Name: John M. McManus

Title: Vice-President, Environmental Service

Company: American Electric Power

Sign Date: 7/29/2010

Name: Scott W. Banach

Title: Director, Project Engineering

Company: Platt Environmental Services, Inc.

Sign Date: 7/28/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Cardinal Unit 3

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.

Tuesday, January 18, 2011 Page 1 of 18
Cardinal Unit 3

7/29/2010

Facility Information:

Cardinal Plant Unit 3

306 County Road 7 East

Brilliant OH 43913

Contact: Paul Jackson

Phone: 614-716-3278

Fax: 614-716-1252

Email: pmjackson@aep.com

Testing Company:

Platt Environmental Services, Inc.

1520 Kensington Road

Suite 204

Oak Brook IL 60523

Contact: Scott Banach

Phone: 630-521-9400

Fax: 630-521-9494

Email: sbanach@plattenv.com

Air Permit Number:

06-41-05-0002

Permitted Source ID/Name:

Unit 3 Boiler 3

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

Electric generating dry bottom boiler utilizing bituminous coal as the primary fuel.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description 10100202 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (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 0 222 144 0 66 157.2 6 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Carbon Monoxide Method 10 3 0

Total organic compounds 

(TOC)

Stack Method 25A 3 0

Stack Hydrogen Fluoride Method 26A 3 0

Stack Hydrogen Chloride Method 26A 3 0

Stack Total PM2.5 OTM - 27/28 3 0

Stack Filterable PM2.5 OTM - 27/28 3 0

Stack Filterable Particulate OTM - 27/28 3 0

Tuesday, January 18, 2011 Page 2 of 18
Cardinal Unit 3

7/29/2010

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.

Stack Total Particulate OTM - 27/28 3 0

Stack Selenium Method 29 3 0

Stack Antimony Method 29 3 0

Stack Arsenic Method 29 3 0

Stack Beryllium Method 29 3 0

Stack Cadmium Method 29 3 0

Stack Chromium Method 29 3 0

Stack Cobalt Method 29 3 0

Stack Lead Method 29 3 0

Stack Nickel Method 29 3 0

Stack Filterable Particulate Method 29 3 0

Stack Manganese Method 29 3 0

Stack Co2 Method 3A CO2 3 60 0

Stack O2 Method 3A O2 3 60 0

Tuesday, January 18, 2011 Page 3 of 18
Cardinal Unit 3

7/29/2010

Sampling / Stack Data Results Summary

Location Stack - 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 - 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

Tuesday, January 18, 2011 Page 4 of 18
Cardinal Unit 3

7/29/2010

Location Stack - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 5/18/2010 5/19/2010 5/19/2010

Run Start Time 11:35:00 AM 11:35:00 

AM

1:25:00 PM

Run Finish Time 2:47:00 PM 2:47:00 PM 4:37:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 87.933 93.373 90.086 90.464

Moisture Content of Stack Gas, % 7.09 6.98 8.77 7.613

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 11 11 11 11.000

Oxygen, % 8.3 8.3 8.3 8.300

Average Stack Gas Temperature, °F 293.63 285.67 306.54 295.280

Dry Volumetric Flow Rate, dry scfm 840,583.1 891,750.8 845,267.8 859,200.567

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,353,312.0 1,418,846.4 1,409,655.6 1,393,938.00

0

Percent Isokinetic of Sampling Rate, % 98.5 98.6 100.3 99.133

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - 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

Tuesday, January 18, 2011 Page 5 of 18
Cardinal Unit 3

7/29/2010

Location Stack - Method 3A CO2

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 - Method 3A O2

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

Tuesday, January 18, 2011 Page 6 of 18
Cardinal Unit 3

7/29/2010

Location Stack - 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

Tuesday, January 18, 2011 Page 7 of 18
Cardinal Unit 3

7/29/2010

Emissions Summary

Location: Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 2.86E-02 3.58E-02 1.94E-02 0.028

ppm 2.37E+01 2.99E+01 1.62E+01 23.267

ppm@7%O2 2.68E+01 3.35E+01 1.82E+01 26.167

Location: Stack - Method 25A

Compound: Total organic compounds (TOC)

Average

Run 1 2 3

lb/mmBtuO2 9.03E-05 9.31E-05 9.37E-05 0.000

ppm 1.74E-01 1.81E-01 1.82E-01 0.179

ppm@7%O2 1.97E-01 2.03E-01 2.04E-01 0.201

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 84.33611 86.98896 90.16213 87.162

lb/mmBtuO2 3.43E-02 3.33E-02 3.58E-02 0.034

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 8.0322 8.32068 7.44818 7.934

lb/mmBtuO2 3.27E-03 3.19E-03 2.96E-03 0.003

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.001378 0.001385 0.001388 0.001

lb/mmBtuO2 4.01E-07 4.05E-07 4.10E-07 0.000

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.002219 0.002476 0.003689 0.003

lb/mmBtuO2 6.45E-07 7.24E-07 1.09E-06 0.000

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.000359 0.000421 0.000454 0.000

lb/mmBtuO2 1.04E-07 1.23E-07 1.34E-07 0.000

Tuesday, January 18, 2011 Page 8 of 18
Cardinal Unit 3

7/29/2010

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.000534 0.000346 0.000347 0.000

lb/mmBtuO2 1.55E-07 1.01E-07 1.02E-07 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.012291 0.007193 0.014199 0.011

lb/mmBtuO2 3.57E-06 2.10E-06 4.19E-06 0.000

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.000878 0.000961 0.00111 0.001

lb/mmBtuO2 2.55E-07 2.81E-07 3.28E-07 0.000

Compound: Filterable Particulate

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 49 41.1 137.6 75.900

lb/mmBtuO2 1.42E-02 1.20E-02 4.06E-02 0.022

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.002012 0.002182 0.002995 0.002

lb/mmBtuO2 5.85E-07 6.38E-07 8.84E-07 0.000

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.008502 0.00648 0.007386 0.007

lb/mmBtuO2 2.47E-06 1.89E-06 2.18E-06 0.000

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.013864 0.007501 0.017428 0.013

lb/mmBtuO2 4.03E-06 2.19E-06 5.14E-06 0.000

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.165394 0.21009 0.298933 0.225

lb/mmBtuO2 4.81E-05 6.14E-05 8.82E-05 0.000

Location: Stack - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 42.2 47.1 58.3 49.200

