Name: Jon Hays

Title: Environmental Specialist

Company: Duke Energy

Sign Date: 9/30/2010

Name: Patrick Ford

Title: Techical Director, Air Measurement

Company: AECOM

Sign Date: 9/30/2010

Permitted Facility Representative / Date Testing Company Representative / Date

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.

Wednesday, February 02, 2011 Page 1 of 29
9/30/2010

Facility Information:

KY_East Bend Station

6293 Beaver Road

Union KY 41091

Contact: Jon Hays

Phone: 317-838-4445

Fax: 317-8382490

Email: jon.hays@duke.energy.com

Testing Company:

AECOM

2 Technology Park Drive

Westford MA 01886

Contact: Patrick Ford

Phone: 978-589-3427

Fax: 978-589-3100

Email: pat.ford@aecom.com

Air Permit Number:

V-06-038

Permitted Source ID/Name:

Unit 2 Pulverized Coal Boiler

Permitted Maximum Process Rate:

6,313 MMBtu/Hr

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:

This description should describe the process and associated controls to differentiate this facility from, or document 

similarity with others of same SCC.

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 Exit 388 0 0 0 8 2 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 60 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 Hydrogen Fluoride Method 26A 3 120 0

Stack Exit Hydrogen Chloride Method 26A 3 120 0

Stack Exit Arsenic Method 29 3 180 0

Stack Exit Manganese Method 29 3 180 0

Wednesday, February 02, 2011 Page 2 of 29
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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.

Stack Exit Lead Method 29 3 180 0

Stack Exit Antimony Method 29 3 180 0

Stack Exit Beryllium Method 29 3 180 0

Stack Exit Cobalt Method 29 3 180 0

Stack Exit Chromium Method 29 3 180 0

Stack Exit Selenium Method 29 3 180 0

Stack Exit Cadmium Method 29 3 180 0

Stack Exit Nickel Method 29 3 180 0

Stack Exit O2 Method 3A O2 3 60 0

Stack Exit Co2 Method 3A CO2 3 60 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit Method 5/OTM-28 3 180 0

Organic Condensible 

Particulate

Stack Exit Method 5/OTM-28 3 180 0

Stack Exit Total Particulate Method 5/OTM-28 3 180 0

Stack Exit Filterable Particulate Method 5/OTM-28 3 180 0

Stack Exit Sulfur Dioxide Method 6C 3 60 0

Stack Exit Nitrogen oxides (NOx) Method 7E 3 60 0

Wednesday, February 02, 2011 Page 3 of 29
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Sampling / Stack Data Results Summary

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

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

Wednesday, February 02, 2011 Page 4 of 29
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Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 7/13/2010 7/13/2010 7/13/2010

Run Start Time 11:10:00 AM 2:47:00 

PM

4:20:00 PM

Run Finish Time 12:27:00 PM 4:05:00 

PM

7:29:00 PM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 46.508 46.824 47.223 46.852

Moisture Content of Stack Gas, % 15.34 15.30 15.06 15.233

Moisture Saturation at Stack Gas Temperature, % 16.77 16.55 16.22 16.513

Carbon Dioxide, % 10.88 10.86 10.88 10.873

Oxygen, % 8.62 8.63 8.64 8.630

Average Stack Gas Temperature, °F 133.00 132.50 131.75 132.417

Dry Volumetric Flow Rate, dry scfm 1,804,013.3 1,825,246.

9

1,830,189.7 1,819,816.63

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,453,909.6 2,479,527.

6

2,476,079.0 2,469,838.73

3

Percent Isokinetic of Sampling Rate, % 103.5 103.0 103.6 103.367

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

Wednesday, February 02, 2011 Page 5 of 29
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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 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

Wednesday, February 02, 2011 Page 6 of 29
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Location Stack Exit - Method 3A CO2 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 3A CO2 3 6

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

Wednesday, February 02, 2011 Page 7 of 29
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Location Stack Exit - 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

Location Stack Exit - Method 3A O2 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

Wednesday, February 02, 2011 Page 8 of 29
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Location Stack Exit - Method 3A O2 3 6

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 5/OTM-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

Wednesday, February 02, 2011 Page 9 of 29
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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

