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:

B2 Stack 2

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 0 0 0 4.24 2 4 1

Unit 2, 0010, 

29

127.2 0 0 0 4.24 2 4 24

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

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

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 

Location Points Comments

Unit 2, 0010, Cobalt Method 29 3 240 0

29

Unit 2, 0010, Antimony Method 29 3 240 0

29

Unit 2, 0010, Arsenic Method 29 3 240 0

29

Unit 2, 0010, Beryllium Method 29 3 240 0

29

Unit 2, 0010, Chromium Method 29 3 240 0

29

Unit 2, 0010, Nickel Method 29 3 240 0

29

Unit 2, 0010, Lead Method 29 3 240 0

29

Unit 2, 0010, Manganese Method 29 3 240 0

29

Unit 2, 0010, Selenium Method 29 3 240 0

29

Unit 2, 0010, Cadmium Method 29 3 240 0

29

Unit 2, 27, 28 Filterable PM2.5 OTM - 27/28 0

Unit 2, 27, 28 Total PM2.5 OTM - 27/28 0

Unit 2 Carbon Monoxide Method 10 3 120 0

Total organic compounds 

(TOC) as Propane

Unit 2 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

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