Facility _Information facility _id utility

_code legal_owner_nam e

legl_operator_name

legal_address_type

legal_address

legal_city legal_state legal_zip 6055 11252 Louisiana Generating LLC Louisiana Generating LLC

legal owner112 Telly

Street New RoadsLA 70760

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 Big Cajun 210431 Hwy

981 - Cajun 2 Road New RoadsLA 70760 P.O. Box 39 Ventress LA 70783

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 Quarterly, semiannual and annual reporting Yes annual Title V compliance report to EPA; quarterly, semiannual and annual Title V report to Louisiana DEQ No. 2 fuel oil is only

used for startup and flame stabilizationDesign steam pressure value is turbine throttle pressureOperating steam pressure is boiler operating pressure The flue gas temperature at sampling port input would not allow a number above 300F. Here are the temperatures:Flue gas temperature Run 1 was 334FFlue gas temperature Run 2 was 331FFlue gas temperature Run 3 was 327FNo HAPS fuel sampling was conducted during Source Testing for TSP and THC for all three unitsCEM data for opacity from January

2005, and CO CEM data is available back to October 2005

Page 4Facility _Information No. 2 fuel oil is only

used for startup and flame stabilizationDesign steam pressure value is turbine throttle pressureOperating steam pressure is boiler operating pressure The flue gas temperature at sampling port input would not allow a number above 300F. Here are the temperatures:Flue gas temperature Run 1 was 334FFlue gas temperature Run 2 was 331FFlue gas temperature Run 3 was 327FNo HAPS fuel sampling was conducted during Source Testing for TSP and THC for all three unitsCEM data for opacity from January

2005, and CO CEM data is available back to October 2005

Page 5Facility _Information No. 2 fuel oil is only

used for startup and flame stabilizationDesign steam pressure value is turbine throttle pressureOperating steam pressure is boiler operating pressure The flue gas temperature at sampling port input would not allow a number above 300F. Here are the temperatures:Flue gas temperature Run 1 was 334FFlue gas temperature Run 2 was 331FFlue gas temperature Run 3 was 327FNo HAPS fuel sampling was conducted during Source Testing for TSP and THC for all three unitsCEM data for opacity from January

2005, and CO CEM data is available back to October 2005

Page 6Facility _Information No. 2 fuel oil is only

used for startup and flame stabilizationDesign steam pressure value is turbine throttle pressureOperating steam pressure is boiler operating pressure The flue gas temperature at sampling port input would not allow a number above 300F. Here are the temperatures:Flue gas temperature Run 1 was 334FFlue gas temperature Run 2 was 331FFlue gas temperature Run 3 was 327FNo HAPS fuel sampling was conducted during Source Testing for TSP and THC for all three unitsCEM data for opacity from January

2005, and CO CEM data is available back to October 2005

Page 7Facility _Information No. 2 fuel oil is only

used for startup and flame stabilizationDesign steam pressure value is turbine throttle pressureOperating steam pressure is boiler operating pressure The flue gas temperature at sampling port input would not allow a number above 300F. Here are the temperatures:Flue gas temperature Run 1 was 334FFlue gas temperature Run 2 was 331FFlue gas temperature Run 3 was 327FNo HAPS fuel sampling was conducted during Source Testing for TSP and THC for all three unitsCEM data for opacity from January

2005, and CO CEM data is available back to October 2005

Page 8Facility _Information No. 2 fuel oil is only

used for startup and flame stabilizationDesign steam pressure value is turbine throttle pressureOperating steam pressure is boiler operating pressure The flue gas temperature at sampling port input would not allow a number above 300F. Here are the temperatures:Flue gas temperature Run 1 was 334FFlue gas temperature Run 2 was 331FFlue gas temperature Run 3 was 327FNo HAPS fuel sampling was conducted during Source Testing for TSP and THC for all three unitsCEM data for opacity from January

2005, and CO CEM data is available back to October 2005

Page 9Facility _Information No. 2 fuel oil is only

used for startup and flame stabilizationDesign steam pressure value is turbine throttle pressureOperating steam pressure is boiler operating pressure The flue gas temperature at sampling port input would not allow a number above 300F. Here are the temperatures:Flue gas temperature Run 1 was 334FFlue gas temperature Run 2 was 331FFlue gas temperature Run 3 was 327FNo HAPS fuel sampling was conducted during Source Testing for TSP and THC for all three unitsCEM data for opacity from January

