21boiler_information

design_reheat_temp2

operating_reheat_multiple

operating_reheat_temp1

operating_reheat_temp2

hours_operated

vg_capacity

_factor applicable_NSPS

retirement_year

retirement_year_CBI FALSE 1 8081 87 Subpart D FALSE FALSE 1 8237 88.1 Subpart D FALSE

Page 22boiler_information

NOx_control

SO2_control

combustion_additives Yes Yes No Yes Yes No

Page 23boiler_fuels

facility _id boiler_id fuel_type fuel_year percentage_massvol percentage_btu

other_type 6077 1 coal - subbituminous 2007 0 0 6077 1 coal - subbituminous 2008 0 0 6077 1 coal - subbituminous 2009 0 0 6077 1 natural gas 2007 0 0 6077 1 natural gas 2008 0 0 6077 1 natural gas 2009 0 0 6077 2 coal - subbituminous 2007 0 0 6077 2 coal - subbituminous 2008 0 0 6077 2 coal - subbituminous 2009 0 0 6077 2 natural gas 2007 0 0 6077 2 natural gas 2008 0 0 6077 2 natural gas 2009 0 0

Page 24boiler_control_NOx

facility _id boiler_id NOx_type NOx_other NOx_online 6077 1 Low NOx Burner 5/1/2006 6077 1 Overfire Air 5/1/2006 6077 2 Low NOx Burner 7/1/1981

Page 25boiler_control_SO2

facility _id boiler_id SO2_type SO2_other SO2_online 6077 1 Low Sulfur Coal 2/1/1979 6077 2 Low Sulfur Coal 7/1/1981

Page 26boiler_additives

facility _id boiler_id boiler_additive additive_other

additive_online

Page 27facility _units facility _id unit_id 6077 1 6077 2

Page 28unit_boilers

facility _id unit_id boiler_id 6077 1 1 6077 2 2

Page 29facility _controls facility _id control_id control_group control_type

control_other

legacy _control cntrol_online

control_offline

NOx_reagent 6077 BH1 PM control Fabric Filter, reverse air FALSE 12/1/2000 6077 BH2 PM control Fabric Filter, reverse air FALSE 5/1/2001

Page 30facility _controls reagent_other

NOx_ammonia

SO2_sorbent

oher_sorbent

SO2_scrubber_additive

Page 31facility _sampling_ports facility _id sampling_port_id 6077 GGS1DILU 6077 GGS1FLOW 6077 GGS1HG 6077 GGS1OPAC 6077 GGS2DILU 6077 GGS2FLOW 6077 GGS2HG 6077 GGS2OPAC 6077 SP1E 6077 SP1N 6077 SP1S 6077 SP1W 6077 SP2E 6077 SP2N 6077 SP2S 6077 SP2W

Page 32facility _stacks facility _id stack_id stack_height stack_diameter

sack_gas_velocity 6077 Stack1 553 27.8 77 6077 Stack2 550 28 77

Page 33configurations

facility _id configuration_id 6077 U1 6077 U2

Page 34configuration_components

facility _id configuration_id

component_id

order component_type port_near 6077 U1 1 1 Unit 6077 U1 BH1 2 PM control 6077 U1 GGS1DILU 7 Sam pling Port next 6077 U1 GGS1FLOW 8 Sam pling Port next 6077 U1 GGS1HG 9 Sam pling Port next 6077 U1 GGS1OPAC 10 Sam pling Port next 6077 U1 SP1E 6 Sam pling Port next 6077 U1 SP1N 3 Sam pling Port next 6077 U1 SP1S 5 Sam pling Port next 6077 U1 SP1W 4 Sam pling Port next 6077 U1 Stack1 11 Stack 6077 U2 2 1 Unit 6077 U2 BH2 2 PM control 6077 U2 GGS2DILU 7 Sam pling Port next 6077 U2 GGS2FLOW 8 Sam pling Port next 6077 U2 GGS2HG 9 Sam pling Port next 6077 U2 GGS2OPAC 10 Sam pling Port next 6077 U2 SP2E 6 Sam pling Port next 6077 U2 SP2N 3 Sam pling Port next 6077 U2 SP2S 5 Sam pling Port next 6077 U2 SP2W 4 Sam pling Port next 6077 U2 Stack2 11 Stack

