Name: Caitlin Schiebel

Title: Air Compliance Specialist

Company: American Municipal Power

Sign Date:

Name: Carl Vineyard

Title: Utility MACT Program Manager

Company: Grace Consulting, Inc.

Sign Date: 9/3/2010

Permitted Facility Representative / Date Testing Company Representative / Date

AMERICAN MUNICIPAL POWER

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, January 18, 2011 Page 1 of 28
AMERICAN MUNICIPAL POWER

Facility Information:

American Municipal Power, RH Gorsuch St

1111Schrock Road

Suite 100

Columbus OH 43229

Contact: Caitlin Schiebel

Phone: 614-540-1111

Fax:

Email: cschiebel@amppartners.org

Testing Company:

Grace Consulting, Inc.

510 Dickson Street

Wellington OH 44090

Contact:Carl Vineyard

Phone: 440-647-6672

Fax: 440-647-6673

Email: carlvineyard@gcitest.com

Air Permit Number:

06-84-02-0037

Permitted Source ID/Name:

AMP RHGorsuch

Permitted Maximum Process Rate: Max. Normal Operation Process Rate:

510 mmBtu/hr

Target Process Test Rate

510 mmBtu/hr

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

 process flow diagram:

Unit 3 is a 53.3 MW coal-fired boiler, using bituminous coal the feed rate is approsimately 25 tons of coal per hour. 

A Upstream Downstream drawing is attached.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 3911900004 FRS #: 110000850525

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

Duct 3 120 96 106.8 148 236 5 25

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Duct 3 Carbon Monoxide Method 10 3 180 0

Total organic compounds 

(TOC) as Propane

Duct 3 Method 25A 3 180 0

Duct 3 Hydrogen Chloride Method 26A 3 188 0

Duct 3 Hydrogen Fluoride Method 26A 3 188 0

Duct 3 Total PM2.5 OTM - 27/28 3 180 0

Duct 3 Filterable Particulate OTM - 27/28 3 180 0

Duct 3 Filterable PM2.5 OTM - 27/28 3 180 0

Tuesday, January 18, 2011 Page 2 of 28
AMERICAN MUNICIPAL POWER

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 HCN was sampled using CTM 033 with 2 Normal NaOH and an additional impinger for one hour per the 

clarification givenby the USEPA. The Comment Section has additional explanations.

Inorganic (Aqueous) 

Condensible Part.

Duct 3 OTM - 27/28 3 180 0

Duct 3 Total Particulate OTM - 27/28 3 180 0

Organic Condensible 

Particulate

Duct 3 OTM - 27/28 3 180 0

Duct 3 Cobalt Method 29 3 250 0

Duct 3 Phosphorus (yellow or white) Method 29 3 250 0

Duct 3 Nickel Method 29 3 250 0

Duct 3 Manganese Method 29 3 250 0

Duct 3 Filterable Particulate Method 29 3 250 0

Duct 3 Beryllium Method 29 3 250 0

Duct 3 Chromium Method 29 3 250 0

Duct 3 Cadmium Method 29 3 250 0

Duct 3 Selenium Method 29 3 250 0

Duct 3 Antimony Method 29 3 250 0

Duct 3 Arsenic Method 29 3 250 0

Duct 3 Lead Method 29 3 250 0

Duct 3 Co2 Method 3A CO2 3 180 0

Duct 3 O2 Method 3A O2 3 180 0

Duct 3 Sulfur Dioxide Method 6C 3 180 0

Duct 3 Nitrogen oxides (NOx) Method 7E 3 180 0

Tuesday, January 18, 2011 Page 3 of 28
AMERICAN MUNICIPAL POWER

Sampling / Stack Data Results Summary

Location Duct 3 - Method 10

Average

Run Number 1 2 3

Test Date 6/17/2010 6/17/2010 6/17/2010

Run Start Time 12:15:00 PM 3:15:00 PM 6:00:00 PM

Run Finish Time 2:45:00 PM 5:43:00 PM 8:29:00 PM

Carbon Dioxide, % 9.5 9.3 9.3 9.367

Oxygen, % 8.1 7.9 7.7 7.900

Dry Volumetric Flow Rate, dry scfm 267656 271415 275855 271,642.000

F-Factor, dscfm/MMBtu @ %O2 9789 9785 9106 9,560.000

Moisture, % 6.42 6.65 6.45 6.507

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Duct 3 - Method 25A

Average

Run Number 1 2 3

Test Date 6/17/2010 6/17/2010 6/17/2010

Run Start Time 12:15:00 PM 3:15:00 PM 6:00:00 PM

Run Finish Time 2:45:00 PM 5:43:00 PM 8:29:00 PM

Carbon Dioxide, % 9.5 9.3 9.3 9.367

Oxygen, % 8.1 7.9 7.7 7.900

Dry Volumetric Flow Rate, dry scfm 267656 271415 275855 271,642.000

F-Factor, dscfm/MMBtu @ %O2 9789 9785 9106 9,560.000

Moisture, % 6.42 6.65 6.45 6.507

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 4 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 26A

Average

Run Number 1 2 3

Test Date 6/16/2010 6/16/2010 6/17/2010

Run Start Time 1:45:00 PM 5:20:00 PM 8:05:00 AM

Run Finish Time 4:53:45 PM 8:28:45 PM 11:14:45 AM

Net Run Time, minutes 187.5 187.5 187.5

Dry Gas Meter Volume Sampled, dscf 154.191 158.783 155.354 156.109

Moisture Content of Stack Gas, % 6.80 6.66 6.38 6.613

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

Carbon Dioxide, % 10.1 9.7 8.9 9.567

Oxygen, % 8.3 8.6 9.3 8.733

Average Stack Gas Temperature, °F 316.48 307.96 316.26 313.567

Dry Volumetric Flow Rate, dry scfm 251,475.8 256,239.5 252,107.6 253,274.300

Actual Wet Volumetric Flue Gas Flow Rate, acfm 396,672.0 399,552.0 395,376.0 397,200.000

Percent Isokinetic of Sampling Rate, % 99.1 100.2 99.6 99.633

F-Factor, dscfm/MMBtu @ %O2 9712 9068 9055 9,278.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Duct 3 - Method 29

