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 1

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 1 No. 2 Fuel Oil/Coal-Fired Electric Utility Boilers

Permitted Maximum Process Rate:

5875 MMBtu/Hr

Max. Normal Operation Process Rate:

5875 MMBtu/Hr

Target Process Test Rate

5875 MMBtu/Hr

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 294.6 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 6/24/2010 6/24/2010 6/24/2010

Run Start Time 7:56:00 AM 11:28:00 

AM

2:56:00 PM

Run Finish Time 11:11:00 AM 2:41:00 

PM

6:09:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 115.983 116.352 115.990 116.108

Moisture Content of Stack Gas, % 17.99 17.24 17.66 17.630

Moisture Saturation at Stack Gas Temperature, % 16.30 16.11 16.17 16.193

Carbon Dioxide, % 13.19 13.23 13.2 13.207

Oxygen, % 6.18 6.18 6.17 6.177

Average Stack Gas Temperature, °F 132.03 131.61 131.75 131.797

Dry Volumetric Flow Rate, dry scfm 1,515,409.8 1,528,560.

4

1,521,494.5 1,521,821.56

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,075,877.3 2,086,954.

0

2,079,285.5 2,080,705.60

0

Percent Isokinetic of Sampling Rate, % 99.1 98.5 98.7 98.767

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 0.00078 0.00083 0.00093 0.001

Elb/hr 1.35E-03 1.44E-03 1.61E-03 0.001

lb/mmBtuO2 2.06E-07 2.18E-07 2.45E-07 0.000

ug/dscm 2.38E-01 2.52E-01 2.83E-01 0.258

ug/dscm@7%O2 2.25E-01 2.38E-01 2.67E-01 0.243

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00718 0.00739 0.00835 0.008

Elb/hr 1.24E-02 1.28E-02 1.45E-02 0.013

lb/mmBtuO2 1.90E-06 1.94E-06 2.20E-06 0.000

ug/dscm 2.19E+00 2.24E+00 2.54E+00 2.323

ug/dscm@7%O2 2.07E+00 2.12E+00 2.40E+00 2.197

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00014 0.00016 0.00019 0.000

Elb/hr 2.42E-04 2.78E-04 3.30E-04 0.000

lb/mmBtuO2 3.70E-08 4.21E-08 5.01E-08 0.000

ug/dscm 4.26E-02 4.86E-02 5.79E-02 0.050

ug/dscm@7%O2 4.02E-02 4.59E-02 5.46E-02 0.047

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00227 0.00131 0.00043 0.001

Elb/hr 3.92E-03 2.28E-03 7.46E-04 0.002

lb/mmBtuO2 5.99E-07 3.45E-07 1.13E-07 0.000

ug/dscm 6.91E-01 3.98E-01 1.31E-01 0.407

ug/dscm@7%O2 6.53E-01 3.76E-01 1.24E-01 0.384

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0025 0.0028 0.0048 0.003

Elb/hr 4.32E-03 4.87E-03 8.33E-03 0.006

lb/mmBtuO2 6.60E-07 7.37E-07 1.27E-06 0.000

ug/dscm 7.61E-01 8.50E-01 1.46E+00 1.024

ug/dscm@7%O2 7.19E-01 8.03E-01 1.38E+00 0.967

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00035 0.00027 0.0008 0.000

Elb/hr 6.05E-04 4.69E-04 1.39E-03 0.001

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

lb/mmBtuO2 9.24E-08 7.10E-08 2.11E-07 0.000

ug/dscm 1.07E-01 8.20E-02 2.44E-01 0.144

ug/dscm@7%O2 1.01E-01 7.74E-02 2.30E-01 0.136

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00143 0.00131 0.00171 0.001

Elb/hr 2.47E-03 2.28E-03 2.97E-03 0.003

lb/mmBtuO2 3.77E-07 3.45E-07 4.51E-07 0.000

ug/dscm 4.35E-01 3.98E-01 5.21E-01 0.451

ug/dscm@7%O2 4.11E-01 3.76E-01 4.92E-01 0.426

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.3319 0.0815 0.0799 0.164

Elb/hr 5.74E-01 1.42E-01 1.39E-01 0.285

lb/mmBtuO2 8.76E-05 2.14E-05 2.11E-05 0.000

ug/dscm 1.01E+02 2.47E+01 2.43E+01 50.000

ug/dscm@7%O2 9.54E+01 2.33E+01 2.29E+01 47.200

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.00264 0.00361 0.0043 0.004

Elb/hr 4.56E-03 6.27E-03 7.46E-03 0.006

lb/mmBtuO2 6.97E-07 9.50E-07 1.13E-06 0.000

ug/dscm 8.04E-01 1.10E+00 1.31E+00 1.071

ug/dscm@7%O2 7.59E-01 1.04E+00 1.24E+00 1.013

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.06074 0.05494 0.06604 0.061

