Name: Terry P. Jensky

Title: Vice President - Energy Supply Operat

Company: Wisconsin Public Service

Sign Date: 9/1/2010

Name: Kevin O'Halloren

Title: Project Manager

Company: Clean Air Engineering

Sign Date: 9/1/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Weston 3

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 15
Weston 3

9/1/2010

Facility Information:

Weston

2501 Morrison Avenue

Rothschild WI 54474

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 60067-4975

Contact: Kevin Ohalloren

Phone: 800-627-0033 ext 4661

Fax: 847-991-0036

Email: kohalloren@cleanair.com

Air Permit Number:

4078

Permitted Source ID/Name:

737009020 Weston 3

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:

Weston unit 3 is a drum style, pulverized coal fired boiler equipped with low Nox burners and separated overfired air 

for NOx control, powder activated carbon injection system for mercury control, and a fabric filter baghouse for 

particulate control

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: Enter ARS ID FRS #: Enter FRS ID

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 192 0 0 0 1536 384 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 15
Weston 3

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 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

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 15
Weston 3

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.

No modifications or deviations.

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

Friday, February 25, 2011 Page 4 of 15
Weston 3

9/1/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 29

Average

Run Number M5 and 29-1 M5 and 29-

2

M5 and 29-3

Test Date 5/4/2010 5/5/2010 5/6/2010

Run Start Time 1:03:00 PM 8:00:00 

AM

7:52:00 AM

Run Finish Time 5:24:00 PM 12:09:00 

PM

12:08:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 174.846 166.452 172.660 171.319

Moisture Content of Stack Gas, % 11.25 11.28 11.37 11.300

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

Carbon Dioxide, % 13.825 14.025 14.1 13.983

Oxygen, % 5.275 5.175 5.1 5.183

Average Stack Gas Temperature, °F 324.94 312.38 308.92 315.413

Dry Volumetric Flow Rate, dry scfm 769,707.3 784,574.1 743,450.7 765,910.700

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,374,781.5 1,384,311.9 1,300,227.7 1,353,107.03

3

Percent Isokinetic of Sampling Rate, % 98.7 92.2 100.9 97.267

F-Factor, dscfm/MMBtu @ %O2 9555 9606 9570 9,577.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 25, 2011 Page 5 of 15
Weston 3

9/1/2010

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

Friday, February 25, 2011 Page 6 of 15
Weston 3

9/1/2010

Emissions Summary

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 0.001076 0.000611 0.000589 0.001

Elb/hr 6.27E-04 3.81E-04 3.35E-04 0.000

lb/mmBtuO2 1.73E-07 1.03E-07 9.52E-08 0.000

mg/dscm 2.17E-04 1.30E-04 1.20E-04 0.000

mg/dscm@7%O2 1.93E-04 1.15E-04 1.06E-04 0.000

Compound: Arsenic

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 0.00275 0.00253 0.002487 0.003

Elb/hr 1.60E-03 1.58E-03 1.42E-03 0.002

lb/mmBtuO2 4.43E-07 4.28E-07 4.02E-07 0.000

mg/dscm 5.56E-04 5.37E-04 5.09E-04 0.001

mg/dscm@7%O2 4.95E-04 4.75E-04 4.48E-04 0.000

Compound: Beryllium

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 0.0003 0.000305 0.0003 0.000

Elb/hr 1.75E-04 1.90E-04 1.71E-04 0.000

lb/mmBtuO2 4.83E-08 5.16E-08 4.85E-08 0.000

mg/dscm 6.06E-05 6.47E-05 6.14E-05 0.000

mg/dscm@7%O2 5.39E-05 5.72E-05 5.40E-05 0.000

Compound: Cadmium

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 0.000202 0.000217 0.000243 0.000

Elb/hr 1.18E-04 1.35E-04 1.38E-04 0.000

lb/mmBtuO2 3.26E-08 3.67E-08 3.93E-08 0.000

mg/dscm 4.08E-05 4.60E-05 4.97E-05 0.000

mg/dscm@7%O2 3.63E-05 4.07E-05 4.37E-05 0.000

Compound: Chromium

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 0.00218 0.00314 0.16115 0.055

Elb/hr 1.27E-03 1.96E-03 9.18E-02 0.032

lb/mmBtuO2 3.51E-07 5.31E-07 2.60E-05 0.000

mg/dscm 4.40E-04 6.66E-04 3.30E-02 0.011

mg/dscm@7%O2 3.91E-04 5.89E-04 2.90E-02 0.010

Compound: Cobalt

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 0.000768 0.00117 0.00278 0.002

