Name: Robert A. Greco

Title: Manager Air Quality

Company: We Energies

Sign Date: 7/30/2010

Name: Scott Banach

Title: Director, Project Engineering

Company: Platt Environmental Services, Inc.

Sign Date: 7/30/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Monday, February 07, 2011 Page 1 of 14
7/30/2010

Facility Information:

South Oak Creek (ORIS Facility ID #4041)

11060 S. Chicago Road

Oak Creek WI 53154

Contact: Robert A. Greco

Phone: (414) 221-5441

Fax: (414) 221-2022

Email: bob.greco@we-energies.com

Testing Company:

Platt Environmental Services, Inc.

1520 Kensington Road, Suite 204

Oak Brook IL 60523

Contact: Scott W. Banach

Phone: (630) 521-9400

Fax: (630) 521-9494

Email: sbanach@plattenv.com

Air Permit Number:

4041

Permitted Source ID/Name:

7 South Oak Creek

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:

The South Oak Creek Power Plant is an electric power generating station consisting of 4 boilers which use 

subbituminous coal with natural gas for coal flame stabilization at low loads and boiler startup. Boilers #5 and #6 are 

wall-fired boilers, while Boilers #7 and #8 are tangentially fired. Particulate matter emissions are controlled by 

electrostatic precipitators, which were installed in 1972 (Boilers #5 and #6) and 1991 and 1992 (Boiler #7 and #8, 

respectively).

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 5507900017 FRS #: 20847

SCC / Description 10100212 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Tangential) (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 252 0 0 0 504 448 4 24

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

Monday, February 07, 2011 Page 2 of 14
7/30/2010

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

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 Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26 3 180 0

Stack Exit Hydrogen Chloride Method 26 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

Monday, February 07, 2011 Page 3 of 14
7/30/2010

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.

All methods described in the EU MACT ICR were used.

Organic Condensible 

Particulate

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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 Beryllium Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit O2 Method 3A O2 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 3 480 0

Stack Exit Co2 Method 3A CO2 3 480 0

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Organic Condensible 

Particulate

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

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

Monday, February 07, 2011 Page 4 of 14
7/30/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 6/30/2010 7/1/2010 7/2/2010

Run Start Time 10:22:00 AM 8:00:00 

AM

8:30:00 AM

Run Finish Time 2:40:00 PM 1:03:00 PM 12:50:00 PM

Net Run Time, minutes 240 235 240

Dry Gas Meter Volume Sampled, dscf 195.314 188.579 190.613 191.502

Moisture Content of Stack Gas, % 10.84 10.89 10.50 10.743

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

Carbon Dioxide, % 12.7 12.7 12.7 12.700

Oxygen, % 7.1 7.1 7.1 7.100

Average Stack Gas Temperature, °F 275.92 276.87 279.69 277.493

Dry Volumetric Flow Rate, dry scfm 658,894.4 653,350.8 652,270.4 654,838.533

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,035,550.1 1,024,951.5 1,026,821.8 1,029,107.80

0

Percent Isokinetic of Sampling Rate, % 104.5 103.9 103.0 103.800

F-Factor, dscfm/MMBtu @ %O2 9820 9820 9820 9,820.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Monday, February 07, 2011 Page 5 of 14
7/30/2010