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

Wednesday, February 02, 2011 Page 10 of 29
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Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 1.53E+02 3.28E+01 4.98E+01 78.533

lb/mmBtuO2 2.33E-02 5.00E-03 7.62E-03 0.012

ppm 1.95E+01 4.19E+00 6.42E+00 10.037

ppm@7%O2 2.18E+01 4.68E+00 7.13E+00 11.203

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 7.72E+00 7.74E+00 8.74E+00 8.067

lb/mmBtuO2 1.18E-03 1.18E-03 1.34E-03 0.001

ppm 6.24E-01 6.28E-01 7.16E-01 0.656

ppm@7%O2 6.99E-01 7.02E-01 7.95E-01 0.732

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.662 0.746 0.614 0.674

Elb/hr 3.40E+00 3.85E+00 3.15E+00 3.467

lb/mmBtuO2 5.22E-04 5.85E-04 4.78E-04 0.001

mg/dscm 5.03E-01 5.63E-01 4.59E-01 0.508

mg/dscm@7%O2 5.69E-01 6.38E-01 5.20E-01 0.576

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.22 0.22 0.23 0.223

Elb/hr 1.13E+00 1.13E+00 1.18E+00 1.147

lb/mmBtuO2 1.74E-04 1.73E-04 1.79E-04 0.000

mg/dscm 1.67E-01 1.66E-01 1.72E-01 0.168

mg/dscm@7%O2 1.89E-01 1.88E-01 1.95E-01 0.191

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00058 0.00052 0.0005304 0.001

Elb/hr 1.04E-03 9.35E-04 9.53E-04 0.001

lb/mmBtuO2 1.60E-07 1.43E-07 1.47E-07 0.000

ug/dscm 1.54E-01 1.39E-01 1.42E-01 0.145

ug/dscm@7%O2 1.73E-01 1.56E-01 1.60E-01 0.163

Compound: Arsenic

Average

RunNumber 1 2 3

Wednesday, February 02, 2011 Page 11 of 29
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Mass_mg 0.0143 0.0123 0.01358 0.013

Elb/hr 2.57E-02 2.21E-02 2.44E-02 0.024

lb/mmBtuO2 3.94E-06 3.39E-06 3.76E-06 0.000

ug/dscm 3.81E+00 3.28E+00 3.63E+00 3.573

ug/dscm@7%O2 4.29E+00 3.69E+00 4.10E+00 4.027

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000182 0.000142 0.000152 0.000

Elb/hr 3.27E-04 2.55E-04 2.73E-04 0.000

lb/mmBtuO2 5.01E-08 3.91E-08 4.21E-08 0.000

ug/dscm 4.85E-02 3.79E-02 4.06E-02 0.042

ug/dscm@7%O2 5.46E-02 4.27E-02 4.58E-02 0.048

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0018 0.0007 0.00095 0.001

Elb/hr 3.23E-03 1.26E-03 1.71E-03 0.002

lb/mmBtuO2 4.96E-07 1.93E-07 2.63E-07 0.000

ug/dscm 4.79E-01 1.87E-01 2.54E-01 0.307

ug/dscm@7%O2 5.40E-01 2.10E-01 2.87E-01 0.346

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0251 0.0148 0.0234 0.021

Elb/hr 4.50E-02 2.66E-02 4.20E-02 0.038

lb/mmBtuO2 6.91E-06 4.08E-06 6.48E-06 0.000

ug/dscm 6.69E+00 3.95E+00 6.26E+00 5.633

ug/dscm@7%O2 7.54E+00 4.45E+00 7.07E+00 6.353

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00059 0.00041 0.0011 0.001

Elb/hr 1.06E-03 7.37E-04 1.98E-03 0.001

lb/mmBtuO2 1.62E-07 1.13E-07 3.05E-07 0.000

ug/dscm 1.57E-01 1.09E-01 2.94E-01 0.187

ug/dscm@7%O2 1.77E-01 1.23E-01 3.32E-01 0.211

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00464 0.0022 0.00381 0.004

Elb/hr 8.33E-03 3.95E-03 6.84E-03 0.006

lb/mmBtuO2 1.28E-06 6.06E-07 1.06E-06 0.000

ug/dscm 1.24E+00 5.87E-01 1.02E+00 0.949

ug/dscm@7%O2 1.40E+00 6.61E-01 1.15E+00 1.070

Compound: Manganese

Average

RunNumber 1 2 3

Wednesday, February 02, 2011 Page 12 of 29
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Mass_mg 0.0161 0.00736 0.00946 0.011