Average

Run Number 1 2 3

Test Date 6/15/2010 6/15/2010 6/16/2010

Run Start Time 11:15:00 AM 4:45:00 PM 8:05:00 AM

Run Finish Time 4:00:00 PM 9:25:00 PM 12:40:00 PM

Net Run Time, minutes 250 250 250

Dry Gas Meter Volume Sampled, dscf 202.604 206.323 209.787 206.238

Moisture Content of Stack Gas, % 7.17 7.54 7.68 7.463

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

Carbon Dioxide, % 9.6 9.9 10.1 9.867

Oxygen, % 9.6 9.4 9.2 9.400

Average Stack Gas Temperature, °F 316.98 315.82 316.28 316.360

Dry Volumetric Flow Rate, dry scfm 246,013.9 247,788.5 249,119.6 247,640.667

Actual Wet Volumetric Flue Gas Flow Rate, acfm 390,768.0 394,704.0 396,864.0 394,112.000

Percent Isokinetic of Sampling Rate, % 99.8 100.9 102.1 100.933

F-Factor, dscfm/MMBtu @ %O2 9266 9907 9814 9,662.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 5 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 6/15/2010 6/15/2010 6/16/2010

Run Start Time 11:15:00 AM 4:45:00 PM 8:05:00 AM

Run Finish Time 4:00:00 PM 9:25:00 PM 12:37:00 PM

Carbon Dioxide, % 9.6 9.9 10.1 9.867

Oxygen, % 9.6 9.4 9.2 9.400

Dry Volumetric Flow Rate, dry scfm 264982 267999 269812 267,597.667

F-Factor, dscfm/MMBtu @ %O2 9266 9907 9814 9,662.333

Moisture, % 7.17 7.54 7.68 7.463

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Duct 3 - Method 3A CO2 3

Average

Run Number 4 5 6

Test Date 6/16/2010 6/16/2010 6/17/2010

Run Start Time 1:45:00 PM 5:20:00 PM 8:05:00 AM

Run Finish Time 4:53:00 PM 8:28:00 PM 11:13:00 AM

Carbon Dioxide, % 10.1 9.7 8.9 9.567

Oxygen, % 8.3 8.6 9.3 8.733

Dry Volumetric Flow Rate, dry scfm 270025 274527 269454 271,335.333

F-Factor, dscfm/MMBtu @ %O2 9712 9068 9055 9,278.333

Moisture, % 6.81 6.67 6.38 6.620

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 6 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 3A CO2 3 6

Average

Run Number 7 8 9

Test Date 6/17/2010 6/17/2010 6/17/2010

Run Start Time 12:15:00 PM 3:15:00 PM 6:00:00 PM

Run Finish Time 2:45:00 PM 5:43:00 PM 8:29:00 PM

Carbon Dioxide, % 9.5 9.3 9.3 9.367

Oxygen, % 8.1 7.9 7.7 7.900

Dry Volumetric Flow Rate, dry scfm 267656 271415 275855 271,642.000

F-Factor, dscfm/MMBtu @ %O2 9789 9785 9106 9,560.000

Moisture, % 6.42 6.65 6.45 6.507

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Duct 3 - Method 3A O2

Average

Run Number 1 2 3

Test Date 6/15/2010 6/15/2010 6/16/2010

Run Start Time 11:15:00 AM 4:45:00 PM 8:05:00 AM

Run Finish Time 4:00:00 PM 9:25:00 PM 12:37:00 PM

Carbon Dioxide, % 9.6 9.9 10.1 9.867

Oxygen, % 9.6 9.4 9.2 9.400

Dry Volumetric Flow Rate, dry scfm 264982 267999 269812 267,597.667

F-Factor, dscfm/MMBtu @ %O2 9266 9907 9814 9,662.333

Moisture, % 7.17 7.54 7.68 7.463

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 7 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 3A O2 3

Average

Run Number 4 5 6

Test Date 6/16/2010 6/16/2010 6/17/2010

Run Start Time 1:45:00 PM 5:20:00 PM 8:05:00 AM

Run Finish Time 4:53:00 PM 8:28:00 PM 11:13:00 AM

Carbon Dioxide, % 10.1 9.7 8.9 9.567

Oxygen, % 8.3 8.6 9.3 8.733

Dry Volumetric Flow Rate, dry scfm 270025 274527 269454 271,335.333

F-Factor, dscfm/MMBtu @ %O2 9712 9068 9055 9,278.333

Moisture, % 6.81 6.67 6.38 6.620

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Duct 3 - Method 3A O2 3 6

Average

Run Number 7 8 9

Test Date 6/17/2010 6/17/2010 6/17/2010

Run Start Time 12:15:00 PM 3:15:00 PM 6:00:00 PM

Run Finish Time 2:45:00 PM 5:43:00 PM 8:29:00 PM

Carbon Dioxide, % 9.5 9.3 9.3 9.367

Oxygen, % 8.1 7.9 7.7 7.900

Dry Volumetric Flow Rate, dry scfm 267656 271415 275855 271,642.000

F-Factor, dscfm/MMBtu @ %O2 9789 9785 9106 9,560.000

Moisture, % 6.42 6.65 6.45 6.507

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 1800 0 0 600.000

Tuesday, January 18, 2011 Page 8 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 6C

Average

Run Number 1 2 3

Test Date 6/16/2010 6/16/2010 6/17/2010

Run Start Time 1:45:00 PM 5:20:00 PM 8:05:00 AM

Run Finish Time 4:53:00 PM 8:28:00 PM 11:13:00 AM

Carbon Dioxide, % 10.1 9.7 8.9 9.567

Oxygen, % 8.3 8.6 9.3 8.733

Dry Volumetric Flow Rate, dry scfm 270025 274527 269454 271,335.333

F-Factor, dscfm/MMBtu @ %O2 9712 9068 9055 9,278.333

Moisture, % 6.81 6.67 6.38 6.620

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Duct 3 - Method 7E

Average

Run Number 1 2 3

Test Date 6/16/2010 6/16/2010 6/17/2010

Run Start Time 1:45:00 PM 5:20:00 PM 8:05:00 AM

Run Finish Time 4:53:00 PM 8:28:00 PM 11:13:00 AM

Carbon Dioxide, % 10.1 9.7 8.9 9.567

Oxygen, % 8.3 8.6 9.3 8.733

Dry Volumetric Flow Rate, dry scfm 270025 274527 269454 271,335.333

F-Factor, dscfm/MMBtu @ %O2 9712 9068 9055 9,278.333

Moisture, % 6.81 6.67 6.38 6.620

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 9 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - OTM - 27/28

