Name: Jason Wilkerson

Title: Senior Environmental Engineer

Company: EON-US

Sign Date: 8/31/2010

Name: Mike Taylor

Title: President

Company: Catalyst Air Management

Sign Date: 8/31/2010

Permitted Facility Representative / Date Testing Company Representative / Date

KY 1363 Cane Run 5

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, February 12, 2011 Page 1 of 13
KY 1363 Cane Run 5

8/31/2010

Facility Information:

KY1363 Cane Run 5

5252 Cane Run Rd.

Louisville KY 40216

Contact: Jason Wilkerson

Phone: 502-627-4043

Fax: 502-627-2550

Email: jason.wilkerson@eon-us.com

Testing Company:

Catalyst Air Management, Inc.

2505 Byington-Solway Rd

Knoxville TN 37931

Contact:Mike Taylor

Phone: 865-531-0075

Fax: 865-531-0750

Email: mike.taylor@catalystair.com

Air Permit Number:

1363

Permitted Source ID/Name:

5 LG&E Cane Run Generating Station

Permitted Maximum Process Rate: Max. Normal Operation Process Rate: Target Process Test Rate

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

 process flow diagram:

Cane Run Unit 5 is a wall-fired, utility boiler that combusts bituminous coal. The unit is equipped with an 

electrostatic precipitator (ESP) for particulate matter (PM) control and a flue gas desulfurization (FGD) system for 

SO2 control.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 2111100126 FRS #: 110000378537

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

KY1363 CR5 186.7 0 0 734 982 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

KY1363 CR5 Lead Method 29 3 240 0

KY1363 CR5 Selenium Method 29 3 240 0

KY1363 CR5 Manganese Method 29 3 240 0

KY1363 CR5 Mercury Method 29 3 240 0

KY1363 CR5 Antimony Method 29 3 240 0

KY1363 CR5 Arsenic Method 29 3 240 0

KY1363 CR5 Cobalt Method 29 3 240 0

Saturday, February 12, 2011 Page 2 of 13
KY 1363 Cane Run 5

8/31/2010

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.

KY1363 CR5 Chromium Method 29 3 240 0

KY1363 CR5 Beryllium Method 29 3 240 0

KY1363 CR5 Cadmium Method 29 3 240 0

KY1363 CR5 Nickel Method 29 3 240 0

KY1363 CR5 Co2 Method 3A CO2 3 240 0

KY1363 CR5 O2 Method 3A O2 3 240 0

Inorganic (Aqueous) 

Condensible Part.

KY1363 CR5 Method 5/OTM-28 3 240 0

KY1363 CR5 Filterable Particulate Method 5/OTM-28 3 240 0

KY1363 CR5 Total Particulate Method 5/OTM-28 3 240 0

Organic Condensible 

Particulate

KY1363 CR5 Method 5/OTM-28 3 240 0

Saturday, February 12, 2011 Page 3 of 13
KY 1363 Cane Run 5

8/31/2010

Sampling / Stack Data Results Summary

Location KY1363 CR5 - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 5/19/2010 5/20/2010 5/20/2010

Run Start Time 1:38:00 PM 7:00:00 

AM

12:31:00 PM

Run Finish Time 6:02:00 PM 11:24:00 

AM

4:55:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 157.807 159.869 165.233 160.970

Moisture Content of Stack Gas, % 13.87 13.30 13.77 13.647

Moisture Saturation at Stack Gas Temperature, % 12.07 11.33 11.96 11.787

Carbon Dioxide, % 12.9 12.9 13 12.933

Oxygen, % 5.9 6 5.8 5.900

Average Stack Gas Temperature, °F 121.25 119.08 121.04 120.457

Dry Volumetric Flow Rate, dry scfm 359,813.4 352,201.6 372,362.3 361,459.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 456,732.3 440,192.3 470,306.5 455,743.700

Percent Isokinetic of Sampling Rate, % 101.9 105.5 103.1 103.500

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 KY1363 CR5 - Method 3A CO2

Average

Run Number CO2-1 CO2-2 CO2-3

Test Date 5/19/2010 5/20/2010 5/20/2010

Run Start Time 1:38:00 PM 7:00:00 

AM

12:31:00 PM

Run Finish Time 6:01:00 PM 11:23:00 

AM

4:54:00 PM

Carbon Dioxide, % 12.9 12.9 13 12.933

Oxygen, % 5.9 6 5.8 5.900

Dry Volumetric Flow Rate, dry scfm 359813 354347 374399 362,853.000

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

Moisture, % 12.1 11.3 12 11.800

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, February 12, 2011 Page 4 of 13
KY 1363 Cane Run 5