Page 35configuration_pollutants1

facility _id configuration_id

pollutant_nam e

permit_type_1

em lim it_1 em lim it_units_1 avg_period_1

em lim it_2 em lim it_units_2 6077 U1 Nitrogen Oxide (NOx) Federal - Title V Operating Permit

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

3 hours 0.46 pound per million British Thermal Unit (lb/MMBtu) 6077 U1 Sulfur Dioxide (SO2) Federal - Title V Operating Permit

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

3 hours 6077 U1 Carbon Monoxide (CO) State - Permit to Contruct

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

30 days 6077 U2 Nitrogen Oxide (NOx) Federal - Title V Operating Permit

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

3 hours 0.46 pound per million British Thermal Unit (lb/MMBtu) 6077 U2 Sulfur Dioxide (SO2) Federal - Title V Operating Permit

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

3 hours 6077 U1 PM (Filterable) Fderal - Title V Operating Permit

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

3 hours 6077 U2 PM (Filterable) Fderal - Title V Operating Permit

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

3 hours

Page 36configuration_pollutants1

avg_period_2

em lim it_details

test_method

em rate em rate_units guarantee_level

_explain

req_monitoring

eq_recordkeeping pound per million British Thermal Unit (lb/MMBtu) As per Class I Acid Rain Operating Permit standard annual average emission limitation of 0.46 lb/mmBtu 0 pound per million British Thermal Unit (lb/MMBtu)

No No Guaranteed Emission Rates Continuous Emssions Monitoring System per 40 CFR Part 75

Per 40 CFR Part 60.7(b), 60.7(f), and 60.13(h) and 40 CFR Part 75 0 pound per million British Thermal Unit (lb/MMBtu)

No No Guaranteed Emission Rates Continuous Emssions Monitoring System per 40 CFR Part 75

Per 40 CFR Part 60.7(b), 60.7(f), and 60.13(h) and 40 CFR Part 75 0 pound per million British Thermal Unit (lb/MMBtu)

No No Guaranteed Emission Rates Continuous Emssions Monitoring System per 40 CFR Part 60

Per 40 CFR Part 60.7(f) pound per million British Thermal Unit (lb/MMBtu) As per Class I Acid Rain Operating Permit standard annual average emission limitation of 0.46 lb/mmBtu 0 pound per million British Thermal Unit (lb/MMBtu)

No No Guaranteed Emission Rates Continuous Emissions Monitoring System per 40 CFR Part 75

Per 40 CFR Part 60.7(b), 60.7(f),and 60.13(h) and 40 CFR Part 75 0 pound per million British Thermal Unit (lb/MMBtu)

No No Guaranteed Emission Rates Continuous Emissions Monitoring System per 40 CFR Part 75

Per 40 CFR Part 60.7(b), 60.7(f), and 60.13(h) and 40 CFR Part 75 calculated heat input from unit max heat input

calculated heat input0 pound per million British Thermal Unit (lb/MMBtu) No No Guaranteed Emission Rates COMS and Operational Data per State Title V Operating Permit

Per 40 CFR Part 60.7(b) and 60.7(f) calculated heat input from unit max heat input

calculated heat input0 pound per million British Thermal Unit (lb/MMBtu) No No Guaranteed Emission Rates COMS and Operational Data per State Title V Operating Permit

Per 40 CFR Part 60.7(b) and 60.7(f)