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

Monday, February 07, 2011 Page 6 of 14
7/30/2010

Emissions Summary

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0028 0.0028 0.0028 0.003

Elb/hr 1.25E-03 1.28E-03 1.27E-03 0.001

lb/mmBtuO2 4.70E-07 4.87E-07 4.82E-07 0.000

mg/dscm 5.06E-04 5.24E-04 5.19E-04 0.001

mg/dscm@7%O2 5.10E-04 5.28E-04 5.23E-04 0.001

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0028 0.0028 0.0028 0.003

Elb/hr 1.25E-03 1.28E-03 1.27E-03 0.001

lb/mmBtuO2 4.70E-07 4.87E-07 4.82E-07 0.000

mg/dscm 5.06E-04 5.24E-04 5.19E-04 0.001

mg/dscm@7%O2 5.10E-04 5.28E-04 5.23E-04 0.001

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0007 0.0007 0.0007 0.001

Elb/hr 3.12E-04 3.21E-04 3.17E-04 0.000

lb/mmBtuO2 1.18E-07 1.22E-07 1.20E-07 0.000

mg/dscm 1.27E-04 1.31E-04 1.30E-04 0.000

mg/dscm@7%O2 1.28E-04 1.32E-04 1.31E-04 0.000

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00339 0.00098 0.0007 0.002

Elb/hr 1.51E-03 4.49E-04 3.17E-04 0.001

lb/mmBtuO2 5.69E-07 1.70E-07 1.20E-07 0.000

mg/dscm 6.13E-04 1.84E-04 1.30E-04 0.000

mg/dscm@7%O2 6.17E-04 1.85E-04 1.31E-04 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00302 0.0036 0.00336 0.003

Elb/hr 1.35E-03 1.65E-03 1.52E-03 0.002

lb/mmBtuO2 5.07E-07 6.26E-07 5.78E-07 0.000

mg/dscm 5.46E-04 6.74E-04 6.23E-04 0.001

mg/dscm@7%O2 5.50E-04 6.79E-04 6.28E-04 0.001

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00075 0.00075 0.0007 0.001

Elb/hr 3.35E-04 3.44E-04 3.17E-04 0.000

Monday, February 07, 2011 Page 7 of 14
7/30/2010

lb/mmBtuO2 1.26E-07 1.30E-07 1.20E-07 0.000

mg/dscm 1.36E-04 1.40E-04 1.30E-04 0.000

mg/dscm@7%O2 1.37E-04 1.41E-04 1.31E-04 0.000

Compound: Filterable Particulate

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 4.6 12.9 5.2 7.567

Elb/hr 2.05E+00 5.91E+00 2.35E+00 3.437

lb/mmBtuO2 7.72E-04 2.24E-03 8.94E-04 0.001

mg/dscm 8.32E-01 2.42E+00 9.64E-01 1.405

mg/dscm@7%O2 8.38E-01 2.44E+00 9.71E-01 1.416

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00188 0.00165 0.00154 0.002

Elb/hr 8.39E-04 7.56E-04 6.97E-04 0.001

lb/mmBtuO2 3.16E-07 2.87E-07 2.65E-07 0.000

mg/dscm 3.40E-04 3.09E-04 2.85E-04 0.000

mg/dscm@7%O2 3.42E-04 3.11E-04 2.87E-04 0.000

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0083 0.006 0.00485 0.006

Elb/hr 3.70E-03 2.75E-03 2.20E-03 0.003

lb/mmBtuO2 1.39E-06 1.04E-06 8.34E-07 0.000

mg/dscm 1.50E-03 1.12E-03 8.99E-04 0.001

mg/dscm@7%O2 1.51E-03 1.13E-03 9.06E-04 0.001

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00769 0.02289 0.01799 0.016

Elb/hr 3.43E-03 1.05E-02 8.14E-03 0.007

lb/mmBtuO2 1.29E-06 3.98E-06 3.09E-06 0.000

mg/dscm 1.39E-03 4.29E-03 3.33E-03 0.003

mg/dscm@7%O2 1.40E-03 4.32E-03 3.35E-03 0.003

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0089 0.009 0.0169 0.012

Elb/hr 3.97E-03 4.12E-03 7.65E-03 0.005

lb/mmBtuO2 1.49E-06 1.56E-06 2.91E-06 0.000

mg/dscm 1.61E-03 1.69E-03 3.13E-03 0.002

mg/dscm@7%O2 1.62E-03 1.70E-03 3.15E-03 0.002

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Monday, February 07, 2011 Page 8 of 14
7/30/2010