2005, and CO CEM data is available back to October 2005

Page 10facility _contacts facility _id contact_id contact_title contact_name

contact_phone1

contact_phone2

contact_email

contact_primary 6055 1 Regional Environm ental Manager Gary Ellender 22563837735625

2256184465

gary.ellender@nrgenergy.com

TRUE 6055 2 Senior Engineer Ash Namjoshi

22563837735695 ash.namjoshi@nrgenergy.com TRUE 6055 3 Plant Manager Abe Burrell 22563837735650 abe.burrell@nrgenergy.com FALSE

Page 11facility _coal_utilized facility _id coal_type percentage_mass percentage_btu

synfuel_type

coal_note 6055 subbituminous 100 100

Page 12facility _oil_utilized facility _id oil_type percentage_volume percentage_btu

other_type 6055 No.2 Fuel Oil (distillate) 100 100

Page 13facility _other_materials facility _id other_material

permitted_burn

actually _burn other_quantity

other_quantity

_units other_note rcra_utilize rcra_explain

Page 14facility _other_materials rcra_explain

Page 15boiler_information

facility _id boiler_id boiler_type boiler_other bottom_design

design_fuel heat_input max_heat_input MW e_capacity 6055 2B1 Wa ll firing - opposed firing Dry Bottom coal 6420 6420 616 6055 2B2 Wa ll firing - opposed firing Dry Bottom coal 6420 6420 611 6055 2B3 Wa ll firing - opposed firing Dry Bottom coal 6420 6420 613

Page 16boiler_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 580 84.51 84.51 2400 2620 1005 1005 FALSE 1005 575 84.51 84.51 2400 2620 1005 1005 FALSE 1005 588 86.39 86.39 2400 2640 1005 1005 FALSE 1005

Page 17boiler_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 7916 82 Subpart D FALSE FALSE 1005 7936 83.4 Subpart D FALSE FALSE 1005 7725 79 Subpart D FALSE

Page 18boiler_information

NOx_control

SO2_control

combustion_additives Yes Yes No Yes Yes No Yes Yes No

Page 19boiler_fuels

facility _id boiler_id fuel_type fuel_year percentage_massvol percentage_btu

other_type 6055 2B1 coal - subbituminous 2007 0 99.9 6055 2B1 coal - subbituminous 2008 0 99.9 6055 2B1 coal - subbituminous 2009 0 99.8 6055 2B1 oil - distillate 2007 0 0.1 6055 2B1 oil - distillate 2008 0 0.1 6055 2B1 oil - distillate 2009 0 0.2 6055 2B2 coal - subbituminous 2007 0 99.9 6055 2B2 coal - subbituminous 2008 0 99.9 6055 2B2 coal - subbituminous 2009 0 99.9 6055 2B2 oil - distillate 2007 0 0.1 6055 2B2 oil - distillate 2008 0 0.1 6055 2B2 oil - distillate 2009 0 0.1 6055 2B3 coal - subbituminous 2007 0 99.8 6055 2B3 coal - subbituminous 2008 0 99.9 6055 2B3 coal - subbituminous 2009 0 99.8 6055 2B3 oil - distillate 2007 0 0.2 6055 2B3 oil - distillate 2008 0 0.1 6055 2B3 oil - distillate 2009 0 0.2

Page 20boiler_control_NOx

facility _id boiler_id NOx_type NOx_other NOx_online 6055 2B1 Low NOx Burner 5/1/2005 6055 2B1 Overfire Air 5/1/2005 6055 2B2 Low NOx Burner 4/1/2004 6055 2B2 Overfire Air 4/1/2004 6055 2B3 Advanced Overfire Air 4/1/2002 6055 2B3 Low NOx Burner 4/1/2002

Page 21boiler_control_SO2

facility _id boiler_id SO2_type SO2_other SO2_online 6055 2B1 Low Sulfur Coal 7/1/1981 6055 2B2 Low Sulfur Coal 7/1/1982 6055 2B3 Low Sulfur Coal 12/1/1983