Elb/hr 4.47E-04 7.29E-04 1.58E-03 0.001

Friday, February 25, 2011 Page 7 of 15
Weston 3

9/1/2010

lb/mmBtuO2 1.24E-07 1.98E-07 4.49E-07 0.000

mg/dscm 1.55E-04 2.48E-04 5.69E-04 0.000

mg/dscm@7%O2 1.38E-04 2.19E-04 5.01E-04 0.000

Compound: Filterable Particulate

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 12.8 22.33 21.5 18.877

Elb/hr 7.45E+00 1.39E+01 1.22E+01 11.183

lb/mmBtuO2 2.06E-03 3.78E-03 3.48E-03 0.003

mg/dscm 2.59E+00 4.74E+00 4.40E+00 3.910

mg/dscm@7%O2 2.30E+00 4.19E+00 3.87E+00 3.453

Compound: Lead

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 0.00339 0.004405 0.004104 0.004

Elb/hr 1.97E-03 2.75E-03 2.34E-03 0.002

lb/mmBtuO2 5.46E-07 7.45E-07 6.63E-07 0.000

mg/dscm 6.85E-04 9.35E-04 8.40E-04 0.001

mg/dscm@7%O2 6.09E-04 8.26E-04 7.39E-04 0.001

Compound: Manganese

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 0.004549 0.009359 0.024519 0.013

Elb/hr 2.65E-03 5.84E-03 1.40E-02 0.007

lb/mmBtuO2 7.33E-07 1.58E-06 3.96E-06 0.000

mg/dscm 9.19E-04 1.99E-03 5.02E-03 0.003

mg/dscm@7%O2 8.18E-04 1.76E-03 4.42E-03 0.002

Compound: Nickel

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 0.002252 0.003292 0.066832 0.024

Elb/hr 1.31E-03 2.05E-03 3.81E-02 0.014

lb/mmBtuO2 3.63E-07 5.57E-07 1.08E-05 0.000

mg/dscm 4.55E-04 6.99E-04 1.37E-02 0.005

mg/dscm@7%O2 4.05E-04 6.18E-04 1.21E-02 0.004

Compound: Selenium

Average

RunNumber M5 and 29-1 M5 and 29-2 M5 and 29-3

Mass_mg 0.022 0.0139 0.0136 0.017

Elb/hr 1.28E-02 8.67E-03 7.75E-03 0.010

lb/mmBtuO2 3.55E-06 2.35E-06 2.20E-06 0.000

mg/dscm 4.44E-03 2.95E-03 2.78E-03 0.003

mg/dscm@7%O2 3.95E-03 2.61E-03 2.45E-03 0.003

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

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

Friday, February 25, 2011 Page 8 of 15
Weston 3

9/1/2010

Process Run Data

Mass_mg 31.96 25.77 32.14 29.957

lb/mmBtuO2 1.72E-02 6.10E-03 7.24E-03 0.010

Compound: Filterable PM2.5

Average

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

Mass_mg 2.93 2.89 2.94 2.920

lb/mmBtuO2 1.57E-03 6.84E-04 6.62E-04 0.001

Compound: Inorganic (Aqueous) Condensible Pa

Average

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

Mass_mg 37.8 9.02 11.65 19.490

lb/mmBtuO2 2.03E-02 2.14E-03 2.62E-03 0.008

Compound: Organic Condensible Particulate

Average

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

Mass_mg 0.64 0.67 0.78 0.697

lb/mmBtuO2 3.43E-04 1.59E-04 1.76E-04 0.000

Compound: Total Particulate

Average

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

Mass_mg 70.4 35.46 44.58 50.147

lb/mmBtuO2 3.78E-02 8.40E-03 1.00E-02 0.019

Compound: Total PM2.5

Average

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

Mass_mg 41.37 12.58 15.38 23.110

lb/mmBtuO2 2.22E-02 2.98E-03 3.46E-03 0.010

Friday, February 25, 2011 Page 9 of 15
Weston 3

9/1/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Burned 160 Tons/hr Run 1 data for 

Method 5/29 and 

OTM 27/28 Run 1

160

1 Average Heat Input 2803 MMBtu/hr Run 1 data for 

Method 5/29 and 

OTM 27/28 Run 1

2900

1 Steam Output 2101 1000 lb steam/hr Run 1 data for 

Method 5/29 and 

OTM 27/28 Run 1

2150

1 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

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

1 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 Carbon 23 lb/hr Run 1 data for 

