Name: Kevin Frizzell

Title: Director of Power Production

Company: Owensboro Municipal Utilities

Sign Date: 8/27/2010

Name: Chet Gutwein

Title: Engineer

Company: Airtech Environmental Services Inc.

Sign Date: 8/27/2010

Permitted Facility Representative / Date Testing Company Representative / Date

3302 Owensboro Municipal Utilities

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.

Monday, January 31, 2011 Page 1 of 16
3302 Owensboro Municipal Utilities

8/27/2010

Facility Information:

Elmer Smith Station

4301 US 60 East

Owensboro KY 42303

Contact: Kevin Frizzell

Phone: 270-926-3200 ext. 298

Fax: 270-686-8541

Email: frizzellkd@omu.org

Testing Company:

Airtech Environmental Services Inc.

601A Country Club Drive

Bensenville IL 60106

Contact:Brandon Check

Phone: (630) 860-4740

Fax: (630) 860-4745

Email: bcheck@airtechenv.com

Air Permit Number:

1374

Permitted Source ID/Name:

1/2 Combined Stack

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 2105900027 FRS #: 110000741653

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 0 0 294 2 14.4 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Monday, January 31, 2011 Page 2 of 16
3302 Owensboro Municipal Utilities

8/27/2010

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.

The following is a list of the test methods that are to be used for this test program and their respective promulgation 

dates:

Methods 1 through 29 – August 1997

Method 30B – January 2008

Other Test Method 28 – April 2009

Stack Exit Lead Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Filterable Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Organic Condensible 

Particulate

Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Total Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

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

Monday, January 31, 2011 Page 3 of 16
3302 Owensboro Municipal Utilities

8/27/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 6/29/2010 6/30/2010 6/30/2010

Run Start Time 11:08:00 AM 6:45:00 

AM

11:45:00 AM

Run Finish Time 2:08:00 PM 9:45:00 

AM

2:45:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 92.372 94.074 90.837 92.428

Moisture Content of Stack Gas, % 17.21 16.54 17.13 16.960

Moisture Saturation at Stack Gas Temperature, % 16.67 16.10 15.99 16.253

Carbon Dioxide, % 13 13 13 13.000

Oxygen, % 7 7 7 7.000

Average Stack Gas Temperature, °F 133.75 132.58 132.33 132.887

Dry Volumetric Flow Rate, dry scfm 875,399.6 894,101.8 886,503.9 885,335.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,180,944.7 1,190,844.8 1,178,681.8 1,183,490.43

3

Percent Isokinetic of Sampling Rate, % 104.7 104.4 101.7 103.600

F-Factor, dscfm/MMBtu @ %O2 9621 9554 9613 9,596.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Monday, January 31, 2011 Page 4 of 16
3302 Owensboro Municipal Utilities

8/27/2010

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 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

Monday, January 31, 2011 Page 5 of 16
3302 Owensboro Municipal Utilities

8/27/2010

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

Monday, January 31, 2011 Page 6 of 16
3302 Owensboro Municipal Utilities

8/27/2010

Emissions Summary

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 4.26 3.72 3.67 3.883

Elb/hr 5.34E+00 4.68E+00 4.74E+00 4.920

lb/mmBtuO2 1.47E-03 1.25E-03 1.29E-03 0.001

mg/dscm 1.63E+00 1.40E+00 1.43E+00 1.487

mg/dscm@7%O2 1.63E+00 1.40E+00 1.43E+00 1.487

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.706 0.644 0.579 0.643

Elb/hr 8.85E-01 8.10E-01 7.47E-01 0.814

lb/mmBtuO2 2.44E-04 2.17E-04 2.03E-04 0.000

mg/dscm 2.70E-01 2.42E-01 2.25E-01 0.246

mg/dscm@7%O2 2.70E-01 2.42E-01 2.25E-01 0.246

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00343 0.006 0.00322 0.004

Elb/hr 3.40E-03 5.80E-03 3.14E-03 0.004

lb/mmBtuO2 9.20E-07 1.56E-06 8.44E-07 0.000

mg/dscm 1.02E-03 1.74E-03 9.36E-04 0.001

mg/dscm@7%O2 1.02E-03 1.74E-03 9.36E-04 0.001

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0552 0.0415 0.0539 0.050

Elb/hr 5.47E-02 4.01E-02 5.25E-02 0.049

lb/mmBtuO2 1.48E-05 1.08E-05 1.41E-05 0.000

mg/dscm 1.64E-02 1.20E-02 1.57E-02 0.015

mg/dscm@7%O2 1.64E-02 1.20E-02 1.57E-02 0.015

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00101 0.000322 0.000375 0.001