Page 22boiler_additives

facility _id boiler_id boiler_additive additive_other

additive_online

Page 23facility _units facility _id unit_id 6055 U1 6055 U2 6055 U3

Page 24unit_boilers

facility _id unit_id boiler_id 6055 U1 2B1 6055 U2 2B2 6055 U3 2B3

Page 25facility _controls facility _id control_id control_group control_type

control_other

legacy _control cntrol_online

control_offline

NOx_reagent 6055 2P1 PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 7/1/1981 6055 2P2 PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 7/1/1982 6055 2P3 PM control Electrostatic precipitator, cold side, w/o flue gas conditioning FALSE 4/1/1983

Page 26facility _controls reagent_other

NOx_ammonia

SO2_sorbent

oher_sorbent

SO2_scrubber_additive

Page 27facility _sampling_ports facility _id sampling_port_id 6055 2SP1 6055 2SP2 6055 2SP3

Page 28facility _stacks facility _id stack_id stack_height stack_diameter

sack_gas_velocity 6055 2S1 600 26.5 75 6055 2S2 600 26.5 75 6055 2S3 600 26.5 75

Page 29configurations

facility _id configuration_id 6055 U1 6055 U2 6055 U3

Page 30configuration_components

facility _id configuration_id

component_id

order component_type port_near 6055 U1 2P1 2 PM control 6055 U1 2S1 4 Stack 6055 U1 2SP1 3 Sam pling Port next 6055 U1 U1 1 Unit 6055 U2 2P2 2 PM control 6055 U2 2S2 4 Stack 6055 U2 2SP2 3 Sam pling Port next 6055 U2 U2 1 Unit 6055 U3 2P3 2 PM control 6055 U3 2S3 4 Stack 6055 U3 2SP3 3 Sam pling Port next 6055 U3 U3 1 Unit

Page 31configuration_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 6055 U1 PM (Filterable) State - State Operating Permit

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

3 hours 0.6 pound per million British Thermal Unit (lb/MMBtu) 6055 U1 Sulfur Dioxide (SO2) State - State Operating Permit

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

3 hours 2000 parts per million by volum e (dry) (ppmvd) 6055 U1 Nitrogen Oxide (NOx) State - State Operating Permit

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

30 days 0.7 pound per million British Thermal Unit (lb/MMBtu) 6055 U2 PM (Filterable) State - State Operating Permit

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

3 hours 0.6 pound per million British Thermal Unit (lb/MMBtu) 6055 U2 Sulfur Dioxide (SO2) State - State Operating Permit

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

3 hours 2000 parts per million by volum e (dry) (ppmvd) 6055 U2 Nitrogen Oxide (NOx) State - State Operating Permit

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

30 days 0.7 pound per million British Thermal Unit (lb/MMBtu) 6055 U3 PM (Filterable) State - State Operating Permit

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

3 hours 0.6 pound per million British Thermal Unit (lb/MMBtu) 6055 U3 Sulfur Dioxide (SO2) State - State Operating Permit

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

3 hours 2000 parts per million by volum e (dry) (ppmvd) 6055 U3 Nitrogen Oxide (NOx) State - State Operating Permit

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

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

Page 32configuration_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 3 hours 2812 tons per year (tons/yr) annual Method 5 3 hours 33743.5 tons per year (tons/yr) annual 3 hours 0.46 pound per million British Thermal Unit (lb/MMBtu) annual 0.21 lb/m mBtu applies during ozone season only 3 hours 2812 tons per year (tons/yr) annual Method 5 3 hours 33743.5 tons per year (tons/yr) annual 3 hours 0.46 pound per million British Thermal Unit (lb/MMBtu) annual 0.21 lb/m mBtu applies during ozone season only 3 hours 2568 tons per year (tons/yr) annual Method 5 3 hours 30815.9 tons per year (tons/yr) annual 3 hours 0.46 pound per million British Thermal Unit (lb/MMBtu) annual 0.21 lb/m mBtu applies to ozone season only

Page 33configuration_pollutants1

em rate em rate_units guarantee_level

_explain

req_monitoring

eq_recordkeeping

req_reporting 0.01 No Units are gr/ACF. Original guarantee by ESP vendor None None Calculated for annual emissions inventory 1.2 pound per million British Thermal Unit (lb/MMBtu)

