### Instructions for filling in the Emission Test Template

This Information Collection Request (ICR) spreadsheet is intended to collect information about emission data from fossil fuel burning power plants and which test methods were used to do so for cases where the test methods are not currently supported by the Electronic Reporting Tool (ERT). This spreadsheet should only be used if the method is not in the ERT or if you do not have access to a lab which performs methods that are in the ERT. You must complete at least 3 separate runs or sampling events for each of the requested constituents. This spreadsheet is intended to be used for one boiler of one facility. Data for multiple boilers should be handled by using separate copies of this spreadsheet. yellow are required. All cells that are shaded in green are populated using drop

- down lists. You do not need to populate cells shaded in gray, as they are automatically populated from the Boiler Information worksheet. resulting spreadsheet with the following naming convention: [FacilityID]_Unit_[BoilerID]_EmisTestMethods.xls (example: 8100_Unit_2_EmisTestMethods.xls).

Please refer to the following steps when using these spreadsheets.

Boiler Information Worksheet

1. Please enter the EIA Facility Code, Facility Name and Boiler ID of your boiler on the Boiler Information worksheet. 2. Please enter the control device configuration.

Emission Data Worksheets

The emission data worksheets are provided for each constituent or constituent family required for this analysis. On each spreadsheet, you must enter boiler operating information during sampling, fuel input information, and emission test results. There are generally 1 to 3 emission test results records to be entered depending on the constituent or constituent family. For example, CO only requires 1 record with 3 sample events, while Mercury requires that you enter both Hg Hg +2

### , or if the Ontario

- Hydro Method was used, you would need to enter Hg 0

### , HgP, and Hg Volatile Organic HAP and Speciated Semi

-Volatile Organic HAP worksheets allow you to use a drop Constituent field to define as many records as needed to record each HAP that you have results for. General instructions follow for these worksheets:

Boiler Operation Information

1. Please provide the values of all requested parameters for each of test run/sample. 2. Please provide any other supporting information or comments in the Other Supporting Information field.

Fuel Information

1. Please enter what types of fuel are being used in your boiler using the drop

- downs in the Fuel Type Selection field. You may enter up to 4 fuel types. If you are not burning one or more of the fuel types entered in one or more samples, then enter an input rate of zero. 2. Please enter the unit of measure using the drop down provided. 3. Please enter the test method used to determine the fuel input rate. 4. Please provide any other information that you feel may be important in the Other Supporting Information field.

Emission Data

### 1. Some constituents ask for the emission rate results of each run in two different units of measure, while others do not. If emission rate results are requested in two different units of measure (ex. lb/MMBtu (Pounds per million BTU) and ppmvd @ 7% O 2 

### (parts per million by volume dry basis at 7 percent oxygen)), you are required to provide both. 2. Please provide the test method used. This may or may not match the example given in the Test Method Used field. Please ensure that the name includes the owning organization of the test method (ex. U.S. EPA Method 0010). 3. Please provide any other information that you feel may be important in the Other Supporting Information field. 4. If data sheets and QA/QC documentation tables are provided for the test method you are entering data for please also enter these data.

### This Information Collection Request (ICR) spreadsheet is intended to collect information about emission data from fossil fuel burning power plants and which test methods were used to do so for cases where the test methods are not currently supported by the Electronic Reporting Tool (ERT). This spreadsheet should only be used if the method is not in the ERT or if you do not have access to a lab which performs methods that are in the ERT. You must complete at least 3 separate This spreadsheet is intended to be used for one boiler of one facility. Data for multiple boilers should be handled by using separate copies of this spreadsheet. Fields shaded in down lists. You do not need to populate cells shaded in gray, as they are automatically populated from the Boiler Information worksheet. Please name each resulting spreadsheet with the following naming convention: [FacilityID]_Unit_[BoilerID]_EmisTestMethods.xls

1. Please enter the EIA Facility Code, Facility Name and Boiler ID of your boiler on the Boiler Information worksheet.

The emission data worksheets are provided for each constituent or constituent family required for this analysis. On each spreadsheet, you must enter boiler operating information during sampling, fuel input information, and emission test results. There are generally 1 to 3 emission test results records to be entered depending on the constituent or constituent family. For example, CO only requires 1 record with 3 sample events, while Mercury requires that you enter both Hg0 

### and , HgP, and Hg+2 

### . However, both the Speciated Volatile Organic HAP worksheets allow you to use a drop

- down provided in the Constituent field to define as many records as needed to record each HAP that you have results for. General instructions

2. Please provide any other supporting information or comments in the Other Supporting Information field.

downs in the Fuel Type Selection field. You may enter up to 4 fuel types. If you are not burning one or more of the fuel types entered in one or more samples,

4. Please provide any other information that you feel may be important in the Other Supporting Information field.

### 1. Some constituents ask for the emission rate results of each run in two different units of measure, while others do not. If emission rate results are requested in two different units of measure (ex. lb/MMBtu (Pounds per million BTU) and

(parts per million by volume dry basis at 7 percent oxygen)), you are required to provide both. 2. Please provide the test method used. This may or may not match the example given in the Test Method Used field. Please ensure that the name includes the owning organization of the test method (ex. U.S. EPA Method 0010). 3. Please provide any other information that you feel may be important in the Other Supporting Information field. 4. If data sheets and QA/QC documentation tables are provided for the test method you are entering data for please alsoEIA

Facility Code Facility Name Boiler ID

10384 Edgecombe Power Station 2Control Device Configuraton

Listed (by

boiler) in the Configuration Order Section of the Facility Unit Configurations Section of the Electronic ICRListed (by boiler) in the Configuration Order Section of the Facility Unit Configurations Section of the Electronic ICREIA

Facility Code Facility Name Boiler ID

10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start TimeMeasured Value (ppm) Test End Time Test End DateBasis (Wet or Dry) Test Method Used Data Flag (ADL, BDL, DDL) CO Emission Test ResultsTest Method Comments lb/mmBtu ppmdv @ 7% O 2 Calculated Emission RateSteam Output (1000 lb/hr) Total Heat Input (mmBtu/hr) Flue Gas Moisture (%)Flue Gas CO 2(%) Flue Gas O 2(%) Flue Gas Flow Rate (dscfm)Fuel Input Rate Fuel Type

