Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

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 23, 2011 Page 1 of 10
Facility Information:

Vectren FB Culley Generating Station

Contact:

Phone:

Fax:

Email:

Testing Company:

Contact:

Phone:

Fax:

Email:

Air Permit Number: Permitted Source ID/Name:

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:

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description

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

2/3 Common 

Stack

23.969 0 0 0 8 2 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

2/3 Common Custom CTM033 3 60 0

Stack

2/3 Common Hydrogen Fluoride Method 26A 3 60 0

Stack

2/3 Common Hydrogen Chloride Method 26A 3 60 0

Stack

2/3 Common Co2 Method 3A CO2 3 60 0

Stack

Wednesday, February 23, 2011 Page 2 of 10
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.

2/3 Common O2 Method 3A O2 3 60 0

Stack

Wednesday, February 23, 2011 Page 3 of 10
Sampling / Stack Data Results Summary

Location 2/3 Common Stack - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 3/31/2010 3/31/2010 3/31/2010

Run Start Time 5:55:00 PM 7:10:00 PM 8:30:00 PM

Run Finish Time 7:01:00 PM 8:16:00 PM 9:36:00 PM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 38.509 38.074 38.824 38.469

Moisture Content of Stack Gas, % 13.60 13.57 13.15 13.440

Moisture Saturation at Stack Gas Temperature, % 14.09 14.09 14.09 14.090

Carbon Dioxide, % 11.5 11.5 11.5 11.500

Oxygen, % 7.3 7.5 7.4 7.400

Average Stack Gas Temperature, °F 127.00 127.00 127.00 127.000

Dry Volumetric Flow Rate, dry scfm 6,630.1 6,560.2 6,705.3 6,631.867

Actual Wet Volumetric Flue Gas Flow Rate, acfm 8,626.4 8,532.4 8,679.0 8,612.600

Percent Isokinetic of Sampling Rate, % 100.7 100.6 100.4 100.567

F-Factor, dscfm/MMBtu @ %O2 9619 9600 9612 9,610.333

Fw 0 0 0 0.000

Fc 1775 1776 1785 1,778.667

Location 2/3 Common Stack - 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 23, 2011 Page 4 of 10
Location 2/3 Common Stack - 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

Wednesday, February 23, 2011 Page 5 of 10
Emissions Summary

Process Run Data

Location: 2/3 Common Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 120 120 120 120.000

lb/mmBtuO2 1.02E-01 1.04E-01 1.01E-01 0.102

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 80 80 80 80.000

lb/mmBtuO2 6.77E-02 6.94E-02 6.76E-02 0.068

Wednesday, February 23, 2011 Page 6 of 10
Process Run Data

APCD Run Data

Process Lab Run Data

Wednesday, February 23, 2011 Page 7 of 10
Sampling / Stack Data Results Detail

Location 2/3 Common Stack - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 3/31/2010 3/31/2010 3/31/2010

Run Start Time 5:55:00 PM 7:10:00 PM 8:30:00 PM

Run Finish Time 7:01:00 PM 8:16:00 PM 9:36:00 PM

Net Traversing Points 16 16 16

Net Run Time, minutes 60 60 60

Nozzle Diameter, inches 0.235 0.235 0.235 0.235

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.991 0.991 0.991 0.991

Barometric Pressure, inches of Mercury 29.61 29.61 29.61 29.610

Average Orifice Meter Differential, inches H2O 1.18 1.15 1.19 1.173

Dry Gas Meter Volume Sampled, cubic feet 40.686 40.279 40.994 40.653

Average Dry Gas Meter Temperature, °F 88.71 89.38 88.38 88.823

Dry Gas Meter Volume Sampled, dscf 38.509 38.074 38.824 38.469

Total Moisture Liquid collected, g 128.7 127.1 125 126.933

Volume of Water Vapor, standard cubic feet 6.06 5.98 5.88 5.973

Moisture Content of Stack Gas, % 13.60 13.57 13.15 13.440

Moisture Saturation at Stack Gas Temperature, % 14.09 14.09 14.09 14.090

Dry Mole Fraction 0.864 0.8643 0.8685 0.866

Carbon Dioxide, % 11.5 11.5 11.5 11.500

Oxygen, % 7.3 7.5 7.4 7.400

Carbon Monoxide & Nitrogen, % 81.2 81 81.1 81.100

Fuel Factor 1.18 1.17 1.17

Dry Molecular Weight, lb/lb-Mole 30.13 30.14 30.14 30.137

Wet Molecular weight, lb/lb-Mole 28.48 28.49 28.54 28.503

Flue Gas Static Pressure, inches of H2O -0.25 -0.25 -0.25 -0.250

Absolute Flue Gas Pressure, inches of Mercury 29.59 29.59 29.59 29.590

Average Stack Gas Temperature, °F 127.00 127.00 127.00 127.000

Average Velocity Head, inches of H2O 0.5863876029

68825

0.573805610

776973

0.594662022

11534

0.585

Average Stack Gas Velocity, feet/second 45.89 45.39 46.17 45.817

Stack Cross-Sectional Area, square feet 3.133 3.133 3.133 3.133

Dry Volumetric Flow Rate, dry scfm 6,630.1 6,560.2 6,705.3 6,631.867

Actual Wet Volumetric Flue Gas Flow Rate, acfm 8,626.4 8,532.4 8,679.0 8,612.600

Percent Isokinetic of Sampling Rate, % 100.7 100.6 100.4 100.567

Percent Excess Air, % 51.6 54.0 52.8 52.800

F-Factor, dscfm/MMBtu @ %O2 9619 9600 9612 9,610.333

Round Duct Diameter, inches 23.969 23.969 23.969

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 1775 1776 1785 1,778.667

Wednesday, February 23, 2011 Page 8 of 10
Location 2/3 Common Stack - 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 23, 2011 Page 9 of 10
Location 2/3 Common Stack - 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 23, 2011 Page 10 of 10