Name: Jon Hays

Title: Project Specialist

Company: Duke Energy

Sign Date: 9/2/2010

Name: Pat Ford

Title: Project Manager

Company: AECOM

Sign Date: 8/26/2010

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.

Tuesday, February 01, 2011 Page 1 of 27
9/2/2010

Facility Information:

IN_Wabash River Generating Station Unit 4

450 Bolton Road

West Terre Haute IN 47885

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:

167-27200-00021

Permitted Source ID/Name:

Unit 4,6 No. 2 Fuel Oil/Coal-Fired Electric Utility Boilers

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:

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 #: 1816700021 FRS #: 330015654589

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 300 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 60 0

Stack Exit Hydrogen Chloride Method 26A 3 60 0

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 280 0 R1 284 Min, R2 284 

Min, R3 296 Min

Stack Exit

Tuesday, February 01, 2011 Page 2 of 27
9/2/2010

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.

EPA Method 26A was modified to include the provisions cited in Method CTM-033 to allow for the collection and 

analysis of HCN. Also, a higher strength NaOH was used in order to maintain the pH at a level that would ensure 

good HCN collection efficiency. This involved using 100 ml of 6N NaOH in the first impinger and 100 ml each of 

2N NaOH in impingers 3 and 4. The sample time was also reduced to 1-hour as allowed by EPA (see FAQ's section 

on the ICR website) again to ensure that the pH of the absorbing solution remained high.

Organic Condensible 

Particulate

OTM - 27/28 3 280 0 R1 284 Min, R2 284 

Min, R3 296 Min

Stack Exit

Total PM2.5 OTM - 27/28 3 280 0 R1 284 Min, R2 284 

Min, R3 296 Min

Stack Exit

Filterable PM2.5 OTM - 27/28 3 280 0 R1 284 Min, R2 284 

Min, R3 296 Min

Stack Exit

Stack Exit Arsenic Method 29 3 180 0

Stack Exit Manganese Method 29 3 180 0

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 Filterable Particulate 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

Stack Exit Sulfur Dioxide Method 6C 3 60 0

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

Tuesday, February 01, 2011 Page 3 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 4 of 27
9/2/2010

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 6/4/2010 6/4/2010 6/4/2010

Run Start Time 8:33:00 AM 11:35:00 

AM

2:44:00 PM

Run Finish Time 11:01:00 AM 2:13:00 

PM

5:09:00 PM

Net Run Time, minutes 132 132 132

Dry Gas Meter Volume Sampled, dscf 86.022 85.007 85.031 85.353

Moisture Content of Stack Gas, % 9.38 9.42 8.97 9.257

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

Carbon Dioxide, % 12.25 12.2 12.11 12.187

Oxygen, % 7.28 7.26 7.31 7.283

Average Stack Gas Temperature, °F 274.00 279.25 282.50 278.583

Dry Volumetric Flow Rate, dry scfm 1,268,193.3 1,260,412.

5

1,250,847.1 1,259,817.63

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,007,183.8 2,010,718.

1

1,993,635.7 2,003,845.86

7

Percent Isokinetic of Sampling Rate, % 97.3 96.8 97.5 97.200

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

Tuesday, February 01, 2011 Page 5 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 6 of 27
9/2/2010

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 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, February 01, 2011 Page 7 of 27
9/2/2010

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

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

Tuesday, February 01, 2011 Page 8 of 27
9/2/2010

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

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

Tuesday, February 01, 2011 Page 9 of 27
9/2/2010

Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 3.81E+01 4.08E+01 5.15E+01 43.467

lb/mmBtuO2 7.48E-03 8.00E-03 1.09E-02 0.009

ppm 6.84E+00 7.31E+00 9.99E+00 8.047

ppm@7%O2 6.99E+00 7.48E+00 1.02E+01 8.223

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 3.11E+00 2.24E+00 4.14E+00 3.163

