Name: Terry P. Jensky

Title: Vice President - Energy Supply Operat

Company: Wisconsin Public Service

Sign Date: 9/1/2010

Name: Kevin O'Halloren

Title: Clean Air Engineering

Company: Project Manager

Sign Date: 9/1/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Pulliam 8 Boiler

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.

Friday, February 25, 2011 Page 1 of 22
Pulliam 8 Boiler

9/1/2010

Facility Information:

Pulliam

1530 North Bylsby Avenue

Green Bay WI 54301

Contact: Shelly Heston

Phone: 920-433-1294

Fax: 920-430-6369

Email: srheston@integrysgroup.com

Testing Company:

Clean Air Engineering

500 West Wood Street

Palatine

IL 600 4975

Contact: Kevin Ohalloren

Phone: 847-654-4661

Fax: 847-991-0036

Email: kohalloren@cleanair.com

Air Permit Number:

4072

Permitted Source ID/Name:

8 Enter the Boiler ID of the tested boiler (left)

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:

Unit 8 is a rear wall-fired dry-bottom boiler installed in 1964. The boiler fires pulverized coal from the Powder River 

Basin. Unit 8 is equipped with low Nox burner, Overfire Air, and an electrostatic precipitator.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 110000421534 FRS #: 110040955393

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 186 0 0 0 372 1488 4 3

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 180 0

Stack Exit Carbon Monoxide Method 10 3 120 0

Stack Exit Formaldehyde Method 0011 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

Friday, February 25, 2011 Page 2 of 22
Pulliam 8 Boiler

9/1/2010

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

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26 3 180 0

Stack Exit Hydrogen Fluoride Method 26 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Organic Condensible 

Particulate

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Friday, February 25, 2011 Page 3 of 22
Pulliam 8 Boiler

9/1/2010

The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

In this section, identify the promulgation date of any specified test method that you use for determining the 

procedures followed. This field is also used to document any modifications that are necessary to conduct the 

emissions test if they are outside the requirements of the cited method. If this modification was approved verbally by 

a regulatory agency, the name and date of approval should be included. Written formal approval should be attached 

to this file using the "Attach File" button. Test procedures that are different from those published in the Federal 

Register should be attached using the "Attach File" button.

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Filterable Particulate Method 29 3 240 0

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 Lead Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit Co2 Method 3A CO2 3 240 0

Stack Exit O2 Method 3A O2 3 240 0

Inorganic (Aqueous) 

Condensible Part.

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Organic Condensible 

Particulate

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Filterable Particulate Method 5 3 240 0

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Friday, February 25, 2011 Page 4 of 22
Pulliam 8 Boiler

9/1/2010

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 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

Friday, February 25, 2011 Page 5 of 22
Pulliam 8 Boiler

9/1/2010

Location Stack Exit - Method 29

Average

Run Number M5/29-1 M5/29-2 M5/29-3

Test Date 4/6/2010 4/7/2010 4/8/2010

Run Start Time 11:53:00 AM 8:57:00 

AM

8:46:00 AM

Run Finish Time 3:48:00 PM 12:52:00 

PM

12:41:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 151.489 148.758 150.990 150.412

Moisture Content of Stack Gas, % 12.20 11.38 11.47 11.683

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

Carbon Dioxide, % 13 13.1 12.7 12.933

Oxygen, % 6 6.3 6.8 6.367

Average Stack Gas Temperature, °F 352.46 343.10 338.31 344.623

Dry Volumetric Flow Rate, dry scfm 305,463.4 304,292.6 305,022.4 304,926.133

Actual Wet Volumetric Flue Gas Flow Rate, acfm 542,414.0 529,167.8 527,809.3 533,130.367

Percent Isokinetic of Sampling Rate, % 103.4 101.9 103.2 102.833

F-Factor, dscfm/MMBtu @ %O2 9133 9027 9223 9,127.667

Fw 0 0 0 0.000

Fc 0 0 0 0.000

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

Friday, February 25, 2011 Page 6 of 22
Pulliam 8 Boiler

9/1/2010

Friday, February 25, 2011 Page 7 of 22
Pulliam 8 Boiler

9/1/2010

Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000

gr/dscf 5.59E-02 7.94E-02 1.47E-01 0.094

lb/mmBtuO2 1.04E-01 1.46E-01 2.66E-01 0.172

mg/dscm 1.28E+02 1.82E+02 3.35E+02 215.000

ppm 1.10E+02 1.56E+02 2.88E+02 184.667

ppm@7%O2 1.04E+02 1.45E+02 2.66E+02 171.667

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 5.21E-01 1.50E-01 0.00E+00 0.224