Average

Run Number 27/28-1 27/28-2 27/28-3

Test Date 6/15/2010 6/15/2010 6/16/2010

Run Start Time 11:15:00 AM 4:45:00 PM 8:00:00 AM

Run Finish Time 2:30:18 PM 8:07:24 PM 11:27:54 AM

Net Run Time, minutes 179.8 179.9 180

Dry Gas Meter Volume Sampled, dscf 66.166 63.786 65.945 65.299

Moisture Content of Stack Gas, % 7.79 7.91 7.74 7.813

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

Carbon Dioxide, % 9.6 9.9 10.1 9.867

Oxygen, % 9.6 9.4 9.2 9.400

Average Stack Gas Temperature, °F 316.75 313.50 312.75 314.333

Dry Volumetric Flow Rate, dry scfm 240,107.0 236,101.3 239,821.0 238,676.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 384,480.0 376,848.0 380,688.0 380,672.000

Percent Isokinetic of Sampling Rate, % 102.6 100.6 102.3 101.833

F-Factor, dscfm/MMBtu @ %O2 9266 9907 9814 9,662.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 10 of 28
AMERICAN MUNICIPAL POWER

Emissions Summary

Location: Duct 3 - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.07E-02 1.82E-02 1.63E-02 0.015

ppm 9.23E+00 1.59E+01 1.55E+01 13.543

ppm@7%O2 1.00E+01 1.70E+01 1.63E+01 14.433

Location: Duct 3 - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 4.44E-03 5.73E-03 7.31E-03 0.006

ppm 2.43E+00 3.18E+00 4.43E+00 3.347

ppm@7%O2 2.64E+00 3.40E+00 4.66E+00 3.567

Location: Duct 3 - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 34.8 35.9 32.9 34.533

lb/mmBtuO2 8.02E-03 7.68E-03 7.62E-03 0.008

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 185 192 201 192.667

lb/mmBtuO2 4.26E-02 4.11E-02 4.65E-02 0.043

Location: Duct 3 - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00335 0.00295 0.00275 0.003

lb/mmBtuO2 6.25E-07 5.68E-07 5.07E-07 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0272 0.0235 0.0295 0.027

lb/mmBtuO2 5.07E-06 4.52E-06 5.43E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.0015 0.00166 0.00156 0.002

lb/mmBtuO2 2.80E-07 3.19E-07 2.87E-07 0.000

Tuesday, January 18, 2011 Page 11 of 28
AMERICAN MUNICIPAL POWER

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00119 0.00316 0.00112 0.002

lb/mmBtuO2 2.22E-07 6.08E-07 2.06E-07 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.03132 0.03822 0.02572 0.032

lb/mmBtuO2 5.84E-06 7.35E-06 4.74E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.0095 0.00683 0.0061 0.007

lb/mmBtuO2 1.77E-06 1.31E-06 1.12E-06 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 76 178.8 283.5 179.433

lb/mmBtuO2 1.42E-02 3.44E-02 5.22E-02 0.034

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.0498 0.0432 0.0219 0.038

lb/mmBtuO2 9.29E-06 8.31E-06 4.03E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.02777 0.02807 0.01907 0.025

lb/mmBtuO2 5.18E-06 5.40E-06 3.51E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0278 0.0254 0.0211 0.025

lb/mmBtuO2 5.18E-06 4.89E-06 3.89E-06 0.000

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Mass_mg 0.2623 0.2283 0.2233 0.238

lb/mmBtuO2 4.89E-05 4.39E-05 4.11E-05 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.4687 0.9927 1.1947 0.885

lb/mmBtuO2 8.74E-05 1.91E-04 2.20E-04 0.000

Tuesday, January 18, 2011 Page 12 of 28
AMERICAN MUNICIPAL POWER

Location: Duct 3 - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 2.76E+00 2.58E+00 2.70E+00 2.680

ppm 1.03E+03 1.01E+03 9.97E+02 1,012.333

ppm@7%O2 1.14E+03 1.14E+03 1.19E+03 1,156.667

Location: Duct 3 - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 2.79E-01 2.49E-01 2.49E-01 0.259

ppm 1.45E+02 1.35E+02 1.28E+02 136.000

ppm@7%O2 1.60E+02 1.53E+02 1.53E+02 155.333

Location: Duct 3 - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 27/28-1 27/28-2 27/28-3