Process Run Data

Mass_mg 7.9 7.1 5.7 6.900

lb/mmBtuO2 2.01E-03 1.82E-03 1.46E-03 0.002

Compound: Filterable PM2.5

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 6.8 5.8 5.1 5.900

lb/mmBtuO2 1.73E-03 1.49E-03 1.30E-03 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 23.6 19.7 22.5 21.933

lb/mmBtuO2 6.02E-03 5.05E-03 5.75E-03 0.006

Compound: Organic Condensible Particulate

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 0 0.9 1 0.633

lb/mmBtuO2 0.00E+00 2.30E-04 2.56E-04 0.000

Compound: Total Particulate

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 31.5 27.7 29.2 29.467

lb/mmBtuO2 8.03E-03 7.09E-03 7.47E-03 0.008

Compound: Total PM2.5

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 30.4 26.4 28.6 28.467

lb/mmBtuO2 7.75E-03 6.76E-03 7.31E-03 0.007

Monday, February 07, 2011 Page 9 of 14
7/30/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 148.36 1000 ton/hr 0

2 Bituminous Coal Burned 144.87 1000 ton/hr 0

3 Bituminous Coal Burned 144.93 1000 ton/hr 0

1 Average Heat Input 3072.7 MMBtu/hr 0

2 Average Heat Input 2993 MMBtu/hr 0

3 Average Heat Input 2934 MMBtu/hr 0

1 Steam Output 1903.0 1000 lb steam/hr 0

2 Steam Output 1851.8 1000 lb steam/hr 0

3 Steam Output 1892.1 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 1000 Tons/hr 0

2 Synfuel Firing Rate 0 1000 Tons/hr 0

3 Synfuel Firing Rate 0 1000 Tons/hr 0

1 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

2 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

3 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

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

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

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

1 Fuel Oil Firing Rate 0 gal/hr 0

2 Fuel Oil Firing Rate 0 gal/hr 0

3 Fuel Oil Firing Rate 0 gal/hr 0

1 Flue Gas Flow Rate 0 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 0

1 Flue Gas Oxygen Content 7.1 % 0

1 Flue Gas Carbon Dioxide Content 12.7 % 0

1 Flue Gas Moisture Content 10.8 % 0

1 Flue Gas Sampling Point Temperature 275.9 Deg F 0

1 Flue Gas Pressure 0.9946 atm 0

1 Standard Pressure 1 atm 0

1 Standard Temperature 63.33 Deg F 0

Monday, February 07, 2011 Page 10 of 14
7/30/2010

APCD Run Data

Process Lab Run Data

1 Unit Gross Electrical Output 308.8 Mwe 0

1 Unit Net Electric Generation 285.53 MWh 0

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0.002 lb/mmBtu 0.03

2 ELECTROSTATIC PRECIPITATOR 0.002 lb/mmBtu 0.03

3 ELECTROSTATIC PRECIPITATOR 0.002 lb/mmBtu 0.03

Run Name Value UOM Comments

1 Fuel Higher Heating Value 12069 Btu/lb

2 Fuel Higher Heating Value 11950 Btu/lb

3 Fuel Higher Heating Value 12074 Btu/lb

1 Fuel Moisture 28.36 %

2 Fuel Moisture 28 %

3 Fuel Moisture 27.71 %

1 Fuel Mercury Content 0.055 ppm

2 Fuel Mercury Content 0.052 ppm

3 Fuel Mercury Content 0.056 ppm

1 Fuel Cadmium Content 0.082 ppm

2 Fuel Cadmium Content 0.072 ppm

3 Fuel Cadmium Content 0.053 ppm

1 Ultimate/Proximate Analysis 0

2 Ultimate/Proximate Analysis 0

3 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 4 ppm

2 Fuel Nickel Content 3.2 ppm