No Guanantee by fuel contract CEM Par 75 quarterly data to EPA CAMD 0.2 pound per million British Thermal Unit (lb/MMBtu)

No Guarantee by boiler vendor CEM Part 75 quarterly data to EPA CAMD 0.01 No Units are gr/ACF. Original guarantee by ESP vendor. None None Calculated for annual emissions inventory 1.2 pound per million British Thermal Unit (lb/MMBtu)

No Guarantee by fuel contract CEM Part 75 quarterlly data to EPA CAMD 0.2 pound per million British Thermal Unit (lb/MMBtu)

No Guarantee by boiler vendor CEM Part 75 quarterly data to EPA CAMD 0.01 No Units are gr/ACF. Original guarantee by ESP vendor. None None Calculated for annual emissions inventory 1.2 pound per million British Thermal Unit (lb/MMBtu)

No Guarantee by fuel contract CEM Part 75 quarterly data to EPA CAMD 0.17 pound per million British Thermal Unit (lb/MMBtu)

No Guarantee by boiler vendor CEM Part 75 quarterly data to EPA CAMD

Page 34configuration_pollutants1 Calculated for annual emissions inventory Calculated for annual emissions inventory Calculated for annual emissions inventory

Page 35control_technologies

facility _id configuration_id

component_id

control_id project_titleproject_type vendor_name

vndor_contact

vendor_phone

Page 36control_technologies

vendor_address

vndor_city

vendor_state

vendor_zip actual_start_date projected_start_date

end_date sorbent chemical_additive

Page 37control_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 38control_technologies feed_rate_units

Page 39control_coal_ranks

facility _id configuration_id

component_id

control_id coal_type

Page 40control_pollutants1

facility _id configuration_id

component_id

control_id pollutant_nam e

Page 41control_costs

facility _id configuration_id

component_id

control_id boiler_retrofit boiler_new_install

total_capital_investm ent

total_operating_costs

base_year

Page 42control_costs

CBI

Page 43misc_controls

facility _id misc_control_id

control_description

Page 44misc_control_configurations

facility _id misc_control_id

configuration_id

Page 45fuel_shipments

facility _id shipment_id

shipment_date

am ount_received

am ount_units

fuel_type state_country other_country

county 6055 April 2009 4/1/2009 849012.8 short tons (2000 lbs) coal WY WY - Campbell 6055 August 2009 8/1/2009 723758.6 short tons (2000 lbs) coal WY WY - Campbell 6055 December 2009

12/1/2009 619016.8 short tons (2000 lbs) coal WY WY - Campbell 6055 February

2009 2/1/2009 845097.8 short tons (2000 lbs) coal WY WY - Campbell 6055 January

20091/1/2009 805070.7 short tons (2000 lbs) coal WY WY - Campbell 6055 July

2009 7/1/2009 787371.8 short tons (2000 lbs) coal WY WY - Campbell 6055 June 2009 6/1/2009 819656 short tons (2000 lbs) coal WY WY - Campbell 6055 March 2009 3/1/2009 863397.3 short tons (2000 lbs) coal WY WY - Campbell 6055 May

2009 5/1/2009 881949.1 short tons (2000 lbs) coal WY WY - Campbell 6055 Novem ber 2009

11/1/2009 639467.3 short tons (2000 lbs) coal WY WY - Campbell 6055 October 2009

10/1/2009 766033.6 short tons (2000 lbs) coal WY WY - Campbell 6055 Septem ber 2009

9/1/2009 492530.9 short tons (2000 lbs) coal WY WY - Campbell

Page 46fuel_shipments

coal_seam shipment_method WY - Campbell Barge WY - Campbell Barge WY - Campbell Barge WY - Campbell Barge WY - Campbell Barge WY - Campbell Barge WY - Campbell Barge WY - Campbell Barge WY - Campbell Barge WY - Campbell Barge WY - Campbell Barge WY - Campbell Barge

Page 47fuel_shipment_configurations

facility _id shipment_id

configuration_id 6055 April 2009 U1 6055 April 2009 U2 6055 April 2009 U3 6055 August 2009

