Name: Jason McLaurin

Title: Environmental Coordinator

Company: Southern Illinois Power

Sign Date: 8/30/2010

Name: Chet Gutwein

Title: Engineer

Company: Airtech Environmental Services Inc.

Sign Date: 8/30/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Marion Generating Station Boiler 123

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.

Thursday, February 03, 2011 Page 1 of 24
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Facility Information:

Marion Generating Station

11543 LAKE OF EGYPT ROAD

Marion IL 62959

Contact: Jason McLaurin

Phone: (618) 964-1448

Fax: (618) 964-1867

Email: jmclaurin@sipower.org

Testing Company:

Airtech Environmental Services Inc.

601A Country Club Drive

Bensenville IL 60106

Contact:Jim Christ

Phone: (630) 860-4740

Fax: (630) 860-4745

Email: jchrist@airtechenv.com

Air Permit Number:

976

Permitted Source ID/Name:

B123

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:

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 1719900020 FRS #: 110017420049

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 Exit 114 0 0 114 9.17 5.26 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 120 0

Stack Exit Carbon Monoxide Method 10 3 120 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Chlorine Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Filterable PM2.5 OTM - 27/28 3 240 0

Thursday, February 03, 2011 Page 2 of 24
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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.

The following is a list of the test methods that are to be used for this test program and their respective promulgation 

dates:

Methods 1 through 29 – August 1997

Other Test Methods 27 and 28 – April 2009

Stack Exit Total PM2.5 OTM - 27/28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 240 0

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Sulfur Dioxide Method 6C 3 120 0

Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0

Thursday, February 03, 2011 Page 3 of 24
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Sampling / Stack Data Results Summary

Location Stack Exit - Method 1 - 4

Average

Run Number 1 2 3

Test Date 6/9/2010 6/10/2010 6/11/2010

Run Start Time 1:45:00 PM 6:04:00 

AM

5:49:00 AM

Run Finish Time 4:05:00 PM 8:27:00 

AM

8:03:00 AM

Net Run Time, minutes 210 120 120

Dry Gas Meter Volume Sampled, dscf 83.811 74.116 75.388 77.772

Moisture Content of Stack Gas, % 6.70 7.55 7.13 7.127

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

Carbon Dioxide, % 14.3 14.9 14.7 14.633

Oxygen, % 5.15 4.79 5.15 5.030

Average Stack Gas Temperature, °F 344.67 342.75 334.83 340.750

Dry Volumetric Flow Rate, dry scfm 303,907.1 292,498.1 296,294.1 297,566.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 496,911.2 480,537.4 480,112.1 485,853.567

Percent Isokinetic of Sampling Rate, % 59.1 97.2 101.2 85.833

F-Factor, dscfm/MMBtu @ %O2 10348 10382 10009 10,246.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - 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

Thursday, February 03, 2011 Page 4 of 24
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Location Stack Exit - 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

Location Stack Exit - Method 26A

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

Thursday, February 03, 2011 Page 5 of 24
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Location Stack Exit - 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 Stack Exit - 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

Thursday, February 03, 2011 Page 6 of 24
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Location Stack Exit - Method 6C 3

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 Exit - 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

Thursday, February 03, 2011 Page 7 of 24
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Location Stack Exit - 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

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Emissions Summary

Location: Stack Exit - Method 1 - 4

Compound: % H2O

Average

RunNumber 1 2 3

Mass_mg 128000 128600 123000 126,533.333

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 8.29E+01 7.56E+01 7.67E+02 308.500

lb/mmBtuO2 6.25E-02 5.80E-02 5.73E-02 0.059

ppm 6.26E+01 5.93E+01 5.93E+01 60.400

ppm@7%O2 5.52E+01 5.12E+01 5.23E+01 52.900

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 1.41E+00 1.09E+00 1.10E+00 1.200

lb/mmBtuO2 1.03E-03 8.36E-04 8.20E-04 0.001

ppm 7.02E-01 5.42E-01 5.39E-01 0.594

ppm@7%O2 6.06E-01 4.68E-01 4.76E-01 0.517

Location: Stack Exit - Method 26A

Compound: Chlorine

Average

RunNumber 1 2 3

Mass_mg 89.872 64.974 77.184 77.343

lb/mmBtuO2 2.32E-02 1.79E-02 1.96E-02 0.020

mg/dscm 2.71E+01 2.12E+01 2.37E+01 24.000

mg/dscm@7%O2 2.39E+01 1.83E+01 2.09E+01 21.033

ppm 9.20E+00 7.21E+00 8.02E+00 8.143

ppm@7%O2 8.10E+00 6.22E+00 7.06E+00 7.127

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 92.7 66.6 79.4 79.567

lb/mmBtuO2 2.39E-02 1.83E-02 2.01E-02 0.021

mg/dscm 2.80E+01 2.18E+01 2.43E+01 24.700

mg/dscm@7%O2 2.47E+01 1.88E+01 2.14E+01 21.633

ppm 1.85E+01 1.44E+01 1.61E+01 16.333

ppm@7%O2 1.63E+01 1.24E+01 1.42E+01 14.300

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.376 0.374 0.368 0.373

lb/mmBtuO2 9.71E-05 1.03E-04 9.33E-05 0.000

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mg/dscm 1.14E-01 1.22E-01 1.13E-01 0.116

