Name: Thomas Reed

Title: Environmental Engineer

Company: Manitowoc Public Utilities

Sign Date: 8/11/2010

Name: Chet Gutwein

Title: Engineer

Company: Airtech Environmental Services Inc.

Sign Date: 8/10/2010

Permitted Facility Representative / Date Testing Company Representative / Date

3225 Manitowoc Public 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.

Sunday, January 30, 2011 Page 1 of 43
3225 Manitowoc Public Utilities

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Facility Information:

MPU Power Plant

1303 S 8TH ST

Manitowoc WI 54220

Contact: Thomas Reed

Phone: (920) 686-4384

Fax: (920) 686-4315

Email: tomreed@mpu.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:

4125

Permitted Source ID/Name:

B09 Boiler 9

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:

Manitowoc Public Utilities Unit #9 is an atmospheric pressure circulating fluidized bed (CFB) boiler that fires coal, 

petroleum coke, paper pellets or a combination of any of the three fuels, along with natural gas as a start-up fuel. The 

boiler produces steam, which is used to turn a steam turbine/electric generator set and to provide steam for off-site 

utilization (cogeneration). The Manitowoc Public Utilities Power Plant is located at 701 Columbus Street in the City 

of Manitowoc, in Manitowoc County, Wisconsin. The Manitowoc Public Utilities business office is located on the 

same site with an address of 1303 South 8th Street.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 5507100008 FRS #: 110000421384

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 108 0 0 108 2.8 2.8 2 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Carbon Monoxide Method 10 3 120 0

Stack Exit 2,3,7,8-TCDD Method 23 3 480 0

Stack Exit 1,2,3,7,8-PeCDD Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 480 0

Sunday, January 30, 2011 Page 2 of 43
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Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

Stack Exit OCDD Method 23 3 480 0

Stack Exit 2,3,7,8-TCDF Method 23 3 480 0

Stack Exit 1,2,3,7,8-PeCDF Method 23 3 480 0

Stack Exit 2,3,4,7,8-PeCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,7,8,9-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

Stack Exit OCDF Method 23 3 480 0

Stack Exit Other TCDD Method 23 0

Stack Exit Other PeCDD Method 23 0

Stack Exit Other HxCDD Method 23 0

Stack Exit Other HpCDD Method 23 0

Stack Exit Other TCDF Method 23 0

Stack Exit Other PeCDF Method 23 0

Stack Exit Other HxCDF Method 23 0

Stack Exit Other HpCDF Method 23 0

Stack Exit Total Dioxins Method 23 3 480 0

Stack Exit Total Furans Method 23 3 480 0

Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 480 0

Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Stack Exit Method 23 3 480 0

Stack Exit 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Stack Exit Method 23 3 480 0

Stack Exit Total PCBs Method 23 3 480 0

Stack Exit Total TEQ Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Hydrogen Fluoride Method 26A 3 180 0 Measured using 

NaOH impingers

Stack Exit

Hydrogen Chloride Method 26A 3 180 0 Measured using 

NaOH impingers

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 240 0

Stack Exit Filterable Particulate OTM - 27/28 3 240 0

Stack Exit Filterable PM2.5 OTM - 27/28 3 240 0

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 240 0

Stack Exit Total PM2.5 OTM - 27/28 3 240 0

Stack Exit Total Particulate OTM - 27/28 3 240 0

Stack Exit Nickel Method 29 3 240 0

Sunday, January 30, 2011 Page 3 of 43
3225 Manitowoc Public Utilities

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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

Method 316 - March 1997

Other Test Methods 27 and 28 – April 2009

SW-846 0010 – September 1986

SW-846 0030 – December 1996

Stack Exit Antimony 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

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Sunday, January 30, 2011 Page 4 of 43
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Sampling / Stack Data Results Summary

Location Stack Exit - Method 10

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 10 3

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

Sunday, January 30, 2011 Page 5 of 43
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Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 5/18/2010 5/19/2010 5/20/2010

Run Start Time 9:00:00 AM 8:00:00 

AM

7:51:00 AM

Run Finish Time 5:20:00 PM 4:11:00 PM 4:05:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 325.588 334.028 327.676 329.097

Moisture Content of Stack Gas, % 6.13 6.60 6.64 6.457

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

Carbon Dioxide, % 14.9 14.3 15.4 14.867

Oxygen, % 4.57 4.5 4.23 4.433

Average Stack Gas Temperature, °F 357.67 362.88 361.33 360.627

Dry Volumetric Flow Rate, dry scfm 126,527.3 128,796.8 128,174.0 127,832.700

Actual Wet Volumetric Flue Gas Flow Rate, acfm 211,997.3 218,638.9 217,264.8 215,967.000

