Name: John Oelbracht

Title: Plant Manager

Company: WPS Westwood Generation, LLC.

Sign Date: 9/3/2010

Name: Michael T. Karter

Title: General Manager

Company: Empire Stack Testing, LLC

Sign Date: 8/31/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Westwood

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 18, 2011 Page 1 of 15
Westwood

9/3/2010

Facility Information:

Westwood

45 Westwood Road

Tremont PA 17981

Contact: Mark Metcalf

Phone: 920-433-1833

Fax:

Email: mwmetcalf@integrysgroup.com

Testing Company:

Empire Stack Testing, LLC

5252 Ramsey Road

Ashville NY 14710

Contact:Michael Karter

Phone: Of above person

Fax: Of above person

Email: Of above person

Air Permit Number:

50611

Permitted Source ID/Name:

031 Westwood

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 WPS Westwood Generation Station (WPS), located in Tremont, Pennsylvania, began operation in 1987 and 

consists of a circulating fluidized bed (CFB) boiler whose steam is used to produce electricity for sale to the grid. 

The boiler combusts waste anthracite coal (culm), which is high in ash content, low in volatiles and sulfur content. 

The boiler also combusts No. 2 fuel oil on a limited basis, used mainly during startups and shutdowns. The boiler has 

emission controls for particulate matter (PM) and SO2. Particulate emissions are controlled with a bag house. SO2 

emissions are controlled by introducing limestone (CaCO3) in with the fuel. Limestone reacts to remove SO2 as 

solid calcium sulfate.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

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

SCC / Description 10100101 External Combustion Boilers - Electric Generation - Anthracite Coal - Pulverized 

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 147 0 0 0 294 735 3 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

Friday, February 18, 2011 Page 2 of 15
Westwood

9/3/2010

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

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

Total PM2.5 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

Friday, February 18, 2011 Page 3 of 15
Westwood

9/3/2010

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.

Organic Condensible 

Particulate

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

Total 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

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Beryllium 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 O2 Method 3A O2 3 120 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit O2 Method 3A O2 3 480 0

Filterable 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

Organic Condensible 

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 18, 2011 Page 4 of 15
Westwood

9/3/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 6/8/2010 6/8/2010 6/8/2010

Run Start Time 12:05:00 PM 2:25:00 PM 4:46:00 PM

Run Finish Time 2:05:00 PM 4:25:00 PM 6:46:00 PM

Carbon Dioxide, % 11.9 12 12.1 12.000

Oxygen, % 8.7 8.6 8.5 8.600

Dry Volumetric Flow Rate, dry scfm 124919 122980 122465 123,454.667

F-Factor, dscfm/MMBtu @ %O2 11965 13481 12137 12,527.667

Moisture, % 5.8 5.5 6.1 5.800

Fuel Type Override Override Override

Fw 0 0 0.000

Fc 0 0 1420 473.333

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 18, 2011 Page 5 of 15
Westwood

9/3/2010

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

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

Friday, February 18, 2011 Page 6 of 15
Westwood

9/3/2010

Emissions Summary

Process Run Data

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 1.39E+01 1.37E+01 1.38E+01 13.800

gr/dscf 1.30E-02 1.30E-02 1.32E-02 0.013

lb/mmBtuO2 3.80E-02 4.27E-02 3.85E-02 0.040

mg/dscm 2.97E+01 2.98E+01 3.01E+01 29.867

ppm 2.55E+01 2.56E+01 2.59E+01 25.667

ppm@7%O2 2.91E+01 2.89E+01 2.90E+01 29.000

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 5.41E-01 4.78E-01 4.15E-01 0.478