gr/dscf 1.88E-04 4.91E-05 3.53E-04 0.000

lb/mmBtuO2 3.51E-04 9.01E-05 6.40E-04 0.000

mg/dscm 4.31E-01 1.12E-01 8.07E-01 0.450

ppm 2.35E-01 6.13E-02 4.40E-01 0.245

ppm@7%O2 2.22E-01 5.70E-02 4.06E-01 0.228

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 0.000342 0.000706 0.000384 0.000

Elb/hr 9.12E-05 1.91E-04 1.03E-04 0.000

lb/mmBtuO2 6.38E-08 1.35E-07 7.67E-08 0.000

mg/dscm 7.97E-05 1.68E-04 8.98E-05 0.000

mg/dscm@7%O2 7.44E-05 1.60E-04 8.85E-05 0.000

Compound: Arsenic

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 0.0122 0.00532 0.00658 0.008

Elb/hr 3.25E-03 1.44E-03 1.76E-03 0.002

lb/mmBtuO2 2.27E-06 1.02E-06 1.31E-06 0.000

mg/dscm 2.84E-03 1.26E-03 1.54E-03 0.002

mg/dscm@7%O2 2.65E-03 1.20E-03 1.52E-03 0.002

Compound: Beryllium

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 0.0002 0.0002 0.0002 0.000

Elb/hr 5.33E-05 5.41E-05 5.34E-05 0.000

lb/mmBtuO2 3.73E-08 3.83E-08 3.99E-08 0.000

mg/dscm 4.66E-05 4.75E-05 4.68E-05 0.000

mg/dscm@7%O2 4.35E-05 4.52E-05 4.61E-05 0.000

Friday, February 25, 2011 Page 8 of 22
Pulliam 8 Boiler

9/1/2010

Compound: Cadmium

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 0.0001 0.0001 0.0001 0.000

Elb/hr 2.67E-05 2.71E-05 2.67E-05 0.000

lb/mmBtuO2 1.86E-08 1.92E-08 2.00E-08 0.000

mg/dscm 2.33E-05 2.37E-05 2.34E-05 0.000

mg/dscm@7%O2 2.17E-05 2.26E-05 2.31E-05 0.000

Compound: Chromium

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 0.00358 0.00262 0.00273 0.003

Elb/hr 9.55E-04 7.09E-04 7.30E-04 0.001

lb/mmBtuO2 6.67E-07 5.02E-07 5.45E-07 0.000

mg/dscm 8.35E-04 6.22E-04 6.39E-04 0.001

mg/dscm@7%O2 7.79E-04 5.92E-04 6.30E-04 0.001

Compound: Cobalt

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 0.00092 0.000688 0.000657 0.001

Elb/hr 2.45E-04 1.86E-04 1.76E-04 0.000

lb/mmBtuO2 1.72E-07 1.32E-07 1.31E-07 0.000

mg/dscm 2.15E-04 1.63E-04 1.54E-04 0.000

mg/dscm@7%O2 2.01E-04 1.55E-04 1.52E-04 0.000

Compound: Filterable Particulate

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 15.51 11.16 11.52 12.730

Elb/hr 4.14E+00 3.02E+00 3.08E+00 3.413

lb/mmBtuO2 2.89E-03 2.14E-03 2.30E-03 0.002

mg/dscm 3.62E+00 2.65E+00 2.69E+00 2.987

mg/dscm@7%O2 3.38E+00 2.52E+00 2.65E+00 2.850

Compound: Lead

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 0.00212 0.00213 0.00195 0.002

Elb/hr 5.65E-04 5.76E-04 5.21E-04 0.001

lb/mmBtuO2 3.95E-07 4.08E-07 3.89E-07 0.000

mg/dscm 4.94E-04 5.06E-04 4.56E-04 0.000

mg/dscm@7%O2 4.61E-04 4.82E-04 4.50E-04 0.000

Compound: Manganese

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 0.00746 0.00498 0.00372 0.005