Flue Gas Temperature (F) Fuel #1Units of Measure Me asurement Method Fuel Input Rate Fuel #1Fuel Type Units of Measure Me asurement Method Fuel #2Fuel Input Rate Fuel Type Units of Measure Fuel #3Me asurement Method Fuel Input Rate Fuel Type Fuel #4Units of Measure Me asurement Method Fuel #4 Other Supporting InformationEIA

Facility Code Facility Name Boiler ID 10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start Time Test End DateMe asured Value (ppm) Basis (Wet or Dry) Test Method Used Data Flag (ADL, BDL, DDL) Test End Time Formaldehyde Emission Test ResultsTest Method

Comments lb/mmBtu ppmdv @ 7% O 2 Steam Output (1000 lb/hr) Total Heat Input

(mmBtu/hr) Calculated Emission RateFuel Input Rate Fuel Type Units of Me asure Flue Gas Temperature (F) Fuel #1 Flue Gas Moisture (%) Flue Gas

CO 2(%) Flue Gas

O 2(%) Flue Gas Flow

Rate (dscfm)Me asurement

Method Fuel Input

Rate Fuel Type Units of Measure Me asurement

Method Fuel Input

Rate Fuel Type Units of

Me asure Fuel #2 Fuel #3Me asurement

Method Fuel Input

Rate Fuel Type Units of

Measure Measurement

Method Fuel #4 Other Supporting InformationEIA

Facility Code Facility Name Boiler ID 10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start TimeMeasured Value (ppm) Basis (Wet or Dry) Test End Time Test End Date Methane Emission Test ResultsTest Method Used Data Flag (ADL, BDL, DDL) Test Method Comments lb/mmBtu Methane Emission Test Results Calculated Emission Rateppmdv @ 7% O 2 Flue Gas Moisture (%) Flue Gas CO 2(%) Flue Gas

O 2(%) Flue Gas

Flow Rate (dscfm) Calculated Emission Rate Steam Output (1000 lb/hr) Total Heat

Input (mmBtu/hr)Fuel Input Rate Fuel Type Units of

Me asure Measurement

Method Fuel

Input Rate Fuel Type Units of

Me asure Flue Gas Temperat ure (F) Fuel #1 Fuel #2Me asurement

Method Fuel

Input Rate Fuel Type Units of

Me asure Measurement

Method Fuel

Input Rate Fuel Type Units of

Me asure Fuel #4 Fuel #3Me asurement

Method Other Supporting InformationEIA

Facility Code Facility Name Boiler ID 10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start Time Test End DateMe asured Value (ppm) Basis (Wet or Dry) Test Method Used Test End Time SO 2Emission Test ResultsData Flag (ADL,

BDL, DDL) Test Method

Comments lb/mmBtu ppmdv @ 7% O 2 Calculated Emission Rate Steam Output (1000 lb/hr)Fuel Input Rate Fuel Type Flue Gas Moisture (%) Flue Gas

CO 2(%) Flue Gas

O 2(%) Flue Gas

Flow Rate (dscfm) Total Heat Input (mmBtu/hr) Flue Gas Temperature (F) Fuel #1Units of

Me asure Me asurement

Method Fuel Input

Rate Fuel Type Units of

Me asure Me asurement

Method Fuel Input

Rate Fuel Type Fuel #1 Fuel #2 Fuel #3Units of

Me asure Me asurement

Method Fuel Input

Rate Fuel Type Units of Measure Me asurement

Method Fuel #4 Fuel #3Other Supporting InformationEIA

Facility Code Facility Name Boiler ID 10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start TimePlease note QA/QC documentation starting in Column "AI"

Measured Value (μg/dscm) Basis (Wet or Dry) Test End Time Total Vapor Phase Mercury Emission Test Results

Test End DatePlease note QA/QC documentation starting in Column "AI"

Test Method Used Data Flag (ADL, BDL, DDL) Test Method

Comments (lb/mmBtu) Total Vapor Phase Mercury Emission Test Results Steam Output (1000 lb/hr)Fuel Input Rate Flue Gas O 2(%) Flue Gas

Flow Rate (dscfm) Flue Gas

Temperature (F) Flue Gas Moisture (%) Total Heat Input (mmBtu/hr) Flue Gas CO 2(%)Fuel Type Units of Me asure Me asurement

Method Fuel Input

Rate Fuel Type Units of

Measure Measurement

Method Fuel Input

Rate Fuel #1 Fuel #2Fuel Type Units of Me asure Me asurement

Method Fuel Input

Rate Fuel Type Units of Measure Me asurement

Method Fuel #3 Fuel #4QA /QC Documentation

Trap ID Section 1

Mass (ng) Section 2

Mass (ng) Total

Mass (ng) Initial

Spike (ng) Total NonSpike (ng) Other Supporting InformationSample

Volume (dscm) Volume

Difference (%) Volume Diff. Limit Breaktrough

(%) Breaktrough

Limit Concentration

(μg/dscm) Trap ID

#DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! ≤20% of field recovery test ≤10% of Section 1 Hg

mass for Hg conc. >1

μg/dscm: or ≤ 20% of Section Trap #1Section 1

Mass Section 2

Mass Total

Mass Initial

Spike Total NonSpike Sample

Volume Volume

Difference (%) Volume Diff. Limit

≤20% of field recovery test Trap #2Breaktrough (%) Breaktrough Limit Concentration

(μg/dscm) Abs. diff. RD (%) Limit C rec

#DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! #DIV/0! Me asured Spike Recovery ( R ) Paired Trap Agreement (RD)

≥ 10 % RD mass for Hg conc. >1 μg/dscm: or

≤20% RD or ≤ 0.2 μg/dscm abs.diff. for Hg conc. ≤1 ≤10% of Section 1 Hg mass for Hg conc. >1

μg/dscm: or ≤ 20% of Section 1 for Hg conc. ≤1R (%) by

Run Ravg(%) Limit

Average Recovery

, between 85 and 115% Me asured Spike Recovery ( R )