U1 6055 August 2009

U2 6055 August 2009

U3 6055 December 2009

U1 6055 December 2009

U2 6055 December 2009

U3 6055 February

2009 U1 6055 February

2009 U2 6055 February

2009 U3 6055 January

2009 U1 6055 January

2009 U2 6055 January

2009 U3 6055 July

2009 U1 6055 July

2009 U2 6055 July

2009 U3 6055 June 2009 U1 6055 June 2009 U2 6055 June 2009 U3 6055 March 2009

U1 6055 March 2009

U2 6055 March 2009

U3 6055 May

2009 U1 6055 May

2009 U2 6055 May

2009 U3 6055 Novem ber 2009

U1 6055 Novem ber 2009

U2 6055 Novem ber 2009

U3 6055 October 2009

U1 6055 October 2009

U2 6055 October 2009

U3 6055 Septem ber 2009

U1 6055 Septem ber 2009

U2 6055 Septem ber 2009

U3

Page 48fuel_shipment_samples

facility _id shipment_id

sample_id am ount_fuel am ount_fuel_units

total_sulfur ash_content heating_value

hating_units

Page 49fuel_shipment_samples

chlorine chlorine_units fluorine fluorine_units data_provided

data_other_specified

supplier_type

supplier_name

supplier_address

Page 50fuel_shipment_samples

supplier_city

supplier_state

supplier_zip

lab_nam e lab_address lab_city lab_state lab_zip analysis_copies

Page 51fuel_shipment_samples analysis_copies

Page 52fuel_sample_pollutants

facility _id shipment_id

sample_id fuel_pollutant pollutant_conc

pollutant_conc_units

pollutant_conc_ND

pollutant_conc_MDL

Page 53test_reports

facility _id report_id report_type other_type report_description report_begin_date

report_end_date

before_control

during_deviation 6055 Source Emissions Survey Unit 1 compliance Performance test for determining PM and total hydrocarbons at full load 10/3/2005 10/4/2005 No No 6055 Source Emissions Survey Unit 2 compliance Performance test for determining PM and total hydrocarbons at full load 10/4/2005 10/4/2005 No No 6055 Source Emissions Survey Unit 3 compliance Performance test for determining PM and total hydrocarbons at full load 10/4/2005 10/4/2005 No No

Page 54test_reports

deviation_reports No No No

Page 55test_report_configurations

facility _id report_id configuration_id 6055 Source Emissions Survey Unit 1 U1 6055 Source Emissions Survey Unit 2 U2 6055 Source Emissions Survey Unit 3 U3

Page 56test_report_fuels

facility _id report_id fuel_id 6055 Source Emissions Survey Unit 1 coal 6055 Source Emissions Survey Unit 2 coal 6055 Source Emissions Survey Unit 3 coal

Page 57test_report_fuel_types

facility _id report_id fuel_id fuel_type percentage_massvol percentage_btu

other_type 6055 Source Emissions Survey Unit 1 coal coal - subbituminous 100 100 6055 Source Emissions Survey Unit 2 coal coal - subbituminous 100 100 6055 Source Emissions Survey Unit 3 coal coal - subbituminous 100 100

Page 58cem_data

facility _id tim e_period

cem_period_description 6055 01/01/2005-present

Opacity (COMS) data available from 1/1/05 to the present; CO (CEMs) data available from 10/2005 to the present 6055 5 years

Page 59cem_data Opacity (COMS) data available from 1/1/05 to the present; CO (CEMs) data available from 10/2005 to the present

Page 60cem_data_pollutants1

facility _id tim e_period

pollutant_nam e 6055 5 years Carbon Monoxide (CO) 6055 01/01/2005-present

Carbon Monoxide (CO)

Page 61test_report_sampling

facility _id report_id sampling_port_id point_differ point_description befre_SO2_device

point_orientation

normal_bypass_percent

testing_bypass_percent 6055 Source Emissions Survey Unit 1 2SP1 No No 6055 Source Emissions Survey Unit 2 2SP2 No No 6055 Source Emissions Survey Unit 3 2SP3 No No

