### Name:

Title: Company: Sign Date: Name: Title: Company: Sign Date: Permitted Facility Representative / Date Testing Company Representative / Date 

## Albright Unit 2 Final Test Report for

/ / Based on information and belief formed after reasonable inquiry, I certify that the statements and information in this test report are true, accurate, and complete. I have reviewed all testing details and results in this test report and hereby certify that the test report is authentic and accurate.

Saturday, January 15, 2011 Page 1 of 19

### Albright Unit 2

Facility Information: Albright Power Station Monongahela Power Company

530 Power Plant Road Albright W 26519
Contact: James Lefik

Phone: 724-838-6136

Fax: 724-830-7711

Email: jlefik@alleghenyenergy.com Testing Company:
Air/Compliance Consultants, Inc. 1050 Wm Pitt Way

Pittsburgh PA 15238
Contact: Jaimes Contreras

Phone: 412-826-3636

Fax: 412-826-3640

Email: jcontreras@air-comp.com

Air Permit Number:
R30-07700001-2009 Permitted Source ID/Name:
Stack 2 B2

Permitted Maximum Process Rate: Max. Normal Operation Process Rate:
75 MW NSOC Target Process Test Rate 67.5 MW (net)

Description of the source (including control equipment). Please see the attachments for source or process flow diagram:
Facility Description The Albright Power Station is a fossil fuel fired electric generation facility with two 80 MW and one 140 MW unit and operates under Standard Industrial Classification (SIC) code 4911. The facility consists of two (2) 954 MM Btu/hr coal-fired boilers, one (1) 1342 MM Btu/hr coal-fired auxiliary boiler, one (1) 350 KW diesel-fired emergency generator, and various supporting operations such as coal handling, ash handling and various tanks with insignificant emissions. The facility has the potential to operate seven (7) days per week, twenty-four (24) hours per day and fifty-two (52) weeks per year. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 110000586143 FRS #:

SCC / Description 10100204 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous Coal - Spreader Stoker (Bituminous Coal)

The following state and federal regulations that apply to the proposed testing:

Location Round

Duct Diam. Distance from upstream dist. Distance from

downstream dist. Number of

Traverse Ports Equiv. Diam Min.Travers Points Rect. Duct Length /Width
Unit 2 127.2 4.24 2 4 0 1 0 0 Unit 2, 0010, 29 127.2 4.24 2 4 0 24 0 0

Unit 2, 27, 28 127.2 4.24 2 4 0 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location Regulation Description Compound Limit Unit

NA 0



### Saturday, January 15, 2011 Page 2 of 19

### Albright Unit 2

The following describes any modifications and/or deviations to the applicable test methods. If alternative methods were requested, see the attachments for documentation of request AND approval, including dates. Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location

Cobalt Method 29 3 240 0 Unit 2, 0010, 29 Antimony Method 29 3 240 0 Unit 2, 0010, 29 Arsenic Method 29 3 240 0 Unit 2, 0010, 29 Beryllium Method 29 3 240 0 Unit 2, 0010, 29 Chromium Method 29 3 240 0 Unit 2, 0010, 29 Nickel Method 29 3 240 0 Unit 2, 0010, 29 Lead Method 29 3 240 0 Unit 2, 0010, 29 Manganese Method 29 3 240 0 Unit 2, 0010, 29 Selenium Method 29 3 240 0 Unit 2, 0010, 29 Cadmium Method 29 3 240 0 Unit 2, 0010, 29 Filterable PM2.5 OTM - 27/28 0 Unit 2, 27, 28 Total PM2.5 OTM - 27/28 0 Unit 2, 27, 28 Carbon Monoxide Method 10 3 120 0 Unit 2 Total organic compounds

(TOC) as Propane Method 25A 3 120 0 Unit 2

Hydrogen Fluoride Method 26 3 180 0 Unit 2 Hydrogen Chloride Method 26 3 180 0 Unit 2 Filterable Particulate Method 5 3 240 0 Unit 2 Sulfur Dioxide Method 6C 3 120 0 Unit 2 Nitrogen oxides (NOx) Method 7E 3 120 0 Unit 2



### Saturday, January 15, 2011 Page 3 of 19

### Albright Unit 2

Sampling / Stack Data Results Summary



### Location Unit 2 - Method 10 Average
Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Location Unit 2 - Method 25A Average
Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Saturday, January 15, 2011 Page 4 of 19

### Albright Unit 2

Location Unit 2 - Method 26 Average
Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/28/2010

Run Start Time 4:00:00 PM 7:32:00 AM 11:15:00 AM

Run Finish Time 7:00:00 PM 10:32:00 AM 3:54:00 PM

Net Run Time, minutes 135 135 135 Dry Gas Meter Volume Sampled, dscf 116.372 131.055 124.048 123.825
Moisture Content of Stack Gas, % 5.75 5.40 6.83 5.993 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000
Carbon Dioxide, % 12.49 12.17 11.96 12.207 Oxygen, % 6.93 7.35 7.43 7.237 Average Stack Gas Temperature, °F 323.56 310.74 318.37 317.557 Dry Volumetric Flow Rate, dry scfm 222,952.4 222,229.6 210,653.8 218,611.933
Actual Wet Volumetric Flue Gas Flow Rate, acfm 369,578.4 357,241.5 347,234.3 358,018.067 Percent Isokinetic of Sampling Rate, %
F-Factor, dscfm/MMBtu @ %O2 9882 9904 9856 9,880.667