Method 5/29 and 

OTM 27/28 Run 1

20

1 Flue Gas Oxygen Content 2.9 % Run 1 data for 

Method 5/29 and 

OTM 27/28 Run 1

2.7

1 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 307 Mwe Run 1 data for 

Method 5/29 and 

OTM 27/28 Run 1

315

1 Unit Net Electric Generation 279 MWh Run 1 data for 

Method 5/29 and 

OTM 27/28 Run 1

290

1 Baghouse Pressure Drop 6.89 in. H2O 6.89 side A; 6.58 

side B

6.8

4 Coal Burned 166 Tons/hr Run 2 data for 

Method 5/29 and 

OTM 27/28

160

Friday, February 25, 2011 Page 10 of 15
Weston 3

9/1/2010

4 Average Heat Input 2905 MMBtu/hr Run 2 data for 

Method 5/29 and 

OTM 27/28

2900

4 Steam Output 2158 1000 lb steam/hr Run 2 data for 

Method 5/29 and 

OTM 27/28

2150

4 Synfuel Firing Rate 0 1000 Tons/hr 0

4 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

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

4 Fuel Oil Firing Rate 0 gal/hr 0

4 Flue Gas Flow Rate 0 0

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

4 FGD Scrubber Liquor pH 0 pH 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 Sorbent Type and Sorbent Injection Rate Carbon 23 lb/hr Run 2 data for 

Method 5/29 and 

OTM 27/28

20

4 Flue Gas Oxygen Content 2.7 % Run 2 data for 

Method 5/29 and 

OTM 27/28

2.7

4 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

4 Flue Gas Sampling Point Temperature 0 Deg F 0

4 Flue Gas Pressure 0 atm 0

4 Standard Pressure 0 atm 0

4 Standard Temperature 0 Deg F 0

4 Unit Gross Electrical Output 319 Mwe Run 2 data for 

Method 5/29 and 

OTM 27/28

315

4 Unit Net Electric Generation 290 MWh Run 2 data for 

Method 5/29 and 

OTM 27/28

290

4 Baghouse Pressure Drop 6.52 in. H2O 6.52 for Side A; 

6.7 for Side B

6.8

5 Coal Burned 174 Tons/hr Run 3 data for 

Method 5/29 and 

OTM 27/28

160

5 Average Heat Input 3039 MMBtu/hr Run 3 data for 

Method 5/29 and 

OTM 27/28

2900

5 Steam Output 2352 1000 lb steam/hr Run 3 data for 

Method 5/29 and 

OTM 27/28

2150

Friday, February 25, 2011 Page 11 of 15
Weston 3

9/1/2010

APCD Run Data

Process Lab Run Data

5 Synfuel Firing Rate 0 1000 Tons/hr 0

5 Petroleum Coke Firing Rate 0 1000 Tons/hr 0

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

5 Fuel Oil Firing Rate 0 gal/hr 0

5 Flue Gas Flow Rate 0 0

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

5 FGD Scrubber Liquor pH 0 pH 0

5 FGD Scrubber Liquor Flow Rate 0 gal/min 0

5 Sorbent Type and Sorbent Injection Rate Carbon 23 lb/hr Run 3 data for 

Method 5/29 and 

OTM 27/28

20

5 Flue Gas Oxygen Content 2.6 % Run 3 data for 

Method 5/29 and 

OTM 27/28

2.7

5 Flue Gas Carbon Dioxide Content 0 % 0

5 Flue Gas Moisture Content 0 % 0

5 Flue Gas Sampling Point Temperature 0 Deg F 0

5 Flue Gas Pressure 0 atm 0

5 Standard Pressure 0 atm 0

5 Standard Temperature 0 Deg F 0

5 Unit Gross Electrical Output 335 Mwe Run 3 data for 

Method 5/29 and 

OTM 27/28

315

5 Unit Net Electric Generation 305 MWh Run 3 data for 

Method 5/29 and 

OTM 27/28

290

5 Baghouse Pressure Drop 7.2 in. H2O 7.2 Side A; 6.9 

Side B

6.8

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 OVERFIRE AIR 0 lb/mmbtu 0.12