8/31/2010

Location KY1363 CR5 - Method 3A O2

Average

Run Number O2-1 O2-2 O2-3

Test Date 5/19/2010 5/20/2010 5/20/2010

Run Start Time 1:38:00 PM 7:00:00 

AM

12:31:00 PM

Run Finish Time 6:01:00 PM 11:23:00 

AM

4:54:00 PM

Carbon Dioxide, % 12.9 12.9 13 12.933

Oxygen, % 5.9 6 5.8 5.900

Dry Volumetric Flow Rate, dry scfm 359813 354347 374399 362,853.000

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

Moisture, % 12.1 11.3 12 11.800

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location KY1363 CR5 - Method 5/OTM-28

Average

Run Number OTM28-1 OTM28-2 OTM28-3

Test Date 5/19/2010 5/20/2010 5/20/2010

Run Start Time 1:38:00 PM 7:00:00 

AM

12:31:00 PM

Run Finish Time 6:02:00 PM 11:24:00 

AM

4:55:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 147.021 148.862 151.605 149.163

Moisture Content of Stack Gas, % 14.61 13.30 12.31 13.407

Moisture Saturation at Stack Gas Temperature, % 12.75 12.41 12.99 12.717

Carbon Dioxide, % 12.9 12.9 13 12.933

Oxygen, % 5.9 6 5.8 5.900

Average Stack Gas Temperature, °F 123.25 122.38 124.04 123.223

Dry Volumetric Flow Rate, dry scfm 367,394.3 370,000.5 373,935.7 370,443.500

Actual Wet Volumetric Flue Gas Flow Rate, acfm 471,447.2 470,648.7 476,466.2 472,854.033

Percent Isokinetic of Sampling Rate, % 93.0 93.5 94.2 93.567

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

Saturday, February 12, 2011 Page 5 of 13
KY 1363 Cane Run 5

8/31/2010

Emissions Summary

Location: KY1363 CR5 - Method 29

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.004 0.0043 0.0049 0.004

lb/mmBtuO2 7.61E-07 8.13E-07 8.85E-07 0.000

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.02357 0.03077 0.03367 0.029

lb/mmBtuO2 4.49E-06 5.82E-06 6.08E-06 0.000

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00133 0.00154 0.00175 0.002

lb/mmBtuO2 2.53E-07 2.91E-07 3.16E-07 0.000

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.001 0.001 0.00096 0.001

lb/mmBtuO2 1.90E-07 1.89E-07 1.73E-07 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00797 0.00937 0.00958 0.009

lb/mmBtuO2 1.52E-06 1.77E-06 1.73E-06 0.000

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00178 0.00242 0.00239 0.002

lb/mmBtuO2 3.39E-07 4.58E-07 4.32E-07 0.000

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.01923 0.07903 0.02933 0.043

lb/mmBtuO2 3.66E-06 1.50E-05 5.30E-06 0.000

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0065 0.00913 0.008 0.008

lb/mmBtuO2 1.24E-06 1.73E-06 1.44E-06 0.000

Compound: Mercury

Average

Saturday, February 12, 2011 Page 6 of 13
KY 1363 Cane Run 5

8/31/2010

Process Run Data

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00764 0.00854 0.0103 0.009

lb/mmBtuO2 1.45E-06 1.62E-06 1.86E-06 0.000

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0113 0.014 0.0135 0.013

lb/mmBtuO2 2.15E-06 2.65E-06 2.44E-06 0.000

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0889 0.0861 0.0921 0.089

lb/mmBtuO2 1.69E-05 1.63E-05 1.66E-05 0.000

Location: KY1363 CR5 - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber OTM28-1 OTM28-2 OTM28-3