Percent Isokinetic of Sampling Rate, % 100.0 100.8 99.4 100.067

F-Factor, dscfm/MMBtu @ %O2 9847 9794 9828 9,823.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - Method 25A

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

Sunday, January 30, 2011 Page 6 of 43
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Location Stack Exit - Method 25A 3

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 26A

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

Sunday, January 30, 2011 Page 7 of 43
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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 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

Sunday, January 30, 2011 Page 8 of 43
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Location Stack Exit - Method 3A CO2 3

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 3A CO2 3 6

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

Sunday, January 30, 2011 Page 9 of 43
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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 3A O2 3

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

Sunday, January 30, 2011 Page 10 of 43
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Location Stack Exit - Method 3A O2 3 6

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 6C

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

Sunday, January 30, 2011 Page 11 of 43
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Location Stack Exit - Method 6C 3

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 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

Sunday, January 30, 2011 Page 12 of 43
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Location Stack Exit - Method 7E 3

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 - OTM - 27/28

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

Sunday, January 30, 2011 Page 13 of 43
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Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 5-20B 5-20C 5-21A

lb/mmBtuO2 4.23E-03 5.07E-03 5.15E-03 0.005

ppm 4.72E+00 5.66E+00 5.50E+00 5.293

ppm@7%O2 3.94E+00 4.72E+00 4.80E+00 4.487

Location: Stack Exit - Method 10 3

Compound: Carbon Monoxide

Average

Run 5-21B

lb/mmBtuO2 5.37E-03 0.005

ppm 6.03E+00 6.030

ppm@7%O2 5.00E+00 5.000

Location: Stack Exit - Method 23

Compound: 1,2,3,4,6,7,8-HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000007 0.0000000056 0.0000000066 0.000

lb/mmBtuO2 5.97E-13 4.61E-13 5.47E-13 0.000

ng/dscm 7.59E-04 5.92E-04 7.11E-04 0.001

ng/dscm@7%O2 6.46E-04 5.02E-04 5.93E-04 0.001

Compound: 1,2,3,4,6,7,8-HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000017 0.000000012 0.0000000087 0.000

lb/mmBtuO2 1.45E-12 9.89E-13 7.21E-13 0.000

ng/dscm 1.84E-03 1.27E-03 9.38E-04 0.001

ng/dscm@7%O2 1.57E-03 1.08E-03 7.82E-04 0.001

Compound: 1,2,3,4,7,8,9-HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000037 0.0000000043 0.000000003 0.000

lb/mmBtuO2 3.16E-13 3.54E-13 2.49E-13 0.000

ng/dscm 4.01E-04 4.55E-04 3.23E-04 0.000

ng/dscm@7%O2 3.41E-04 3.86E-04 2.69E-04 0.000

Compound: 1,2,3,4,7,8-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000028 0.0000000021 0.0000000025 0.000

lb/mmBtuO2 2.39E-13 1.73E-13 2.07E-13 0.000

ng/dscm 3.04E-04 2.22E-04 2.69E-04 0.000

ng/dscm@7%O2 2.59E-04 1.88E-04 2.24E-04 0.000

Sunday, January 30, 2011 Page 14 of 43
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Compound: 1,2,3,4,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000015 0.000000012 0.000000011 0.000

lb/mmBtuO2 1.28E-12 9.89E-13 9.12E-13 0.000

ng/dscm 1.63E-03 1.27E-03 1.19E-03 0.001

ng/dscm@7%O2 1.39E-03 1.08E-03 9.92E-04 0.001

Compound: 1,2,3,6,7,8-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000027 0.000000002 0.0000000025 0.000

lb/mmBtuO2 2.30E-13 1.65E-13 2.07E-13 0.000

ng/dscm 2.93E-04 2.11E-04 2.69E-04 0.000

ng/dscm@7%O2 2.49E-04 1.79E-04 2.24E-04 0.000

Compound: 1,2,3,6,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000081 0.0000000063 0.0000000049 0.000

lb/mmBtuO2 6.91E-13 5.19E-13 4.06E-13 0.000

ng/dscm 8.79E-04 6.66E-04 5.28E-04 0.001

ng/dscm@7%O2 7.48E-04 5.64E-04 4.40E-04 0.001

Compound: 1,2,3,7,8,9-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000028 0.0000000021 0.0000000025 0.000