Page 62test_report_sampling

fg_fraction 100% 100% 100%

Page 63sampling_runs

facility _id report_id sampling_port_id run_id start_datetime end_datetim e

unit_load net_generation fg_moisture_content 6055 Source Emissions Survey Unit 1 2SP1 1 10/3/2005 10/3/2005 600.7 560 12.59 6055 Source Emissions Survey Unit 1 2SP1 2 10/3/2005 10/3/2005 600.7 570.3 12.24 6055 Source Emissions Survey Unit 1 2SP1 3 10/4/2005 10/4/2005 600.7 560 12.14 6055 Source Emissions Survey Unit 2 2SP2 1 10/5/2005 10/5/2005 552.9 522.4 12.6 6055 Source Emissions Survey Unit 2 2SP2 2 10/5/2005 10/5/2005 552.9 522.4 12.51 6055 Source Emissions Survey Unit 2 2SP2 3 10/5/2005 10/5/2005 552.9 522.4 12.41 6055 Source Emissions Survey Unit 3 2SP3 1 10/4/2005 10/4/2005 582.4 557.7 11.96 6055 Source Emissions Survey Unit 3 2SP3 2 10/4/2005 10/4/2005 582.4 557.7 11.43 6055 Source Emissions Survey Unit 3 2SP3 3 10/4/2005 10/4/2005 582.4 557.7 11.2

Page 64sampling_runs

fg_flow_rate

fg_flow_rate_units

standard_temperature

standard_pressure

normal_temperature

normal_pressure

fg_oxygen_content

fg_CO2_content

fg_temperature 1323659 dscfm 68 1 7.1 12.9 300 1335648 dscfm 68 1 7 13.1 300 1351583 dscfm 68 1 6.9 13.1 300 1285130 dscfm 68 1 8.2 12.3 300 1284253 dscfm 68 1 8.1 12.2 300 1309592 dscfm 68 1 8.1 12.1 300 1541285 dscfm 68 1 8.3 11.5 291 1543884 dscfm 68 1 8.2 11.7 300 1627175 dscfm 68 1 8.3 11.7 298

Page 65sampling_runs

fg_pressure

Hg_loi test_method run_comments

fuel_id fuel_unit_load fuel_flow_rate

fuel_ash fuel_heating_value 0.985 Method 5 for PM; Method 25A for THC 0.985 Method 5 for PM; Method 25A for THC 0.986 Method 5 for PM; Method 25A for THC 0.983 Method 5 for PM; Method 25A for THC 0.983 Method 5 for PM; Method 25A for THC 0.98 Method 5 for PM; Method 25A for THC 0.984 Method 5 for PM; Method 25A for THC 0.983 Method 5 for PM; Method 25A for THC 0.982 Method 5 for PM; Method 25A for THC

Page 66sampling_runs

fuel_sulfur

Page 67sampling_run_pollutants1

facility _id report_id sampling_port_id run_id pollutant_nam e conc conc_units conc_ND conc_MDL 6055 Source Emissions Survey Unit 1 2SP1 1 Total Suspended Particulates (TSP) 0.006 FALSE 6055 Source Emissions Survey Unit 1 2SP1 2 Total Suspended Particulates (TSP) 0.0038 FALSE 6055 Source Emissions Survey Unit 1 2SP1 3 Total Suspended Particulates (TSP) 0.0106 FALSE 6055 Source Emissions Survey Unit 2 2SP2 1 Total Suspended Particulates (TSP) 0.0089 FALSE 6055 Source Emissions Survey Unit 2 2SP2 2 Total Suspended Particulates (TSP) 0.0054 FALSE 6055 Source Emissions Survey Unit 2 2SP2 3 Total Suspended Particulates (TSP) 0.0049 FALSE 6055 Source Emissions Survey Unit 3 2SP3 1 Total Suspended Particulates (TSP) 0.0065 FALSE 6055 Source Emissions Survey Unit 3 2SP3 2 Total Suspended Particulates (TSP) 0.0056 FALSE 6055 Source Emissions Survey Unit 3 2SP3 3 Total Suspended Particulates (TSP) 0.0063 FALSE 6055 Source Emissions Survey Unit 3 2SP3 1 Total Hydrocarbons (THC) (as Methane) 0.3 parts per million by volum e (dry) (ppmvd) FALSE 6055 Source Emissions Survey Unit 1 2SP1 1 Total Hydrocarbons (THC) (as Methane) 0.3 parts per million by volum e (dry) (ppmvd) FALSE 6055 Source Emissions Survey Unit 1 2SP1 2 Total Hydrocarbons (THC) (as Methane) 0.3 parts per million by volum e (dry) (ppmvd) FALSE 6055 Source Emissions Survey Unit 1 2SP1 3 Total Hydrocarbons (THC) (as Methane) 0.3 parts per million by volum e (dry) (ppmvd) FALSE 6055 Source Emissions Survey Unit 2 2SP2 1 Total Hydrocarbons (THC) (as Methane) 0.3 parts per million by volum e (dry) (ppmvd) FALSE 6055 Source Emissions Survey Unit 2 2SP2 2 Total Hydrocarbons (THC) (as Methane) 0.3 parts per million by volum e (dry) (ppmvd) FALSE 6055 Source Emissions Survey Unit 2 2SP2 3 Total Hydrocarbons (THC) (as Methane) 0.3 parts per million by volum e (dry) (ppmvd) FALSE 6055 Source Emissions Survey Unit 3 2SP3 2 Total Hydrocarbons (THC) (as Methane) 0.3 parts per million by volum e (dry) (ppmvd) FALSE 6055 Source Emissions Survey Unit 3 2SP3 3 Total Hydrocarbons (THC) (as Methane) 0.3 parts per million by volum e (dry) (ppmvd) FALSE