lb/mmBtuO2 6.11E-04 4.39E-04 8.76E-04 0.001

ppm 3.55E-01 2.55E-01 5.10E-01 0.373

ppm@7%O2 3.63E-01 2.61E-01 5.20E-01 0.381

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 34.9 32.7 30.5 32.700

Elb/hr 6.81E+01 6.41E+01 5.93E+01 63.833

lb/mmBtuO2 1.34E-02 1.27E-02 1.19E-02 0.013

mg/dscm 1.43E+01 1.36E+01 1.27E+01 13.533

mg/dscm@7%O2 1.46E+01 1.39E+01 1.30E+01 13.833

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 12.1 12 11.7 11.933

Elb/hr 2.36E+01 2.35E+01 2.28E+01 23.300

lb/mmBtuO2 4.65E-03 4.66E-03 4.56E-03 0.005

mg/dscm 4.97E+00 4.99E+00 4.86E+00 4.940

mg/dscm@7%O2 5.07E+00 5.09E+00 4.97E+00 5.043

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00689 0.00669 0.00559 0.006

Elb/hr 1.00E-02 8.47E-03 7.14E-03 0.009

gr/dscf 9.98E-07 7.84E-07 6.37E-07 0.000

gr/dscf@7%O2 1.02E-06 8.07E-07 6.42E-07 0.000

lb/mmBtuO2 2.14E-06 1.70E-06 1.35E-06 0.000

ug/dscm 2.28E+00 1.79E+00 1.46E+00 1.843

ug/dscm@7%O2 2.33E+00 1.84E+00 1.47E+00 1.880

Tuesday, February 01, 2011 Page 10 of 27
9/2/2010

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.1161 0.1356 0.1075 0.120

Elb/hr 1.69E-01 1.72E-01 1.37E-01 0.159

gr/dscf 1.68E-05 1.59E-05 1.22E-05 0.000

gr/dscf@7%O2 1.72E-05 1.64E-05 1.23E-05 0.000

lb/mmBtuO2 3.61E-05 3.44E-05 2.59E-05 0.000

ug/dscm 3.85E+01 3.64E+01 2.80E+01 34.300

ug/dscm@7%O2 3.93E+01 3.75E+01 2.82E+01 35.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.004712 0.005312 0.00391 0.005