Mass_mg 8.4 30.1 11.6 16.700

lb/mmBtuO2 4.80E-03 1.87E-02 6.80E-03 0.010

Compound: Filterable PM2.5

Average

RunNumber 27/28-1 27/28-2 27/28-3

Mass_mg 4.2 11.4 5 6.867

lb/mmBtuO2 2.40E-03 7.09E-03 2.93E-03 0.004

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 27/28-1 27/28-2 27/28-3

Mass_mg 63.5 48.4 39.6 50.500

lb/mmBtuO2 3.63E-02 3.01E-02 2.32E-02 0.030

Compound: Organic Condensible Particulate

Average

RunNumber 27/28-1 27/28-2 27/28-3

Mass_mg 11.8 13.8 7.4 11.000

lb/mmBtuO2 6.74E-03 8.59E-03 4.34E-03 0.007

Compound: Total Particulate

Average

RunNumber 27/28-1 27/28-2 27/28-3

Mass_mg 83.7 92.3 58.6 78.200

lb/mmBtuO2 4.78E-02 5.74E-02 3.43E-02 0.047

Compound: Total PM2.5

Average

RunNumber 27/28-1 27/28-2 27/28-3

Mass_mg 79.5 73.6 52 68.367

lb/mmBtuO2 4.54E-02 4.58E-02 3.05E-02 0.041

Tuesday, January 18, 2011 Page 13 of 28
AMERICAN MUNICIPAL POWER

Process Run Data

Tuesday, January 18, 2011 Page 14 of 28
AMERICAN MUNICIPAL POWER

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 549 mmBtu/hr 510

1 Steam Flow 540 Klb/hr 500

1 Net MW 47 MWh 43

2 Heat Input 538 mmBtu/hr 510

2 Steam Flow 530 Klb/hr 500

2 Net MW 47 MWh 43

3 Heat Input 517 mmBtu/hr 510

3 Steam Flow 513 Klb/hr 500

3 Net MW 45 MWh 43

Tuesday, January 18, 2011 Page 15 of 28
AMERICAN MUNICIPAL POWER

Sampling / Stack Data Results Detail

Location Duct 3 - Method 10

Average

Run Number 1 2 3

Test Date 6/17/2010 6/17/2010 6/17/2010

Run Start Time 12:15:00 PM 3:15:00 PM 6:00:00 PM

Run Finish Time 2:45:00 PM 5:43:00 PM 8:29:00 PM

Carbon Dioxide, % 9.5 9.3 9.3 9.367

Oxygen, % 8.1 7.9 7.7 7.900

Fuel Factor 1.35 1.4 1.42

Dry Volumetric Flow Rate, dry scfm 267656 271415 275855 271,642.000

F-Factor, dscfm/MMBtu @ %O2 9789 9785 9106 9,560.000

Moisture, % 6.42 6.65 6.45 6.507

Analyzer Make Horiba Horiba Horiba

Analyzer Model VIA-510 VIA-510 VIA-510

Analyzer Serial Number 570124044 570124044 570124044 570,124,044

.000

Operating Range 45.6 45.6 45.6 45.600

Operating Units ppm ppm ppm

No. Readings/Avg. 125 125 125 125.000

Calibration Set 12 12 12 12.000

Calibration Pre Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Pre Zero Cylinder Instrument Response 0.08 0.16 0.01 0.083

Calibration Pre Zero Cylinder Bias -0.33 -0.15 -0.48 -0.320

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0003219 EB0003219 EB0003219

Calibration Pre High Cylinder Instrument Response 30.29 30.33 30.01 30.210

Calibration Pre High Cylinder Bias 0.37 0.46 -0.24 0.197

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Post Zero Cylinder Instrument Response 0.16 0.01 0.09 0.087

Calibration Post Zero Cylinder Bias -0.15 -0.48 -0.31 -0.313

Calibration Post Zero Cylinder Drift 0.18 0.33 0.17 0.227

Calibration Post High Cylinder ID EB0003219 EB0003219 EB0003219

Calibration Post High Cylinder Instrument Response 30.33 30.01 30.17 30.170

Calibration Post High Cylinder Bias 0.46 -0.24 0.11 0.110

Calibration Post High Cylinder Drift 0.09 0.7 0.35 0.380

Cavg 9.17 15.62 15.19 13.327

Cavg Units ppmvd ppmvd ppmvd

Cgas 9.2329 15.9042 15.523 13.553

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 16 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 25A

Average

Run Number 1 2 3

Test Date 6/17/2010 6/17/2010 6/17/2010

Run Start Time 12:15:00 PM 3:15:00 PM 6:00:00 PM

Run Finish Time 2:45:00 PM 5:43:00 PM 8:29:00 PM

Carbon Dioxide, % 9.5 9.3 9.3 9.367

Oxygen, % 8.1 7.9 7.7 7.900

Fuel Factor 1.35 1.4 1.42

Dry Volumetric Flow Rate, dry scfm 267656 271415 275855 271,642.000

F-Factor, dscfm/MMBtu @ %O2 9789 9785 9106 9,560.000

Moisture, % 6.42 6.65 6.45 6.507

Analyzer Make Thermo Env. Thermo Env. Thermo Env.

Analyzer Model 51 51 51 51.000

Analyzer Serial Number 4723 4723 4723 4,723.000

Operating Range 9.03 9.03 9.03 9.030

Operating Units ppm ppm ppm

No. Readings/Avg. 125 125 125 125.000

Calibration Set 11 11 11 11.000

Calibration Pre Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Pre Zero Cylinder Instrument Response 0.02 0.02 0.07 0.037

Calibration Pre Zero Cylinder Bias -0.33 -0.33 0.22 -0.147

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC243371 CC243371 CC243371

Calibration Pre High Cylinder Instrument Response 5.23 5.33 5.31 5.290

Calibration Pre High Cylinder Bias 0.22 1.33 1.11 0.887

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Post Zero Cylinder Instrument Response 0.02 0.07 0.01 0.033

Calibration Post Zero Cylinder Bias -0.33 0.22 -0.44 -0.183

Calibration Post Zero Cylinder Drift 0 0.55 0.66 0.403

Calibration Post High Cylinder ID CC243371 CC243371 CC243371

Calibration Post High Cylinder Instrument Response 5.33 5.31 5.26 5.300

Calibration Post High Cylinder Bias 1.33 1.11 0.55 0.997

Calibration Post High Cylinder Drift 1.11 0.22 0.56 0.630

Cavg 2.42 3.2 4.41 3.343

Cavg Units ppmvd ppmvd ppmvd

Cgas 2.4274 3.1819 4.4325 3.347

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 17 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 26A