Mass_mg 40.5 47.3 80.7 56.167

lb/mmBtuO2 8.28E-03 9.61E-03 1.59E-02 0.011

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber OTM28-1 OTM28-2 OTM28-3

Mass_mg 32 97 51 60.000

lb/mmBtuO2 6.54E-03 1.97E-02 1.00E-02 0.012

Compound: Organic Condensible Particulate

Average

RunNumber OTM28-1 OTM28-2 OTM28-3

Mass_mg 1.3 3.8 7.2 4.100

lb/mmBtuO2 2.66E-04 7.72E-04 1.42E-03 0.001

Compound: Total Particulate

Average

RunNumber OTM28-1 OTM28-2 OTM28-3

Mass_mg 73.8 148.1 138.9 120.267

lb/mmBtuO2 1.51E-02 3.01E-02 2.73E-02 0.024

Saturday, February 12, 2011 Page 7 of 13
KY 1363 Cane Run 5

8/31/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input Million Btus/million BTU using O2 1881.3 Cane Run 5, 

Methods 5, OTM28, and 29, Run 1, 

5/19/2010, 

1:38PM-6:02PM

1 Steam Rate 1105.9 1000 lbs/hr Cane Run 5, 

Methods 5, OTM28, and 29, Run 1, 

5/19/2010, 

1:38PM-6:02PM

1 Fuel Rate 151791 lb/hr Cane Run 5, 

Methods 5, OTM28, and 29, Run 1, 

5/19/2010, 

1:38PM-6:02PM

1 Unit Load 174 MW Cane Run 5, 

Methods 5, OTM28, and 29, Run 1, 

5/19/2010, 

1:38PM-6:02PM

2 Heat Input Million Btus/million BTU using O2 1895.8 Cane Run 5, 

Methods 5, OTM28, and 29, Run 2, 

5/20/2010, 

7:00AM-11:24AM

2 Steam Rate 1108.7 1000 lbs/hr Cane Run 5, 

Methods 5, OTM28, and 29, Run 2, 

5/20/2010, 

7:00AM-11:24AM

2 Fuel Rate 154695 lb/hr Cane Run 5, 

Methods 5, OTM28, and 29, Run 2, 

5/20/2010, 

7:00AM-11:24AM

2 Unit Load 175.8 MW Cane Run 5, 

Methods 5, OTM28, and 29, Run 2, 

5/20/2010, 

7:00AM-11:24AM

3 Heat Input Million Btus/million BTU using O2 1895.5 Cane Run 5, 

Methods 5, OTM28, and 29, Run 3, 

5/20/2010, 

12:31PM-4:55PM

Saturday, February 12, 2011 Page 8 of 13
KY 1363 Cane Run 5

8/31/2010

APCD Run Data

Process Lab Run Data

3 Steam Rate 1144.6 1000 lbs/hr Cane Run 5, 

Methods 5, OTM28, and 29, Run 3, 

5/20/2010, 

12:31PM-4:55PM

3 Fuel Rate 158730 lb/hr Cane Run 5, 

Methods 5, OTM28, and 29, Run 3, 

5/20/2010, 

12:31PM-4:55PM

3 Unit Load 181 MW Cane Run 5, 

Methods 5, OTM28, and 29, Run 3, 

5/20/2010, 

12:31PM-4:55PM

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 250.1 Volts

2 ELECTROSTATIC PRECIPITATOR 237.3 Volts

3 ELECTROSTATIC PRECIPITATOR 241.2 Volts

1 WET SCRUBBER 50.4 GPM

2 WET SCRUBBER 53.1 GPM

3 WET SCRUBBER 59.6 GPM

Saturday, February 12, 2011 Page 9 of 13
KY 1363 Cane Run 5

8/31/2010

Sampling / Stack Data Results Detail

Location KY1363 CR5 - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 5/19/2010 5/20/2010 5/20/2010

Run Start Time 1:38:00 PM 7:00:00 AM 12:31:00 PM

Run Finish Time 6:02:00 PM 11:24:00 AM 4:55:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.25 0.25 0.25 0.250