Elb/hr 1.99E-03 1.35E-03 9.94E-04 0.001

lb/mmBtuO2 1.39E-06 9.54E-07 7.43E-07 0.000

mg/dscm 1.74E-03 1.18E-03 8.70E-04 0.001

mg/dscm@7%O2 1.62E-03 1.12E-03 8.58E-04 0.001

Friday, February 25, 2011 Page 9 of 22
Pulliam 8 Boiler

9/1/2010

Compound: Nickel

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 0.003695 0.002065 0.003115 0.003

Elb/hr 9.86E-04 5.59E-04 8.32E-04 0.001

lb/mmBtuO2 6.89E-07 3.95E-07 6.22E-07 0.000

mg/dscm 8.61E-04 4.90E-04 7.29E-04 0.001

mg/dscm@7%O2 8.03E-04 4.67E-04 7.19E-04 0.001

Compound: Selenium

Average

RunNumber M5/29-1 M5/29-2 M5/29-3

Mass_mg 0.392 0.214 0.224 0.277

Elb/hr 1.05E-01 5.79E-02 5.99E-02 0.074

lb/mmBtuO2 7.31E-05 4.10E-05 4.47E-05 0.000

mg/dscm 9.14E-02 5.08E-02 5.24E-02 0.065

mg/dscm@7%O2 8.53E-02 4.84E-02 5.17E-02 0.062

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber M27/28-1 M27/28-2 M27/28-3

Mass_mg 31.9 43.59 5.71 27.067

lb/mmBtuO2 6.41E-03 1.00E-02 1.36E-03 0.006

Compound: Filterable PM2.5

Average

RunNumber M27/28-1 M27/28-2 M27/28-3

Mass_mg 2.87 13.95 4.26 7.027

lb/mmBtuO2 5.77E-04 3.21E-03 1.01E-03 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber M27/28-1 M27/28-2 M27/28-3