mg/dscm@7%O2 1.00E-01 1.05E-01 9.95E-02 0.102

ppm 1.36E-01 1.47E-01 1.36E-01 0.140

ppm@7%O2 1.20E-01 1.27E-01 1.20E-01 0.122

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000798 0.000783 0.001197 0.001

lb/mmBtuO2 1.41E-07 1.53E-07 2.43E-07 0.000

mg/dscm 1.78E-04 1.80E-04 2.84E-04 0.000

mg/dscm@7%O2 1.53E-04 1.57E-04 2.50E-04 0.000

ppm 3.51E-05 3.56E-05 5.62E-05 0.000

ppm@7%O2 3.01E-05 3.11E-05 4.94E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.004893 0.008843 0.010473 0.008

lb/mmBtuO2 8.64E-07 1.73E-06 2.13E-06 0.000

mg/dscm 1.09E-03 2.04E-03 2.49E-03 0.002

mg/dscm@7%O2 9.34E-04 1.78E-03 2.19E-03 0.002

ppm 3.50E-04 6.54E-04 7.99E-04 0.001

ppm@7%O2 3.00E-04 5.71E-04 7.02E-04 0.001

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000733 0.00104 0.00233 0.001

lb/mmBtuO2 1.29E-07 2.03E-07 4.74E-07 0.000

mg/dscm 1.63E-04 2.40E-04 5.54E-04 0.000

mg/dscm@7%O2 1.40E-04 2.10E-04 4.87E-04 0.000

ppm 4.36E-04 6.39E-04 1.48E-03 0.001

ppm@7%O2 3.74E-04 5.58E-04 1.30E-03 0.001

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.002535 0.001705 0.002445 0.002

lb/mmBtuO2 4.47E-07 3.33E-07 4.97E-07 0.000

mg/dscm 5.64E-04 3.93E-04 5.81E-04 0.001

mg/dscm@7%O2 4.83E-04 3.43E-04 5.10E-04 0.000

ppm 1.21E-04 8.40E-05 1.24E-04 0.000

ppm@7%O2 1.04E-04 7.34E-05 1.09E-04 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.01757 0.02357 0.03507 0.025

lb/mmBtuO2 3.10E-06 4.61E-06 7.13E-06 0.000

mg/dscm 3.91E-03 5.43E-03 8.33E-03 0.006

mg/dscm@7%O2 3.35E-03 4.74E-03 7.32E-03 0.005

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ppm 1.81E-03 2.51E-03 3.85E-03 0.003

ppm@7%O2 1.55E-03 2.19E-03 3.38E-03 0.002

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.003418 0.005538 0.008608 0.006

lb/mmBtuO2 6.03E-07 1.08E-06 1.75E-06 0.000

mg/dscm 7.61E-04 1.28E-03 2.05E-03 0.001

mg/dscm@7%O2 6.52E-04 1.12E-03 1.80E-03 0.001

ppm 3.11E-04 5.21E-04 8.35E-04 0.001

ppm@7%O2 2.67E-04 4.55E-04 7.34E-04 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.020503 0.030603 0.0316 0.028

lb/mmBtuO2 3.62E-06 5.98E-06 6.43E-06 0.000

mg/dscm 4.56E-03 7.05E-03 7.51E-03 0.006

mg/dscm@7%O2 3.91E-03 6.16E-03 6.60E-03 0.006

ppm 5.30E-04 8.18E-04 8.71E-04 0.001

ppm@7%O2 4.54E-04 7.15E-04 7.65E-04 0.001

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.05982 0.09922 0.17122 0.110

lb/mmBtuO2 1.06E-05 1.94E-05 3.48E-05 0.000

mg/dscm 1.33E-02 2.29E-02 4.07E-02 0.026

mg/dscm@7%O2 1.14E-02 2.00E-02 3.58E-02 0.022

ppm 5.83E-03 1.00E-02 1.78E-02 0.011

ppm@7%O2 5.00E-03 8.74E-03 1.56E-02 0.010

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.01075 0.01675 0.02855 0.019

lb/mmBtuO2 1.90E-06 3.27E-06 5.81E-06 0.000

mg/dscm 2.39E-03 3.86E-03 6.78E-03 0.004

mg/dscm@7%O2 2.05E-03 3.37E-03 5.96E-03 0.004

ppm 9.80E-04 1.58E-03 2.78E-03 0.002

ppm@7%O2 8.40E-04 1.38E-03 2.44E-03 0.002

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.00221 0.00283 0.00545 0.003