Average

Run Number 1 2 3

Test Date 6/16/2010 6/16/2010 6/17/2010

Run Start Time 1:45:00 PM 5:20:00 PM 8:05:00 AM

Run Finish Time 4:53:45 PM 8:28:45 PM 11:14:45 AM

Net Traversing Points 50 50 50

Net Run Time, minutes 187.5 187.5 187.5

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 1 1 1.000

Barometric Pressure, inches of Mercury 29.83 29.83 29.87 29.843

Average Orifice Meter Differential, inches H2O 2.44 2.56 2.34 2.447

Dry Gas Meter Volume Sampled, cubic feet 160.877 166.842 159.482 162.400

Average Dry Gas Meter Temperature, °F 92.54 96.62 84.24 91.133

Dry Gas Meter Volume Sampled, dscf 154.191 158.783 155.354 156.109

Total Moisture Liquid collected, g 239 240.7 224.9 234.867

Volume of Water Vapor, standard cubic feet 11.25 11.33 10.59 11.057

Moisture Content of Stack Gas, % 6.80 6.66 6.38 6.613

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

Dry Mole Fraction 0.932 0.9334 0.9362 0.934

Carbon Dioxide, % 10.1 9.7 8.9 9.567

Oxygen, % 8.3 8.6 9.3 8.733

Carbon Monoxide & Nitrogen, % 81.6 81.7 81.8 81.700

Fuel Factor 1.25 1.27 1.30

Dry Molecular Weight, lb/lb-Mole 29.95 29.90 29.80 29.883

Wet Molecular weight, lb/lb-Mole 29.14 29.11 29.05 29.100

Flue Gas Static Pressure, inches of H2O 1.4 0.91 1.2 1.170

Absolute Flue Gas Pressure, inches of Mercury 29.93 29.90 29.96 29.930

Average Stack Gas Temperature, °F 316.48 307.96 316.26 313.567

Average Velocity Head, inches of H2O 1.4875060540

291

1.522842636

71977

1.475119635

51515

1.495

Average Stack Gas Velocity, feet/second 82.64 83.24 82.37 82.750

Stack Cross-Sectional Area, square feet 80.000 80.000 80.000 80.000

Dry Volumetric Flow Rate, dry scfm 251,475.8 256,239.5 252,107.6 253,274.300

Actual Wet Volumetric Flue Gas Flow Rate, acfm 396,672.0 399,552.0 395,376.0 397,200.000

Percent Isokinetic of Sampling Rate, % 99.1 100.2 99.6 99.633

Percent Excess Air, % 62.7 66.3 75.6 68.200

F-Factor, dscfm/MMBtu @ %O2 9712 9068 9055 9,278.333

Round Duct Diameter, inches

Rectangular Duct Width, inches 96 96 96

Rectangular Duct Length, inches 120 120 120

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 18 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 29

Average

Run Number 1 2 3

Test Date 6/15/2010 6/15/2010 6/16/2010

Run Start Time 11:15:00 AM 4:45:00 PM 8:05:00 AM

Run Finish Time 4:00:00 PM 9:25:00 PM 12:40:00 PM

Net Traversing Points 50 50 50

Net Run Time, minutes 250 250 250

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 1 1 1.000

Barometric Pressure, inches of Mercury 29.78 29.78 29.83 29.797

Average Orifice Meter Differential, inches H2O 2.39 2.48 2.39 2.420

Dry Gas Meter Volume Sampled, cubic feet 211.944 217.363 216.755 215.354

Average Dry Gas Meter Temperature, °F 93.00 97.04 87.10 92.380

Dry Gas Meter Volume Sampled, dscf 202.604 206.323 209.787 206.238

Total Moisture Liquid collected, g 332.4 357.3 370.7 353.467

Volume of Water Vapor, standard cubic feet 15.65 16.82 17.45 16.640

Moisture Content of Stack Gas, % 7.17 7.54 7.68 7.463

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

Dry Mole Fraction 0.9283 0.9246 0.9232 0.925

Carbon Dioxide, % 9.6 9.9 10.1 9.867

Oxygen, % 9.6 9.4 9.2 9.400

Carbon Monoxide & Nitrogen, % 80.8 80.7 80.7 80.733

Fuel Factor 1.18 1.16 1.16

Dry Molecular Weight, lb/lb-Mole 29.92 29.96 29.98 29.953

Wet Molecular weight, lb/lb-Mole 29.07 29.06 29.06 29.063

Flue Gas Static Pressure, inches of H2O 1.1 0.91 1.1 1.037

Absolute Flue Gas Pressure, inches of Mercury 29.86 29.85 29.91 29.873

Average Stack Gas Temperature, °F 316.98 315.82 316.28 316.360

Average Velocity Head, inches of H2O 1.4357124850

1176

1.465997135

2393

1.484422448

5935

1.462

Average Stack Gas Velocity, feet/second 81.41 82.23 82.68 82.107

Stack Cross-Sectional Area, square feet 80.000 80.000 80.000 80.000

Dry Volumetric Flow Rate, dry scfm 246,013.9 247,788.5 249,119.6 247,640.667

Actual Wet Volumetric Flue Gas Flow Rate, acfm 390,768.0 394,704.0 396,864.0 394,112.000

Percent Isokinetic of Sampling Rate, % 99.8 100.9 102.1 100.933

Percent Excess Air, % 81.8 79.0 76.0 78.933

F-Factor, dscfm/MMBtu @ %O2 9266 9907 9814 9,662.333

Round Duct Diameter, inches

Rectangular Duct Width, inches 96 96 96

Rectangular Duct Length, inches 120 120 120

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 19 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 6/15/2010 6/15/2010 6/16/2010

Run Start Time 11:15:00 AM 4:45:00 PM 8:05:00 AM

Run Finish Time 4:00:00 PM 9:25:00 PM 12:37:00 PM

Carbon Dioxide, % 9.6 9.9 10.1 9.867

Oxygen, % 9.6 9.4 9.2 9.400

Fuel Factor 1.18 1.16 1.16

Dry Volumetric Flow Rate, dry scfm 264982 267999 269812 267,597.667

F-Factor, dscfm/MMBtu @ %O2 9266 9907 9814 9,662.333

Moisture, % 7.17 7.54 7.68 7.463

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 18 18 18 18.000

Operating Units % % %

No. Readings/Avg. 250 250 250 250.000

Calibration Set 1 1 2 1.333

Calibration Pre Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Pre Zero Cylinder Instrument Response 0.06 0.12 0.11 0.097

Calibration Pre Zero Cylinder Bias 0.28 0.61 0.28 0.390

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0018561 EB0018561 EB0018561

Calibration Pre High Cylinder Instrument Response 9.07 9.12 9.09 9.093

Calibration Pre High Cylinder Bias 0 0.28 0.61 0.297

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Post Zero Cylinder Instrument Response 0.12 0.04 0.03 0.063