Elb/hr 6.85E-03 6.72E-03 5.00E-03 0.006

gr/dscf 6.82E-07 6.23E-07 4.45E-07 0.000

gr/dscf@7%O2 6.97E-07 6.41E-07 4.48E-07 0.000

lb/mmBtuO2 1.47E-06 1.35E-06 9.43E-07 0.000

ug/dscm 1.56E+00 1.42E+00 1.02E+00 1.333

ug/dscm@7%O2 1.59E+00 1.46E+00 1.03E+00 1.360

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00103 0.0005 0.00047 0.001

Elb/hr 1.50E-03 6.33E-04 6.01E-04 0.001

gr/dscf 1.49E-07 5.86E-08 5.35E-08 0.000

gr/dscf@7%O2 1.52E-07 6.03E-08 5.39E-08 0.000

lb/mmBtuO2 3.20E-07 1.27E-07 1.13E-07 0.000

ug/dscm 3.41E-01 1.34E-01 1.23E-01 0.199

ug/dscm@7%O2 3.49E-01 1.38E-01 1.24E-01 0.204

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0422 0.0472 0.0324 0.041

Elb/hr 6.14E-02 5.97E-02 4.14E-02 0.054

gr/dscf 6.11E-06 5.53E-06 3.69E-06 0.000

gr/dscf@7%O2 6.24E-06 5.69E-06 3.72E-06 0.000

lb/mmBtuO2 1.31E-05 1.20E-05 7.81E-06 0.000

ug/dscm 1.40E+01 1.27E+01 8.45E+00 11.717

ug/dscm@7%O2 1.43E+01 1.31E+01 8.51E+00 11.970

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.01 0.01144 0.0103 0.011

Elb/hr 1.45E-02 1.45E-02 1.32E-02 0.014

gr/dscf 1.45E-06 1.34E-06 1.17E-06 0.000

gr/dscf@7%O2 1.48E-06 1.38E-06 1.18E-06 0.000

lb/mmBtuO2 3.11E-06 2.90E-06 2.48E-06 0.000

ug/dscm 3.31E+00 3.07E+00 2.69E+00 3.023

Tuesday, February 01, 2011 Page 11 of 27
9/2/2010

ug/dscm@7%O2 3.38E+00 3.16E+00 2.71E+00 3.083

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 352.2 566 318.6 412.267

Elb/hr 5.12E+02 7.16E+02 4.07E+02 545.000

gr/dscf 5.10E-02 6.63E-02 3.63E-02 0.051

gr/dscf@7%O2 5.21E-02 6.83E-02 3.66E-02 0.052

lb/mmBtuO2 1.10E-01 1.43E-01 7.68E-02 0.110

ug/dscm 1.17E+05 1.52E+05 8.31E+04 117,366.667

ug/dscm@7%O2 1.20E+05 1.57E+05 8.37E+04 120,233.333

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.0376 0.0357 0.0304 0.035

Elb/hr 5.47E-02 4.52E-02 3.88E-02 0.046

gr/dscf 5.45E-06 4.18E-06 3.46E-06 0.000

gr/dscf@7%O2 5.57E-06 4.30E-06 3.49E-06 0.000

lb/mmBtuO2 1.17E-05 9.05E-06 7.33E-06 0.000

ug/dscm 1.25E+01 9.58E+00 7.93E+00 10.003

ug/dscm@7%O2 1.28E+01 9.86E+00 7.99E+00 10.217

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0412 0.0602 0.2666 0.123

Elb/hr 5.99E-02 7.62E-02 3.41E-01 0.159

gr/dscf 5.97E-06 7.05E-06 3.04E-05 0.000

gr/dscf@7%O2 6.10E-06 7.26E-06 3.06E-05 0.000

lb/mmBtuO2 1.28E-05 1.53E-05 6.43E-05 0.000

ug/dscm 1.37E+01 1.61E+01 6.95E+01 33.100

ug/dscm@7%O2 1.40E+01 1.66E+01 7.00E+01 33.533

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0486 0.0474 0.0352 0.044

Elb/hr 7.07E-02 6.00E-02 4.50E-02 0.059

gr/dscf 7.04E-06 5.55E-06 4.01E-06 0.000

gr/dscf@7%O2 7.20E-06 5.71E-06 4.04E-06 0.000

lb/mmBtuO2 1.51E-05 1.20E-05 8.49E-06 0.000

ug/dscm 1.61E+01 1.27E+01 9.18E+00 12.660

ug/dscm@7%O2 1.65E+01 1.31E+01 9.25E+00 12.950

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.2407 0.4039 0.3159 0.320

Elb/hr 3.50E-01 5.11E-01 4.04E-01 0.422

gr/dscf 3.49E-05 4.73E-05 3.60E-05 0.000

gr/dscf@7%O2 3.57E-05 4.87E-05 3.63E-05 0.000

lb/mmBtuO2 7.49E-05 1.02E-04 7.62E-05 0.000

Tuesday, February 01, 2011 Page 12 of 27
9/2/2010

ug/dscm 7.98E+01 1.08E+02 8.24E+01 90.067

ug/dscm@7%O2 8.16E+01 1.11E+02 8.30E+01 91.867

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run M26A/CTM033-1 M26A/CTM033-2 M26A/CTM033-3

Elb/hr 1.85E+04 1.90E+04 1.83E+04 18,600.000

lb/mmBtuO2 3.61E+00 3.73E+00 3.65E+00 3.663

ppm 1.45E+03 1.50E+03 1.46E+03 1,470.000

ppm@7%O2 1.48E+03 1.53E+03 1.49E+03 1,500.000

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run M26A/CTM033-1 M26A/CTM033-2 M26A/CTM033-3

Elb/hr 1.51E+03 1.51E+03 1.51E+03 1,510.000

lb/mmBtuO2 2.94E-01 2.98E-01 3.00E-01 0.297

ppm 1.64E+02 1.66E+02 1.67E+02 165.667

ppm@7%O2 1.67E+02 1.69E+02 1.71E+02 169.000

Location: Stack Exit - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 184.3 189.4 187.9 187.200

Elb/hr 2.55E+02 2.66E+02 2.59E+02 260.000

gr/dscf 2.57E-02 2.70E-02 2.52E-02 0.026

gr/dscf@7%O2 2.63E-02 2.78E-02 2.54E-02 0.027

lb/mmBtuO2 5.52E-02 5.85E-02 5.32E-02 0.056

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 17.8 28.4 10.6 18.933

Elb/hr 2.46E+01 3.99E+01 1.46E+01 26.367

gr/dscf 2.48E-03 4.05E-03 1.42E-03 0.003

gr/dscf@7%O2 2.53E-03 4.17E-03 1.43E-03 0.003

lb/mmBtuO2 5.33E-03 8.77E-03 3.00E-03 0.006

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 286 258 318 287.333

Elb/hr 3.95E+02 3.63E+02 4.39E+02 399.000

gr/dscf 3.99E-02 3.68E-02 4.26E-02 0.040

gr/dscf@7%O2 4.08E-02 3.79E-02 4.29E-02 0.041

lb/mmBtuO2 8.57E-02 7.96E-02 9.01E-02 0.085

Compound: Total PM2.5

Average

RunNumber 1 2 3

Tuesday, February 01, 2011 Page 13 of 27
9/2/2010

Process Run Data

Mass_mg 486.1 473.8 514.5 491.467

Elb/hr 6.72E+02 6.66E+02 7.10E+02 682.667

gr/dscf 6.78E-02 6.76E-02 6.89E-02 0.068

gr/dscf@7%O2 6.93E-02 6.96E-02 6.94E-02 0.069

lb/mmBtuO2 1.46E-01 1.46E-01 1.46E-01 0.146

Tuesday, February 01, 2011 Page 14 of 27
9/2/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