Page 68sampling_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 68.47 pound per hour (lb/hr)

FALSE FALSE Units are in grains/dscf 43.17 pound per hour (lb/hr)

FALSE FALSE Units for concentration are grains/dscf 122.21 pound per hour (lb/hr)

FALSE FALSE Units are in grains/dscf 98.07 pound per hour (lb/hr)

FALSE FALSE Units are grains/dscf 59.59 pound per hour (lb/hr)

FALSE FALSE Units are grains/dscf 54.79 pound per hour (lb/hr)

FALSE FALSE Units are grains/dscf 86.27 pound per hour (lb/hr)

FALSE FALSE Units are grains/dscf 74.56 pound per hour (lb/hr)

FALSE FALSE Units are grains/dscf 88.35 pound per hour (lb/hr)

FALSE FALSE Units are grains/dscf 3.18 pound per hour (lb/hr)

FALSE FALSE Report was Total Hydrocarbons as Propane, was converted to methane 2.73 pound per hour (lb/hr)

FALSE FALSE Report was Total Hydrocarbons as Propane, was converted to methane 2.76 pound per hour (lb/hr)

FALSE FALSE Report was Total Hydrocarbons as Propane, was converted to methane 2.79 pound per hour (lb/hr)

FALSE FALSE Report was Total Hydrocarbons as Propane, was converted to methane 2.64 pound per hour (lb/hr)

FALSE FALSE Report was Total Hydrocarbons as Propane, was converted to methane 2.64 pound per hour (lb/hr)

FALSE FALSE Report was Total Hydrocarbons as Propane, was converted to methane 2.7 pound per hour (lb/hr)

FALSE FALSE Report was Total Hydrocarbons as Propane, was converted to methane 3.18 pound per hour (lb/hr)

FALSE FALSE Report was Total Hydrocarbons as Propane, was converted to methane 3.36 pound per hour (lb/hr)

FALSE FALSE Report was Total Hydrocarbons as Propane, was converted to methane

Page 69sampling_run_pollutants1 run_pollutant_comment Units are in grains/dscf Units for concentration are grains/dscf Units are in grains/dscf Units are grains/dscf Units are grains/dscf Units are grains/dscf Units are grains/dscf Units are grains/dscf Units are grains/dscf Report was Total Hydrocarbons as Propane, was converted to methane Report was Total Hydrocarbons as Propane, was converted to methane Report was Total Hydrocarbons as Propane, was converted to methane Report was Total Hydrocarbons as Propane, was converted to methane Report was Total Hydrocarbons as Propane, was converted to methane Report was Total Hydrocarbons as Propane, was converted to methane Report was Total Hydrocarbons as Propane, was converted to methane Report was Total Hydrocarbons as Propane, was converted to methane Report was Total Hydrocarbons as Propane, was converted to methane

Page 70sampling_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 71sampling_run_fuel fuel_conc_MDL

Page 72