Calibration Post Zero Cylinder Bias 0.61 0.17 -0.17 0.203

Calibration Post Zero Cylinder Drift 0.33 0.44 0.45 0.407

Calibration Post High Cylinder ID EB0018561 EB0018561 EB0018561

Calibration Post High Cylinder Instrument Response 9.12 9.01 8.97 9.033

Calibration Post High Cylinder Bias 0.28 -0.33 -0.06 -0.037

Calibration Post High Cylinder Drift 0.28 0.61 0.67 0.520

Cavg 9.72 9.93 10.11 9.920

Cavg Units ppmvd ppmvd ppmvd

Cgas 9.646 9.8884 10.1072 9.881

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 20 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 3A CO2 3

Average

Run Number 4 5 6

Test Date 6/16/2010 6/16/2010 6/17/2010

Run Start Time 1:45:00 PM 5:20:00 PM 8:05:00 AM

Run Finish Time 4:53:00 PM 8:28:00 PM 11:13:00 AM

Carbon Dioxide, % 10.1 9.7 8.9 9.567

Oxygen, % 8.3 8.6 9.3 8.733

Fuel Factor 1.25 1.27 1.3

Dry Volumetric Flow Rate, dry scfm 270025 274527 269454 271,335.333

F-Factor, dscfm/MMBtu @ %O2 9712 9068 9055 9,278.333

Moisture, % 6.81 6.67 6.38 6.620

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 18.1 18.1 18.1 18.100

Operating Units % % %

No. Readings/Avg. 188 188 188 188.000

Calibration Set 3 3 4 3.333

Calibration Pre Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Pre Zero Cylinder Instrument Response 0.02 0.09 0.13 0.080

Calibration Pre Zero Cylinder Bias -0.39 0 0.66 0.090

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0001460_C

O2

EB0001460_

CO2

EB0001460_

CO2

Calibration Pre High Cylinder Instrument Response 9.07 9.02 9.16 9.083

Calibration Pre High Cylinder Bias -0.28 -0.55 0.39 -0.147

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Post Zero Cylinder Instrument Response 0.09 0.07 0.11 0.090

Calibration Post Zero Cylinder Bias 0 -0.11 0.55 0.147

Calibration Post Zero Cylinder Drift 0.39 0.11 0.11 0.203

Calibration Post High Cylinder ID EB0001460_C

O2

EB0001460_

CO2

EB0001460_

CO2

Calibration Post High Cylinder Instrument Response 9.02 9.12 8.93 9.023

Calibration Post High Cylinder Bias -0.55 0 -0.88 -0.477

Calibration Post High Cylinder Drift 0.27 0.55 1.27 0.697

Cavg 10.15 9.85 9.01 9.670

Cavg Units ppmvd ppmvd ppmvd

Cgas 10.0725 9.7483 8.9348 9.585

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 21 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 3A CO2 3 6

Average

Run Number 7 8 9

Test Date 6/17/2010 6/17/2010 6/17/2010

Run Start Time 12:15:00 PM 3:15:00 PM 6:00:00 PM

Run Finish Time 2:45:00 PM 5:43:00 PM 8:29:00 PM

Carbon Dioxide, % 9.5 9.3 9.3 9.367

Oxygen, % 8.1 7.9 7.7 7.900

Fuel Factor 1.35 1.4 1.42

Dry Volumetric Flow Rate, dry scfm 267656 271415 275855 271,642.000

F-Factor, dscfm/MMBtu @ %O2 9789 9785 9106 9,560.000

Moisture, % 6.42 6.65 6.45 6.507

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 18.1 18.1 18.1 18.100

Operating Units % % %

No. Readings/Avg. 125 125 125 125.000

Calibration Set 5 5 5 5.000

Calibration Pre Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Pre Zero Cylinder Instrument Response 0.09 0.09 0.09 0.090

Calibration Pre Zero Cylinder Bias 0.17 0.17 0.17 0.170

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0001460_C

O2

EB0001460_

CO2

EB0001460_

CO2

Calibration Pre High Cylinder Instrument Response 9.01 9.01 9.07 9.030

Calibration Pre High Cylinder Bias -0.72 -0.72 -0.39 -0.610

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Post Zero Cylinder Instrument Response 0.09 0.09 0.09 0.090

Calibration Post Zero Cylinder Bias 0.17 0.17 0.17 0.170

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID EB0001460_C

O2

EB0001460_

CO2

EB0001460_

CO2

Calibration Post High Cylinder Instrument Response 9.07 9.07 9.12 9.087

Calibration Post High Cylinder Bias -0.39 -0.39 -0.11 -0.297

Calibration Post High Cylinder Drift 0.33 0.33 0.28 0.313

Cavg 9.54 9.37 9.43 9.447

Cavg Units ppmvd ppmvd ppmvd

Cgas 9.4711 9.3007 9.3037 9.359

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 22 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 3A O2

Average

Run Number 1 2 3

Test Date 6/15/2010 6/15/2010 6/16/2010

Run Start Time 11:15:00 AM 4:45:00 PM 8:05:00 AM

Run Finish Time 4:00:00 PM 9:25:00 PM 12:37:00 PM

Carbon Dioxide, % 9.6 9.9 10.1 9.867

Oxygen, % 9.6 9.4 9.2 9.400

Fuel Factor 1.18 1.16 1.16

Dry Volumetric Flow Rate, dry scfm 264982 267999 269812 267,597.667

F-Factor, dscfm/MMBtu @ %O2 9266 9907 9814 9,662.333

Moisture, % 7.17 7.54 7.68 7.463

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 22.4 22.4 22.4 22.400

Operating Units % % %

No. Readings/Avg. 250 250 250 250.000

Calibration Set 6 6 7 6.333

Calibration Pre Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Pre Zero Cylinder Instrument Response 0.09 0.11 0.02 0.073

Calibration Pre Zero Cylinder Bias 0.31 0.4 -0.13 0.193

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0001460 EB0001460 EB0001460

Calibration Pre High Cylinder Instrument Response 11.08 11.02 11.08 11.060

Calibration Pre High Cylinder Bias 0.13 -0.13 0.45 0.150

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Post Zero Cylinder Instrument Response 0.11 0.09 0.15 0.117

