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:

B1 Stack 1

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 0 0 0 545.4 933.2 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack B1 Carbon Monoxide Method 10 3 240 0

Total organic compounds 

(TOC) as Propane

Stack B1 Method 25A 3 240 0

Stack B1 Hydrogen Chloride Method 26 3 120 0

Stack B1 Hydrogen Fluoride Method 26 3 120 0

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

Stack B1 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

Inorganic (Aqueous) 

Condensible Part.

Stack B1 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

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 Tons/million BTU using O2 0 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