Elb/hr 1.00E-03 3.12E-04 3.65E-04 0.001

lb/mmBtuO2 2.71E-07 8.37E-08 9.83E-08 0.000

mg/dscm 3.00E-04 9.34E-05 1.09E-04 0.000

mg/dscm@7%O2 3.00E-04 9.34E-05 1.09E-04 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0019 0.00107 0.00259 0.002

Monday, January 31, 2011 Page 7 of 16
3302 Owensboro Municipal Utilities

8/27/2010

Elb/hr 1.88E-03 1.04E-03 2.52E-03 0.002

lb/mmBtuO2 5.09E-07 2.78E-07 6.79E-07 0.000

mg/dscm 5.64E-04 3.10E-04 7.52E-04 0.001

mg/dscm@7%O2 5.64E-04 3.10E-04 7.52E-04 0.001

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00875 0.00848 0.00716 0.008

Elb/hr 8.67E-03 8.20E-03 6.97E-03 0.008

lb/mmBtuO2 2.35E-06 2.20E-06 1.88E-06 0.000

mg/dscm 2.60E-03 2.46E-03 2.08E-03 0.002

mg/dscm@7%O2 2.60E-03 2.46E-03 2.08E-03 0.002

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.001642 0.001682 0.001292 0.002

Elb/hr 1.63E-03 1.63E-03 1.26E-03 0.002

lb/mmBtuO2 4.40E-07 4.37E-07 3.39E-07 0.000

mg/dscm 4.87E-04 4.88E-04 3.75E-04 0.000

mg/dscm@7%O2 4.87E-04 4.88E-04 3.75E-04 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 55.2 74.4 51.9 60.500

Elb/hr 5.47E+01 7.20E+01 5.05E+01 59.067

lb/mmBtuO2 1.48E-02 1.93E-02 1.36E-02 0.016

mg/dscm 1.64E+01 2.16E+01 1.51E+01 17.700

mg/dscm@7%O2 1.64E+01 2.16E+01 1.51E+01 17.700

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.003467 0.004587 0.005587 0.005

Elb/hr 3.44E-03 4.44E-03 5.44E-03 0.004

lb/mmBtuO2 9.29E-07 1.19E-06 1.46E-06 0.000

mg/dscm 1.03E-03 1.33E-03 1.62E-03 0.001

mg/dscm@7%O2 1.03E-03 1.33E-03 1.62E-03 0.001

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.00819 0.00777 0.00959 0.009

Elb/hr 8.12E-03 7.52E-03 9.34E-03 0.008

lb/mmBtuO2 2.20E-06 2.02E-06 2.51E-06 0.000

mg/dscm 2.43E-03 2.25E-03 2.79E-03 0.002

mg/dscm@7%O2 2.43E-03 2.25E-03 2.79E-03 0.002

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.010648 0.011248 0.009528 0.010

Monday, January 31, 2011 Page 8 of 16
3302 Owensboro Municipal Utilities

8/27/2010

Elb/hr 1.06E-02 1.09E-02 9.28E-03 0.010

lb/mmBtuO2 2.85E-06 2.92E-06 2.50E-06 0.000

mg/dscm 3.16E-03 3.26E-03 2.77E-03 0.003

mg/dscm@7%O2 3.16E-03 3.26E-03 2.77E-03 0.003

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.351 0.287 0.312 0.317

Elb/hr 3.48E-01 2.78E-01 3.04E-01 0.310

lb/mmBtuO2 9.41E-05 7.46E-05 8.18E-05 0.000

mg/dscm 1.04E-01 8.32E-02 9.06E-02 0.093

mg/dscm@7%O2 1.04E-01 8.32E-02 9.06E-02 0.093

Location: Stack Exit - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 29.8 54.1 69.4 51.100