Calibration Post Zero Cylinder Bias 0.4 0.31 0.45 0.387

Calibration Post Zero Cylinder Drift 0.09 0.09 0.58 0.253

Calibration Post High Cylinder ID EB0001460 EB0001460 EB0001460

Calibration Post High Cylinder Instrument Response 11.02 11.01 11.03 11.020

Calibration Post High Cylinder Bias -0.13 -0.18 0.22 -0.030

Calibration Post High Cylinder Drift 0.26 0.05 0.23 0.180

Cavg 9.7 9.41 9.23 9.447

Cavg Units ppmvd ppmvd ppmvd

Cgas 9.6438 9.3825 9.17 9.399

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 23 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 3A O2 3

Average

Run Number 4 5 6

Test Date 6/16/2010 6/16/2010 6/17/2010

Run Start Time 1:45:00 PM 5:20:00 PM 8:05:00 AM

Run Finish Time 4:53:00 PM 8:28:00 PM 11:13:00 AM

Carbon Dioxide, % 10.1 9.7 8.9 9.567

Oxygen, % 8.3 8.6 9.3 8.733

Fuel Factor 1.25 1.27 1.3

Dry Volumetric Flow Rate, dry scfm 270025 274527 269454 271,335.333

F-Factor, dscfm/MMBtu @ %O2 9712 9068 9055 9,278.333

Moisture, % 6.81 6.67 6.38 6.620

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 22.4 22.4 22.4 22.400

Operating Units % % %

No. Readings/Avg. 188 188 188 188.000

Calibration Set 8 8 9 8.333

Calibration Pre Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Pre Zero Cylinder Instrument Response 0.05 0.01 0.01 0.023

Calibration Pre Zero Cylinder Bias 0 -0.18 -0.09 -0.090

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0001460 EB0001460 EB0001460

Calibration Pre High Cylinder Instrument Response 11.03 11.11 11.09 11.077

Calibration Pre High Cylinder Bias 0.04 0.4 0.22 0.220

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Post Zero Cylinder Instrument Response 0.01 0.04 0.09 0.047

Calibration Post Zero Cylinder Bias -0.18 -0.04 0.27 0.017

Calibration Post Zero Cylinder Drift 0.18 0.14 0.36 0.227

Calibration Post High Cylinder ID EB0001460 EB0001460 EB0001460

Calibration Post High Cylinder Instrument Response 11.11 11.07 11.01 11.063

Calibration Post High Cylinder Bias 0.4 0.22 -0.13 0.163

Calibration Post High Cylinder Drift 0.36 0.18 0.35 0.297

Cavg 8.31 8.71 9.36 8.793

Cavg Units ppmvd ppmvd ppmvd

Cgas 8.25 8.634 9.31 8.731

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 24 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 3A O2 3 6

Average

Run Number 7 8 9

Test Date 6/17/2010 6/17/2010 6/17/2010

Run Start Time 12:15:00 PM 3:15:00 PM 6:00:00 PM

Run Finish Time 2:45:00 PM 5:43:00 PM 8:29:00 PM

Carbon Dioxide, % 9.5 9.3 9.3 9.367

Oxygen, % 8.1 7.9 7.7 7.900

Fuel Factor 1.35 1.4 1.42

Dry Volumetric Flow Rate, dry scfm 267656 271415 275855 271,642.000

F-Factor, dscfm/MMBtu @ %O2 9789 9785 9106 9,560.000

Moisture, % 6.42 6.65 6.45 6.507

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 22.4 22.4 22.4 22.400

Operating Units % % %

No. Readings/Avg. 125 125 125 125.000

Calibration Set 10 10 10 10.000

Calibration Pre Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Pre Zero Cylinder Instrument Response 0.03 0.01 0.02 0.020

Calibration Pre Zero Cylinder Bias 0 -0.09 -0.04 -0.043

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0001460 EB0001460 EB0001460

Calibration Pre High Cylinder Instrument Response 11.02 11.08 11.01 11.037

Calibration Pre High Cylinder Bias -0.13 0.13 -0.18 -0.060

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Post Zero Cylinder Instrument Response 0.01 0.02 0.07 0.033

Calibration Post Zero Cylinder Bias -0.09 -0.04 0.18 0.017

Calibration Post Zero Cylinder Drift 0.09 0.05 0.22 0.120

Calibration Post High Cylinder ID EB0001460 EB0001460 EB0001460

Calibration Post High Cylinder Instrument Response 11.08 11.01 11.09 11.060

Calibration Post High Cylinder Bias 0.13 -0.18 0.18 0.043

Calibration Post High Cylinder Drift 0.26 0.31 0.36 0.310

Cavg 8.1 7.89 7.76 7.917

Cavg Units ppmvd ppmvd ppmvd

Cgas 8.058 7.8536 7.7115 7.874

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 1800 0 0 600.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 25 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 6C

Average

Run Number 1 2 3

Test Date 6/16/2010 6/16/2010 6/17/2010

Run Start Time 1:45:00 PM 5:20:00 PM 8:05:00 AM

Run Finish Time 4:53:00 PM 8:28:00 PM 11:13:00 AM

Carbon Dioxide, % 10.1 9.7 8.9 9.567

Oxygen, % 8.3 8.6 9.3 8.733

Fuel Factor 1.25 1.27 1.3

Dry Volumetric Flow Rate, dry scfm 270025 274527 269454 271,335.333

F-Factor, dscfm/MMBtu @ %O2 9712 9068 9055 9,278.333

Moisture, % 6.81 6.67 6.38 6.620

Analyzer Make Western 

research

Western 

Research

Western 

research

Analyzer Model 721M 721M 721M

Analyzer Serial Number 93-721M8062-693-721M8062-693-721M8062-6

Operating Range 898 1812 1812 1,507.333

Operating Units ppm ppm ppm

No. Readings/Avg. 188 188 188 188.000

Calibration Set 15 15 16 15.333

Calibration Pre Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Pre Zero Cylinder Instrument Response 1.18 0.09 0.17 0.480

Calibration Pre Zero Cylinder Bias -0.06 -0.12 -0.05 -0.077

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0001096 EB0001096 EB0001096

Calibration Pre High Cylinder Instrument Response 900.1 902.26 904.42 902.260

Calibration Pre High Cylinder Bias -0.06 0.06 0.13 0.043

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Post Zero Cylinder Instrument Response 0.09 2.83 2.33 1.750