#DIV/0!EIA

Facility Code Facility Name Boiler ID 10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start TimeMeasured Hg 0Value (μg/dscm) Measured Hg +2Value (μg/dscm) Test End Time Test End DateMe asured Hg PValue

(μg/dscm) Basis (Wet or Dry) Test Method Used Data Flag (ADL, BDL, DDL) Total Vapor Phase Mercury Emission Test ResultsTest Method

Comments Total Mercury (lb/mmBtu) Steam Output

(1000 lb/hr) Total Heat

Input (mmBtu/hr) Flue Gas

Moisture (%) Flue Gas

CO 2(%)Fuel Input Rate Fuel Type Units of Me asure Measurement

Method Fuel #1 Flue Gas O 2(%) Flue Gas

Flow Rate (dscfm) Flue Gas

Temperature (F)Fuel Input Rate Fuel Type Units of Me asure Me asurement

Method Fuel Input

Rate Fuel Type Units of Me asure Measurement

Method Fuel #2 Fuel #3Fuel Input

Rate Fuel Type Units of Me asure Me asurement

Method Other Supporting Information Fuel #4Measured Value (μg/m3) Basis Test Method Used Data Flag (ADL, BDL, DDL) Front

Half Mass (ng) Back Half

Mass (ng) Total

Mass (ng) Test

Method Comments lb/mmBtu ppmdv @ 7% O 2 Fuel Input Rate Fuel Type Units of

Measure Measurement Method

Benzene 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 4.9E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 138.6 0.0 138.6 4.15E-06 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Bromochloromethane 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 0.0E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B BDL 0.0 0.0 0.0 0.00E+00 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Bromodichloromethane 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 2.9E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 8.1 0.0 8.1 2.43E-07 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Bromomethane 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 5.3E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 150.0 0.0 150.0 4.49E-06 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Carbon Disulfide 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 7.3E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 208.0 0.0 208.0 6.23E-06 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Carbon Tetrachloride 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 2.1E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 5.9 0.0 5.9 1.77E-07 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Chloroform 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 1.8E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B ADL 45.0 6.7 51.7 1.55E-06 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Methyl chloride 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 3.4E+01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 958.0 0.0 958.0 2.87E-05 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Dichlorodifluoromethane 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 9.4E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 26.7 0.0 26.7 8.00E-07 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation 2-Hexanone 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 2.3E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B ADL 39.0 26.0 65.0 1.95E-06 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Methylene Chloride 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 1.6E+03 Dry U.S. EPA Method 0031 with SW-846 Method 8260B ADL 996.0 43,333.3 44,329.3 1.33E-03 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Styrene 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 1.3E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 3.7 0.0 3.7 1.11E-07 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Tetrachloroethylene 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 8.8E-02 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 2.5 0.0 2.5 7.49E-08 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Toluene 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 1.6E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B ADL 41.2 5.3 46.5 1.39E-06 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Trichloroethylene 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 0.0E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B BDL 0.0 0.0 0.0 0.00E+00 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Trichlorofluoromethane 1 5/10/2010 9:15 AM 5/10/2010 11:15 AM 6.5E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 18.4 0.0 18.4 5.51E-07 580 783 10.3 13.32 5.87 170151 193 783 bituminous MMBtu/hr boiler efficiency calculation Benzene 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 3.9E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 122.5 0.0 122.5 3.34E-06 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Bromochloromethane 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 1.7E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 0.0 5.3 5.3 1.46E-07 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Bromodichloromethane 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 2.8E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 8.9 0.0 8.9 2.43E-07 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Bromomethane 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 8.1E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 253.0 0.0 253.0 6.90E-06 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Carbon Disulfide 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 2.0E+01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 625.6 0.0 625.6 1.71E-05 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Carbon Tetrachloride 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 4.8E-02 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 1.5 0.0 1.5 4.09E-08 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Chloroform 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 2.0E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B ADL 55.0 6.3 61.3 1.67E-06 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Methyl chloride 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 3.3E+01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 1,031.8 0.0 1,031.8 2.82E-05 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Dichlorodifluoromethane 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 6.3E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 19.6 0.0 19.6 5.35E-07 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation 2-Hexanone 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 1.1E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 35.0 0.0 35.0 9.55E-07 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Methylene Chloride 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 1.3E+03 Dry U.S. EPA Method 0031 with SW-846 Method 8260B ADL 213.0 40,000.0 40,213.0 1.10E-03 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Styrene 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 1.5E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 4.8 0.0 4.8 1.31E-07 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Tetrachloroethylene 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 5.5E-02 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 0.0 1.7 1.7 4.73E-08 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Toluene 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 1.1E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 32.9 0.0 32.9 8.98E-07 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Trichloroethylene 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 4.3E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 13.6 0.0 13.6 3.71E-07 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Trichlorofluoromethane 2 5/10/2010 11:58 AM 5/10/2010 1:58 PM 3.1E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 9.6 0.0 9.6 2.62E-07 577 769 10.4 13.54 5.96 169729 201 769 bituminous MMBtu/hr boiler efficiency calculation Benzene 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 2.0E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B ADL 50.6 1.0 51.6 1.80E-06 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Bromochloromethane 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 2.0E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 0.0 5.0 5.0 1.75E-07 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Bromodichloromethane 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 2.2E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 5.7 0.0 5.7 1.99E-07 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Bromomethane 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 3.0E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 76.4 0.0 76.4 2.67E-06 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Carbon Disulfide 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 6.1E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 157.0 0.0 157.0 5.49E-06 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Carbon Tetrachloride 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 1.1E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 2.7 0.0 2.7 9.45E-08 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Chloroform 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 1.5E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B ADL 33.6 6.0 39.6 1.39E-06 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Methyl chloride 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 8.4E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 215.6 0.0 215.6 7.54E-06 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Dichlorodifluoromethane 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 3.8E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 9.6 0.0 9.6 3.36E-07 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation 2-Hexanone 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 8.6E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 0.0 22.0 22.0 7.70E-07 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Methylene Chloride 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 1.6E+03 Dry U.S. EPA Method 0031 with SW-846 Method 8260B ADL 142.0 40,000.0 40,142.0 1.40E-03 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Styrene 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 0.0E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B BDL 0.0 0.0 0.0 0.00E+00 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Tetrachloroethylene 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 4.3E-02 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 1.1 0.0 1.1 3.85E-08 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Toluene 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 6.8E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B ADL 10.6 6.7 17.3 6.04E-07 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Trichloroethylene 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 0.0E+00 Dry U.S. EPA Method 0031 with SW-846 Method 8260B BDL 0.0 0.0 0.0 0.00E+00 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Trichlorofluoromethane 3 5/10/2010 2:40 PM 5/10/2010 4:40 PM 2.3E-01 Dry U.S. EPA Method 0031 with SW-846 Method 8260B DDL 5.8 0.0 5.8 2.03E-07 519 701 10.2 12.85 6.63 169042 198 701 bituminous MMBtu/hr boiler efficiency calculation Flue Gas O 2(%) Flue Gas