5 Unit Gross Electrical Output 434 MW Run 3 Acid Gases, 

Unit 4-90 MW and 

Unit 6-344MW, 

Combined Stack 

Test

434

6 Unit Gross Electrical Output 435 MW Run 1 Non-Dioxin 

Organics, Unit 4-

90 MW and Unit 6-

344MW, 

Combined Stack 

Test

434

7 Unit Gross Electrical Output 434 MW Run 2 Non-Dioxin 

Organics, Unit 4-

90 MW and Unit 6-

344MW, 

Combined Stack 

Test

434

8 Unit Gross Electrical Output 434 MW Run 3 Non-Dioxin 

Organics, Unit 4-

90 MW and Unit 6-

344MW, 

Combined Stack 

Test

434

9 Unit Gross Electrical Output 436 MW Run 1 PM/Metals, 

Unit 4-90 MW and 

Unit 6-344MW, 

Combined Stack 

Test

434

10 Unit Gross Electrical Output 436 MW Run 2 PM/Metals, 

Unit 4-90 MW and 

Unit 6-344MW, 

Combined Stack 

Test

434

11 Unit Gross Electrical Output 435 MW Run 3 PM/Metals, 

Unit 4-90 MW and 

Unit 6-344MW, 

Combined Stack 

Test

434

1 Unit Gross Electrical Output 434 MW Run 1 Acid Gases, 

Unit 4-90 MW and 

Unit 6-344MW, 

Combined Stack 

Test

434

4 Unit Gross Electrical Output 434 MW Run 2 Acid Gases, 

Unit 4-90 MW and 

Unit 6-344MW, 

Combined Stack 

Test

434

Tuesday, February 01, 2011 Page 15 of 27
9/2/2010

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 List all emissions control devices in order of 

process flow. Choose from

0 0

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

Tuesday, February 01, 2011 Page 16 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 17 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 18 of 27
9/2/2010

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 6/4/2010 6/4/2010 6/4/2010

Run Start Time 8:33:00 AM 11:35:00 AM 2:44:00 PM

Run Finish Time 11:01:00 AM 2:13:00 PM 5:09:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 132 132 132

Nozzle Diameter, inches 0.218 0.218 0.218 0.218

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.974 0.974 0.974 0.974

Barometric Pressure, inches of Mercury 29.1 29.1 29.1 29.100

Average Orifice Meter Differential, inches H2O 1.58 1.57 1.55 1.567

Dry Gas Meter Volume Sampled, cubic feet 92.423 92.118 92.833 92.458

Average Dry Gas Meter Temperature, °F 79.54 84.17 88.21 83.973

Dry Gas Meter Volume Sampled, dscf 86.022 85.007 85.031 85.353

Total Moisture Liquid collected, g 189.1 187.8 178 184.967

Volume of Water Vapor, standard cubic feet 8.90 8.84 8.38 8.707

Moisture Content of Stack Gas, % 9.38 9.42 8.97 9.257

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

Dry Mole Fraction 0.9062 0.9058 0.9103 0.907

Carbon Dioxide, % 12.25 12.2 12.11 12.187

Oxygen, % 7.28 7.26 7.31 7.283

Carbon Monoxide & Nitrogen, % 80.47 80.54 80.58 80.530

Fuel Factor 1.11 1.12 1.12

Dry Molecular Weight, lb/lb-Mole 30.25 30.24 30.23 30.240

Wet Molecular weight, lb/lb-Mole 29.10 29.09 29.13 29.107

Flue Gas Static Pressure, inches of H2O -1.3 -1.5 -1.4 -1.400

Absolute Flue Gas Pressure, inches of Mercury 29.00 28.99 29.00 28.997

Average Stack Gas Temperature, °F 274.00 279.25 282.50 278.583

Average Velocity Head, inches of H2O 1.0353408704

3733

1.031017747

26471

1.010905006

55847

1.026

Average Stack Gas Velocity, feet/second 68.15 68.27 67.69 68.037

Stack Cross-Sectional Area, square feet 490.874 490.874 490.874 490.874

Dry Volumetric Flow Rate, dry scfm 1,268,193.3 1,260,412.5 1,250,847.1 1,259,817.6

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,007,183.8 2,010,718.1 1,993,635.7 2,003,845.8

67

Percent Isokinetic of Sampling Rate, % 97.3 96.8 97.5 97.200

Percent Excess Air, % 52.1 51.8 52.4 52.100

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

Round Duct Diameter, inches 300 300 300

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

Tuesday, February 01, 2011 Page 19 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 20 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 21 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 22 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 23 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 24 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 25 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 26 of 27
9/2/2010

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

Tuesday, February 01, 2011 Page 27 of 27