lb/mmBtuO2 2.39E-13 1.73E-13 2.07E-13 0.000

ng/dscm 3.04E-04 2.22E-04 2.69E-04 0.000

ng/dscm@7%O2 2.59E-04 1.88E-04 2.24E-04 0.000

Compound: 1,2,3,7,8,9-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000023 0.0000000017 0.000000002 0.000

lb/mmBtuO2 1.96E-13 1.40E-13 1.66E-13 0.000

ng/dscm 2.50E-04 1.80E-04 2.16E-04 0.000

ng/dscm@7%O2 2.13E-04 1.53E-04 1.80E-04 0.000

Compound: 1,2,3,7,8-PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000031 0.0000000027 0.0000000031 0.000

lb/mmBtuO2 2.65E-13 2.22E-13 2.57E-13 0.000

ng/dscm 3.36E-04 2.85E-04 3.34E-04 0.000

ng/dscm@7%O2 2.86E-04 2.42E-04 2.79E-04 0.000

Compound: 1,2,3,7,8-PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000013 0.0000000042 0.0000000076 0.000

lb/mmBtuO2 1.11E-12 3.46E-13 6.30E-13 0.000

Sunday, January 30, 2011 Page 15 of 43
3225 Manitowoc Public Utilities

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ng/dscm 1.41E-03 4.44E-04 8.19E-04 0.001

ng/dscm@7%O2 1.20E-03 3.76E-04 6.83E-04 0.001

Compound: 2,3,3',4,4',5,5'-HpCB (PCB189)

Average

RunNumber 1 2 3

Mass_mg 0.0000000071 0.000000007 0.0000000066 0.000

lb/mmBtuO2 6.06E-13 5.77E-13 5.47E-13 0.000

ng/dscm 7.70E-04 7.40E-04 7.11E-04 0.001

ng/dscm@7%O2 6.55E-04 6.27E-04 5.93E-04 0.001

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 1 2 3

Mass_mg 0.000000072 0.0000000136 0.0000000116 0.000

lb/mmBtuO2 6.14E-12 1.12E-12 9.62E-13 0.000

ng/dscm 7.81E-03 1.44E-03 1.25E-03 0.004

ng/dscm@7%O2 6.65E-03 1.22E-03 1.04E-03 0.003

Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber 1 2 3

Mass_mg 0.000000157 0.000000203 0.000000208 0.000

lb/mmBtuO2 1.34E-11 1.67E-11 1.72E-11 0.000

ng/dscm 1.70E-02 2.15E-02 2.24E-02 0.020

ng/dscm@7%O2 1.45E-02 1.82E-02 1.87E-02 0.017

Compound: 2,3',4,4',5,5'-HxCB (PCB167)

Average

RunNumber 1 2 3

Mass_mg 0.0000000167 0.0000000146 0.000000009 0.000

lb/mmBtuO2 1.43E-12 1.20E-12 7.46E-13 0.000

ng/dscm 1.81E-03 1.54E-03 9.70E-04 0.001

ng/dscm@7%O2 1.54E-03 1.31E-03 8.09E-04 0.001

Compound: 2,3,4,4',5-PeCB (PCB114)

Average

RunNumber 1 2 3

Mass_mg 0.0000000086 0.0000000089 0.0000000087 0.000

lb/mmBtuO2 7.34E-13 7.33E-13 7.21E-13 0.000

ng/dscm 9.33E-04 9.41E-04 9.38E-04 0.001

ng/dscm@7%O2 7.94E-04 7.98E-04 7.82E-04 0.001

Compound: 2,3',4,4',5-PeCB (PCB118)

Average

RunNumber 1 2 3

Mass_mg 0.00000046 0.0000005 0.00000061 0.000

lb/mmBtuO2 3.93E-11 4.12E-11 5.06E-11 0.000

ng/dscm 4.99E-02 5.29E-02 6.58E-02 0.056

ng/dscm@7%O2 4.25E-02 4.48E-02 5.49E-02 0.047

Compound: 2',3,4,4',5-PeCB (PCB123)