Flow Rate (scfm) Flue Gas

Temperat ure (F) Fuel #1 Calculated Emission Steam Output (1000 lb/hr) Total

Heat Input (mmBtu/ hr) Flue Gas Moisture (%) Flue Gas CO 2(%) Compound (use drop down to define for as many rows as

needed) Run Number Test Start Date Test Start

Time Test End

Date Test End

TimeEIA

Facility Code Facility Name Boiler ID 10384 Edgecombe Power Station 2

Speciated Semi-Volatile Organic HAP Emission Data

Benzoic Acid 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Bis(2-ethylhexyl) phthalate 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Di-n-octyl phthalate 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Acenaphthene 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Acenaphthylene 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Chrysene 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Fluoranthene 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Fluorene 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM 2-Methylnaphthalene 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Naphthalene 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Phenanthrene 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Pyrene 1 5/10/2010 9:15 AM 5/10/2010 11:31 AM Benzoic Acid 2 5/10/2010 11:59 AM 5/10/2010 2:07 PM Acenaphthene 2 5/10/2010 11:59 AM 5/10/2010 2:07 PM Acenaphthylene 2 5/10/2010 11:59 AM 5/10/2010 2:07 PM Chrysene 2 5/10/2010 11:59 AM 5/10/2010 2:07 PM Fluoranthene 2 5/10/2010 11:59 AM 5/10/2010 2:07 PM Fluorene 2 5/10/2010 11:59 AM 5/10/2010 2:07 PM 2-Methylnaphthalene 2 5/10/2010 11:59 AM 5/10/2010 2:07 PM Naphthalene 2 5/10/2010 11:59 AM 5/10/2010 2:07 PM Phenanthrene 2 5/10/2010 11:59 AM 5/10/2010 2:07 PM Benzoic Acid 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM Acenaphthene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM Benzo(g,h,i)perylene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM Benzo(a)pyrene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM Benzo(e)pyrene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM Chrysene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM Fluoranthene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM Fluorene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM 2-Methylnaphthalene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM Naphthalene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM Phenanthrene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM Pyrene 3 5/10/2010 2:41 PM 5/10/2010 4:48 PM

Compound (use drop down to define for as many rows as

needed) Run Number Test Start

Date Test Start

Time Test End

Date Test End

TimeFootnote

s: * Front Half Composite contains particulate filter, front half of the filter holder, and probe solvent rinses ** Back Half Composite contains XAD-2 resin tube, back half of the filter holder, and coil condenser solvent rinses *** Condensate Composite contains condensate and Impinger contents and the glassware solvent rinses

Me asured Value (μg/m3) Basis

(Wet or Dry) Test

Method Used Data Flag

(ADL, BDL, DDL) Front

Half mass* (ng) Back Half

mass* (ng) Condens

ate Mass*** (ng) Total Composit e (ng) Test

Method Comment

s lb/mmBtu

2.13E+01 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 0.0 52000.0 0.0 52000 1.81E-05 1.68E+00 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 4100.0 0.0 0.0 4100 1.43E-06 4.06E+00 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 9900.0 0.0 0.0 9900 3.44E-06 6.55E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 16.0 0.0 0.0 16 5.57E-09 1.27E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 3.1 0.0 0.0 3.1 1.08E-09 1.47E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 2.7 0.0 0.9 3.6 1.25E-09 5.00E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 5.7 6.5 0.0 12.2 4.24E-09 6.15E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 15.0 0.0 0.0 15 5.22E-09 9.42E-02 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 210.0 20.0 0.0 230 8.00E-08 3.24E-01 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 790.0 0.0 0.0 790 2.75E-07 1.15E-02 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 28.0 0.0 0.0 28 9.74E-09 4.51E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 0.0 11.0 0.0 11 3.83E-09 1.62E+01 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 0.0 40000.0 0.0 40000 1.38E-05 4.86E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 12.0 0.0 0.0 12 4.15E-09 1.22E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 3.0 0.0 0.0 3 1.04E-09 8.10E-04 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 2.0 0.0 0.0 2 6.92E-10 3.97E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 3.1 6.7 0.0 9.8 3.39E-09 6.48E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 9.9 6.1 0.0 16 5.54E-09 9.32E-02 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 230.0 0.0 0.0 230 7.96E-08 4.05E-01 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 1000.0 0.0 0.0 1000 3.46E-07 8.51E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 21.0 0.0 0.0 21 7.27E-09 1.53E+01 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 0.0 39000.0 0.0 39000 1.37E-05 3.06E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 7.8 0.0 0.0 7.8 2.74E-09 3.18E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 8.1 0.0 0.0 8.1 2.84E-09 9.03E-04 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 2.3 0.0 0.0 2.3 8.07E-10 1.49E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 3.8 0.0 0.0 3.8 1.33E-09 8.24E-04 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 2.1 0.0 0.0 2.1 7.37E-10 6.91E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 8.3 9.3 0.0 17.6 6.18E-09 6.08E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 8.3 7.2 0.0 15.5 5.44E-09 5.93E-02 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 130.0 0.0 21.0 151 5.30E-08 3.02E-01 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 590.0 0.0 180.0 770 2.70E-07 7.07E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 18.0 0.0 0.0 18 6.32E-09 6.67E-03 Dry U.S. EPA Method 0010 with SW -846 Method 8270D DDL 0.0 17.0 0.0 17 5.97E-09 Semi-Volatile Organic HAP Emission Test Results Calculated Emission* Front Half Composite contains particulate filter, front half of the filter holder, and probe solvent rinses ** Back Half Composite contains XAD-2 resin tube, back half of the filter holder, and coil condenser solvent rinses *** Condensate Composite contains condensate and Impinger contents and the glassware solvent rinses