Fw 0 0 10640 3,546.667

Fc 0 0 1800 600.000



### Location Unit 2 - Method 5 Average
Run Number

Test Date

Run Start Time

Run Finish Time
Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf
Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, %
Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm
Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, %
F-Factor, dscfm/MMBtu @ %O2

Fw

Fc



### Saturday, January 15, 2011 Page 5 of 19

### Albright Unit 2

Location Unit 2 - Method 6C Average
Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Location Unit 2 - Method 7E Average
Run Number

Test Date

Run Start Time

Run Finish Time
Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm
F-Factor, dscfm/MMBtu @ %O2
Moisture, % Fuel Type

Fw

Fc



### Saturday, January 15, 2011 Page 6 of 19

### Albright Unit 2

Location Unit 2, 0010, 29 - Method 29 Average
Run Number

Test Date

Run Start Time

Run Finish Time
Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf
Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, %
Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm
Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, %
F-Factor, dscfm/MMBtu @ %O2

Fw

Fc



### Location Unit 2, 27, 28 - OTM - 27/28 Average
Run Number

Test Date

Run Start Time

Run Finish Time
Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf
Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, %
Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm
Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, %
F-Factor, dscfm/MMBtu @ %O2

Fw

Fc



### Saturday, January 15, 2011 Page 7 of 19

### Albright Unit 2

Emissions Summary



### Location: Unit 2 - Method 10 Compound: Carbon Monoxide Average
Run 1 2 3 lb/mmBtuO2 2.22E-02 1.87E-02 1.33E-02 0.018



### Location: Unit 2 - Method 25A 

### Compound: Total organic compounds (TOC) as Average
Run 1 2 3 lb/mmBtuO2 6.31E-04 1.05E-03 9.28E-04 0.001



### Location: Unit 2 - Method 26 Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 110 140 120 123.333 lb/mmBtuO2 3.08E-02 3.60E-02 3.26E-02 0.033



### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 26 31 28 28.333 lb/mmBtuO2 7.28E-03 7.97E-03 7.61E-03 0.008



### Location: Unit 2 - Method 5 Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 49.52 38.98 55.32 47.940 lb/mmBtuO2 1.03E-02 8.05E-03 1.15E-02 0.010



### Location: Unit 2 - Method 6C Compound: Sulfur Dioxide Average
Run 1 2 3 lb/mmBtuO2 2.39E+00 2.75E+00 9.00E-01 2.013



### Location: Unit 2 - Method 7E Compound: Nitrogen oxides (NOx) Average
Run 1 2 3 lb/mmBtuO2 6.09E-01 6.29E-01 1.99E+00 1.076



### Location: Unit 2, 0010, 29 - Method 29 Compound: Antimony Average RunNumber 1 2 3



### Saturday, January 15, 2011 Page 8 of 19

### Albright Unit 2

Mass_mg 0.002 0.002 0.002 0.002 lb/mmBtuO2 4.15E-07 4.13E-07 4.17E-07 0.000


### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.0399 0.04 0.048 0.043 lb/mmBtuO2 8.28E-06 8.26E-06 1.00E-05 0.000



### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.0005 0.0005 0.00321 0.001 lb/mmBtuO2 1.04E-07 1.03E-07 6.70E-07 0.000


### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.0079 0.0114 0.00309 0.007 lb/mmBtuO2 1.64E-06 2.36E-06 6.45E-07 0.000


### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.0766 0.0667 0.0746 0.073 lb/mmBtuO2 1.59E-05 1.38E-05 1.56E-05 0.000



### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.00552 0.00538 0.00613 0.006 lb/mmBtuO2 1.15E-06 1.11E-06 1.28E-06 0.000


### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.0136 0.0141 0.0166 0.015 lb/mmBtuO2 2.82E-06 2.91E-06 3.46E-06 0.000


### Compound: Manganese Average RunNumber 1 2 3 Mass_mg 0.0444 0.0389 0.0853 0.056 lb/mmBtuO2 9.22E-06 8.04E-06 1.78E-05 0.000


### Compound: Nickel Average RunNumber 1 2 3 Mass_mg 0.283 0.0895 0.075 0.149 lb/mmBtuO2 5.87E-05 1.85E-05 1.56E-05 0.000


### Compound: Selenium Average RunNumber 1 2 3



### Saturday, January 15, 2011 Page 9 of 19

### Albright Unit 2

Process Run Data Mass_mg 0.2162 0.222 0.3056 0.248 lb/mmBtuO2 4.49E-05 4.59E-05 6.37E-05 0.000