Average

RunNumber 1 2 3

Sunday, January 30, 2011 Page 16 of 43
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Mass_mg 0.0000000122 0.000000108 0.0000000097 0.000

lb/mmBtuO2 1.04E-12 8.90E-12 8.04E-13 0.000

ng/dscm 1.32E-03 1.14E-02 1.05E-03 0.005

ng/dscm@7%O2 1.12E-03 9.66E-03 8.76E-04 0.004

Compound: 2,3,4,6,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000004 0.0000000015 0.0000000028 0.000

lb/mmBtuO2 3.41E-13 1.24E-13 2.32E-13 0.000

ng/dscm 4.34E-04 1.59E-04 3.02E-04 0.000

ng/dscm@7%O2 3.69E-04 1.35E-04 2.52E-04 0.000

Compound: 2,3,4,7,8-PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000008 0.0000000064 0.0000000051 0.000

lb/mmBtuO2 6.83E-13 5.27E-13 4.23E-13 0.000

ng/dscm 8.68E-04 6.77E-04 5.50E-04 0.001

ng/dscm@7%O2 7.39E-04 5.74E-04 4.59E-04 0.001

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000058 0.0000000052 0.0000000061 0.000

lb/mmBtuO2 4.95E-13 4.28E-13 5.06E-13 0.000

ng/dscm 6.29E-04 5.50E-04 6.58E-04 0.001

ng/dscm@7%O2 5.35E-04 4.66E-04 5.49E-04 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000016 0.00000001 0.0000000096 0.000

lb/mmBtuO2 1.37E-12 8.24E-13 7.96E-13 0.000

ng/dscm 1.74E-03 1.06E-03 1.03E-03 0.001

ng/dscm@7%O2 1.48E-03 8.98E-04 8.59E-04 0.001

Compound: 3,3',4,4',5,5'-HxCB (PCB169)

Average

RunNumber 1 2 3

Mass_mg 0.0000000102 0.0000000108 0.0000000093 0.000

lb/mmBtuO2 8.70E-13 8.90E-13 7.71E-13 0.000

ng/dscm 1.11E-03 1.14E-03 1.00E-03 0.001

ng/dscm@7%O2 9.45E-04 9.66E-04 8.34E-04 0.001

Compound: 3,3',4,4',5-PeCB (PCB126)

Average

RunNumber 1 2 3

Mass_mg 0.0000000097 0.0000000106 0.0000000097 0.000

lb/mmBtuO2 8.28E-13 8.73E-13 8.04E-13 0.000

ng/dscm 1.05E-03 1.12E-03 1.05E-03 0.001

ng/dscm@7%O2 8.94E-04 9.49E-04 8.76E-04 0.001

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Compound: 3,3',4,4'-TCB (PCB77)

Average

RunNumber 1 2 3

Mass_mg 0.0000000314 0.00000005 0.000000047 0.000

lb/mmBtuO2 2.68E-12 4.12E-12 3.90E-12 0.000

ng/dscm 3.41E-03 5.29E-03 5.07E-03 0.005

ng/dscm@7%O2 2.90E-03 4.48E-03 4.23E-03 0.004

Compound: 3,4,4',5-TCB (PCB81)

Average

RunNumber 1 2 3

Mass_mg 0.0000000143 0.0000000146 0.0000000132 0.000

lb/mmBtuO2 1.22E-12 1.20E-12 1.09E-12 0.000

ng/dscm 1.55E-03 1.54E-03 1.42E-03 0.002

ng/dscm@7%O2 1.32E-03 1.31E-03 1.18E-03 0.001

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000021 0.00000002 0.000000019 0.000

lb/mmBtuO2 1.79E-12 1.65E-12 1.58E-12 0.000

ng/dscm 2.28E-03 2.11E-03 2.05E-03 0.002

ng/dscm@7%O2 1.94E-03 1.79E-03 1.71E-03 0.002

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000047 0.0000000086 0.0000000081 0.000

lb/mmBtuO2 4.01E-13 7.08E-13 6.72E-13 0.000

ng/dscm 5.10E-04 9.09E-04 8.73E-04 0.001

ng/dscm@7%O2 4.34E-04 7.70E-04 7.28E-04 0.001

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000012 0.0000000044 0.0000000064 0.000

lb/mmBtuO2 1.02E-12 3.62E-13 5.31E-13 0.000

ng/dscm 1.30E-03 4.65E-04 6.90E-04 0.001

ng/dscm@7%O2 1.11E-03 3.94E-04 5.75E-04 0.001

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0 0.0000000037 0 0.000

lb/mmBtuO2 0.00E+00 3.05E-13 0.00E+00 0.000

ng/dscm 0.00E+00 3.91E-04 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 3.31E-04 0.00E+00 0.000

