### Name:

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

## Albright Unit 1 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 1

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 1 B1

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: Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 1100005860143 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
Stack B1 121.2 545.4 933.2 4 0 24 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location
Carbon Monoxide Method 10 3 240 0 Stack B1 Total organic compounds

(TOC) as Propane Method 25A 3 240 0 Stack B1

Hydrogen Chloride Method 26 3 120 0 Stack B1 Hydrogen Fluoride Method 26 3 120 0 Stack B1 Regulation Description Compound Limit Unit

NA 0



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

### Albright Unit 1

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.

Organic Condensible Particulate OTM - 27/28 3 240 0 Stack B1

Total PM2.5 OTM - 27/28 3 240 0 Stack B1 Filterable PM2.5 OTM - 27/28 3 240 0 Stack B1 Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 240 0 Stack B1

Selenium Method 29 3 240 0 Stack B1 Antimony Method 29 3 240 0 Stack B1 Arsenic Method 29 3 240 0 Stack B1 Beryllium Method 29 3 240 0 Stack B1 Cadmium Method 29 3 240 0 Stack B1 Chromium Method 29 3 240 0 Stack B1 Cobalt Method 29 3 240 0 Stack B1
Lead Method 29 3 240 0 Stack B1 Manganese Method 29 3 240 0 Stack B1 Nickel Method 29 3 240 0 Stack B1 Filterable Particulate Method 5 3 240 0 Stack B1 Sulfur Dioxide Method 6C 3 240 0 Stack B1 Nitrogen oxides (NOx) Method 7E 3 240 0 Stack B1



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

### Albright Unit 1

Sampling / Stack Data Results Summary



### Location Stack B1 - 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 Stack B1 - 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 1

Location Stack B1 - Method 26 Average
Run Number 1 2 3

Test Date 5/4/2010 5/4/2010 5/4/2010

Run Start Time 7:00:00 AM 10:15:00 AM 1:47:00 PM

Run Finish Time 10:00:00 AM 1:15:00 PM 5:46:00 PM
Net Run Time, minutes 180 180 180 Dry Gas Meter Volume Sampled, dscf 125.751 124.289 129.746 126.595
Moisture Content of Stack Gas, % 3.19 6.49 4.98 4.887 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000
Carbon Dioxide, % 11.86 11.85 11.86 11.857 Oxygen, % 7.38 7.21 7.33 7.307 Average Stack Gas Temperature, °F 336.00 342.00 336.33 338.110 Dry Volumetric Flow Rate, dry scfm 143,545.8 214,157.0 210,503.2 189,402.000
Actual Wet Volumetric Flue Gas Flow Rate, acfm 232,230.0 361,396.3 348,080.7 313,902.333 Percent Isokinetic of Sampling Rate, %
F-Factor, dscfm/MMBtu @ %O2 9747 9825 9761 9,777.667

Fw 0 0 0 0.000

Fc 0 0 0 0.000



### Location Stack B1 - 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



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

### Albright Unit 1

Location Stack B1 - 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



### Location Stack B1 - 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



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

### Albright Unit 1

Location Stack B1 - 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



### Location Stack B1 - 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 1

Emissions Summary



### Location: Stack B1 - Method 10 Compound: Carbon Monoxide Average
Run 1 2 3 lb/mmBtuO2 5.52E-03 4.14E-03 6.66E-03 0.005
ppm 4.83E+00 3.80E+00 6.23E+00 4.953 ppm@7%O2 5.15E+00 3.84E+00 6.27E+00 5.087



### Location: Stack B1 - Method 25A Compound: Total organic compounds (TOC) as Average
Run 1 2 3 lb/mmBtuO2 6.93E-04 5.14E-04 4.37E-04 0.001
ppm 3.85E-01 3.00E-01 2.60E-01 0.315 ppm@7%O2 4.11E-01 3.03E-01 2.62E-01 0.325



### Location: Stack B1 - Method 26 Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 39 100 94 77.667 lb/mmBtuO2 1.03E-02 2.66E-02 2.40E-02 0.020
ppm 7.23E+00 1.87E+01 1.69E+01 14.277 ppm@7%O2 7.43E+00 1.90E+01 1.73E+01 14.577



### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 11 27 25 21.000 lb/mmBtuO2 2.91E-03 7.18E-03 6.39E-03 0.005
ppm 3.71E+00 9.22E+00 8.18E+00 7.037 ppm@7%O2 3.81E+00 9.36E+00 8.38E+00 7.183



### Location: Stack B1 - Method 29 Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.0266 0.027 0.0255 0.026 lb/mmBtuO2 5.18E-06 5.41E-06 5.23E-06 0.000



### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.184 0.173 0.145 0.167 lb/mmBtuO2 3.58E-05 3.46E-05 2.97E-05 0.000


### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.01148 0.01166 0.01016 0.011



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

### Albright Unit 1

lb/mmBtuO2 2.24E-06 2.33E-06 2.08E-06 0.000


### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.00764 0.0075 0.00665 0.007 lb/mmBtuO2 1.49E-06 1.50E-06 1.36E-06 0.000



### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 1.665 0.157 0.0942 0.639 lb/mmBtuO2 3.24E-04 3.14E-05 1.93E-05 0.000



### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.039 0.0359 0.0303 0.035 lb/mmBtuO2 7.59E-06 7.19E-06 6.21E-06 0.000


### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.0938 0.0982 0.0794 0.090 lb/mmBtuO2 1.83E-05 1.97E-05 1.63E-05 0.000



### Compound: Manganese Average RunNumber 1 2 3 Mass_mg 0.207 0.152 0.13 0.163 lb/mmBtuO2 4.03E-05 3.04E-05 2.67E-05 0.000



