Name: Jon Hays

Title: Environmental 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.

Wednesday, February 02, 2011 Page 1 of 13
9/2/2010

Facility Information:

IN_Gubson Generating Station Unit 2

1097 N 950 W

Owensville IN 47665

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:

051-23526-00013

Permitted Source ID/Name:

Unit 2 Coal-Fired Electric Utility Boilers

Permitted Maximum Process Rate:

5875

Max. Normal Operation Process Rate:

5875

Target Process Test Rate

5875

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 #: 1805100013 FRS #: 330015651387

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 298.8 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 Cobalt 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 Nickel Method 29 3 180 0

Stack Exit Arsenic Method 29 3 180 0

Wednesday, February 02, 2011 Page 2 of 13
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.

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 Beryllium 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

Wednesday, February 02, 2011 Page 3 of 13
9/2/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 6/22/2010 6/23/2010 6/23/2010

Run Start Time 12:45:00 PM 8:03:00 

AM

11:45:00 AM

Run Finish Time 4:00:00 PM 11:18:00 

AM

3:04:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 118.590 116.861 116.221 117.224

Moisture Content of Stack Gas, % 17.73 17.77 17.73 17.743

Moisture Saturation at Stack Gas Temperature, % 16.11 16.20 16.33 16.213

Carbon Dioxide, % 12.98 13.16 13.23 13.123

Oxygen, % 6.51 6.38 6.32 6.403

Average Stack Gas Temperature, °F 131.56 132.17 132.47 132.067

Dry Volumetric Flow Rate, dry scfm 1,606,469.1 1,576,432.

9

1,569,103.5 1,584,001.83

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,195,387.9 2,136,953.

3

2,131,402.0 2,154,581.06

7

Percent Isokinetic of Sampling Rate, % 98.3 98.7 98.6 98.533

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack 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 4 of 13
9/2/2010

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 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 5 of 13
9/2/2010

Emissions Summary

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00087 0.00063 0.00086 0.001

Elb/hr 1.56E-03 1.12E-03 1.54E-03 0.001

lb/mmBtuO2 2.30E-07 1.67E-07 2.29E-07 0.000

ug/dscm 2.59E-01 1.90E-01 2.61E-01 0.237

ug/dscm@7%O2 2.50E-01 1.82E-01 2.49E-01 0.227

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.01051 0.00758 0.00997 0.009

Elb/hr 1.88E-02 1.35E-02 1.78E-02 0.017

lb/mmBtuO2 2.78E-06 2.01E-06 2.65E-06 0.000

ug/dscm 3.13E+00 2.29E+00 3.03E+00 2.817

ug/dscm@7%O2 3.02E+00 2.19E+00 2.89E+00 2.700

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00019 0.00013 0.00017 0.000

Elb/hr 3.40E-04 2.32E-04 3.04E-04 0.000

lb/mmBtuO2 5.02E-08 3.45E-08 4.52E-08 0.000

ug/dscm 5.66E-02 3.93E-02 5.17E-02 0.049

ug/dscm@7%O2 5.47E-02 3.76E-02 4.93E-02 0.047

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00068 0.00041 0.00037 0.000

Elb/hr 1.22E-03 7.32E-04 6.61E-04 0.001

lb/mmBtuO2 1.80E-07 1.09E-07 9.84E-08 0.000

ug/dscm 2.03E-01 1.24E-01 1.12E-01 0.146

ug/dscm@7%O2 1.96E-01 1.19E-01 1.07E-01 0.141

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0032 0.0035 0.0035 0.003

Elb/hr 5.73E-03 6.25E-03 6.25E-03 0.006

lb/mmBtuO2 8.45E-07 9.30E-07 9.31E-07 0.000

ug/dscm 9.53E-01 1.06E+00 1.06E+00 1.024

ug/dscm@7%O2 9.21E-01 1.01E+00 1.01E+00 0.980

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00047 0.00026 0.00101 0.001

Elb/hr 8.42E-04 4.64E-04 1.80E-03 0.001

Wednesday, February 02, 2011 Page 6 of 13
9/2/2010

lb/mmBtuO2 1.24E-07 6.90E-08 2.69E-07 0.000

ug/dscm 1.40E-01 7.86E-02 3.07E-01 0.175

ug/dscm@7%O2 1.35E-01 7.52E-02 2.93E-01 0.168

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00218 0.00158 0.00258 0.002

Elb/hr 3.91E-03 2.82E-03 4.61E-03 0.004

lb/mmBtuO2 5.76E-07 4.20E-07 6.86E-07 0.000

ug/dscm 6.49E-01 4.78E-01 7.84E-01 0.637

ug/dscm@7%O2 6.27E-01 4.58E-01 7.47E-01 0.611

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.3174 0.5909 0.5729 0.494

Elb/hr 5.69E-01 1.05E+00 1.02E+00 0.880

lb/mmBtuO2 8.38E-05 1.57E-04 1.52E-04 0.000

ug/dscm 9.45E+01 1.79E+02 1.74E+02 149.167

ug/dscm@7%O2 9.13E+01 1.71E+02 1.66E+02 142.767

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0041 0.00263 0.0045 0.004

Elb/hr 7.35E-03 4.69E-03 8.04E-03 0.007

lb/mmBtuO2 1.08E-06 6.98E-07 1.20E-06 0.000

ug/dscm 1.22E+00 7.95E-01 1.37E+00 1.128

ug/dscm@7%O2 1.18E+00 7.61E-01 1.31E+00 1.084

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.054 0.0567 0.0481 0.053

Elb/hr 9.68E-02 1.01E-01 8.59E-02 0.095

lb/mmBtuO2 1.43E-05 1.51E-05 1.28E-05 0.000

ug/dscm 1.61E+01 1.71E+01 1.46E+01 15.933

ug/dscm@7%O2 1.56E+01 1.64E+01 1.39E+01 15.300

Location: Stack Exit - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 18.5 13.4 15.2 15.700