### Location: Unit 2, 27, 28 - OTM - 27/28 Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 37.23 68.86 34.96 47.017 lb/mmBtuO2 9.34E-03 1.68E-02 8.83E-03 0.012


### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 540.27 278.02 120.85 313.047 lb/mmBtuO2 1.35E-01 6.80E-02 3.05E-02 0.078



### Saturday, January 15, 2011 Page 10 of 19

### Albright Unit 2

Process Run Data

APCD Run Data

Process Lab Run Data 

### Run Name Value UOM Comments Target Value
1 Heat Input 0 Million Btus/hr 0

Run Name Value UOM Comments Target Value


### 1 ELECTROSTATIC PRECIPITATOR 0 0

1 LOW NOX BURNERS 0 0



### Saturday, January 15, 2011 Page 11 of 19

### Albright Unit 2

Sampling / Stack Data Results Detail



### Location Unit 2 - Method 10 Average Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Saturday, January 15, 2011 Page 12 of 19

### Albright Unit 2

Location Unit 2 - Method 25A Average Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Saturday, January 15, 2011 Page 13 of 19

### Albright Unit 2

Location Unit 2 - Method 26 Average Run Number 1 2 3
Test Date 4/27/2010 4/28/2010 4/28/2010 Run Start Time 4:00:00 PM 7:32:00 AM 11:15:00 AM Run Finish Time 7:00:00 PM 10:32:00 AM 3:54:00 PM Net Traversing Points 27 27 27 Net Run Time, minutes 135 135 135 Nozzle Diameter, inches Pitot Tube Coefficient 0.84 0.84 0.81 0.830 Dry Gas Meter Calibration Factor 0.998 0.998 0.998 0.998 Barometric Pressure, inches of Mercury 28.41 28.71 28.71 28.610 Average Orifice Meter Differential, inches H2O 1.60 1.60 1.60 1.600 Dry Gas Meter Volume Sampled, cubic feet 124.543 134.290 131.313 130.049 Average Dry Gas Meter Temperature, °F 77.70 60.24 77.44 71.793 Dry Gas Meter Volume Sampled, dscf 116.372 131.055 124.048 123.825 Total Moisture Liquid collected, g 150.9 159 193.2 167.700 Volume of Water Vapor, standard cubic feet 7.10 7.48 9.09 7.890 Moisture Content of Stack Gas, % 5.75 5.40 6.83 5.993 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9425 0.946 0.9317 0.940 Carbon Dioxide, % 12.49 12.17 11.96 12.207 Oxygen, % 6.93 7.35 7.43 7.237 Carbon Monoxide & Nitrogen, % 80.58 80.48 80.61 80.557 Fuel Factor 1.12 1.11 1.13 Dry Molecular Weight, lb/lb-Mole 30.28 30.24 30.21 30.243 Wet Molecular weight, lb/lb-Mole 29.57 29.58 29.38 29.510 Flue Gas Static Pressure, inches of H2O 0.15 0.15 0.15 0.150 Absolute Flue Gas Pressure, inches of Mercury 28.42 28.72 28.72 28.620 Average Stack Gas Temperature, °F 323.56 310.74 318.37 317.557 Average Velocity Head, inches of H2O 1.0131905257 0344 0.972986577

352098 0.972324506

223779 0.986

Average Stack Gas Velocity, feet/second 69.80 67.47 65.58 67.617 Stack Cross-Sectional Area, square feet 88.247 88.247 88.247 88.247 Dry Volumetric Flow Rate, dry scfm 222,952.4 222,229.6 210,653.8 218,611.933 Actual Wet Volumetric Flue Gas Flow Rate, acfm 369,578.4 357,241.5 347,234.3 358,018.067 Percent Isokinetic of Sampling Rate, % Percent Excess Air, % 48.3 52.9 53.6 51.600 F-Factor, dscfm/MMBtu @ %O2 9882 9904 9856 9,880.667 Round Duct Diameter, inches 127.2 127.2 127.2 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0
Fw 0 0 10640 3,546.667
Fc 0 0 1800 600.000



### Saturday, January 15, 2011 Page 14 of 19

### Albright Unit 2

Location Unit 2 - Method 5 Average Run Number
Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches
Fw
Fc



### Saturday, January 15, 2011 Page 15 of 19

### Albright Unit 2

Location Unit 2 - Method 6C Average Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Saturday, January 15, 2011 Page 16 of 19

### Albright Unit 2

Location Unit 2 - Method 7E Average Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type
Fw
Fc Cgasw Cgasw Units



### Saturday, January 15, 2011 Page 17 of 19

### Albright Unit 2

Location Unit 2, 0010, 29 - Method 29 Average Run Number
Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches
Fw
Fc



### Saturday, January 15, 2011 Page 18 of 19

### Albright Unit 2

Location Unit 2, 27, 28 - OTM - 27/28 Average Run Number
Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches
Fw
Fc



### Saturday, January 15, 2011 Page 19 of 19