lb/mmBtuO2 3.90E-07 5.53E-07 1.11E-06 0.000

mg/dscm 4.92E-04 6.52E-04 1.29E-03 0.001

mg/dscm@7%O2 4.22E-04 5.70E-04 1.13E-03 0.001

ppm 1.50E-04 1.99E-04 3.94E-04 0.000

ppm@7%O2 1.29E-04 1.74E-04 3.46E-04 0.000

Location: Stack Exit - Method 6C

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Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 5.51E+02 6.88E+02 6.70E+02 636.333

lb/mmBtuO2 4.15E-01 5.28E-01 5.01E-01 0.481

ppm 1.82E+02 2.36E+02 2.27E+02 215.000

ppm@7%O2 1.61E+02 2.04E+02 2.00E+02 188.333

Location: Stack Exit - Method 6C 3

Compound: Sulfur Dioxide

Average

Run 4 5 6

Elb/hr 5.41E+02 6.70E+02 6.79E+02 630.000

lb/mmBtuO2 4.07E-01 5.15E-01 5.07E-01 0.476

ppm 1.79E+02 2.30E+02 2.30E+02 213.000

ppm@7%O2 1.58E+02 1.98E+02 2.03E+02 186.333

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 1.25E+02 1.35E+02 1.21E+02 127.000

lb/mmBtuO2 9.43E-02 1.04E-01 9.00E-02 0.096

ppm 5.75E+01 6.46E+01 5.69E+01 59.667

ppm@7%O2 5.07E+01 5.58E+01 5.01E+01 52.200

Location: Stack Exit - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 28.7 19.9 16.2 21.600

Elb/hr 9.16E+00 6.45E+00 5.45E+00 7.020

lb/mmBtuO2 6.27E-03 4.72E-03 4.00E-03 0.005

mg/dscm 7.90E+00 5.57E+00 4.68E+00 6.050

mg/dscm@7%O2 6.77E+00 4.86E+00 4.10E+00 5.243

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 14.8 12.5 15.9 14.400

Elb/hr 4.72E+00 4.05E+00 5.35E+00 4.707

lb/mmBtuO2 3.23E-03 2.97E-03 3.93E-03 0.003

mg/dscm 4.07E+00 3.50E+00 4.60E+00 4.057

mg/dscm@7%O2 3.49E+00 3.06E+00 4.03E+00 3.527

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 44 87.2 101.1 77.433

Elb/hr 1.40E+01 2.83E+01 3.40E+01 25.433

lb/mmBtuO2 9.61E-03 2.07E-02 2.50E-02 0.018

mg/dscm 1.21E+01 2.44E+01 2.92E+01 21.900

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Process Run Data

mg/dscm@7%O2 1.04E+01 2.13E+01 2.56E+01 19.100

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 87.6 119.6 133.2 113.467

Elb/hr 2.80E+01 3.88E+01 4.48E+01 37.200

lb/mmBtuO2 1.91E-02 2.84E-02 3.29E-02 0.027

mg/dscm 2.41E+01 3.35E+01 3.85E+01 32.033

mg/dscm@7%O2 2.07E+01 2.92E+01 3.37E+01 27.867

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Process Run Data

APCD Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Firing Rate 1638 tons/day 1700

2 Coal Firing Rate 1772 tons/day 1700

3 Coal Firing Rate 1753 tons/day 1700

4 Coal Firing Rate 1683 tons/day 1700

1 Average Heat Input 1246 MMBtu/hr 1250

2 Average Heat Input 1262.8 MMBtu/hr 1250

3 Average Heat Input 1276 MMBtu/hr 1250

4 Average Heat Input 1279.5 MMBtu/hr 1250

1 Steam Output 994 1000 lb steam/hr 1000

2 Steam Output 992 1000 lb steam/hr 1000

3 Steam Output 991 1000 lb steam/hr 1000

4 Steam Output 991 1000 lb steam/hr 1000

1 Flue Gas Flow Rate 2E+07 dscfm 2E+07

2 Flue Gas Flow Rate 2E+07 dscfm 2E+07

3 Flue Gas Flow Rate 2E+07 dscfm 2E+07

4 Flue Gas Flow Rate 2E+07 dscfm 2E+07

1 Flue Gas Oxygen Content 5.2 % 5

2 Flue Gas Oxygen Content 5.1 % 5

3 Flue Gas Oxygen Content 4.9 % 5

4 Flue Gas Oxygen Content 5.1 % 5

1 Flue Gas Carbon Dioxide Content 14.1 % 14.5

2 Flue Gas Carbon Dioxide Content 14.3 % 14.5

3 Flue Gas Carbon Dioxide Content 14.5 % 14.5

4 Flue Gas Carbon Dioxide Content 14.3 % 14.5

1 Flue Gas Sampling Point Temperature 229.6 Deg F 230

2 Flue Gas Sampling Point Temperature 228.6 Deg F 230

3 Flue Gas Sampling Point Temperature 230.5 Deg F 230

4 Flue Gas Sampling Point Temperature 230.4 Deg F 230

1 Unit Gross Electrical Output 229.6 MW 105

2 Unit Gross Electrical Output 105 MW 105

3 Unit Gross Electrical Output 105 MW 105

4 Unit Gross Electrical Output 105 MW 105

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Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 NSCR (NON-SELECTIVE CATALYTIC 