1 ACTIVATED CARBON ADSORPTION 0 0

1 BAGHOUSE 0

1 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 9555 Btu/lb

Friday, February 25, 2011 Page 12 of 15
Weston 3

9/1/2010 1 9555 Btu/lb

1 Fuel Moisture 18.85 %

1 Fuel Mercury Content 0.086 ppm

1 Fuel Cadmium Content 0.051 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 5.62 ppm

1 Fuel Arsenic Content 1.75 ppm

1 Fuel Chromium Content 4.43 ppm

1 Fuel Beryllium Content 0.266 ppm

1 Fuel Lead Content 2.33 ppm

1 Fuel Manganese Content 12.2 ppm

1 Fuel Chlorine Content 18 ppm

1 Fuel Fluorine Content 0 ppm

2 Fuel Higher Heating Value 9606 Btu/lb

2 Fuel Moisture 24.15 %

2 Fuel Mercury Content 0.077 ppm

2 Fuel Cadmium Content 0.158 ppm

2 Ultimate/Proximate Analysis 0

2 Fuel Nickel Content 15.4 ppm

2 Fuel Arsenic Content 6.31 ppm

2 Fuel Chromium Content 8.54 ppm

2 Fuel Beryllium Content 1.06 ppm

2 Fuel Lead Content 4.65 ppm

2 Fuel Manganese Content 52.5 ppm

2 Fuel Chlorine Content 34 ppm

2 Fuel Fluorine Content 0 ppm

3 Fuel Higher Heating Value 9570 Btu/lb

3 Fuel Moisture 24.01 %

3 Fuel Mercury Content 0.063 ppm

3 Fuel Cadmium Content 0.083 ppm

3 Ultimate/Proximate Analysis 0

3 Fuel Nickel Content 8.07 ppm

3 Fuel Arsenic Content 1.48 ppm

3 Fuel Chromium Content 4.26 ppm

3 Fuel Beryllium Content 0.421 ppm

3 Fuel Lead Content 2.2 ppm

3 Fuel Manganese Content 18.7 ppm

3 Fuel Chlorine Content 34 ppm

3 Fuel Fluorine Content 0 ppm

Friday, February 25, 2011 Page 13 of 15
Weston 3

9/1/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 29

Average

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

Test Date 5/4/2010 5/5/2010 5/6/2010

Run Start Time 1:03:00 PM 8:00:00 AM 7:52:00 AM

Run Finish Time 5:24:00 PM 12:09:00 PM 12:08:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.188 0.188 0.188 0.188

Pitot Tube Coefficient 0.816 0.816 0.816 0.816

Dry Gas Meter Calibration Factor 0.9904165410

65016

0.990416541

065016

0.990416541

065016

0.990

Barometric Pressure, inches of Mercury 28.25 28.15 28.3 28.233

Average Orifice Meter Differential, inches H2O 1.95 1.75 1.85 1.850

Dry Gas Meter Volume Sampled, cubic feet 196.145 184.280 187.840 189.422

Average Dry Gas Meter Temperature, °F 96.71 87.19 80.70 88.200

Dry Gas Meter Volume Sampled, dscf 174.846 166.452 172.660 171.319

Total Moisture Liquid collected, g 471 449.8 470.8 463.867

Volume of Water Vapor, standard cubic feet 22.17 21.17 22.16 21.833

Moisture Content of Stack Gas, % 11.25 11.28 11.37 11.300

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

Dry Mole Fraction 0.8875 0.8872 0.8863 0.887

Carbon Dioxide, % 13.825 14.025 14.1 13.983

Oxygen, % 5.275 5.175 5.1 5.183

Carbon Monoxide & Nitrogen, % 80.9 80.8 80.8 80.833

Fuel Factor 1.13 1.12 1.12

Dry Molecular Weight, lb/lb-Mole 30.42 30.45 30.46 30.443

Wet Molecular weight, lb/lb-Mole 29.02 29.05 29.04 29.037

Flue Gas Static Pressure, inches of H2O -2.6 -2.6 -2.6 -2.600

Absolute Flue Gas Pressure, inches of Mercury 28.06 27.96 28.11 28.043

Average Stack Gas Temperature, °F 324.94 312.38 308.92 315.413

Average Velocity Head, inches of H2O 2.7685109141

6722

2.845290288

7998

2.534127628

0389

2.716

Average Stack Gas Velocity, feet/second 113.96 114.75 107.78 112.163

Stack Cross-Sectional Area, square feet 201.062 201.062 201.062 201.062

Dry Volumetric Flow Rate, dry scfm 769,707.3 784,574.1 743,450.7 765,910.700

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,374,781.5 1,384,311.9 1,300,227.7 1,353,107.0

33

Percent Isokinetic of Sampling Rate, % 98.7 92.2 100.9 97.267

Percent Excess Air, % 32.8 32.0 31.4 32.067

F-Factor, dscfm/MMBtu @ %O2 9555 9606 9570 9,577.000

Round Duct Diameter, inches 192 192 192

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 14 of 15
Weston 3

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 15 of 15