gr/dscf 5.05E-04 4.54E-04 3.96E-04 0.000

lb/mmBtuO2 1.48E-03 1.48E-03 1.16E-03 0.001

mg/dscm 1.16E+00 1.04E+00 9.05E-01 1.035

ppm 6.31E-01 5.66E-01 4.94E-01 0.564

ppm@7%O2 7.19E-01 6.40E-01 5.54E-01 0.638

Friday, February 18, 2011 Page 7 of 15
Westwood

9/3/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Burned 49 Tons/hr 49

2 Coal Burned 49 Tons/hr 49

3 Coal Burned 49 Tons/hr 49

1 Average Heat Input 444 MMBtu/hr 444

2 Average Heat Input 444 MMBtu/hr 444

3 Average Heat Input 444 MMBtu/hr 444

1 Steam Output 297 1000 lb steam/hr 297

2 Steam Output 297 1000 lb steam/hr 297

3 Steam Output 297 1000 lb steam/hr 297

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 140887 dscfm 140887

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 0 lb/hr

1 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 12.3

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

Friday, February 18, 2011 Page 8 of 15
Westwood

9/3/2010

1 Unit Gross Electrical Output 793 Mwe 793

1 Unit Net Electric Generation 706 MWh 706

1 Baghouse Pressure Drop 0 in. H2O 0

1 Flue Gas Temperature 322 degree F 322

2 Flue Gas Flow Rate 140887 dscfm 140887

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

2 FGD Scrubber Liquor pH 0 pH 0

2 FGD Scrubber Liquor Flow Rate 0 gal/min 0

2 Sorbent Type and Sorbent Injection Rate Carbon 0 lb/hr

2 Flue Gas Oxygen Content 0 % 0

2 Flue Gas Carbon Dioxide Content 12.3 % 12.3

2 Flue Gas Moisture Content 0 % 0

2 Flue Gas Sampling Point Temperature 0 Deg F 0

2 Flue Gas Pressure 0 atm 0

2 Standard Pressure 0 atm 0

2 Standard Temperature 0 Deg F 0

2 Unit Gross Electrical Output 793 Mwe 793

2 Unit Net Electric Generation 706 MWh 706

2 Baghouse Pressure Drop 0 in. H2O 0

2 Flue Gas Temperature 322 degree F 322

3 Flue Gas Flow Rate 140887 dscfm 140887

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

3 FGD Scrubber Liquor pH 0 pH 0

3 FGD Scrubber Liquor Flow Rate 0 gal/min 0

3 Sorbent Type and Sorbent Injection Rate Carbon 0 lb/hr

3 Flue Gas Oxygen Content 0 % 0

3 Flue Gas Carbon Dioxide Content 12.3 % 12.3

3 Flue Gas Moisture Content 0 % 0

3 Flue Gas Sampling Point Temperature 0 Deg F 0

3 Flue Gas Pressure 0 atm 0

3 Standard Pressure 0 atm 0

3 Standard Temperature 0 Deg F 0

3 Unit Gross Electrical Output 793 Mwe 793

3 Unit Net Electric Generation 706 MWh 706

3 Baghouse Pressure Drop 0 in. H2O 0

3 Flue Gas Temperature 322 degree F 322

Friday, February 18, 2011 Page 9 of 15
Westwood

9/3/2010

APCD Run Data

Process Lab Run Data

1 Flue Gas Pressure 0.95 inches Hg 0.95

2 Flue Gas Pressure 0.95 inches Hg 0.95

3 Flue Gas Pressure 0.95 inches Hg 0.95

1 Anthracite Burned Tons/million BTU using CO2 0 0

Run Name Value UOM Comments

Target

Value

1 Limstone Injection for SO2 Control 0 0

1 BAGHOUSE 0 0

1 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 3540 Btu/lb

1 Fuel Moisture 8.66 %

1 Fuel Mercury Content 0 ppm

1 Fuel Cadmium Content 0 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 0 ppm

1 Fuel Arsenic Content 0 ppm

1 Fuel Chromium Content 0 ppm

1 Fuel Beryllium Content 0 ppm

1 Fuel Lead Content 0 ppm

1 Fuel Manganese Content 0 ppm