REDUCTION)

0 0

1 SCRUBBER 0 0

1 Limestone Injection 0 0

Run Name Value UOM Comments

1 See 4b Comments. 0

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Sampling / Stack Data Results Detail

Location Stack Exit - Method 1 - 4

Average

Run Number 1 2 3

Test Date 6/9/2010 6/10/2010 6/11/2010

Run Start Time 1:45:00 PM 6:04:00 AM 5:49:00 AM

Run Finish Time 4:05:00 PM 8:27:00 AM 8:03:00 AM

Net Traversing Points 12 12 12

Net Run Time, minutes 210 120 120

Nozzle Diameter, inches 0.17 0.168 0.165 0.168

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9944 0.9944 0.9963 0.995

Barometric Pressure, inches of Mercury 29.93 29.99 29.97 29.963

Average Orifice Meter Differential, inches H2O 1.54 1.36 1.42 1.440

Dry Gas Meter Volume Sampled, cubic feet 90.880 79.570 77.330 82.593

Average Dry Gas Meter Temperature, °F 111.67 106.88 82.38 100.310

Dry Gas Meter Volume Sampled, dscf 83.811 74.116 75.388 77.772

Total Moisture Liquid collected, g 128 128.6 123 126.533

Volume of Water Vapor, standard cubic feet 6.02 6.05 5.79 5.953

Moisture Content of Stack Gas, % 6.70 7.55 7.13 7.127

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

Dry Mole Fraction 0.933 0.9245 0.9287 0.929

Carbon Dioxide, % 14.3 14.9 14.7 14.633

Oxygen, % 5.15 4.79 5.15 5.030

Carbon Monoxide & Nitrogen, % 80.55 80.31 80.15 80.337

Fuel Factor 1.10 1.08 1.07

Dry Molecular Weight, lb/lb-Mole 30.49 30.58 30.56 30.543

Wet Molecular weight, lb/lb-Mole 29.65 29.63 29.66 29.647

Flue Gas Static Pressure, inches of H2O -0.6 -0.6 -0.6 -0.600

Absolute Flue Gas Pressure, inches of Mercury 29.89 29.95 29.93 29.923

Average Stack Gas Temperature, °F 344.67 342.75 334.83 340.750

Average Velocity Head, inches of H2O 2.9154681803

2002

2.736835877

30999

2.760121117

24337

2.804

Average Stack Gas Velocity, feet/second 116.84 112.99 112.89 114.240

Stack Cross-Sectional Area, square feet 70.882 70.882 70.882 70.882

Dry Volumetric Flow Rate, dry scfm 303,907.1 292,498.1 296,294.1 297,566.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 496,911.2 480,537.4 480,112.1 485,853.567

Percent Isokinetic of Sampling Rate, % 59.1 97.2 101.2 85.833

Percent Excess Air, % 32.0 29.2 32.2 31.133

F-Factor, dscfm/MMBtu @ %O2 10348 10382 10009 10,246.333

Round Duct Diameter, inches 114 114 114

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

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Location Stack Exit - 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

Thursday, February 03, 2011 Page 17 of 24
Marion Generating Station Boiler 123

8/30/2010

Location Stack Exit - 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

Thursday, February 03, 2011 Page 18 of 24
Marion Generating Station Boiler 123

8/30/2010

Location Stack Exit - Method 26A

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

Thursday, February 03, 2011 Page 19 of 24
Marion Generating Station Boiler 123

8/30/2010

Location Stack Exit - 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

Thursday, February 03, 2011 Page 20 of 24
Marion Generating Station Boiler 123

8/30/2010

Location Stack Exit - 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

Thursday, February 03, 2011 Page 21 of 24
Marion Generating Station Boiler 123

8/30/2010

Location Stack Exit - Method 6C 3

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

Thursday, February 03, 2011 Page 22 of 24
Marion Generating Station Boiler 123

8/30/2010

Location Stack Exit - 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

Thursday, February 03, 2011 Page 23 of 24
Marion Generating Station Boiler 123

8/30/2010

Location Stack Exit - 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

Thursday, February 03, 2011 Page 24 of 24