Tuesday, January 18, 2011 Page 9 of 18
Cardinal Unit 3

7/29/2010

Process Run Data

Compound: Filterable PM2.5

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 32.9 33.5 36.7 34.367

Compound: Total Particulate

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 117.4 109.7 123.3 116.800

Compound: Total PM2.5

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 108.1 96.1 101.7 101.967

Tuesday, January 18, 2011 Page 10 of 18
Cardinal Unit 3

7/29/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 80 Tons/hr 80

1 Air Flow 60 SCFM 60

1 Gross Load 667 MW 650

1 Opacity 1.5 % 20

2 Bituminous Coal Burned 80 Tons/hr 80

2 Air Flow 60 SCFM 60

2 Gross Load 667 MW 650

2 Opacity 1.5 % 20

3 Bituminous Coal Burned 80 Tons/hr 80

3 Air Flow 60 SCFM 60

3 Gross Load 667 MW 650

3 Opacity 1.5 % 20

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

1.5 opacity 20

2 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

1.5 opacity 20

3 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

1.5 opacity 20

1 SCR (SELECTIVE CATALYTIC REDUCTION) 0.25 lb/mmBTU 1

2 SCR (SELECTIVE CATALYTIC REDUCTION) 0.25 lb/mmBTU 1

3 SCR (SELECTIVE CATALYTIC REDUCTION) 0.25 lb/mmBTU 1

Tuesday, January 18, 2011 Page 11 of 18
Cardinal Unit 3

7/29/2010

Sampling / Stack Data Results Detail

Location Stack - 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

Tuesday, January 18, 2011 Page 12 of 18
Cardinal Unit 3

7/29/2010

Location Stack - 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

Tuesday, January 18, 2011 Page 13 of 18
Cardinal Unit 3

7/29/2010

Location Stack - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 5/18/2010 5/19/2010 5/19/2010

Run Start Time 11:35:00 AM 11:35:00 AM 1:25:00 PM

Run Finish Time 2:47:00 PM 2:47:00 PM 4:37:00 PM

Net Traversing Points 28 28 28

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.155 0.155 0.155 0.155

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.007 1.007 1.007 1.007

Barometric Pressure, inches of Mercury 28.7 28.7 28.7 28.700

Average Orifice Meter Differential, inches H2O 0.79 0.88 0.82 0.830

Dry Gas Meter Volume Sampled, cubic feet 94.291 99.469 97.800 97.187

Average Dry Gas Meter Temperature, °F 88.00 84.54 94.85 89.130

Dry Gas Meter Volume Sampled, dscf 87.933 93.373 90.086 90.464

Total Moisture Liquid collected, g 142.6 149 184 158.533

Volume of Water Vapor, standard cubic feet 6.71 7.01 8.66 7.460

Moisture Content of Stack Gas, % 7.09 6.98 8.77 7.613

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.9291 0.9302 0.9123 0.924

Carbon Dioxide, % 11 11 11 11.000

Oxygen, % 8.3 8.3 8.3 8.300

Carbon Monoxide & Nitrogen, % 80.7 80.7 80.7 80.700

Fuel Factor 1.15 1.15 1.15

Dry Molecular Weight, lb/lb-Mole 30.09 30.09 30.09 30.090

Wet Molecular weight, lb/lb-Mole 29.23 29.25 29.03 29.170

Flue Gas Static Pressure, inches of H2O -2 -2 -2 -2.000

Absolute Flue Gas Pressure, inches of Mercury 28.55 28.55 28.55 28.550

Average Stack Gas Temperature, °F 293.63 285.67 306.54 295.280

Average Velocity Head, inches of H2O 2.2164732395

8423

2.464081951

97114

2.348453882

19802

2.343

Average Stack Gas Velocity, feet/second 101.60 106.52 105.83 104.650

Stack Cross-Sectional Area, square feet 222.000 222.000 222.000 222.000

Dry Volumetric Flow Rate, dry scfm 840,583.1 891,750.8 845,267.8 859,200.567

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,353,312.0 1,418,846.4 1,409,655.6 1,393,938.0

00

Percent Isokinetic of Sampling Rate, % 98.5 98.6 100.3 99.133

Percent Excess Air, % 63.8 63.8 63.8 63.800

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 144 144 144

Rectangular Duct Length, inches 222 222 222

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, January 18, 2011 Page 14 of 18
Cardinal Unit 3

7/29/2010

Location Stack - 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

Tuesday, January 18, 2011 Page 15 of 18
Cardinal Unit 3

7/29/2010

Location Stack - Method 3A CO2

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

Tuesday, January 18, 2011 Page 16 of 18
Cardinal Unit 3

7/29/2010

Location Stack - Method 3A O2

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

Tuesday, January 18, 2011 Page 17 of 18
Cardinal Unit 3

7/29/2010

Location Stack - 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

Tuesday, January 18, 2011 Page 18 of 18