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000417 0.0000000218 0.0000000225 0.000

lb/mmBtuO2 3.56E-12 1.80E-12 1.87E-12 0.000

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ng/dscm 4.52E-03 2.31E-03 2.43E-03 0.003

ng/dscm@7%O2 3.85E-03 1.96E-03 2.03E-03 0.003

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000356 0.0000000275 0.0000000223 0.000

lb/mmBtuO2 3.04E-12 2.27E-12 1.85E-12 0.000

ng/dscm 3.86E-03 2.91E-03 2.40E-03 0.003

ng/dscm@7%O2 3.29E-03 2.47E-03 2.00E-03 0.003

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000479 0.0000000233 0.0000000289 0.000

lb/mmBtuO2 4.09E-12 1.92E-12 2.40E-12 0.000

ng/dscm 5.20E-03 2.46E-03 3.12E-03 0.004

ng/dscm@7%O2 4.43E-03 2.09E-03 2.60E-03 0.003

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000099 0.0000000544 0.0000000493 0.000

lb/mmBtuO2 8.45E-12 4.48E-12 4.09E-12 0.000

ng/dscm 1.07E-02 5.75E-03 5.31E-03 0.007

ng/dscm@7%O2 9.11E-03 4.87E-03 4.43E-03 0.006

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000472 0.0000000288 0.0000000209 0.000

lb/mmBtuO2 4.03E-12 2.37E-12 1.73E-12 0.000

ng/dscm 5.12E-03 3.05E-03 2.25E-03 0.003

ng/dscm@7%O2 4.36E-03 2.59E-03 1.88E-03 0.003

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000124 0.00000011 0.0000000614 0.000

lb/mmBtuO2 1.06E-11 9.06E-12 5.09E-12 0.000

ng/dscm 1.35E-02 1.16E-02 6.62E-03 0.011

ng/dscm@7%O2 1.15E-02 9.83E-03 5.52E-03 0.009

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.000000173 0.000000098 0.000000102 0.000

lb/mmBtuO2 1.48E-11 8.07E-12 8.46E-12 0.000

ng/dscm 1.88E-02 1.04E-02 1.10E-02 0.013

ng/dscm@7%O2 1.60E-02 8.81E-03 9.17E-03 0.011

Compound: Total Furans

Average

RunNumber 1 2 3

Sunday, January 30, 2011 Page 19 of 43
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Mass_mg 0.000000342 0.000000254 0.000000185 0.000

lb/mmBtuO2 2.92E-11 2.09E-11 1.53E-11 0.000

ng/dscm 3.71E-02 2.69E-02 1.99E-02 0.028

ng/dscm@7%O2 3.16E-02 2.28E-02 1.66E-02 0.024

Compound: Total PCBs

Average

RunNumber 1 2 3

Mass_mg 0.000000733 0.000000632 0.000000973 0.000

lb/mmBtuO2 6.26E-11 5.21E-11 8.07E-11 0.000

ng/dscm 7.95E-02 6.68E-02 1.05E-01 0.084

ng/dscm@7%O2 6.77E-02 5.66E-02 8.76E-02 0.071

Compound: Total TEQ

Average

RunNumber 1 2 3

Mass_mg 0.00000000922 0.00000000649 0.00000000594 0.000

lb/mmBtuO2 7.87E-13 5.35E-13 4.92E-13 0.000

ng/dscm 1.00E-03 6.86E-04 6.40E-04 0.001

ng/dscm@7%O2 8.51E-04 5.81E-04 5.34E-04 0.001

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 5-20B 5-20C 5-21A

lb/mmBtuO2 1.04E-04 1.50E-04 4.50E-04 0.000

ppm 7.23E-02 1.07E-01 3.05E-01 0.161

ppm@7%O2 6.13E-02 8.92E-02 2.66E-01 0.139

Location: Stack Exit - Method 25A 3

Compound: Total organic compounds (TOC) as 

Average

Run 5-21B

lb/mmBtuO2 2.90E-04 0.000

ppm 2.07E-01 0.207

ppm@7%O2 1.72E-01 0.172

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 5.87 16.3 23 15.057

Elb/hr 9.42E-01 2.56E+00 3.66E+00 2.387

lb/mmBtuO2 1.63E-03 4.47E-03 6.18E-03 0.004

mg/dscm 2.11E+00 5.83E+00 8.16E+00 5.367

mg/dscm@7%O2 1.78E+00 4.85E+00 6.70E+00 4.443

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.464 0.637 0.594 0.565

Elb/hr 7.45E-02 1.00E-01 9.45E-02 0.090

Sunday, January 30, 2011 Page 20 of 43
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lb/mmBtuO2 1.29E-04 1.75E-04 1.60E-04 0.000

mg/dscm 1.67E-01 2.28E-01 2.11E-01 0.202

mg/dscm@7%O2 1.41E-01 1.90E-01 1.73E-01 0.168

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000786 0.001206 0.002496 0.001