Mass_mg 32.05 20.7 21.13 24.627

lb/mmBtuO2 6.44E-03 4.77E-03 5.01E-03 0.005

Compound: Organic Condensible Particulate

Average

RunNumber M27/28-1 M27/28-2 M27/28-3

Mass_mg 1.94 2.3 0.47 1.570

lb/mmBtuO2 3.90E-04 5.30E-04 1.12E-04 0.000

Compound: Total Particulate

Average

RunNumber M27/28-1 M27/28-2 M27/28-3

Mass_mg 65.89 66.59 27.31 53.263

lb/mmBtuO2 1.32E-02 1.53E-02 6.48E-03 0.012

Compound: Total PM2.5

Average

RunNumber M27/28-1 M27/28-2 M27/28-3

Mass_mg 36.86 36.95 25.86 33.223

Friday, February 25, 2011 Page 10 of 22
Pulliam 8 Boiler

9/1/2010

Process Run Data

lb/mmBtuO2 7.41E-03 8.51E-03 6.14E-03 0.007

Friday, February 25, 2011 Page 11 of 22
Pulliam 8 Boiler

9/1/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Burned 0 Tons/hr 0

4 Coal Burned 0 Tons/hr 0

5 Coal Burned 0 Tons/hr 0

1 Average Heat Input 1070 MMBtu/hr Run 1 testing on 

4/6/2010 for 

Method 5/29 and 

OTM 27/28

1075

4 Average Heat Input 1063 MMBtu/hr Run 2 testing on 

4/7/2010 for 

Method 5/29 and 

OTM 27/28

1075

5 Average Heat Input 1087 MMBtu/hr Run 3 testing on 

4/8/2010 for 

Method 5/29 and 

OTM 27/28

1075

1 Steam Output 746 1000 lb steam/hr Run 1 testing on 

4/6/2010 for 

Method 5/29 and 

OTM 27/28

750

4 Steam Output 765 1000 lb steam/hr Run 2 testing on 

4/7/2010 for 

Method 5/29 and 

OTM 27/28

750

5 Steam Output 746 1000 lb steam/hr Run 3 testing on 

4/8/2010 for 

Method 5/29 and 

OTM 27/28

750

1 Synfuel Firing Rate 0 1000 Tons/hr 0

4 Synfuel Firing Rate 0 1000 Tons/hr 0

5 Synfuel Firing Rate 0 1000 Tons/hr 0

1 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

4 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

5 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

1 Coal Gas Firing Rate 0 Ft^3/min 0

4 Coal Gas Firing Rate 0 Ft^3/min 0

5 Coal Gas Firing Rate 0 Ft^3/min 0

1 Fuel Oil Firing Rate 0 gal/hr 0

4 Fuel Oil Firing Rate 0 gal/hr 0

5 Fuel Oil Firing Rate 0 gal/hr 0

1 Flue Gas Flow Rate 0 0

Friday, February 25, 2011 Page 12 of 22
Pulliam 8 Boiler

9/1/2010

4 Flue Gas Flow Rate 0 0

5 Flue Gas Flow Rate 0 0

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

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

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

1 FGD Scrubber Liquor pH 0 pH 0

4 FGD Scrubber Liquor pH 0 pH 0

5 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

5 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

5 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

4 Flue Gas Oxygen Content 0 % 0

5 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 11.6 % Run 1 testing on 

4/6/2010 for 

Method 5/29 and 

OTM 27/28

11.75

4 Flue Gas Carbon Dioxide Content 12.1 % Run 2 testing on 

4/7/2010 for 

Method 5/29 and 

OTM 27/28

11.75

5 Flue Gas Carbon Dioxide Content 11.9 % Run 3 testing on 

4/8/2010 for 

Method 5/29 and 

OTM 27/28

11.75

1 Flue Gas Moisture Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

5 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

4 Flue Gas Sampling Point Temperature 0 Deg F 0

5 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

4 Flue Gas Pressure 0 atm 0

5 Flue Gas Pressure 0 atm 0

Friday, February 25, 2011 Page 13 of 22
Pulliam 8 Boiler

9/1/2010

1 Standard Pressure 0 atm 0