Page 37configuration_pollutants1

req_reporting Per 40 CFR Part 60.4, 60.7(a)(4), 60.7(c), 60.7(d), 60.8(c), 60.8(d), and 60.45(g) and 40 CFR Part 75 Per 40 CFR Part 60.4, 60.7(a)(4), 60.7(c), 60.7(d), 60.8(c), 60.8(d), and 60.45(g) and 40 CFR Part 75 Within 30 days of an exceedance. Per 40 CFR Part 60.4, 60.7(a)(4), 60.7(c), 60.7(d), 60.8(c), 60.8(d), and 60.45(g) and 40 CFR Part 75 Per 40 CFR Part 60.4, 60.7(a)(4), 60.7(c), 60.7(d), 60.8(c), 60.8(d), and 60.45(g) and 40 CFR Part 75 Per State Title V Operating Permit Per State Title V Operating Permit

Page 38control_technologies

facility _id configuration_id

component_id

control_id project_titleproject_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 46misc_controls

facility _id misc_control_id

control_description

Page 47misc_control_configurations

facility _id misc_control_id

configuration_id

Page 48fuel_shipments

facility _id shipment_id

shipment_date

amount_received

amount_units

fuel_type state_country other_country

county 6077 APR_CA 4/1/2009 317886 short tons (2000 lbs) coal WY WY - Campbell 6077 APR_CO 4/1/2009 12648 short tons (2000 lbs) coal WY WY - Converse 6077 AUG_CA 8/1/2009 338917 short tons (2000 lbs) coal WY WY - Campbell 6077 DEC_CA 12/1/2009 386183 short tons (2000 lbs) coal WY WY - Campbell 6077 FEB_CA 2/1/2009 327496 short tons (2000 lbs) coal WY WY - Campbell 6077 FEB_CO 2/1/2009 12637 short tons (2000 lbs) coal WY WY - Converse 6077 JAN_CA 1/1/2009 296698 short tons (2000 lbs) coal WY WY - Campbell 6077 JAN_CO 1/1/2009 42430 short tons (2000 lbs) coal WY WY - Converse 6077 JUL_CA 7/1/2009 338745 short tons (2000 lbs) coal WY WY - Campbell 6077 JUN_CA 6/1/2009 298435 short tons (2000 lbs) coal WY WY - Campbell 6077 JUN_CO 6/1/2009 12606 short tons (2000 lbs) coal WY WY - Converse 6077 MAR_CA 3/1/2009 307661 short tons (2000 lbs) coal WY WY - Campbell 6077 MAR_CO 3/1/2009 24982 short tons (2000 lbs) coal WY WY - Converse 6077 MAY_CA 5/1/2009 288093 short tons (2000 lbs) coal WY WY - Campbell 6077 NOV_CA 11/1/2009 361970 short tons (2000 lbs) coal WY WY - Campbell 6077 OCT_CA 10/1/2009 360666 short tons (2000 lbs) coal WY WY - Campbell 6077 SEP_CA 9/1/2009 319258 short tons (2000 lbs) coal WY WY - Campbell

Page 49fuel_shipments

coal_seam shipment_method WY - Campbell Unit Train WY - Converse Unit Train WY - Campbell Unit Train WY - Campbell Unit Train WY - Campbell Unit Train WY - Converse Unit Train WY - Campbell Unit Train WY - Converse Unit Train WY - Campbell Unit Train WY - Campbell Unit Train WY - Converse Unit Train WY - Campbell Unit Train WY - Converse Unit Train WY - Campbell Unit Train WY - Campbell Unit Train WY - Campbell Unit Train WY - Campbell Unit Train

Page 50fuel_shipment_configurations

facility _id shipment_id

configuration_id 6077 APR_CA U1 6077 APR_CA U2 6077 APR_CO U1 6077 APR_CO U2 6077 AUG_CA U1 6077 AUG_CA U2 6077 DEC_CA U1 6077 DEC_CA U2 6077 FEB_CA U1 6077 FEB_CA U2 6077 FEB_CO U1 6077 FEB_CO U2 6077 JAN_CA U1 6077 JAN_CA U2 6077 JAN_CO U1 6077 JAN_CO U2 6077 JUL_CA U1 6077 JUL_CA U2 6077 JUN_CA U1 6077 JUN_CA U2 6077 JUN_CO U1 6077 JUN_CO U2 6077 MAR_CA U1 6077 MAR_CA U2 6077 MAR_CO U1 6077 MAR_CO U2 6077 MAY_CA U1 6077 MAY_CA U2 6077 NOV_CA U1 6077 NOV_CA U2 6077 OCT_CA U1 6077 OCT_CA U2 6077 SEP_CA U1 6077 SEP_CA U2