Elb/hr 3.11E+01 2.26E+01 2.51E+01 26.267

gr/dscf 2.23E-03 1.64E-03 1.83E-03 0.002

gr/dscf@7%O2 2.15E-03 1.57E-03 1.74E-03 0.002

lb/mmBtuO2 4.53E-03 3.31E-03 3.66E-03 0.004

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Wednesday, February 02, 2011 Page 7 of 13
9/2/2010

Process Run Data

Mass_mg 29.6 35.5 37.1 34.067

Elb/hr 4.97E+01 5.98E+01 6.13E+01 56.933

gr/dscf 3.57E-03 4.36E-03 4.46E-03 0.004

gr/dscf@7%O2 3.45E-03 4.17E-03 4.25E-03 0.004

lb/mmBtuO2 7.24E-03 8.76E-03 8.93E-03 0.008

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 5 6.7 8.2 6.633

Elb/hr 8.40E+00 1.13E+01 1.35E+01 11.067

gr/dscf 6.03E-04 8.22E-04 9.86E-04 0.001

gr/dscf@7%O2 5.82E-04 7.87E-04 9.40E-04 0.001

lb/mmBtuO2 1.22E-03 1.65E-03 1.97E-03 0.002

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 51.1 53.6 58.5 54.400

Elb/hr 8.58E+01 9.04E+01 9.66E+01 90.933

gr/dscf 6.16E-03 6.58E-03 7.03E-03 0.007

gr/dscf@7%O2 5.95E-03 6.30E-03 6.70E-03 0.006

lb/mmBtuO2 1.25E-02 1.32E-02 1.41E-02 0.013

Wednesday, February 02, 2011 Page 8 of 13
9/2/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

5 Heat Input 6968 Million Btu/Hr 6444 Run 3 PM/Metals

5 Unit Gross Electrical Output 670 MW 661 Run 3 PM/Metals

1 Heat Input 6991.6 Million Btu/Hr 6444 Run 1 PM/Metals

2 Heat Input 0 Million Btu/Hr 6444

3 Heat Input 0 Million Btu/Hr 6444

4 Heat Input 6962.1 Million Btu/Hr 6444 Run 2 PM/Metals

1 Unit Gross Electrical Output 676 MW 661 Run 1 PM/Metals

4 Unit Gross Electrical Output 670 MW 661 Run 2 PM/Metals

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

Wednesday, February 02, 2011 Page 9 of 13
9/2/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 6/22/2010 6/23/2010 6/23/2010

Run Start Time 12:45:00 PM 8:03:00 AM 11:45:00 AM

Run Finish Time 4:00:00 PM 11:18:00 AM 3:04:00 PM

Net Traversing Points 36 36 36

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.193 0.193 0.193 0.193

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.032 1.032 1.032 1.032

Barometric Pressure, inches of Mercury 29.3 29.6 29.6 29.500

Average Orifice Meter Differential, inches H2O 1.72 1.65 1.64 1.670

Dry Gas Meter Volume Sampled, cubic feet 123.027 119.925 119.815 120.922

Average Dry Gas Meter Temperature, °F 95.96 95.47 98.00 96.477

Dry Gas Meter Volume Sampled, dscf 118.590 116.861 116.221 117.224

Total Moisture Liquid collected, g 542.9 536.4 532.2 537.167

Volume of Water Vapor, standard cubic feet 25.55 25.25 25.05 25.283

Moisture Content of Stack Gas, % 17.73 17.77 17.73 17.743

Moisture Saturation at Stack Gas Temperature, % 16.11 16.20 16.33 16.213

Dry Mole Fraction 0.8389 0.838 0.8367 0.838

Carbon Dioxide, % 12.98 13.16 13.23 13.123

Oxygen, % 6.51 6.38 6.32 6.403

Carbon Monoxide & Nitrogen, % 80.51 80.46 80.45 80.473

Fuel Factor 1.11 1.10 1.10

Dry Molecular Weight, lb/lb-Mole 30.34 30.36 30.37 30.357

Wet Molecular weight, lb/lb-Mole 28.64 28.64 28.60 28.627

Flue Gas Static Pressure, inches of H2O -0.88 -0.84 -0.82 -0.847

Absolute Flue Gas Pressure, inches of Mercury 29.24 29.54 29.54 29.440

Average Stack Gas Temperature, °F 131.56 132.17 132.47 132.067

Average Velocity Head, inches of H2O 1.5498196080

6466

1.482113817

09998

1.471649693

48678

1.501

Average Stack Gas Velocity, feet/second 75.14 73.14 72.95 73.743

Stack Cross-Sectional Area, square feet 486.955 486.955 486.955 486.955

Dry Volumetric Flow Rate, dry scfm 1,606,469.1 1,576,432.9 1,569,103.5 1,584,001.8

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,195,387.9 2,136,953.3 2,131,402.0 2,154,581.0

67

Percent Isokinetic of Sampling Rate, % 98.3 98.7 98.6 98.533

Percent Excess Air, % 44.2 42.9 42.4 43.167

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

Round Duct Diameter, inches 298.8 298.8 298.8

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 10 of 13
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

Wednesday, February 02, 2011 Page 11 of 13
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

Wednesday, February 02, 2011 Page 12 of 13
9/2/2010

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 13 of 13