1 Fuel Chlorine Content 0 ppm

1 Fuel Fluorine Content 0 ppm

2 Fuel Higher Heating Value 3060 Btu/lb

2 Fuel Moisture 7.46 %

2 Fuel Mercury Content 0 ppm

2 Fuel Cadmium Content 0 ppm

2 Ultimate/Proximate Analysis 0

2 Fuel Nickel Content 0 ppm

2 Fuel Arsenic Content 0 ppm

2 Fuel Chromium Content 0 ppm

2 Fuel Beryllium Content 0 ppm

2 Fuel Lead Content 0 ppm

2 Fuel Manganese Content 0 ppm

2 Fuel Chlorine Content 0 ppm

2 Fuel Fluorine Content 0 ppm

3 Fuel Higher Heating Value 3730 Btu/lb

Friday, February 18, 2011 Page 10 of 15
Westwood

9/3/2010

3 Fuel Moisture 8.43 %

3 Fuel Mercury Content 0 ppm

3 Fuel Cadmium Content 0 ppm

3 Ultimate/Proximate Analysis 0

3 Fuel Nickel Content 0 ppm

3 Fuel Arsenic Content 0 ppm

3 Fuel Chromium Content 0 ppm

3 Fuel Beryllium Content 0 ppm

3 Fuel Lead Content 0 ppm

3 Fuel Manganese Content 0 ppm

3 Fuel Chlorine Content 0 ppm

3 Fuel Fluorine Content 0 ppm

Friday, February 18, 2011 Page 11 of 15
Westwood

9/3/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 6/8/2010 6/8/2010 6/8/2010

Run Start Time 12:05:00 PM 2:25:00 PM 4:46:00 PM

Run Finish Time 2:05:00 PM 4:25:00 PM 6:46:00 PM

Carbon Dioxide, % 11.9 12 12.1 12.000

Oxygen, % 8.7 8.6 8.5 8.600

Fuel Factor 1.03 1.03 1.02

Dry Volumetric Flow Rate, dry scfm 124919 122980 122465 123,454.667

F-Factor, dscfm/MMBtu @ %O2 11965 13481 12137 12,527.667

Moisture, % 5.8 5.5 6.1 5.800

Analyzer Make

Analyzer Model

Analyzer Serial Number TECO 48 TECO 48

Operating Range 0 0.000

Operating Units ppm ppm

No. Readings/Avg. 0 0.000

Calibration Set 10 10 10 10.000

Calibration Pre Zero Cylinder ID CC97653 

Zero Air

CC97653 

Zero Air

CC97653 

Zero Air

Calibration Pre Zero Cylinder Instrument Response 0.6 0.5 0.6 0.567

Calibration Pre Zero Cylinder Bias 0.1 0 0.1 0.067

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC100438 CO CC100438 

CO

CC100438 

CO

Calibration Pre High Cylinder Instrument Response 50.6 50.5 50.5 50.533

Calibration Pre High Cylinder Bias 1.43 1.32 1.32 1.357

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC97653 

Zero Air

CC97653 

Zero Air

CC97653 

Zero Air

Calibration Post Zero Cylinder Instrument Response 0.5 0.6 0.5 0.533

Calibration Post Zero Cylinder Bias 0 0.1 0 0.033

Calibration Post Zero Cylinder Drift 0.1 0.1 0.1 0.100

Calibration Post High Cylinder ID CC100438 CO CC100438 

CO

CC100438 

CO

Calibration Post High Cylinder Instrument Response 50.5 50.5 49.9 50.300

Calibration Post High Cylinder Bias 1.32 1.32 0.71 1.117

Calibration Post High Cylinder Drift 0.11 0 0.61 0.240

Cavg 26.3 26.4 26.5 26.400

Cavg Units ppmvd ppmvd ppmvd

Cgas 25.5028 25.6275 25.8821 25.671

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0.000

Fc 0 0 1420 473.333

Cgasw 0 0 0 0.000

Cgasw Units

Friday, February 18, 2011 Page 12 of 15
Westwood

9/3/2010

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 18, 2011 Page 13 of 15
Westwood

9/3/2010

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

Friday, February 18, 2011 Page 14 of 15
Westwood

9/3/2010

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

Friday, February 18, 2011 Page 15 of 15