Name: Robert A. Greco

Title: Manager Air Quality

Company: We Energies

Sign Date: 6/30/2010

Name: Scott W. Banach

Title: Director, Project Engineering

Company: Platt Environmental Services, Inc.

Sign Date: 6/30/2010

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
6/30/2010

Facility Information:

Valley (ORIS Facility ID #4042)

1035 West Canal Street

Milwaukee WI 53233

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:

4042

Permitted Source ID/Name:

2 Valley

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 Valley Power Plant Boilers 1, 2, 3, and 4 are Riley Stoker, dry bottom, wall-fired, pulverized coal-fired boilers 

which currently fire western bituminous coals. These units are also permitted to fire natural gas and propane for unit 

startup, flame stabilization, and supplemental firing. In 1994, low Nox burners were installed on all four boilers, and 

the original electrostatic precipitators on all four boilers were replaced with high efficiency fabric filter baghouses.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 5507900191 FRS #: 20847

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 0 114 152 130.3 107 474 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

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

Monday, February 07, 2011 Page 2 of 14
6/30/2010

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

Organic Condensible 

Particulate

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable PM2.5 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

Monday, February 07, 2011 Page 3 of 14
6/30/2010

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.

Inorganic (Aqueous) 

Condensible Part.

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

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Co2 Method 3A CO2 3 240 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit O2 Method 3A O2 3 120 0

Organic Condensible 

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

Total 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
6/30/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 29 

Average

Run Number M29-1 M29-2 M29-3

Test Date 3/30/2010 3/31/2010 4/1/2010

Run Start Time 9:35:00 AM 8:00:00 

AM

8:10:00 AM

Run Finish Time 1:47:00 PM 12:06:00 

PM

12:22:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 128.182 138.086 142.154 136.141

Moisture Content of Stack Gas, % 9.99 7.46 7.89 8.447

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

Carbon Dioxide, % 12.8 12.8 12.9 12.833

Oxygen, % 6 6 6.2 6.067

Average Stack Gas Temperature, °F 286.75 286.90 287.45 287.033

Dry Volumetric Flow Rate, dry scfm 170,472.3 182,694.6 185,381.1 179,516.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 288,077.2 300,351.2 306,416.0 298,281.467

Percent Isokinetic of Sampling Rate, % 102.3 102.8 104.3 103.133

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Monday, February 07, 2011 Page 5 of 14
6/30/2010

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
6/30/2010

Emissions Summary

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0048 0.0048 0.0048 0.005

Elb/hr 8.44E-04 8.40E-04 8.28E-04 0.001

lb/mmBtuO2 1.13E-06 1.05E-06 1.04E-06 0.000

mg/dscm 1.32E-03 1.23E-03 1.19E-03 0.001

mg/dscm@7%O2 1.23E-03 1.15E-03 1.13E-03 0.001

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0048 0.0048 0.0048 0.005

Elb/hr 8.44E-04 8.40E-04 8.28E-04 0.001

lb/mmBtuO2 1.13E-06 1.05E-06 1.04E-06 0.000

mg/dscm 1.32E-03 1.23E-03 1.19E-03 0.001

mg/dscm@7%O2 1.23E-03 1.15E-03 1.13E-03 0.001

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0012 0.0012 0.0012 0.001

Elb/hr 2.11E-04 2.10E-04 2.07E-04 0.000

lb/mmBtuO2 2.83E-07 2.63E-07 2.59E-07 0.000

mg/dscm 3.31E-04 3.07E-04 2.98E-04 0.000

mg/dscm@7%O2 3.09E-04 2.86E-04 2.82E-04 0.000

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.002 0.004 0.0014 0.002

Elb/hr 3.52E-04 7.00E-04 2.42E-04 0.000

lb/mmBtuO2 4.72E-07 8.76E-07 3.02E-07 0.000

mg/dscm 5.51E-04 1.02E-03 3.48E-04 0.001

mg/dscm@7%O2 5.14E-04 9.52E-04 3.29E-04 0.001

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.51021 0.56921 0.94935 0.676

Elb/hr 8.98E-02 9.96E-02 1.64E-01 0.118

lb/mmBtuO2 1.20E-04 1.25E-04 2.05E-04 0.000

mg/dscm 1.41E-01 1.46E-01 2.36E-01 0.174

mg/dscm@7%O2 1.32E-01 1.36E-01 2.23E-01 0.164

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00653 0.00804 0.0112 0.009

Elb/hr 1.15E-03 1.41E-03 1.93E-03 0.001

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

lb/mmBtuO2 1.54E-06 1.76E-06 2.42E-06 0.000

mg/dscm 1.80E-03 2.06E-03 2.78E-03 0.002

mg/dscm@7%O2 1.68E-03 1.92E-03 2.63E-03 0.002

Compound: Filterable Particulate

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 6.2 14 6.8 9.000

Elb/hr 1.09E+00 2.45E+00 1.17E+00 1.570

lb/mmBtuO2 1.46E-03 3.07E-03 1.47E-03 0.002

mg/dscm 1.71E+00 3.58E+00 1.69E+00 2.327

mg/dscm@7%O2 1.60E+00 3.34E+00 1.60E+00 2.180

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.01301 0.01004 0.00757 0.010