Elb/hr 2.85E+01 5.14E+01 6.69E+01 48.933

lb/mmBtuO2 7.66E-03 1.42E-02 1.84E-02 0.013

mg/dscm 8.48E+00 1.59E+01 2.04E+01 14.927

mg/dscm@7%O2 8.48E+00 1.59E+01 2.04E+01 14.927

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 86.2 56.5 128.1 90.267

Elb/hr 8.25E+01 5.37E+01 1.23E+02 86.400

lb/mmBtuO2 2.22E-02 1.49E-02 3.39E-02 0.024

mg/dscm 2.45E+01 1.66E+01 3.76E+01 26.233

mg/dscm@7%O2 2.45E+01 1.66E+01 3.76E+01 26.233

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 10.3 10.1 9.8 10.067

Elb/hr 9.85E+00 9.59E+00 9.44E+00 9.627

lb/mmBtuO2 2.65E-03 2.66E-03 2.60E-03 0.003

mg/dscm 2.93E+00 2.97E+00 2.88E+00 2.927

mg/dscm@7%O2 2.93E+00 2.97E+00 2.88E+00 2.927

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 126.3 80.9 207.3 138.167

Elb/hr 1.21E+02 7.68E+01 2.00E+02 132.600

lb/mmBtuO2 3.25E-02 2.13E-02 5.49E-02 0.036

mg/dscm 3.60E+01 2.38E+01 6.09E+01 40.233

mg/dscm@7%O2 3.60E+01 2.38E+01 6.09E+01 40.233

Location: Stack Exit - Method 7E

Monday, January 31, 2011 Page 9 of 16
3302 Owensboro Municipal Utilities

8/27/2010

Process Run Data

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 8.26E+02 8.17E+02 7.67E+02 803.333

lb/mmBtuO2 2.27E-01 2.19E-01 2.08E-01 0.218

mg/dscm 2.52E+02 2.44E+02 2.30E+02 242.000

mg/dscm@7%O2 2.52E+02 2.44E+02 2.30E+02 242.000

ppm 1.31E+02 1.27E+02 1.20E+02 126.000

ppm@7%O2 1.31E+02 1.27E+02 1.20E+02 126.000

Monday, January 31, 2011 Page 10 of 16
3302 Owensboro Municipal Utilities

8/27/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 0.1649 1000 Tons/hr Unit 1 and Unit 2 