Page 51fuel_shipment_samples

facility _id shipment_id

sample_id amount_fuel amount_fuel_units

total_sulfur ash_content heating_value

hating_units

Page 52fuel_shipment_samples

chlorine chlorine_units fluorine fluorine_units data_provided

data_other_specified

supplier_type

supplier_name

supplier_address

Page 53fuel_shipment_samples

supplier_city

supplier_state

supplier_zip

lab_nam e lab_address lab_city lab_state lab_zip analysis_copies

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

Page 56test_reports

facility _id report_id report_type other_type report_description report_begin_date

report_end_date

before_control

during_deviation 6077 HG_U1_1 other HG Monitor Performance Test Method 30b Mercury

Rata 7/28/2008 7/29/2008 No No 6077 HG_U2_1 other HG Monitor Performance Test Method 30b Mercury

Rata 7/29/2008 7/30/2008 No No

Page 57test_reports

deviation_reports No No

Page 58test_report_configurations

facility _id report_id configuration_id 6077 HG_U1_1 U1 6077 HG_U2_1 U2

Page 59test_report_fuels

facility _id report_id fuel_id 6077 HG_U1_1 U1_Coal 6077 HG_U2_1 U2_coal

Page 60test_report_fuel_types

facility _id report_id fuel_id fuel_type percentage_massvol percentage_btu

other_type 6077 HG_U1_1 U1_Coal coal - subbituminous 100 100 6077 HG_U2_1 U2_coal coal - subbituminous 100 100

Page 61cem_data

facility _id tim e_period

cem_period_description

Page 62cem_data_pollutants1

facility _id tim e_period

pollutant_nam e

Page 63test_report_sampling

facility _id report_id sampling_port_id point_differ point_description befre_SO2_device

point_orientation

normal_bypass_percent

testing_bypass_percent 6077 HG_U1_1 SP1E No No 6077 HG_U2_1 SP2E No No

Page 64test_report_sampling

fg_fraction 100% 100%

Page 65sampling_runs

facility _id report_id sampling_port_id run_id start_datetime end_datetim e

unit_load net_generation fg_moisture_content 6077 HG_U1_1 SP1E 1 7/28/2008 7/28/2008 659 12.6 6077 HG_U1_1 SP1E 10 7/29/2008 7/29/2008 651 12.6 6077 HG_U1_1 SP1E 2 7/28/2008 7/28/2008 659 11.9 6077 HG_U1_1 SP1E 3 7/28/2008 7/28/2008 659 12.2 6077 HG_U1_1 SP1E 4 7/28/2008 7/28/2008 659 12.2 6077 HG_U1_1 SP1E 5 7/28/2008 7/28/2008 657 11.9 6077 HG_U1_1 SP1E 6 7/28/2008 7/28/2008 653 11.9 6077 HG_U1_1 SP1E 7 7/29/2008 7/29/2008 650 12.8 6077 HG_U1_1 SP1E 8 7/29/2008 7/29/2008 653 13 6077 HG_U1_1 SP1E 9 7/29/2008 7/29/2008 654 12.7 6077 HG_U2_1 SP2E 1 7/29/2008 7/29/2008 696 12.3 6077 HG_U2_1 SP2E 10 7/30/2008 7/30/2008 696 11.4 6077 HG_U2_1 SP2E 2 7/30/2008 7/30/2008 701 12.7 6077 HG_U2_1 SP2E 3 7/30/2008 7/30/2008 697 12.3 6077 HG_U2_1 SP2E 4 7/30/2008 7/30/2008 700 12.1 6077 HG_U2_1 SP2E 5 7/30/2008 7/30/2008 702 12 6077 HG_U2_1 SP2E 6 7/30/2008 7/30/2008 703 12.2 6077 HG_U2_1 SP2E 7 7/30/2008 7/30/2008 703 11.5 6077 HG_U2_1 SP2E 8 7/30/2008 7/30/2008 695 12.1 6077 HG_U2_1 SP2E 9 7/30/2008 7/30/2008 698 11.8