ppmdv @ 7% O 2 Fuel Input Rate Fuel Type

580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 580 783 10.288 13.32 5.87 170161.4 193.03 783 bitum inous 577 769 10.363 13.54 5.96 169798.2 200.82 769 bitum inous 577 769 10.363 13.54 5.96 169798.2 200.82 769 bitum inous 577 769 10.363 13.54 5.96 169798.2 200.82 769 bitum inous 577 769 10.363 13.54 5.96 169798.2 200.82 769 bitum inous 577 769 10.363 13.54 5.96 169798.2 200.82 769 bitum inous 577 769 10.363 13.54 5.96 169798.2 200.82 769 bitum inous 577 769 10.363 13.54 5.96 169798.2 200.82 769 bitum inous 577 769 10.363 13.54 5.96 169798.2 200.82 769 bitum inous 577 769 10.363 13.54 5.96 169798.2 200.82 769 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous 520 701 10.247 12.85 6.63 168962.7 198.4 701 bitum inous Flue Gas O 2(%) Flue Gas

Flow Rate (scfm) Flue Gas

Temperat ure (F) Calculated Emission Steam Output (1000 lb/hr) Total

Heat Input (mmBtu/h r) Flue Gas Moisture (%) Flue Gas CO 2(%)Units of

Me asure Me asurement Method Fuel Input Rate Fuel Type Units of

Me asure Measure

ment Method Fuel

Input Rate Fuel Type

MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation MMBtu/hr boiler efficiency calculation Fuel #1 Fuel #2 Fuel #3Units of

Me asure Me asure

ment Method Fuel

Input Rate Fuel Type Units of

Me asure Measure

ment Method Fuel #4 Other Supporti ng Informati

on Fuel #3EIA

Facility Code Facility Name Boiler ID

10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start Time Test End DateMe asured Value (ppm) Basis (Wet or Dry) Test Method Used Hydrogen Cyanide Emission Test Results Test End TimeData Flag (ADL,

BDL, DDL) Test Method

Comments Steam Output (1000 lb/hr) Total Heat

Input (mmBtu/hr) Calculated Emission Rate (lb/mmBtu) Flue Gas Moisture (%) Flue Gas CO 2(%)Fuel Input Rate Fuel Type Units of Me asure Me asurement

Method Fuel Input

Rate Flue Gas Flow Rate (dscfm) Flue Gas

Temperature (F) Fuel #1 Flue Gas O 2(%)Fuel Type Units of Me asure Me asurement

Method Fuel Input Rate Fuel Type Units of Me asure Measurement

Method Fuel Input

Rate Fuel #2 Fuel #3Fuel Type Units of Me asure Me asurement

Method Fuel #4 Other Supporting InformationEIA

Facility Code Facility Name Boiler ID

10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start Time Test End DateMe asured Value (ppm) Basis (Wet or Dry) Test Method Used Test End Time Hydrogen Chloride Emission Test ResultsData Flag (ADL,

BDL, DDL) Test Method

Comments Calculated

Emission Rate (lb/mmBtu) Flue Gas Moisture (%) Flue Gas CO 2(%) Hydrogen Chloride Emission Test Results Steam Output (1000 lb/hr) Total Heat

Input (mmBtu/hr)Fuel Input Rate Fuel Type Units of Me asure Me asurement

Method Fuel Input

Rate Flue Gas Temperature (F) Fuel #1 Flue Gas O 2(%) Flue Gas

Flow Rate (dscfm)Fuel Type Units of Me asure Me asurement

Method Fuel Input Rate Fuel Type Units of Me asure Measurement

Method Fuel Input

Rate Fuel #2 Fuel #3Fuel Type Units of Me asure Me asurement

Method Fuel #4 Other Supporting InformationEIA

Facility Code Facility Name Boiler ID

10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start Time Test End DateMe asured Value (ppm) Basis (Wet or Dry) Test Method Used Hydrogen Flouride Emission Test Results Test End TimeData Flag (ADL,

BDL, DDL) Test Method

Comments Hydrogen Flouride Emission Test Results Steam Output (1000 lb/hr) Total Heat

Input (mmBtu/hr) Calculated Emission Rate (lb/mmBtu) Flue Gas Moisture (%)Fuel Input Rate Fuel Type Units of Measure Measurement

Method Flue Gas Flow Rate (dscfm) Flue Gas

Temperature (F) Fuel #1 Flue Gas CO 2(%) Flue Gas

O 2(%)Fuel Input

Rate Fuel Type Units of Me asure Me asurement

Method Fuel Input Rate Fuel Type Units of Me asure Me asurement

Method Fuel #2 Fuel #3Fuel Input

Rate Fuel Type Units of Me asure Me asurement

Method Fuel #4 Other Supporting InformationEIA

Facility Code Facility Name Boiler ID 10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start TimeMe asured NO (ppm) Test End Time Test End DateMe asured NO 2(ppm) Basis (Wet or Dry) Test Method Used NOXEmission Test ResultsData Flag (ADL, BDL, DDL) Test Method Comments (lb/mmBtu) Total NOXCalculated Emission Rateppmdv @ 7% O 2 Flue Gas Moisture (%) Flue Gas