Combined Process 

Data

0.16

1 Average Heat Input 3923 MMBtu/hr Unit 1 and Unit 2 

Combined Process 

Data

3900

1 Steam Output 2571.9 1000 lb steam/hr Unit 1 and Unit 2 

Combined Process 

Data

2600

1 Petroleum Coke Firing Rate 0.0042 Unit 1 Process 

Data

0.0042

1 Flue Gas Flow Rate 840497 dscfm 850000

1 Pressure Drop Across FGD (if applicable) 2.29 in H20 2.5

1 FGD Scrubber Liquor pH 5.71 pH 5.6

1 FGD Scrubber Liquor Flow Rate 193.84 gal/min 180

1 Flue Gas Oxygen Content 7 % 7 Stack Testing Data

1 Flue Gas Carbon Dioxide Content 13 % 13 Stack Testing Data

1 Flue Gas Moisture Content 15.6 % 15.6

1 Flue Gas Sampling Point Temperature 133 Deg F 135

1 Standard Pressure 1 atm 1

1 Unit Gross Electrical Output 501 MW Unit 1 and Unit 2 

Combined Process 

Data

400

1 Unit Net Electric Generation 359 MWh Unit 1 and Unit 2 

Combined Process 

Data

360

2 Bituminous Coal Burned 0.1716 1000 Tons/hr Unit 1 and Unit 2 

Combined Process 

Data

0.16

2 Average Heat Input 4062 MMBtu/hr Unit 1 and Unit 2 

Combined Process 

Data

3900

2 Steam Output 2592.2 1000 lb steam/hr Unit 1 and Unit 2 

Combined Process 

Data

2600

2 Petroleum Coke Firing Rate 0.0042 Unit 1 Process 

Data

0.0042

2 Flue Gas Flow Rate 851696 dscfm 850000

2 Pressure Drop Across FGD (if applicable) 2.28 in H20 2.5

2 FGD Scrubber Liquor pH 5.52 pH 5.6

Monday, January 31, 2011 Page 11 of 16
3302 Owensboro Municipal Utilities

8/27/2010

APCD Run Data

Process Lab Run Data

2 FGD Scrubber Liquor Flow Rate 203.5 gal/min 180

2 Flue Gas Oxygen Content 7 % 7 Stack Testing Data

2 Flue Gas Carbon Dioxide Content 13 % 13 Stack Testing Data

2 Flue Gas Moisture Content 15.6 % 15.6

2 Flue Gas Sampling Point Temperature 129 Deg F 135

2 Standard Pressure 1 atm 1

2 Unit Gross Electrical Output 399 MW Unit 1 and Unit 2 

Combined Process 

Data

400

2 Unit Net Electric Generation 361 MWh Unit 1 and Unit 2 

Combined Process 

Data

360

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 0

1 ELECTROSTATIC PRECIPITATOR 0 0

1 SCRUBBER 0 0

1 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 0

Run Name Value UOM Comments

1 See 4b Comments. 0

Monday, January 31, 2011 Page 12 of 16
3302 Owensboro Municipal Utilities

8/27/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 6/29/2010 6/30/2010 6/30/2010

Run Start Time 11:08:00 AM 6:45:00 AM 11:45:00 AM

Run Finish Time 2:08:00 PM 9:45:00 AM 2:45:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.22 0.22 0.22 0.220

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.0013 1.0013 1.0013 1.001

Barometric Pressure, inches of Mercury 29.94 30.06 30.06 30.020

Average Orifice Meter Differential, inches H2O 0.84 0.87 0.83 0.847

Dry Gas Meter Volume Sampled, cubic feet 95.820 94.450 93.080 94.450

Average Dry Gas Meter Temperature, °F 89.92 74.42 85.38 83.240

Dry Gas Meter Volume Sampled, dscf 92.372 94.074 90.837 92.428

Total Moisture Liquid collected, g 408 396 399 401.000

Volume of Water Vapor, standard cubic feet 19.20 18.64 18.78 18.873

Moisture Content of Stack Gas, % 17.21 16.54 17.13 16.960

Moisture Saturation at Stack Gas Temperature, % 16.67 16.10 15.99 16.253

Dry Mole Fraction 0.8333 0.839 0.8401 0.837

Carbon Dioxide, % 13 13 13 13.000

Oxygen, % 7 7 7 7.000

Carbon Monoxide & Nitrogen, % 80 80 80 80.000

Fuel Factor 1.07 1.07 1.07

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

Wet Molecular weight, lb/lb-Mole 28.40 28.45 28.59 28.480

Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200

Absolute Flue Gas Pressure, inches of Mercury 29.93 30.05 30.05 30.010

Average Stack Gas Temperature, °F 133.75 132.58 132.33 132.887

Average Velocity Head, inches of H2O 0.4839317593

7993

0.495761941

330468

0.488283724

992809

0.489

Average Stack Gas Velocity, feet/second 41.75 42.10 41.67 41.840

Stack Cross-Sectional Area, square feet 471.435 471.435 471.435 471.435

Dry Volumetric Flow Rate, dry scfm 875,399.6 894,101.8 886,503.9 885,335.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,180,944.7 1,190,844.8 1,178,681.8 1,183,490.4

33

Percent Isokinetic of Sampling Rate, % 104.7 104.4 101.7 103.600

Percent Excess Air, % 49.6 49.6 49.6 49.600

F-Factor, dscfm/MMBtu @ %O2 9621 9554 9613 9,596.000

Round Duct Diameter, inches 294 294 294

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Monday, January 31, 2011 Page 13 of 16
3302 Owensboro Municipal Utilities

8/27/2010

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

Monday, January 31, 2011 Page 14 of 16
3302 Owensboro Municipal Utilities

8/27/2010

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

Monday, January 31, 2011 Page 15 of 16
3302 Owensboro Municipal Utilities

8/27/2010

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

Monday, January 31, 2011 Page 16 of 16