Calibration Post Zero Cylinder Bias -0.12 0.03 0.07 -0.007

Calibration Post Zero Cylinder Drift 0.06 0.15 0.12 0.110

Calibration Post High Cylinder ID EB0001096 EB0001096 EB0001096

Calibration Post High Cylinder Instrument Response 902.26 904.49 901.34 902.697

Calibration Post High Cylinder Bias 0.06 0.18 -0.04 0.067

Calibration Post High Cylinder Drift 0.12 0.12 0.17 0.137

Cavg 1035.46 1013.21 1002.27 1,016.980

Cavg Units ppmvd ppmvd ppmvd

Cgas 1031.9005 1007.3582 996.9899 1,012.083

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 26 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - Method 7E

Average

Run Number 1 2 3

Test Date 6/16/2010 6/16/2010 6/17/2010

Run Start Time 1:45:00 PM 5:20:00 PM 8:05:00 AM

Run Finish Time 4:53:00 PM 8:28:00 PM 11:13:00 AM

Carbon Dioxide, % 10.1 9.7 8.9 9.567

Oxygen, % 8.3 8.6 9.3 8.733

Fuel Factor 1.25 1.27 1.3

Dry Volumetric Flow Rate, dry scfm 270025 274527 269454 271,335.333

F-Factor, dscfm/MMBtu @ %O2 9712 9068 9055 9,278.333

Moisture, % 6.81 6.67 6.38 6.620

Analyzer Make Thermo Env. Thermo Env. Thermo Env.

Analyzer Model 42C 42C 42C

Analyzer Serial Number 42chl_67507_

357

42chl_67507

_357

42chl_67507_

357

Operating Range 509 509 509 509.000

Operating Units ppm ppm ppm

No. Readings/Avg. 188 188 188 188.000

Calibration Set 13 13 14 13.333

Calibration Pre Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Pre Zero Cylinder Instrument Response 0.06 0.03 1.14 0.410

Calibration Pre Zero Cylinder Bias -0.02 -0.02 0.03 -0.003

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0003850 EB0003850 EB0003850

Calibration Pre High Cylinder Instrument Response 228.92 229.25 229.04 229.070

Calibration Pre High Cylinder Bias -1.34 -1.28 0.26 -0.787

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020529 EB0020529 EB0020529

Calibration Post Zero Cylinder Instrument Response 0.03 0.98 1.74 0.917

Calibration Post Zero Cylinder Bias -0.02 0.16 0.15 0.097

Calibration Post Zero Cylinder Drift 0 0.18 0.12 0.100

Calibration Post High Cylinder ID EB0003850 EB0003850 EB0003850

Calibration Post High Cylinder Instrument Response 229.25 231.12 231.93 230.767

Calibration Post High Cylinder Bias -1.28 -0.91 0.83 -0.453

Calibration Post High Cylinder Drift 6.0000000000

0001E-02

0.37 0.57 0.333

Cavg 143.47 134.49 127.62 135.193

Cavg Units ppmvd ppmvd ppmvd

Cgas 145.2786 135.3384 127.8079 136.142

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, January 18, 2011 Page 27 of 28
AMERICAN MUNICIPAL POWER

Location Duct 3 - OTM - 27/28

Average

Run Number 27/28-1 27/28-2 27/28-3

Test Date 6/15/2010 6/15/2010 6/16/2010

Run Start Time 11:15:00 AM 4:45:00 PM 8:00:00 AM

Run Finish Time 2:30:18 PM 8:07:24 PM 11:27:54 AM

Net Traversing Points 12 12 12

Net Run Time, minutes 179.8 179.9 180

Nozzle Diameter, inches 0.148 0.148 0.148 0.148

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.002 1.002 1.002 1.002

Barometric Pressure, inches of Mercury 29.78 29.78 29.83 29.797

Average Orifice Meter Differential, inches H2O 0.47 0.47 0.47 0.470

Dry Gas Meter Volume Sampled, cubic feet 69.050 67.311 68.162 68.174

Average Dry Gas Meter Temperature, °F 90.17 96.33 85.83 90.777

Dry Gas Meter Volume Sampled, dscf 66.166 63.786 65.945 65.299

Total Moisture Liquid collected, g 118.7 116.4 117.4 117.500

Volume of Water Vapor, standard cubic feet 5.59 5.48 5.53 5.533

Moisture Content of Stack Gas, % 7.79 7.91 7.74 7.813

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

Dry Mole Fraction 0.9221 0.9209 0.9226 0.922

Carbon Dioxide, % 9.6 9.9 10.1 9.867

Oxygen, % 9.6 9.4 9.2 9.400

Carbon Monoxide & Nitrogen, % 80.8 80.7 80.7 80.733

Fuel Factor 1.18 1.16 1.16

Dry Molecular Weight, lb/lb-Mole 29.92 29.96 29.98 29.953

Wet Molecular weight, lb/lb-Mole 28.99 29.01 29.05 29.017

Flue Gas Static Pressure, inches of H2O 0.4 0.6 0.96 0.653

Absolute Flue Gas Pressure, inches of Mercury 29.81 29.82 29.90 29.843

Average Stack Gas Temperature, °F 316.75 313.50 312.75 314.333

Average Velocity Head, inches of H2O 1.3843636509

7125

1.336791862

03922

1.371149953

09655

1.364

Average Stack Gas Velocity, feet/second 80.10 78.51 79.31 79.307

Stack Cross-Sectional Area, square feet 80.000 80.000 80.000 80.000

Dry Volumetric Flow Rate, dry scfm 240,107.0 236,101.3 239,821.0 238,676.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 384,480.0 376,848.0 380,688.0 380,672.000

Percent Isokinetic of Sampling Rate, % 102.6 100.6 102.3 101.833

Percent Excess Air, % 81.8 79.0 76.0 78.933

F-Factor, dscfm/MMBtu @ %O2 9266 9907 9814 9,662.333

Round Duct Diameter, inches

Rectangular Duct Width, inches 96 96 96

Rectangular Duct Length, inches 120 120 120

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 18, 2011 Page 28 of 28