Elb/hr 2.29E-03 1.76E-03 1.31E-03 0.002

lb/mmBtuO2 3.07E-06 2.20E-06 1.63E-06 0.000

mg/dscm 3.58E-03 2.57E-03 1.88E-03 0.003

mg/dscm@7%O2 3.34E-03 2.40E-03 1.78E-03 0.003

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.1076 0.1131 0.0929 0.105

Elb/hr 1.89E-02 1.98E-02 1.60E-02 0.018

lb/mmBtuO2 2.54E-05 2.48E-05 2.00E-05 0.000

mg/dscm 2.96E-02 2.89E-02 2.31E-02 0.027

mg/dscm@7%O2 2.76E-02 2.70E-02 2.18E-02 0.025

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.564 0.653 0.5628 0.593

Elb/hr 9.92E-02 1.14E-01 9.71E-02 0.103

lb/mmBtuO2 1.33E-04 1.43E-04 1.21E-04 0.000

mg/dscm 1.55E-01 1.67E-01 1.40E-01 0.154

mg/dscm@7%O2 1.45E-01 1.56E-01 1.32E-01 0.144

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.012 0.012 0.012 0.012

Elb/hr 2.11E-03 2.10E-03 2.07E-03 0.002

lb/mmBtuO2 2.83E-06 2.63E-06 2.59E-06 0.000

mg/dscm 3.31E-03 3.07E-03 2.98E-03 0.003

mg/dscm@7%O2 3.09E-03 2.86E-03 2.82E-03 0.003

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
6/30/2010

Process Run Data

Mass_mg 58.8 111.2 12 60.667

lb/mmBtuO2 1.39E-02 2.72E-02 2.84E-03 0.015

Compound: Filterable PM2.5

Average

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

Mass_mg 13.8 9.4 4.4 9.200

lb/mmBtuO2 3.26E-03 2.30E-03 1.04E-03 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

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

Mass_mg 69.9 33 48.9 50.600

lb/mmBtuO2 1.65E-02 8.08E-03 1.16E-02 0.012

Compound: Organic Condensible Particulate

Average

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

Mass_mg 1.6 2.5 0.6 1.567

lb/mmBtuO2 3.78E-04 6.12E-04 1.42E-04 0.000

Compound: Total Particulate

Average

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

Mass_mg 130.3 146.7 61.5 112.833

lb/mmBtuO2 3.08E-02 3.59E-02 1.45E-02 0.027

Compound: Total PM2.5

Average

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

Mass_mg 85.3 44.9 53.9 61.367

lb/mmBtuO2 2.01E-02 1.10E-02 1.27E-02 0.015

Monday, February 07, 2011 Page 9 of 14
6/30/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 0.0354 1000 ton/hr 0