Elb/hr 9.72E-05 1.46E-04 3.07E-04 0.000

lb/mmBtuO2 1.68E-07 2.55E-07 5.26E-07 0.000

mg/dscm 2.12E-04 3.25E-04 6.82E-04 0.000

mg/dscm@7%O2 1.82E-04 2.77E-04 5.70E-04 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.015825 0.014825 0.015526 0.015

Elb/hr 1.96E-03 1.80E-03 1.91E-03 0.002

lb/mmBtuO2 3.38E-06 3.14E-06 3.27E-06 0.000

mg/dscm 4.27E-03 4.00E-03 4.24E-03 0.004

mg/dscm@7%O2 3.66E-03 3.42E-03 3.55E-03 0.004

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000261 0.000212 0.000259 0.000

Elb/hr 3.23E-05 2.57E-05 3.19E-05 0.000

lb/mmBtuO2 5.57E-08 4.49E-08 5.46E-08 0.000

mg/dscm 7.04E-05 5.72E-05 7.08E-05 0.000

mg/dscm@7%O2 6.03E-05 4.88E-05 5.92E-05 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000681 0.000647 0.00083 0.001

Elb/hr 8.42E-05 7.84E-05 1.02E-04 0.000

lb/mmBtuO2 1.45E-07 1.37E-07 1.75E-07 0.000

mg/dscm 1.84E-04 1.74E-04 2.27E-04 0.000

mg/dscm@7%O2 1.58E-04 1.49E-04 1.90E-04 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00337 0.00366 0.00292 0.003

Elb/hr 4.17E-04 4.44E-04 3.60E-04 0.000

lb/mmBtuO2 7.20E-07 7.75E-07 6.16E-07 0.000

mg/dscm 9.09E-04 9.87E-04 7.98E-04 0.001

mg/dscm@7%O2 7.79E-04 8.43E-04 6.67E-04 0.001

Compound: Cobalt

Average

RunNumber 1 2 3

Sunday, January 30, 2011 Page 21 of 43
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Mass_mg 0.001253 0.001523 0.002083 0.002

Elb/hr 1.55E-04 1.85E-04 2.57E-04 0.000

lb/mmBtuO2 2.68E-07 3.22E-07 4.39E-07 0.000

mg/dscm 3.38E-04 4.11E-04 5.69E-04 0.000

mg/dscm@7%O2 2.90E-04 3.51E-04 4.76E-04 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 0.76 0.375 1.01 0.715

Elb/hr 9.40E-02 4.55E-02 1.24E-01 0.088

lb/mmBtuO2 1.62E-04 7.94E-05 2.13E-04 0.000

mg/dscm 2.05E-01 1.01E-01 2.76E-01 0.194

mg/dscm@7%O2 1.76E-01 8.62E-02 2.31E-01 0.164

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00297 0.00289 0.00347 0.003

Elb/hr 3.67E-04 3.50E-04 4.27E-04 0.000

lb/mmBtuO2 6.34E-07 6.12E-07 7.32E-07 0.000

mg/dscm 8.01E-04 7.79E-04 9.48E-04 0.001

mg/dscm@7%O2 6.86E-04 6.65E-04 7.93E-04 0.001

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.00988 0.00928 0.00542 0.008

Elb/hr 1.22E-03 1.12E-03 6.67E-04 0.001

lb/mmBtuO2 2.11E-06 1.96E-06 1.14E-06 0.000

mg/dscm 2.66E-03 2.50E-03 1.48E-03 0.002

mg/dscm@7%O2 2.28E-03 2.13E-03 1.24E-03 0.002

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.01524 0.01234 0.01394 0.014

Elb/hr 1.88E-03 1.50E-03 1.72E-03 0.002

lb/mmBtuO2 3.25E-06 2.61E-06 2.94E-06 0.000

mg/dscm 4.11E-03 3.33E-03 3.81E-03 0.004

mg/dscm@7%O2 3.52E-03 2.84E-03 3.19E-03 0.003

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.103803 0.118803 0.114803 0.112