Elb/hr 2.89E-02 1.32E-02 1.70E-02 0.020

lb/mmBtuO2 4.43E-06 2.03E-06 2.62E-06 0.000

ug/dscm 4.29E+00 1.96E+00 2.53E+00 2.927

ug/dscm@7%O2 4.83E+00 2.21E+00 2.86E+00 3.300

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0204 0.00741 0.02971 0.019

Elb/hr 3.66E-02 1.33E-02 5.34E-02 0.034

lb/mmBtuO2 5.62E-06 2.04E-06 8.23E-06 0.000

ug/dscm 5.43E+00 1.98E+00 7.94E+00 5.117

ug/dscm@7%O2 6.12E+00 2.23E+00 8.97E+00 5.773

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.2155 0.1729 0.1664 0.185

Elb/hr 3.87E-01 3.11E-01 2.99E-01 0.332

lb/mmBtuO2 5.93E-05 4.77E-05 4.61E-05 0.000

ug/dscm 5.74E+01 4.61E+01 4.45E+01 49.333

ug/dscm@7%O2 6.47E+01 5.19E+01 5.02E+01 55.600

Location: Stack Exit - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 33.4 33 32.7 33.033

Elb/hr 5.79E+01 5.71E+01 5.69E+01 57.300

gr/dscf 3.72E-03 3.68E-03 3.65E-03 0.004

gr/dscf@7%O2 4.19E-03 4.14E-03 4.12E-03 0.004

lb/mmBtuO2 8.81E-03 8.69E-03 8.66E-03 0.009

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 88.3 78.6 33.2 66.700

Elb/hr 1.53E+02 1.36E+02 5.78E+01 115.600

gr/dscf 9.84E-03 8.75E-03 3.71E-03 0.007

gr/dscf@7%O2 1.11E-02 9.85E-03 4.19E-03 0.008

lb/mmBtuO2 2.33E-02 2.07E-02 8.79E-03 0.018

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 10.8 7.9 4.4 7.700

Elb/hr 1.87E+01 1.37E+01 7.65E+00 13.350

gr/dscf 1.20E-03 8.80E-04 4.91E-04 0.001

gr/dscf@7%O2 1.35E-03 9.90E-04 5.54E-04 0.001

lb/mmBtuO2 2.85E-03 2.08E-03 1.17E-03 0.002

Wednesday, February 02, 2011 Page 13 of 29
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Process Run Data

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 130.5 117.5 68.3 105.433

Elb/hr 2.26E+02 2.03E+02 1.19E+02 182.667

gr/dscf 1.45E-02 1.31E-02 7.63E-03 0.012

gr/dscf@7%O2 1.63E-02 1.47E-02 8.62E-03 0.013

lb/mmBtuO2 3.44E-02 3.09E-02 1.81E-02 0.028

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 4.02E+02 3.75E+02 4.10E+02 395.667

lb/mmBtuO2 6.24E-02 5.75E-02 6.26E-02 0.061

ppm 2.26E+01 2.08E+01 2.26E+01 22.000

ppm@7%O2 2.56E+01 2.36E+01 2.56E+01 24.933

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 3.71E+02 3.94E+02 4.07E+02 390.667

lb/mmBtuO2 5.76E-02 6.05E-02 6.21E-02 0.060

ppm 2.90E+01 3.04E+01 3.12E+01 30.200

ppm@7%O2 3.28E+01 3.44E+01 3.54E+01 34.200

Wednesday, February 02, 2011 Page 14 of 29
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Process Run Data

APCD Run Data

Run Name Value UOM Comments

Target

Value

5 Heat Input 5863.4 MMBtu 6313 Run 3, Acid Gases

5 Unit Gross Electrical Output 648 MW 650 Run 3, Acid Gases

6 Heat Input 5908.9 MMBtu 6313 Run 1, PM/Metals

6 Unit Gross Electrical Output 652 MW 650 Run 1, PM/Metals

7 Heat Input 5914.2 MMBtu 6313 Run 2, PM/Metals

7 Unit Gross Electrical Output 652 MW 650 Run 2, PM/Metals

8 Heat Input 5914.7 MMBtu 6313 Run 3, PM/Metals

8 Unit Gross Electrical Output 652 MW 650 Run 3, PM/Metals

9 Heat Input 0 MMBtu Run 1, NonDioxin/Furan 

Organics

6313

9 Unit Gross Electrical Output 651 MW Run 1, NonDioxin/Furan 

Organics

650

10 Heat Input 5846 MMBtu Run 2, NonDioxin/Furan 

Organics

6313

10 Unit Gross Electrical Output 652 MW Run 2, NonDioxin/Furan 

Organics

650

11 Heat Input 5882.7 MMBtu Run 3, NonDioxin/Furan 

Organics

6313

11 Unit Gross Electrical Output 652 MW Run 3, NonDioxin/Furan 

Organics

650

1 Heat Input 5824.5 MMBtu 6313 Run 1 Acid Gases

2 Heat Input 0 MMBtu 6313

3 Heat Input 0 MMBtu 6313

4 Heat Input 5812.2 MMBtu 6313 Run 2, Acid Gases

1 Unit Gross Electrical Output 649 MW 650 Run 1 Acid Gases

4 Unit Gross Electrical Output 649 MW 650 Run 2, Acid Gases

Run Name Value UOM Comments

Target

Value

1 List all emissions control devices in order of 

process flow. Choose from

0 0

Wednesday, February 02, 2011 Page 15 of 29
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Process Lab Run Data