4 Standard Pressure 0 atm 0

5 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

4 Standard Temperature 0 Deg F 0

5 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 111 Mwe Run 1 testing on 

4/6/2010 for 

Method 5/29 and 

OTM 27/28

110

4 Unit Gross Electrical Output 111 Mwe Run 2 testing on 

4/7/2010 for 

Method 5/29 and 

OTM 27/28

110

5 Unit Gross Electrical Output 112 Mwe Run 3 testing on 

4/8/2010 for 

Method 5/29 and 

OTM 27/28

110

1 Unit Net Electric Generation 102 MWh Run 1 testing on 

4/6/2010 for 

Method 5/29 and 

OTM 27/28

102

4 Unit Net Electric Generation 104 MWh Run 2 testing on 

4/7/2010 for 

Method 5/29 and 

OTM 27/28

102

5 Unit Net Electric Generation 102 MWh Run 3 testing on 

4/8/2010 for 

Method 5/29 and 

OTM 27/28

102

6 Coal Burned 0 Tons/hr 0

6 Average Heat Input 1128 MMBtu/hr Run 1 testing on 

4/9/2010 for 

Method 10 and 

25A

1075

6 Steam Output 815 1000 lb steam/hr Run 1 testing on 

4/9/2010 for 

Method 10 and 

25A

750

6 Synfuel Firing Rate 0 1000 Tons/hr 0

6 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

6 Coal Gas Firing Rate 0 Ft^3/min 0

6 Fuel Oil Firing Rate 0 gal/hr 0

6 Flue Gas Flow Rate 0 0

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

Friday, February 25, 2011 Page 14 of 22
Pulliam 8 Boiler

9/1/2010

6 FGD Scrubber Liquor pH 0 pH 0

6 FGD Scrubber Liquor Flow Rate 0 gal/min 0

6 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

6 Flue Gas Oxygen Content 0 % 0

6 Flue Gas Carbon Dioxide Content 11.8 % Run 1 testing on 

4/9/2010 for 

Method 10 and 

25A

11.75

6 Flue Gas Moisture Content 0 % 0

6 Flue Gas Sampling Point Temperature 0 Deg F 0

6 Flue Gas Pressure 0 atm 0

6 Standard Pressure 0 atm 0

6 Standard Temperature 0 Deg F 0

6 Unit Gross Electrical Output 116 Mwe Run 1 testing on 

4/9/2010 for 

Method 10 and 

25A

110

6 Unit Net Electric Generation 111 MWh Run 1 testing on 

4/9/2010 for 

Method 10 and 

25A

102

7 Coal Burned 0 Tons/hr 0

7 Average Heat Input 1068 MMBtu/hr Run 2 & 3 testing 

on 4/10/2010 for 

Method 10 and 

25A

1075

7 Steam Output 740 1000 lb steam/hr Run 2 & 3 testing 

on 4/10/2010 for 

Method 10 and 

25A

750

7 Synfuel Firing Rate 0 1000 Tons/hr 0

7 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

7 Coal Gas Firing Rate 0 Ft^3/min 0

7 Fuel Oil Firing Rate 0 gal/hr 0

7 Flue Gas Flow Rate 0 0

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

7 FGD Scrubber Liquor pH 0 pH 0

7 FGD Scrubber Liquor Flow Rate 0 gal/min 0

7 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

7 Flue Gas Oxygen Content 0 % 0

Friday, February 25, 2011 Page 15 of 22
Pulliam 8 Boiler

9/1/2010

APCD Run Data

Process Lab Run Data

7 Flue Gas Carbon Dioxide Content 11.7 % Run 2 & 3 testing 

on 4/10/2010 for 

Method 10 and 

25A

11.75

7 Flue Gas Moisture Content 0 % 0

7 Flue Gas Sampling Point Temperature 0 Deg F 0

7 Flue Gas Pressure 0 atm 0

7 Standard Pressure 0 atm 0

7 Standard Temperature 0 Deg F 0

7 Unit Gross Electrical Output 110 Mwe Run 2 & 3 testing 

on 4/10/2010 for 

Method 10 and 

25A

110

7 Unit Net Electric Generation 101 MWh Run 2 & 3 testing 

on 4/10/2010 for 

Method 10 and 

25A

102

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 OVERFIRE AIR 0 lb/mmbtu @ ppm CO 0.21