2 Bituminous Coal Burned 0.0353 1000 ton/hr 0

3 Bituminous Coal Burned 0.037 1000 ton/hr 0

1 Average Heat Input 721.4 MMBtu/hr 0

2 Average Heat Input 747 MMBtu/hr 0

3 Average Heat Input 793.3 MMBtu/hr 0

1 Steam Output 593.5 1000 lb steam/hr 0

2 Steam Output 597.33 1000 lb steam/hr 0

3 Steam Output 606.5 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 6.2 % 0

1 Flue Gas Carbon Dioxide Content 12.8 % 0

1 Flue Gas Moisture Content 10.1 % 0

1 Flue Gas Sampling Point Temperature 290.2 Deg F 0

1 Flue Gas Pressure 0.94 atm 0

1 Standard Pressure 1 atm 0

1 Standard Temperature 63.33 Deg F 0

Monday, February 07, 2011 Page 10 of 14
6/30/2010

APCD Run Data

Process Lab Run Data

1 Unit Gross Electrical Output 63 Mwe 0

1 Unit Net Electric Generation 57.333 MWh 0

Run Name Value UOM Comments

Target

Value

1 BAGHOUSE 2.6 in H2O 0.25

2 BAGHOUSE 2.683 in H2O 0.25

3 BAGHOUSE 2.6 in H2O 0.25

Run Name Value UOM Comments

1 Fuel Higher Heating Value 12964 Btu/lb

1 Fuel Moisture 3.45 %

1 Fuel Mercury Content 0.023 ppm

1 Fuel Cadmium Content 0.13 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 8.9 ppm

1 Fuel Arsenic Content 0.93 ppm

1 Fuel Chromium Content 5.6 ppm

1 Fuel Beryllium Content 0.56 ppm

1 Fuel Lead Content 5 ppm

1 Fuel Manganese Content 24 ppm

1 Fuel Chlorine Content 270 ppm

1 Fuel Fluorine Content 69 ppm

2 Fuel Higher Heating Value 12854 Btu/lb

2 Fuel Moisture 4.09 %

2 Fuel Mercury Content 0.024 ppm

2 Fuel Cadmium Content 0.13 ppm

2 Ultimate/Proximate Analysis 0

2 Fuel Nickel Content 4.5 ppm

2 Fuel Arsenic Content 1 ppm

2 Fuel Chromium Content 4.1 ppm

2 Fuel Beryllium Content 0.56 ppm

2 Fuel Lead Content 4.7 ppm

2 Fuel Manganese Content 14 ppm

2 Fuel Chlorine Content 220 ppm

2 Fuel Fluorine Content 74 ppm

3 Fuel Higher Heating Value 13001 Btu/lb

3 Fuel Moisture 4.2 %

3 Fuel Mercury Content 0.021 ppm

3 Fuel Cadmium Content 0.12 ppm

Monday, February 07, 2011 Page 11 of 14
6/30/2010

3 Ultimate/Proximate Analysis 0

3 Fuel Nickel Content 4.8 ppm

3 Fuel Arsenic Content 0.66 ppm

3 Fuel Chromium Content 4.2 ppm

3 Fuel Beryllium Content 0.61 ppm

3 Fuel Lead Content 4.9 ppm

3 Fuel Manganese Content 15 ppm

3 Fuel Chlorine Content 190 ppm

3 Fuel Fluorine Content 73 ppm

Monday, February 07, 2011 Page 12 of 14
6/30/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 29 

Average

Run Number M29-1 M29-2 M29-3

Test Date 3/30/2010 3/31/2010 4/1/2010

Run Start Time 9:35:00 AM 8:00:00 AM 8:10:00 AM

Run Finish Time 1:47:00 PM 12:06:00 PM 12:22:00 PM

Net Traversing Points 48 48 47

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.26 0.26 0.26 0.260

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1 1 1 1.000

Barometric Pressure, inches of Mercury 29 29 29 29.000

Average Orifice Meter Differential, inches H2O 0.83 0.94 1.02 0.930

Dry Gas Meter Volume Sampled, cubic feet 135.207 147.490 152.430 145.042

Average Dry Gas Meter Temperature, °F 80.95 87.92 90.18 86.350

Dry Gas Meter Volume Sampled, dscf 128.182 138.086 142.154 136.141

Total Moisture Liquid collected, g 302.2 236.5 258.6 265.767

Volume of Water Vapor, standard cubic feet 14.22 11.13 12.17 12.507

Moisture Content of Stack Gas, % 9.99 7.46 7.89 8.447

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

Dry Mole Fraction 0.9001 0.9254 0.9211 0.916

Carbon Dioxide, % 12.8 12.8 12.9 12.833

Oxygen, % 6 6 6.2 6.067

Carbon Monoxide & Nitrogen, % 81.2 81.2 80.9 81.100

Fuel Factor 1.16 1.16 1.14

Dry Molecular Weight, lb/lb-Mole 30.29 30.29 30.31 30.297

Wet Molecular weight, lb/lb-Mole 29.06 29.37 29.34 29.257

Flue Gas Static Pressure, inches of H2O -16 -16 -16 -16.000

Absolute Flue Gas Pressure, inches of Mercury 27.82 27.82 27.82 27.820

Average Stack Gas Temperature, °F 286.75 286.90 287.45 287.033

Average Velocity Head, inches of H2O 0.3342445571

6156

0.367173520

177482

0.381456270

331929

0.361

Average Stack Gas Velocity, feet/second 39.90 41.60 42.44 41.313

Stack Cross-Sectional Area, square feet 120.333 120.333 120.333 120.333

Dry Volumetric Flow Rate, dry scfm 170,472.3 182,694.6 185,381.1 179,516.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 288,077.2 300,351.2 306,416.0 298,281.467

Percent Isokinetic of Sampling Rate, % 102.3 102.8 104.3 103.133

Percent Excess Air, % 38.9 38.9 40.9 39.567

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 152 152 152

Rectangular Duct Length, inches 114 114 114

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Monday, February 07, 2011 Page 13 of 14
6/30/2010

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