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.01 1.01 1.01 1.010

Barometric Pressure, inches of Mercury 29.55 29.65 29.65 29.617

Average Orifice Meter Differential, inches H2O 1.24 1.17 1.31 1.240

Dry Gas Meter Volume Sampled, cubic feet 162.694 158.894 166.774 162.787

Average Dry Gas Meter Temperature, °F 84.67 66.77 75.13 75.523

Dry Gas Meter Volume Sampled, dscf 157.807 159.869 165.233 160.970

Total Moisture Liquid collected, g 539.8 521.1 560.7 540.533

Volume of Water Vapor, standard cubic feet 25.41 24.53 26.39 25.443

Moisture Content of Stack Gas, % 13.87 13.30 13.77 13.647

Moisture Saturation at Stack Gas Temperature, % 12.07 11.33 11.96 11.787

Dry Mole Fraction 0.8793 0.8867 0.8804 0.882

Carbon Dioxide, % 12.9 12.9 13 12.933

Oxygen, % 5.9 6 5.8 5.900

Carbon Monoxide & Nitrogen, % 81.2 81.1 81.2 81.167

Fuel Factor 1.16 1.16 1.16

Dry Molecular Weight, lb/lb-Mole 30.30 30.30 30.31 30.303

Wet Molecular weight, lb/lb-Mole 29.14 29.26 29.16 29.187

Flue Gas Static Pressure, inches of H2O -0.5 -0.5 -0.5 -0.500

Absolute Flue Gas Pressure, inches of Mercury 29.51 29.61 29.61 29.577

Average Stack Gas Temperature, °F 121.25 119.08 121.04 120.457

Average Velocity Head, inches of H2O 0.4600219243

45084

0.432053663

232999

0.489742985

952202

0.461

Average Stack Gas Velocity, feet/second 40.04 38.59 41.23 39.953

Stack Cross-Sectional Area, square feet 190.115 190.115 190.115 190.115

Dry Volumetric Flow Rate, dry scfm 359,813.4 352,201.6 372,362.3 361,459.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 456,732.3 440,192.3 470,306.5 455,743.700

Percent Isokinetic of Sampling Rate, % 101.9 105.5 103.1 103.500

Percent Excess Air, % 38.0 38.9 37.1 38.000

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

Round Duct Diameter, inches 186.7 186.7 186.7

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, February 12, 2011 Page 10 of 13
KY 1363 Cane Run 5

8/31/2010

Location KY1363 CR5 - Method 3A CO2

Average

Run Number CO2-1 CO2-2 CO2-3

Test Date 5/19/2010 5/20/2010 5/20/2010

Run Start Time 1:38:00 PM 7:00:00 AM 12:31:00 PM

Run Finish Time 6:01:00 PM 11:23:00 AM 4:54:00 PM

Carbon Dioxide, % 12.9 12.9 13 12.933

Oxygen, % 5.9 6 5.8 5.900

Fuel Factor 1.16 1.16 1.16

Dry Volumetric Flow Rate, dry scfm 359813 354347 374399 362,853.000

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

Moisture, % 12.1 11.3 12 11.800

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1440 1440 1440 1,440.000

Analyzer Serial Number 01415C/292 01415C/292 01415C/292

Operating Range 20 20 20 20.000

Operating Units % % %

No. Readings/Avg. 60 60 60 60.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID CC179696 CC179696 CC179696

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC86060-CO2 CC86060-

CO2

CC86060-

CO2

Calibration Pre High Cylinder Instrument Response 16.51 16.55 16.47 16.510

Calibration Pre High Cylinder Bias -0.18 0.06 -0.42 -0.180

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC179696 CC179696 CC179696

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID CC86060-CO2 CC86060-

CO2

CC86060-

CO2

Calibration Post High Cylinder Instrument Response 16.55 16.47 16.53 16.517

Calibration Post High Cylinder Bias 0.06 -0.42 -0.06 -0.140

Calibration Post High Cylinder Drift 0.24 0.48 0.36 0.360

Cavg 12.77 12.73 12.84 12.780

Cavg Units %vd %vd %vd

Cgas 12.8859 12.8611 12.9801 12.909

Cgas Units %vd %vd %vd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Saturday, February 12, 2011 Page 11 of 13
KY 1363 Cane Run 5