Page 66sampling_runs

fg_flow_rate

fg_flow_rate_units

standard_temperature

standard_pressure

normal_temperature

normal_pressure

fg_oxygen_content

fg_CO2_content

fg_temperature

Page 67sampling_runs

fg_pressure

Hg_loi test_method run_comments

fuel_id fuel_unit_load fuel_flow_rate

fuel_ash fuel_heating_value 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b 30b

Page 68sampling_runs

fuel_sulfur

Page 69sampling_run_pollutants1

facility _id report_id sampling_port_id run_id pollutant_nam e conc conc_units conc_ND conc_MDL 6077 HG_U1_1 SP1E 1 Total Mercury (Hgt) 5.5 microgram per dry

standard cubic meter ( FALSE 6077 HG_U1_1 SP1E 2 Total Mercury (Hgt) 6.9 microgram per dry

standard cubic meter ( FALSE 6077 HG_U1_1 SP1E 3 Total Mercury (Hgt) 7.1 microgram per dry

standard cubic meter ( FALSE 6077 HG_U1_1 SP1E 4 Total Mercury (Hgt) 6.8 microgram per dry

standard cubic meter ( FALSE 6077 HG_U1_1 SP1E 5 Total Mercury (Hgt) 7.3 microgram per dry

standard cubic meter ( FALSE 6077 HG_U1_1 SP1E 6 Total Mercury (Hgt) 7.5 microgram per dry

standard cubic meter ( FALSE 6077 HG_U1_1 SP1E 7 Total Mercury (Hgt) 5.8 microgram per dry

standard cubic meter ( FALSE 6077 HG_U1_1 SP1E 8 Total Mercury (Hgt) 6.3 microgram per dry

standard cubic meter ( FALSE 6077 HG_U1_1 SP1E 9 Total Mercury (Hgt) 5.8 microgram per dry

standard cubic meter ( FALSE 6077 HG_U1_1 SP1E 10 Total Mercury (Hgt) 6.8 microgram per dry

standard cubic meter ( FALSE 6077 HG_U2_1 SP2E 1 Total Mercury (Hgt) 7.1 microgram per dry

standard cubic meter ( FALSE 6077 HG_U2_1 SP2E 2 Total Mercury (Hgt) 5.8 microgram per dry

standard cubic meter ( FALSE 6077 HG_U2_1 SP2E 3 Total Mercury (Hgt) 8.5 microgram per dry

standard cubic meter ( FALSE 6077 HG_U2_1 SP2E 4 Total Mercury (Hgt) 8.9 microgram per dry

standard cubic meter ( FALSE 6077 HG_U2_1 SP2E 5 Total Mercury (Hgt) 9.1 microgram per dry

standard cubic meter ( FALSE 6077 HG_U2_1 SP2E 6 Total Mercury (Hgt) 9.2 microgram per dry

standard cubic meter ( FALSE 6077 HG_U2_1 SP2E 7 Total Mercury (Hgt) 8.3 microgram per dry

standard cubic meter ( FALSE 6077 HG_U2_1 SP2E 8 Total Mercury (Hgt) 8.1 microgram per dry

standard cubic meter ( FALSE 6077 HG_U2_1 SP2E 9 Total Mercury (Hgt) 7.7 microgram per dry

standard cubic meter ( FALSE 6077 HG_U2_1 SP2E 10 Total Mercury (Hgt) 7.5 microgram per dry

standard cubic meter ( FALSE

Page 70sampling_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 FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE FALSE

Page 71sampling_run_pollutants1 run_pollutant_comment

Page 72sampling_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 73sampling_run_fuel fuel_conc_MDL

Page 74