Elb/hr 1.05E-01 9.55E-02 1.15E-01 0.105

lb/mmBtuO2 1.60E-05 1.45E-05 1.74E-05 0.000

ug/dscm 1.85E+01 1.67E+01 2.01E+01 18.433

ug/dscm@7%O2 1.75E+01 1.58E+01 1.90E+01 17.433

Location: Stack Exit - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 27.8 21.9 20.6 23.433

Elb/hr 4.60E+01 3.56E+01 3.43E+01 38.633

gr/dscf 3.50E-03 2.72E-03 2.64E-03 0.003

gr/dscf@7%O2 3.31E-03 2.57E-03 2.49E-03 0.003

lb/mmBtuO2 6.95E-03 5.40E-03 5.24E-03 0.006

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 31 42.6 42 38.533

Elb/hr 5.13E+01 6.92E+01 6.99E+01 63.467

gr/dscf 3.91E-03 5.30E-03 5.39E-03 0.005

gr/dscf@7%O2 3.69E-03 5.00E-03 5.09E-03 0.005

lb/mmBtuO2 7.75E-03 1.05E-02 1.07E-02 0.010

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 5.5 4.5 4.1 4.700

Elb/hr 9.09E+00 7.31E+00 6.82E+00 7.740

gr/dscf 6.93E-04 5.60E-04 5.26E-04 0.001

gr/dscf@7%O2 6.54E-04 5.29E-04 4.96E-04 0.001

lb/mmBtuO2 1.38E-03 1.11E-03 1.04E-03 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 62.3 67 64.7 64.667

Elb/hr 1.03E+02 1.09E+02 1.08E+02 106.667

gr/dscf 7.85E-03 8.33E-03 8.30E-03 0.008

gr/dscf@7%O2 7.41E-03 7.87E-03 7.83E-03 0.008

lb/mmBtuO2 1.56E-02 1.65E-02 1.65E-02 0.016

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

1 Unit Gross Electrical Output 670.5 MW 661 Run 1 PM/Metals

4 Unit Gross Electrical Output 0 MW 661

1 Heat Input 5734.5 MillionBTU/Hr 6368 Run 1 PM/Metals

5 Unit Gross Electrical Output 670.3 MW 661 Run 2 PM/Metals

5 Heat Input 5756.1 MillionBTU/Hr 6368 Run 2 PM/Metals

6 Unit Gross Electrical Output 670.4 MW 661 Run 3 PM/Metals

6 Heat Input 5742.8 MillionBTU/Hr 6368 Run 3 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 6/24/2010 6/24/2010 6/24/2010

Run Start Time 7:56:00 AM 11:28:00 AM 2:56:00 PM

Run Finish Time 11:11:00 AM 2:41:00 PM 6:09:00 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 29.35 29.35 29.35 29.350

Average Orifice Meter Differential, inches H2O 1.63 1.65 1.64 1.640

Dry Gas Meter Volume Sampled, cubic feet 119.752 120.431 120.180 120.121

Average Dry Gas Meter Temperature, °F 94.14 95.54 96.10 95.260

Dry Gas Meter Volume Sampled, dscf 115.983 116.352 115.990 116.108

Total Moisture Liquid collected, g 540.4 514.9 528.3 527.867

Volume of Water Vapor, standard cubic feet 25.44 24.24 24.87 24.850

Moisture Content of Stack Gas, % 17.99 17.24 17.66 17.630

Moisture Saturation at Stack Gas Temperature, % 16.30 16.11 16.17 16.193

Dry Mole Fraction 0.837 0.8389 0.8383 0.838

Carbon Dioxide, % 13.19 13.23 13.2 13.207

Oxygen, % 6.18 6.18 6.17 6.177

Carbon Monoxide & Nitrogen, % 80.63 80.59 80.63 80.617

Fuel Factor 1.12 1.11 1.12

Dry Molecular Weight, lb/lb-Mole 30.36 30.36 30.36 30.360

Wet Molecular weight, lb/lb-Mole 28.65 28.57 28.63 28.617

Flue Gas Static Pressure, inches of H2O -1.2 -1.1 -1.1 -1.133

Absolute Flue Gas Pressure, inches of Mercury 29.26 29.27 29.27 29.267

Average Stack Gas Temperature, °F 132.03 131.61 131.75 131.797

Average Velocity Head, inches of H2O 1.4666836391

4607

1.480068296

73705

1.472010138

31055

1.473

Average Stack Gas Velocity, feet/second 73.09 73.48 73.21 73.260

Stack Cross-Sectional Area, square feet 473.361 473.361 473.361 473.361

Dry Volumetric Flow Rate, dry scfm 1,515,409.8 1,528,560.4 1,521,494.5 1,521,821.5

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,075,877.3 2,086,954.0 2,079,285.5 2,080,705.6

00

Percent Isokinetic of Sampling Rate, % 99.1 98.5 98.7 98.767

Percent Excess Air, % 40.9 40.9 40.8 40.867

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

Round Duct Diameter, inches 294.6 294.6 294.6

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