1 drop down lists. If not on list add description and 

provide detailed

0 0

1 desription in section 5a. 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %

1 Ultimate/Proximate Analysis 0

1 Fuel Chlorine Content 0 mg/kg

1 Fuel Fluorine Content 0 mg/kg

1 Metals Content 0 mg/kg

Wednesday, February 02, 2011 Page 16 of 29
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Sampling / Stack Data Results Detail

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

Wednesday, February 02, 2011 Page 17 of 29
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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

Wednesday, February 02, 2011 Page 18 of 29
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Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 7/13/2010 7/13/2010 7/13/2010

Run Start Time 11:10:00 AM 2:47:00 PM 4:20:00 PM

Run Finish Time 12:27:00 PM 4:05:00 PM 7:29:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 60 60 60

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 1.025 1.025 1.025 1.025

Barometric Pressure, inches of Mercury 29.08 29.08 29.08 29.080

Average Orifice Meter Differential, inches H2O 2.09 2.14 2.18 2.137

Dry Gas Meter Volume Sampled, cubic feet 47.949 48.247 48.756 48.317

Average Dry Gas Meter Temperature, °F 85.17 84.92 86.08 85.390

Dry Gas Meter Volume Sampled, dscf 46.508 46.824 47.223 46.852

Total Moisture Liquid collected, g 179.2 179.8 177.9 178.967

Volume of Water Vapor, standard cubic feet 8.43 8.46 8.37 8.420

Moisture Content of Stack Gas, % 15.34 15.30 15.06 15.233

Moisture Saturation at Stack Gas Temperature, % 16.77 16.55 16.22 16.513

Dry Mole Fraction 0.8466 0.847 0.8494 0.848

Carbon Dioxide, % 10.88 10.86 10.88 10.873

Oxygen, % 8.62 8.63 8.64 8.630

Carbon Monoxide & Nitrogen, % 80.5 80.51 80.48 80.497

Fuel Factor 1.13 1.13 1.13

Dry Molecular Weight, lb/lb-Mole 30.09 30.08 30.09 30.087

Wet Molecular weight, lb/lb-Mole 28.24 28.23 28.27 28.247

Flue Gas Static Pressure, inches of H2O 1.4 1.4 1.4 1.400

Absolute Flue Gas Pressure, inches of Mercury 29.18 29.18 29.18 29.180

Average Stack Gas Temperature, °F 133.00 132.50 131.75 132.417

Average Velocity Head, inches of H2O 0.6685194779

71958

0.682868015

105236

0.682862706

923991

0.678

Average Stack Gas Velocity, feet/second 49.81 50.33 50.26 50.133

Stack Cross-Sectional Area, square feet 821.090 821.090 821.090 821.090

Dry Volumetric Flow Rate, dry scfm 1,804,013.3 1,825,246.9 1,830,189.7 1,819,816.6

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,453,909.6 2,479,527.6 2,476,079.0 2,469,838.7

33

Percent Isokinetic of Sampling Rate, % 103.5 103.0 103.6 103.367

Percent Excess Air, % 68.2 68.4 68.5 68.367

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

Round Duct Diameter, inches 388 388 388

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, February 02, 2011 Page 19 of 29
9/30/2010

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

Wednesday, February 02, 2011 Page 20 of 29
9/30/2010

Location Stack Exit - 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

Wednesday, February 02, 2011 Page 21 of 29
9/30/2010

Location Stack Exit - Method 3A CO2 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

Wednesday, February 02, 2011 Page 22 of 29
9/30/2010

Location Stack Exit - Method 3A CO2 3 6

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

Wednesday, February 02, 2011 Page 23 of 29
9/30/2010

Location Stack Exit - 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

Wednesday, February 02, 2011 Page 24 of 29
9/30/2010

Location Stack Exit - Method 3A O2 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

Wednesday, February 02, 2011 Page 25 of 29
9/30/2010

Location Stack Exit - Method 3A O2 3 6

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

Wednesday, February 02, 2011 Page 26 of 29
9/30/2010

Location Stack Exit - Method 5/OTM-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

Wednesday, February 02, 2011 Page 27 of 29
9/30/2010

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

Wednesday, February 02, 2011 Page 28 of 29
9/30/2010

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

Wednesday, February 02, 2011 Page 29 of 29