8/31/2010

Location KY1363 CR5 - Method 3A O2

Average

Run Number O2-1 O2-2 O2-3

Test Date 5/19/2010 5/20/2010 5/20/2010

Run Start Time 1:38:00 PM 7:00:00 AM 12:31:00 PM

Run Finish Time 6:01:00 PM 11:23:00 AM 4:54:00 PM

Carbon Dioxide, % 12.9 12.9 13 12.933

Oxygen, % 5.9 6 5.8 5.900

Fuel Factor 1.16 1.16 1.16

Dry Volumetric Flow Rate, dry scfm 359813 354347 374399 362,853.000

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

Moisture, % 12.1 11.3 12 11.800

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1440 1440 1440 1,440.000

Analyzer Serial Number 28203951-

5395

28203951-

5395

28203951-

5395

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 60 60 60 60.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID CC179696 CC179696 CC179696

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC86060-O2 CC86060-O2 CC86060-O2

Calibration Pre High Cylinder Instrument Response 21.9 21.81 21.69 21.800

Calibration Pre High Cylinder Bias -0.23 -0.64 -1.18 -0.683

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC179696 CC179696 CC179696

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID CC86060-O2 CC86060-O2 CC86060-O2

Calibration Post High Cylinder Instrument Response 21.81 21.69 21.7 21.733

Calibration Post High Cylinder Bias -0.64 -1.18 -1.14 -0.987

Calibration Post High Cylinder Drift 0.41 0.54 0.04 0.330

Cavg 5.89 5.95 5.73 5.857

Cavg Units %vd %vd %vd

Cgas 5.9345 6.0239 5.8158 5.925

Cgas Units %vd %vd %vd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Saturday, February 12, 2011 Page 12 of 13
KY 1363 Cane Run 5

8/31/2010

Location KY1363 CR5 - Method 5/OTM-28

Average

Run Number OTM28-1 OTM28-2 OTM28-3

Test Date 5/19/2010 5/20/2010 5/20/2010

Run Start Time 1:38:00 PM 7:00:00 AM 12:31:00 PM

Run Finish Time 6:02:00 PM 11:24:00 AM 4:55:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.25 0.25 0.25 0.250

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.99 0.99 0.99 0.990

Barometric Pressure, inches of Mercury 29.55 29.65 29.65 29.617

Average Orifice Meter Differential, inches H2O 1.33 1.31 1.34 1.327

Dry Gas Meter Volume Sampled, cubic feet 151.845 150.908 154.990 152.581

Average Dry Gas Meter Temperature, °F 74.96 66.83 71.33 71.040

Dry Gas Meter Volume Sampled, dscf 147.021 148.862 151.605 149.163

Total Moisture Liquid collected, g 534.3 485 452.1 490.467

Volume of Water Vapor, standard cubic feet 25.15 22.83 21.28 23.087

Moisture Content of Stack Gas, % 14.61 13.30 12.31 13.407

Moisture Saturation at Stack Gas Temperature, % 12.75 12.41 12.99 12.717

Dry Mole Fraction 0.8725 0.8759 0.8769 0.875

Carbon Dioxide, % 12.9 12.9 13 12.933

Oxygen, % 5.9 6 5.8 5.900

Carbon Monoxide & Nitrogen, % 81.2 81.1 81.2 81.167

Fuel Factor 1.16 1.16 1.16

Dry Molecular Weight, lb/lb-Mole 30.30 30.30 30.31 30.303

Wet Molecular weight, lb/lb-Mole 29.07 28.93 28.79 28.930

Flue Gas Static Pressure, inches of H2O -0.45 -0.42 -0.42 -0.430

Absolute Flue Gas Pressure, inches of Mercury 29.52 29.62 29.62 29.587

Average Stack Gas Temperature, °F 123.25 122.38 124.04 123.223

Average Velocity Head, inches of H2O 0.4874452920

69173

0.485803433

9495

0.494089497

944822

0.489

Average Stack Gas Velocity, feet/second 41.33 41.26 41.77 41.453

Stack Cross-Sectional Area, square feet 190.115 190.115 190.115 190.115

Dry Volumetric Flow Rate, dry scfm 367,394.3 370,000.5 373,935.7 370,443.500

Actual Wet Volumetric Flue Gas Flow Rate, acfm 471,447.2 470,648.7 476,466.2 472,854.033

Percent Isokinetic of Sampling Rate, % 93.0 93.5 94.2 93.567

Percent Excess Air, % 38.0 38.9 37.1 38.000

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

Round Duct Diameter, inches 186.7 186.7 186.7

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, February 12, 2011 Page 13 of 13