CO 2(%) Flue Gas

O 2(%) Calculated Emission Rate Steam Output (1000 lb/hr) Total Heat Input

(mmBtu/hr)Fuel Input Rate Fuel Type Units of Measure Me asurement

Method Fuel Input

Rate Flue Gas Flow Rate (dscfm) Flue Gas

Temperature (F) Fuel #1Fuel Type Units of Me asure Me asurement

Method Fuel Input

Rate Fuel Type Units of Measure Measurement

Method Fuel Input

Rate Fuel #2 Fuel #3Fuel Type Units of Me asure Me asurement

Method Fuel #4 Other Supporting InformationEIA

Facility Code Facility Name Boiler ID 10384 Edgecombe Power Station 2

Run Number Test Start Date Test Start TimeTotal Dissolved Solids (mg solids/liter) Total Suspended Solids (mg solids/liter) Test End Time Test End DateTest Method Used Data Flag (ADL, BDL, DDL) Constisuent Emission Test ResultsTest Method Comments Fuel Input Rate Flue Gas Temperat ure (F) Flue Gas Flow Rate (dscfm) Steam Output (1000 lb/hr) Total Heat Input

(mmBtu/hr)Fuel Type Units of Me asure Me asurement

Method Fuel Input Rate Fuel Type Units of Me asure Measurement

Method Fuel Input Rate Fuel #1 Fuel #2Fuel Type Units of Me asure Me asurement

Method Fuel Input

Rate Fuel Type Units of

Measure Measurement

Method Fuel #3 Fuel #4Other Supporting InformationFuel

anthracite bitum inous subbituminous lignite coal refuse (culm or gob) No.2 Fuel Oil (distillate) No.6 Fuel Oil (residual or bunker C) synfuel petroleum coke other

Relative to Control Device Upstream Downstream

Fuel Input Units of Measure MMBtu/hr standard cubic feet per minute (scfm) gallon/m inute lb/hour ton/day

Exhaust Flow Rate Units of Measure acfm dscfm

Exhaust Temperature Units of Measure deg C deg F

Test Method Used for Fuel Input Rate F-Factor gas fuel meter boiler efficiency

calculation Other

CO Test Method U.S. EPA Method 10A U.S. EPA Method 10B

Formaldehyde Test Method U.S. EPA Method 320U.S. EPA Method 0011

U.S. EPA Method 316

CH4 Test Method U.S. EPA Method 18 U.S. EPA Method 320

SO2 Test Method U.S. EPA Method 6

Hg Test Method U.S. EPA Method 30B

Speciated Volatile Organic HAP M ethod U.S. EPA Method 0031 with SW -846 Method 8260B U.S. EPA Method 0031/TO-15

Speciated Semi-Volatile Organic HAP M ethod U.S. EPA Method 0010 with SW -846 Method 8270C U.S. EPA Method 0010 with SW -846 Method 8270D

HCN Test Method U.S. EPA Conditional Test Method 033 (CTM-033) U.S. EPA Method 320 CARB 426 U.S. EPA Method 26A-Mod

O2/CO2 Test Method U.S. EPA Method 3B

NOX Test Method U.S. EPA Method 7 U.S. EPA Method 7A U.S. EPA Method 7B U.S. EPA Method 7C U.S. EPA Method 7D

TDS/TSS Test Method Standard Test Method for Filterable and Nonfilterable Matter in W ater ASTM D5907 Standard Methods of the Examination of W ater and W astewater Method 2540B

Control Configuration 

### Listed (by boiler) in Question 16 (page 17) of the questionnaire Listed (by boiler) in the Configuration Order Section of the Facility Unit Configurations Section of the Electronic ICRHg Ontario Hydro Test Method

ASTM Method D6784

HCL Test Methods U.S. EPA Method 320 U.S. EPA Method 26

HF Test Methods U.S. EPA Method 320 U.S. EPA Method 26

Basis Wet DryConstituent CAS Methyl chloride 74-87-3 1,1,2-Trichloroethane 79-00-5 1,1-Dimethylhydrazine 57-14-7 1,2,4-Trichlorobenzene 120-82-1 1,2-Dibromo-3-chloropropane 96-12-8 1,2-Epoxybutane (1,2-butylene oxide) 106-88-7 1,2-Propyleneim ine (2-methylaziridine) 75-55-8 1,3-Butadiene 106-99-0 1,3-Dichloropropene 542-75-6 1,3-Propane sultone 1120-71-4 1,4-Dichlorobenzene (p-) 106-46-7 1,4-Dioxane (1,4-Diethylene oxide) 123-91-1 2,2,4-Trimethyl pentane 540-84-1 2-Nitropropane 79-46-9 Acetaldehyde 75-07-0 Acetonitrile (cyanom ethane) 75-05-8 Acetophenone 98-86-2 Acrolein (2-propenal) 107-02-8 Acrylam ide 79-06-1 Acrylic acid 79-10-7 Acrylonitrile (2-propenenitrile) 107-13-1 Allyl chloride (3-chloropropene) 107-05-1 Aniline (am inobenzene) 62-53-3 Benzene 71-43-2 Benzyl chloride (a-chlorotoluene) 100-44-7 Beta-Propiolactone 57-57-8 Bis(2-Chloroethyl)ether 111-44-4 Bromochloromethane 74-97-5 Bromodichloromethane 75-27-4 Carbon disulfide 75-15-0 Carbon tetrachloride 56-23-5 Carbonyl sulfide 463-58-1 Bromomethane 74-83-9 Chloroacetic acid 79-11-8 Chlorobenzene 108-90-7 Chloroform 67-66-3 Chloromethyl m ethyl ether 107-30-2 Chloroprene (2-chloro-1,3-butadiene) 126-99-8 Cresylic acid (cresol isomer mixture) 1319-77-3 Cumene (isopropylbenzene) 98-82-8 Dichlorodifluoromethane 75-71-8 Diethyl sulfate 64-67-5 Dim ethyl sulfate 77-78-1 Dim ethylcarbamyl chloride 79-44-7 Epichlorohydrin (1-chloro-2,3-epoxy propane) 106-89-8 Ethyl acrylate 140-88-5 Ethyl carbamate (urethane) 51-79-6 Ethyl chloride 75-00-3 Speciated Volatile Organic HAPsEthylbenzene 100-41-4 Ethylene dibrom ide (1,2-dibromoethane) 106-93-4 Ethylene dichloride (1,2-dichloroethane) 107-06-2 Ethylene oxide 75-21-8 Ethyleneim ine (aziridine) 151-56-4 Ethylidene dichloride (1,1-dichloroethane) 75-34-3 Formaldehyde 50-00-0 Hexachlorobutadiene 87-68-3 Hexachloroethane 67-72-1 Hexane 110-54-3 Isophorone 78-59-1 1, 1, 2, 2-Tetrachloroethane 79-34-5 Methanol 67-56-1 Methyl bromide 74-83-9. Methyl chloroform (1,1,1-trichloroethane) 71-55-6 Methyl ethyl ketone (2-butanone) 78-93-3 Methyl iodide 74-88-4 Methyl isobutyl ketone (hexone) 108-10-1 Methyl isocyanate 624-83-9 Methyl m ethacrylate 80-62-6 Methyl tert-butyl ether 1634-04-4 Methylene chloride 75-09-2 Methylhydrazine 60-34-4 m-Xylene 108-38-3 N,N-Dimethylaniline 100-23-2 N,N-Dimethylformamide 68-12-2 Nitrobenzene 98-95-3 N-Nitrosodimethylam ine 62-75-9 N-Nitrosomorpholine 59-89-2 2-Hexanone 591-78-6 o-Cresol 95-48-7 o-Xylene 95-47-6 Phenol 108-95-2 Phosgene 75-44-5 Propionaldehyde 123-38-6