### Compound: Nickel Average RunNumber 1 2 3 Mass_mg 5.306 0.323 0.1175 1.916 lb/mmBtuO2 1.03E-03 6.47E-05 2.41E-05 0.000



### Compound: Selenium Average RunNumber 1 2 3 Mass_mg 0.6886 0.6794 0.75303 0.707 lb/mmBtuO2 1.34E-04 1.36E-04 1.54E-04 0.000



### Location: Stack B1 - Method 5 

### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 528.35 415.62 110.13 351.367 lb/mmBtuO2 1.03E-01 8.32E-02 2.26E-02 0.070



### Location: Stack B1 - Method 6C



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

### Albright Unit 1

Process Run Data Compound: Sulfur Dioxide Average
Run 1 2 3 lb/mmBtuO2 2.39E+00 2.36E+00 2.36E+00 2.370
ppm 9.53E+02 9.51E+02 9.42E+02 948.667 ppm@7%O2 9.80E+02 9.66E+02 9.65E+02 970.333



### Location: Stack B1 - Method 7E Compound: Nitrogen oxides (NOx) Average
Run 1 2 3 lb/mmBtuO2 7.95E-01 7.52E-01 7.38E-01 0.762
ppm 4.42E+02 4.20E+02 4.11E+02 424.333 ppm@7%O2 4.54E+02 4.26E+02 4.21E+02 433.667



### Location: Stack B1 - OTM - 27/28 Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 67.66 67.7 56.4 63.920 lb/mmBtuO2 1.69E-02 1.64E-02 1.35E-02 0.016



### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 94.5 66 100 86.833 lb/mmBtuO2 2.36E-02 1.59E-02 2.39E-02 0.021



### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 236.7 145.7 174.2 185.533 lb/mmBtuO2 5.91E-02 3.52E-02 4.17E-02 0.045



### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 396.9 273.1 328.5 332.833 lb/mmBtuO2 9.91E-02 6.60E-02 7.86E-02 0.081



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

### Albright Unit 1

Process Run Data

APCD Run Data

Process Lab Run Data 

### Run Name Value UOM Comments Target Value
1 Bituminous Coal Burned 0 Tons/million BTU using O2 0

Run Name Value UOM Comments Target Value


### 1 ELECTROSTATIC PRECIPITATOR - HIGH EFFICIENCY 0 0

1 LOW NOX BURNERS 0 0



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

### Albright Unit 1

Sampling / Stack Data Results Detail



### Location Stack B1 - 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 1

Location Stack B1 - 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 1

Location Stack B1 - Method 26 Average Run Number 1 2 3
Test Date 5/4/2010 5/4/2010 5/4/2010 Run Start Time 7:00:00 AM 10:15:00 AM 1:47:00 PM Run Finish Time 10:00:00 AM 1:15:00 PM 5:46:00 PM Net Traversing Points 36 36 36 Net Run Time, minutes 180 180 180 Nozzle Diameter, inches Pitot Tube Coefficient 0.54 0.84 0.84 0.740 Dry Gas Meter Calibration Factor 0.998 0.998 0.998 0.998 Barometric Pressure, inches of Mercury 28.79 28.79 28.71 28.763 Average Orifice Meter Differential, inches H2O 1.60 1.60 1.60 1.600 Dry Gas Meter Volume Sampled, cubic feet 135.205 135.195 141.370 137.257 Average Dry Gas Meter Temperature, °F 87.39 93.79 93.19 91.457 Dry Gas Meter Volume Sampled, dscf 125.751 124.289 129.746 126.595 Total Moisture Liquid collected, g 88 183.3 144.4 138.567 Volume of Water Vapor, standard cubic feet 4.14 8.63 6.80 6.523 Moisture Content of Stack Gas, % 3.19 6.49 4.98 4.887 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9681 0.9351 0.9502 0.951 Carbon Dioxide, % 11.86 11.85 11.86 11.857 Oxygen, % 7.38 7.21 7.33 7.307 Carbon Monoxide & Nitrogen, % 80.76 80.94 80.81 80.837 Fuel Factor 1.14 1.16 1.14 Dry Molecular Weight, lb/lb-Mole 30.19 30.18 30.19 30.187 Wet Molecular weight, lb/lb-Mole 29.80 29.39 29.58 29.590 Flue Gas Static Pressure, inches of H2O 0.1 0.1 0.1 0.100 Absolute Flue Gas Pressure, inches of Mercury 28.80 28.80 28.72 28.773 Average Stack Gas Temperature, °F 336.00 342.00 336.33 338.110 Average Velocity Head, inches of H2O 1.1809060541 4739 1.156670783

18904 1.084781448

37945 1.141

Average Stack Gas Velocity, feet/second 48.31 75.18 72.41 65.300 Stack Cross-Sectional Area, square feet 80.118 80.118 80.118 80.118 Dry Volumetric Flow Rate, dry scfm 143,545.8 214,157.0 210,503.2 189,402.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 232,230.0 361,396.3 348,080.7 313,902.333 Percent Isokinetic of Sampling Rate, % Percent Excess Air, % 52.9 50.9 52.3 52.033 F-Factor, dscfm/MMBtu @ %O2 9747 9825 9761 9,777.667 Round Duct Diameter, inches 121.2 121.2 121.2 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0
Fw 0 0 0 0.000
Fc 0 0 0 0.000



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

### Albright Unit 1

Location Stack B1 - 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 15 of 19

### Albright Unit 1

Location Stack B1 - 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 16 of 19

### Albright Unit 1

Location Stack B1 - 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 17 of 19

### Albright Unit 1

Location Stack B1 - 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 18 of 19

### Albright Unit 1

Location Stack B1 - 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