3 Fuel Nickel Content 2.8 ppm

1 Fuel Arsenic Content 0.97 ppm

2 Fuel Arsenic Content 0.85 ppm

3 Fuel Arsenic Content 0.63 ppm

1 Fuel Chromium Content 3.3 ppm

2 Fuel Chromium Content 3.8 ppm

3 Fuel Chromium Content 2.9 ppm

1 Fuel Beryllium Content 0.25 ppm

2 Fuel Beryllium Content 0.24 ppm

3 Fuel Beryllium Content 0.24 ppm

1 Fuel Lead Content 2.2 ppm

2 Fuel Lead Content 2.3 ppm

3 Fuel Lead Content 1.8 ppm

Monday, February 07, 2011 Page 11 of 14
7/30/2010

1 Fuel Manganese Content 7.7 ppm

2 Fuel Manganese Content 6.8 ppm

3 Fuel Manganese Content 5.8 ppm

1 Fuel Chlorine Content 30 ppm

2 Fuel Chlorine Content 33 ppm

3 Fuel Chlorine Content 36 ppm

1 Fuel Fluorine Content 58 ppm

2 Fuel Fluorine Content 60 ppm

3 Fuel Fluorine Content 65 ppm

Monday, February 07, 2011 Page 12 of 14
7/30/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 6/30/2010 7/1/2010 7/2/2010

Run Start Time 10:22:00 AM 8:00:00 AM 8:30:00 AM

Run Finish Time 2:40:00 PM 1:03:00 PM 12:50:00 PM

Net Traversing Points 52 52 52

Net Run Time, minutes 240 235 240

Nozzle Diameter, inches 0.274 0.274 0.274 0.274

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.013 1.013 1.013 1.013

Barometric Pressure, inches of Mercury 29.47 29.56 29.44 29.490

Average Orifice Meter Differential, inches H2O 1.83 1.79 1.78 1.800

Dry Gas Meter Volume Sampled, cubic feet 199.442 192.789 195.123 195.785

Average Dry Gas Meter Temperature, °F 80.41 82.63 81.13 81.390

Dry Gas Meter Volume Sampled, dscf 195.314 188.579 190.613 191.502

Total Moisture Liquid collected, g 504.4 489.5 475.2 489.700

Volume of Water Vapor, standard cubic feet 23.74 23.04 22.37 23.050

Moisture Content of Stack Gas, % 10.84 10.89 10.50 10.743

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

Dry Mole Fraction 0.8916 0.8911 0.895 0.893

Carbon Dioxide, % 12.7 12.7 12.7 12.700

Oxygen, % 7.1 7.1 7.1 7.100

Carbon Monoxide & Nitrogen, % 80.2 80.2 80.2 80.200

Fuel Factor 1.09 1.09 1.09

Dry Molecular Weight, lb/lb-Mole 30.32 30.32 30.32 30.320

Wet Molecular weight, lb/lb-Mole 28.98 28.98 29.03 28.997

Flue Gas Static Pressure, inches of H2O 4 4.2 4.25 4.150

Absolute Flue Gas Pressure, inches of Mercury 29.76 29.87 29.75 29.793

Average Stack Gas Temperature, °F 275.92 276.87 279.69 277.493

Average Velocity Head, inches of H2O 0.5643294211

44286

0.554087842

841653

0.552773757

129851

0.557

Average Stack Gas Velocity, feet/second 49.83 49.32 49.41 49.520

Stack Cross-Sectional Area, square feet 346.361 346.361 346.361 346.361

Dry Volumetric Flow Rate, dry scfm 658,894.4 653,350.8 652,270.4 654,838.533

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,035,550.1 1,024,951.5 1,026,821.8 1,029,107.8

00

Percent Isokinetic of Sampling Rate, % 104.5 103.9 103.0 103.800

Percent Excess Air, % 50.5 50.5 50.5 50.500

F-Factor, dscfm/MMBtu @ %O2 9820 9820 9820 9,820.000

Round Duct Diameter, inches 252 252 252

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Monday, February 07, 2011 Page 13 of 14
7/30/2010

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

Monday, February 07, 2011 Page 14 of 14