Propylene dichloride (1,2-dichloropropane) 78-87-5 Propylene oxide 75-56-9 p-Xylene 106-42-3 Styrene 100-42-5 Trichlorofluoromethane 75-69-4 Tetrachloroethylene 127-18-4 Toluene 108-88-3 Trichloroethylene 79-01-6 Triethylam ine 121-44-8 Vinyl acetate 108-05-04 Vinyl bromide 593-60-2 Vinyl chloride (chloroethene) 75-01-4 Vinylidene chloride 75-35-4 Xylenes (isomer & mixtures) 1330-20-7 

### Listed (by boiler) in the Configuration Order Section of the Facility Unit Configurations Section of the Electronic ICRSpeciated Semi-volatile Organic HAPs

Constituent CAS 2-Methylnaphthalene 91-57-6 Acenaphthene 83-32-9 Acenaphthylene 208-96-8 Anthracene 120-12-7 Benzo(a)anthracene 56-55-3 Benzo(a)pyrene 50-32-8 Benzo(b)fluoranthene 205-99-2 Benzo(e)pyrene 192-97-2 Benzo(g,h,i)perylene 191-24-2 Benzo(k)fluoranthene 207-08-9 Chrysene 218-01-9 Dibenzo(a,h)anthracene 53-70-3 Fluoranthene 206-44-0 Fluorene 86-73-7 Indeno(1,2,3-cd)pyrene 193-39-5 Naphthalene 91-20-3 Perylene 77392-71-3 Phenanthrene 85-01-8 Pyrene 129-00-0 Acetophenone 98-86-2 2-Acetylam inofluorene 53-96-3 1-Acetyl-2-thiourea 591-08-2 Aldrin 309-00-2 2-Aminoanthraquinone 117-79-3 Am inoazobenzene 60-09-3 4-Aminobiphenyl 92-67-1 3-Amino-9-ethylcarbazole 132-32-1 Anilazine 101-05-3 Aniline 62-53-3 o-Anisidine 90-04-0 Aramite 140-57-8 Aroclor 1016 12674-11-2 Aroclor 1221 11104-28-2 Aroclor 1232 11141-16-5 Aroclor 1242 53469-21-9 Aroclor 1248 12672-29-6 Aroclor 1254 11097-69-1 Aroclor 1260 11096-82-5 Azinphos-m ethyl 86-50-0 Barban 101-27-9 Benzidine 92-87-5 Benzoic acid 65-85-0 p-Benzoquinone 106-51-4 Benzyl alcohol 100-51-6

α-BHC 319-84-6 β-BHC 319-85-7 δ-BHC 319-86-8 γ-BHC (Lindane) 58-89-9Bis(2-chloroethoxy)methane 111-91-1

Bis(2-chloroethyl) ether 111-44-4 Bis(2-chloroisopropyl) ether 39638-32-9 Bis(2-ethylhexyl) phthalate 117-81-7 4-Bromophenyl phenyl ether 101-55-3 Bromoxynil 1689-84-5 Butyl benzyl phthalate 85-68-7 Captafol 2425-06-1 Captan 133-06-2 Carbaryl 63-25-2 Carbofuran 1563-66-2 Carbophenothion 786-19-6 Chlordane (NOS) 57-74-9 Chlorfenvinphos 470-90-6 4-Chloroaniline 106-47-8 Chlorobenzilate 510-15-6 5-Chloro-2-methylaniline 95-79-4 4-Chloro-3-methylphenol 59-50-7 3-(Chloromethyl)pyridine hydrochloride 6959-48-4 1-Chloronaphthalene 90-13-1 2-Chloronaphthalene 91-58-7 2-Chlorophenol 95-57-8 4-Chloro-1,2-phenylenediam ine 95-83-0 4-Chloro-1,3-phenylenediam ine 5131-60-2 4-Chlorophenyl phenyl ether 7005-72-3 Coumaphos 56-72-4 p-Cresidine 120-71-8 Crotoxyphos 7700-17-6 2-Cyclohexyl-4,6-dinitro-phenol 131-89-5 4,4'-DDD 72-54-8 4,4'-DDE 72-55-9 4,4'-DDT 50-29-3 Demeton-O 298-03-3 Demeton-S 126-75-0 Diallate (cis or trans) 2303-16-4

2,4-Diaminotoluene 95-80-7 Dibenz(a,j)acridine 224-42-0 Dibenzofuran 132-64-9 Dibenzo(a,e)pyrene 192-65-4 1,2-Dibromo-3-chloropropane 96-12-8 Di-n-butyl phthalate 84-74-2 Dichlone 117-80-6 1,2-Dichlorobenzene 95-50-1 1,3-Dichlorobenzene 541-73-1 1,4-Dichlorobenzene 106-46-7 3,3'-Dichlorobenzidine 91-94-1 2,4-Dichlorophenol 120-83-2 2,6-Dichlorophenol 87-65-0 Dichlorovos 62-73-7 Dicrotophos 141-66-2 Dieldrin 60-57-1Diethyl phthalate 84-66-2