Elb/hr 1.28E-02 1.44E-02 1.41E-02 0.014

lb/mmBtuO2 2.22E-05 2.51E-05 2.42E-05 0.000

mg/dscm 2.80E-02 3.20E-02 3.14E-02 0.030

mg/dscm@7%O2 2.40E-02 2.73E-02 2.63E-02 0.026

Location: Stack Exit - Method 6C

Sunday, January 30, 2011 Page 22 of 43
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Compound: Sulfur Dioxide

Average

Run 5-19B 5-20A 5-20B

Elb/hr 1.79E+02 1.72E+02 1.68E+02 173.000

lb/mmBtuO2 2.88E-01 2.76E-01 2.69E-01 0.278

mg/dscm 3.70E+02 3.59E+02 3.50E+02 359.667

mg/dscm@7%O2 3.14E+02 2.99E+02 2.92E+02 301.667

ppm 1.39E+02 1.35E+02 1.32E+02 135.333

ppm@7%O2 1.18E+02 1.13E+02 1.10E+02 113.667

Location: Stack Exit - Method 6C 3

Compound: Sulfur Dioxide

Average

Run 5-20C 5-21A 5-21B

Elb/hr 1.69E+02 1.51E+02 1.71E+02 163.667

lb/mmBtuO2 2.70E-01 2.57E-01 2.74E-01 0.267

mg/dscm 3.51E+02 3.19E+02 3.59E+02 343.000

mg/dscm@7%O2 2.93E+02 2.79E+02 2.98E+02 290.000

ppm 1.32E+02 1.20E+02 1.35E+02 129.000

ppm@7%O2 1.10E+02 1.05E+02 1.12E+02 109.000

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 5-19B 5-20A 5-20B

Elb/hr 6.26E+01 3.75E+01 3.85E+01 46.200

lb/mmBtuO2 1.01E-01 6.02E-02 6.17E-02 0.074

mg/dscm 1.30E+02 7.82E+01 8.02E+01 96.133

mg/dscm@7%O2 1.10E+02 6.52E+01 6.69E+01 80.700

ppm 6.79E+01 4.09E+01 4.19E+01 50.233

ppm@7%O2 5.75E+01 3.41E+01 3.49E+01 42.167

Location: Stack Exit - Method 7E 3

Compound: Nitrogen oxides (NOx)

Average

Run 5-20C 5-21A 5-21B

Elb/hr 3.54E+01 3.03E+01 3.36E+01 33.100

lb/mmBtuO2 5.67E-02 5.16E-02 5.40E-02 0.054

mg/dscm 7.37E+01 6.41E+01 7.06E+01 69.467

mg/dscm@7%O2 6.15E+01 5.60E+01 5.86E+01 58.700

ppm 3.85E+01 3.35E+01 3.69E+01 36.300

ppm@7%O2 3.21E+01 2.92E+01 3.06E+01 30.633

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 0.3 0 0.1 0.133

lb/mmBtuO2 6.90E-05 0.00E+00 2.20E-05 0.000

Sunday, January 30, 2011 Page 23 of 43
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Process Run Data

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 0.1 0 0 0.033

lb/mmBtuO2 2.30E-05 0.00E+00 0.00E+00 0.000

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 6 23.8 10.1 13.300

lb/mmBtuO2 1.38E-03 5.29E-03 2.23E-03 0.003

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 2.4 2.9 2.1 2.467

lb/mmBtuO2 5.52E-04 6.45E-04 4.63E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 8.7 26.7 12.4 15.933

lb/mmBtuO2 2.00E-03 5.93E-03 2.73E-03 0.004

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 8.5 26.7 12.3 15.833

lb/mmBtuO2 1.96E-03 5.93E-03 2.71E-03 0.004

Sunday, January 30, 2011 Page 24 of 43
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Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Firing Rate 0 1000 tons/hr 0.0202

2 Coal Firing Rate 0 1000 tons/hr 0.0202

3 Coal Firing Rate 0 1000 tons/hr 0.0202

1 Average Heat Input 0 MMBtu/hr 0

2 Average Heat Input 0 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0

1 Steam Output 0 1000 lb steam/hr 400

2 Steam Output 0 1000 lb steam/hr 400

3 Steam Output 0 1000 lb steam/hr 400

1 Flue Gas Flow Rate 0 dscfm 0

1 Pressure Drop Across FGD (if applicable) 0 in H20 0

1 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 11

1 Flue Gas Oxygen Content 0 % 3.5

1 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 300

1 Unit Gross Electrical Output 0 MW 50

1 Unit Net Electric Generation 0 MWh 45

Sunday, January 30, 2011 Page 25 of 43
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Sampling / Stack Data Results Detail