1 ELECTROSTATIC PRECIPITATOR 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 8339 Btu/lb

2 Fuel Higher Heating Value 8477 Btu/lb

3 Fuel Higher Heating Value 8407 Btu/lb

4 Fuel Higher Heating Value 8348 Btu/lb

1 Fuel Moisture 29.94 %

2 Fuel Moisture 28.79 %

3 Fuel Moisture 29.32 %

4 Fuel Moisture 29.81 %

1 Fuel Mercury Content 0.068 ppm

2 Fuel Mercury Content 0.082 ppm

3 Fuel Mercury Content 0.072 ppm

4 Fuel Mercury Content 0 ppm

1 Fuel Cadmium Content 0.083 ppm

2 Fuel Cadmium Content 0.072 ppm

3 Fuel Cadmium Content 0.075 ppm

Friday, February 25, 2011 Page 16 of 22
Pulliam 8 Boiler

9/1/2010

4 Fuel Cadmium Content 0 ppm

1 Ultimate/Proximate Analysis 0

2 Ultimate/Proximate Analysis 0

3 Ultimate/Proximate Analysis 0

4 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 4.8 ppm

2 Fuel Nickel Content 3.81 ppm

3 Fuel Nickel Content 3.61 ppm

4 Fuel Nickel Content 0 ppm

1 Fuel Arsenic Content 1.4 ppm

2 Fuel Arsenic Content 1.08 ppm

3 Fuel Arsenic Content 0.941 ppm

4 Fuel Arsenic Content 0 ppm

1 Fuel Chromium Content 4.98 ppm

2 Fuel Chromium Content 3.92 ppm

3 Fuel Chromium Content 3.79 ppm

4 Fuel Chromium Content 0 ppm

1 Fuel Beryllium Content 0.244 ppm

2 Fuel Beryllium Content 0.257 ppm

3 Fuel Beryllium Content 0.252 ppm

4 Fuel Beryllium Content 0 ppm

1 Fuel Lead Content 2.66 ppm

2 Fuel Lead Content 2.69 ppm

3 Fuel Lead Content 2.82 ppm

4 Fuel Lead Content 0 ppm

1 Fuel Manganese Content 23.5 ppm

2 Fuel Manganese Content 10.7 ppm

3 Fuel Manganese Content 9.05 ppm

4 Fuel Manganese Content 0 ppm

1 Fuel Chlorine Content 37 ppm

2 Fuel Chlorine Content 20 ppm

3 Fuel Chlorine Content 17 ppm

4 Fuel Chlorine Content 0 ppm

1 Fuel Fluorine Content 68.2 ppm

2 Fuel Fluorine Content 69.4 ppm

3 Fuel Fluorine Content 75.5 ppm

4 Fuel Fluorine Content 0 ppm

5 Fuel Higher Heating Value 8214 Btu/lb

5 Fuel Moisture 30.64 %

5 Fuel Mercury Content 0 ppm

5 Fuel Cadmium Content 0 ppm

5 Ultimate/Proximate Analysis 0

5 Fuel Nickel Content 0 ppm

Friday, February 25, 2011 Page 17 of 22
Pulliam 8 Boiler

9/1/2010

5 Fuel Arsenic Content 0 ppm

5 Fuel Chromium Content 0 ppm

5 Fuel Beryllium Content 0 ppm

5 Fuel Lead Content 0 ppm

5 Fuel Manganese Content 0 ppm

5 Fuel Chlorine Content 0 ppm

5 Fuel Fluorine Content 0 ppm

6 Fuel Higher Heating Value 8243 Btu/lb

6 Fuel Moisture 30.21 %

6 Fuel Mercury Content 0 ppm

6 Fuel Cadmium Content 0 ppm

6 Ultimate/Proximate Analysis 0

6 Fuel Nickel Content 0 ppm

6 Fuel Arsenic Content 0 ppm

6 Fuel Chromium Content 0 ppm

6 Fuel Beryllium Content 0 ppm

6 Fuel Lead Content 0 ppm

6 Fuel Manganese Content 0 ppm

6 Fuel Chlorine Content 0 ppm

6 Fuel Fluorine Content 0 ppm

Friday, February 25, 2011 Page 18 of 22
Pulliam 8 Boiler

9/1/2010

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

Friday, February 25, 2011 Page 19 of 22
Pulliam 8 Boiler

9/1/2010

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

Friday, February 25, 2011 Page 20 of 22
Pulliam 8 Boiler

9/1/2010

Location Stack Exit - Method 29

Average

Run Number M5/29-1 M5/29-2 M5/29-3

Test Date 4/6/2010 4/7/2010 4/8/2010

Run Start Time 11:53:00 AM 8:57:00 AM 8:46:00 AM

Run Finish Time 3:48:00 PM 12:52:00 PM 12:41:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.263 0.263 0.263 0.263

Pitot Tube Coefficient 0.822 0.822 0.822 0.822

Dry Gas Meter Calibration Factor 0.9903 0.9903 0.9903 0.990

Barometric Pressure, inches of Mercury 29.6 29.6 29.6 29.600

Average Orifice Meter Differential, inches H2O 1.32 1.27 1.28 1.290

Dry Gas Meter Volume Sampled, cubic feet 154.130 150.140 150.000 151.423

Average Dry Gas Meter Temperature, °F 68.03 63.74 55.53 62.433

Dry Gas Meter Volume Sampled, dscf 151.489 148.758 150.990 150.412

Total Moisture Liquid collected, g 446.9 405.9 415.8 422.867

Volume of Water Vapor, standard cubic feet 21.04 19.11 19.57 19.907

Moisture Content of Stack Gas, % 12.20 11.38 11.47 11.683

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

Dry Mole Fraction 0.878 0.8862 0.8853 0.883

Carbon Dioxide, % 13 13.1 12.7 12.933

Oxygen, % 6 6.3 6.8 6.367

Carbon Monoxide & Nitrogen, % 81 80.6 80.5 80.700

Fuel Factor 1.15 1.11 1.11

Dry Molecular Weight, lb/lb-Mole 30.32 30.35 30.30 30.323

Wet Molecular weight, lb/lb-Mole 28.82 28.94 28.89 28.883

Flue Gas Static Pressure, inches of H2O -0.9 -0.9 -0.9 -0.900

Absolute Flue Gas Pressure, inches of Mercury 29.53 29.53 29.53 29.530

Average Stack Gas Temperature, °F 352.46 343.10 338.31 344.623

Average Velocity Head, inches of H2O 0.4868651861

49339

0.470844202

476304

0.470412236

688096

0.476

Average Stack Gas Velocity, feet/second 47.91 46.74 46.62 47.090

Stack Cross-Sectional Area, square feet 188.692 188.692 188.692 188.692

Dry Volumetric Flow Rate, dry scfm 305,463.4 304,292.6 305,022.4 304,926.133

Actual Wet Volumetric Flue Gas Flow Rate, acfm 542,414.0 529,167.8 527,809.3 533,130.367

Percent Isokinetic of Sampling Rate, % 103.4 101.9 103.2 102.833

Percent Excess Air, % 39.0 42.1 47.1 42.733

F-Factor, dscfm/MMBtu @ %O2 9133 9027 9223 9,127.667

Round Duct Diameter, inches 186 186 186

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

Friday, February 25, 2011 Page 21 of 22
Pulliam 8 Boiler

9/1/2010

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

Friday, February 25, 2011 Page 22 of 22