Diethylstilbestrol 56-53-1 Diethyl sulfate 64-67-5 Dim ethoate 60-51-5 3,3'-Dimethoxybenzidine 119-90-4 Dim ethylam inoazobenzene 60-11-7 7,12-Dimethylbenz(a)-anthracene 57-97-6 3,3'-Dimethylbenzidine 119-93-7 α,α-Dimethylphenethylam ine 122-09-8 2,4-Dimethylphenol 105-67-9 Dim ethyl phthalate 131-11-3 1,2-Dinitrobenzene 528-29-0 1,3-Dinitrobenzene 99-65-0 1,4-Dinitrobenzene 100-25-4 4,6-Dinitro-2-methylphenol 534-52-1 2,4-Dinitrophenol 51-28-5 2,4-Dinitrotoluene 121-14-2 2,6-Dinitrotoluene 606-20-2 Dinocap 39300-45-3 Dinoseb 88-85-7 Diphenylam ine 122-39-4 5,5-Diphenylhydantoin 57-41-0 1,2-Diphenylhydrazine 122-66-7 Di-n-octyl phthalate 117-84-0 Disulfoton 298-04-4 Endosulfan I 959-98-8 Endosulfan II 33213-65-9 Endosulfan sulfate 1031-07-8 Endrin 72-20-8 Endrin aldehyde 7421-93-4 Endrin ketone 53494-70-5 X X ND X X 53494-70-5 EPN 2104-64-5 Ethion 563-12-2 Ethyl carbamate 51-79-6 Ethyl m ethanesulfonate 62-50-0 Famphur 52-85-7 Fensulfothion 115-90-2 Fenthion 55-38-9 Fluchloralin 33245-39-5 2-Fluorobiphenyl (surr) 321-60-8 2-Fluorophenol (surr) 367-12-4 Heptachlor 76-44-8 Heptachlor epoxide 1024-57-3 Hexachlorobenzene 118-74-1 Hexachlorobutadiene 87-68-3 Hexachlorocyclopentadiene 77-47-4 Hexachloroethane 67-72-1 Hexachlorophene 70-30-4 Hexachloropropene 1888-71-7 Hexamethylphosphoramide 680-31-9 Hydroquinone 123-31-9 Isodrin 465-73-6 Isophorone 78-59-1 Isosafrole 120-58-1Kepone 143-50-0

Leptophos 21609-90-5 Malathion 121-75-5 Maleic anhydride 108-31-6 Mestranol 72-33-3 Methapyrilene 91-80-5 Methoxychlor 72-43-5 3-Methylcholanthrene 56-49-5 4,4'-Methylenebis (2-chloroaniline) 101-14-4 4,4'-Methylenebis(N,N-dimethylaniline) 101-61-1 Methyl m ethanesulfonate 66-27-3 Methyl parathion 298-00-0 2-Methylphenol 95-48-7 3-Methylphenol 108-39-4 4-Methylphenol 106-44-5 Mevinphos 7786-34-7 Mexacarbate 315-18-4 Mirex 2385-85-5 Monocrotophos 6923-22-4 Naled 300-76-5 1,4-Naphthoquinone 130-15-4 1-Naphthylam ine 134-32-7 2-Naphthylam ine 91-59-8 Nicotine 54-11-5 5-Nitroacenaphthene 602-87-9 2-Nitroaniline 88-74-4 3-Nitroaniline 99-09-2 4-Nitroaniline 100-01-6 5-Nitro-o-anisidine 99-59-2 Nitrobenzene 98-95-3 4-Nitrobiphenyl 92-93-3 Nitrofen 1836-75-5 2-Nitrophenol 88-75-5 4-Nitrophenol 100-02-7 5-Nitro-o-toluidine 99-55-8 Nitroquinoline-1-oxide 56-57-5 N-Nitrosodi-n-butylam ine 924-16-3 N-Nitrosodiethylam ine 55-18-5 N-Nitrosodimethylam ine 62-75-9 N-Nitrosodiphenylam ine 86-30-6 N-Nitrosodi-n-propylam ine 621-64-7 N-Nitrosomethylethylam ine 10595-95-6 N-Nitrosomorpholine 59-89-2 N-Nitrosopiperidine 100-75-4 N-Nitrosopyrrolidine 930-55-2 Octamethyl pyrophosphoramide 152-16-9 4,4'-Oxydianiline 101-80-4 Parathion 56-38-2 Pentachlorobenzene 608-93-5 Pentachloronitrobenzene 82-68-8 Pentachlorophenol 87-86-5 Phenacetin 62-44-2 Phenobarbital 50-06-6 Phenol 108-95-2 1,4-Phenylenediam ine 106-50-3Phorate 298-02-2

Phosalone 2310-17-0 Phosmet 732-11-6 Phosphamidon 13171-21-6 Phthalic anhydride 85-44-9 2-Picoline (2-Methylpyridine) 109-06-8 Piperonyl sulfoxide 120-62-7 Pronamide 23950-58-5 Propylthiouracil 51-52-5 Resorcinol 108-46-3 Safrole 94-59-7 Strychnine 57-24-9 Sulfallate 95-06-7 Terbufos 13071-79-9 1,2,4,5-Tetrachlorobenzene 95-94-3 2,3,4,6-Tetrachlorophenol 58-90-2 Tetrachlorvinphos 961-11-5 Tetraethyl dithiopyrophosphate 3689-24-5 Tetraethyl pyrophosphate 107-49-3 Thionazine 297-97-2 Thiophenol (Benzenethiol) 108-98-5 Toluene diisocyanate 584-84-9 o-Toluidine 95-53-4 Toxaphene 8001-35-2 1,2,4-Trichlorobenzene 120-82-1 2,4,5-Trichlorophenol 95-95-4 2,4,6-Trichlorophenol 88-06-2 Trifluralin 1582-09-8 2,4,5-Trimethylaniline 137-17-7 Trimethyl phosphate 512-56-1 1,3,5-Trinitrobenzene 99-35-4 Tris(2,3-dibromopropyl) phosphate 126-72-7 Tri-p-tolyl phosphate 78-32-0 O,O,O-Triethyl phosphorothioate 126-68-1