Location Stack Exit - Method 10

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

Sunday, January 30, 2011 Page 26 of 43
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Location Stack Exit - Method 10 3

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

Sunday, January 30, 2011 Page 27 of 43
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Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 5/18/2010 5/19/2010 5/20/2010

Run Start Time 9:00:00 AM 8:00:00 AM 7:51:00 AM

Run Finish Time 5:20:00 PM 4:11:00 PM 4:05:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.25 0.25 0.25 0.250

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9928 0.9928 0.9928 0.993

Barometric Pressure, inches of Mercury 29.45 29.4 29.4 29.417

Average Orifice Meter Differential, inches H2O 1.70 1.77 1.76 1.743

Dry Gas Meter Volume Sampled, cubic feet 344.920 350.480 346.490 347.297

Average Dry Gas Meter Temperature, °F 88.92 82.85 87.06 86.277

Dry Gas Meter Volume Sampled, dscf 325.588 334.028 327.676 329.097

Total Moisture Liquid collected, g 451.8 501.9 495.5 483.067

Volume of Water Vapor, standard cubic feet 21.27 23.62 23.32 22.737

Moisture Content of Stack Gas, % 6.13 6.60 6.64 6.457

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

Dry Mole Fraction 0.9387 0.934 0.9336 0.935

Carbon Dioxide, % 14.9 14.3 15.4 14.867

Oxygen, % 4.57 4.5 4.23 4.433

Carbon Monoxide & Nitrogen, % 80.53 81.2 80.37 80.700

Fuel Factor 1.10 1.15 1.08

Dry Molecular Weight, lb/lb-Mole 30.57 30.47 30.63 30.557

Wet Molecular weight, lb/lb-Mole 29.80 29.65 29.79 29.747

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

Absolute Flue Gas Pressure, inches of Mercury 29.46 29.41 29.41 29.427

Average Stack Gas Temperature, °F 357.67 362.88 361.33 360.627

Average Velocity Head, inches of H2O 0.6421974765

9002

0.674205109

797874

0.670154945

801014

0.662

Average Stack Gas Velocity, feet/second 55.54 57.28 56.92 56.580

Stack Cross-Sectional Area, square feet 63.617 63.617 63.617 63.617

Dry Volumetric Flow Rate, dry scfm 126,527.3 128,796.8 128,174.0 127,832.700

Actual Wet Volumetric Flue Gas Flow Rate, acfm 211,997.3 218,638.9 217,264.8 215,967.000

Percent Isokinetic of Sampling Rate, % 100.0 100.8 99.4 100.067

Percent Excess Air, % 27.4 26.6 24.9 26.300

F-Factor, dscfm/MMBtu @ %O2 9847 9794 9828 9,823.000

Round Duct Diameter, inches 108 108 108

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

Sunday, January 30, 2011 Page 28 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - Method 25A

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

Sunday, January 30, 2011 Page 29 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - Method 25A 3

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

Sunday, January 30, 2011 Page 30 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - Method 26A

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

Sunday, January 30, 2011 Page 31 of 43
3225 Manitowoc Public Utilities

8/11/2010

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

Sunday, January 30, 2011 Page 32 of 43
3225 Manitowoc Public Utilities

8/11/2010

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

Sunday, January 30, 2011 Page 33 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - Method 3A CO2 3

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

Sunday, January 30, 2011 Page 34 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - Method 3A CO2 3 6

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

Sunday, January 30, 2011 Page 35 of 43
3225 Manitowoc Public Utilities

8/11/2010

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

Sunday, January 30, 2011 Page 36 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - Method 3A O2 3

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

Sunday, January 30, 2011 Page 37 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - Method 3A O2 3 6

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

Sunday, January 30, 2011 Page 38 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - Method 6C

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

Sunday, January 30, 2011 Page 39 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - Method 6C 3

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

Sunday, January 30, 2011 Page 40 of 43
3225 Manitowoc Public Utilities

8/11/2010

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

Sunday, January 30, 2011 Page 41 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - Method 7E 3

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

Sunday, January 30, 2011 Page 42 of 43
3225 Manitowoc Public Utilities

8/11/2010

Location Stack Exit - OTM - 27/28

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

Sunday, January 30, 2011 Page 43 of 43