### 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.

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### 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: Westwood 031 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 147 294 735 3 0 3 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location % 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


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### Westwood
9/3/2010 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 Stack Exit 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) 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 Stack Exit 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 0 Stack Exit Total organic compounds

(TOC) as Propane 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 Stack Exit 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



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### 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

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 Stack Exit 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

Filterable Particulate Method 5 3 240 0 Stack Exit Organic Condensible

Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Sulfur Dioxide Method 6C 3 180 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### 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 0 Tons/million BTU using CO2 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