### Name:

Title: Company: Sign Date: Name:
Title: Company: Sign Date: 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.

Wednesday, February 02, 2011 Page 1 of 37

### Facility Information:

NC_GG Allen Units 3,4

253 Plant Allen Road

Belmont NC 28012

Contact: Jon Hays

Phone: 317-838-4445

Fax: 317-8382490

Email: jon.hays@duke.energy.com Testing Company:

AECOM
2 Technology Park Drive

Westford MA 01886

Contact: Patrick Ford

Phone: 978-589-3427

Fax: 978-589-3100

Email: pat.ford@aecom.com

Air Permit Number:

3757T31 Permitted Source ID/Name: No. 2 Fuel Oil/Coal-Fired Electric Utility Boilers Units 3,4

Permitted Maximum Process Rate: Max. Normal Operation Process Rate: Target Process Test Rate

Description of the source (including control equipment). Please see the attachments for source or process flow diagram:
This description should describe the process and associated controls to differentiate this facility from, or document similarity with others of same SCC. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 3707100039 FRS #: 3600039

SCC / Description 10100211 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous Coal - Wet 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 354 8 2 4 0 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location

% H2O Method 1 - 4 3 60 0 Stack Exit
Carbon Monoxide Method 10 4 120 0 Stack Exit Total organic compounds

(TOC) as Propane Method 25A 4 120 0 Stack Exit

Hydrogen Fluoride Method 26A 3 60 0 Stack Exit Hydrogen Chloride Method 26A 3 60 0 Stack Exit
Arsenic Method 29 3 180 0 Stack Exit Manganese Method 29 3 180 0 Stack Exit



### Wednesday, February 02, 2011 Page 2 of 37

### 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.
EPA Method 26A was modified to include the provisions cited in Method CTM-033 to allow simultaneous collection of HCl, HF and HCN. Modification included elimination of the 0.1 N H2SO4 impingers, addition of a third NaOH impinger and use of high normality NaOH absorbing solutions (6N in the 1st impinger and 2 N in the second and third) in order to maintain the pH of the solution high enough to prevent poor HCN analyte collection. The sample time was also reduced to 1-hour as allowed by EPA (see FAQ's section on the ICR website) again to ensure that the pH of the absorbing solution remained high.

Lead Method 29 3 180 0 Stack Exit Antimony Method 29 3 180 0 Stack Exit Beryllium Method 29 3 180 0 Stack Exit
Cobalt Method 29 3 180 0 Stack Exit
Chromium Method 29 3 180 0 Stack Exit
Selenium Method 29 3 180 0 Stack Exit
Cadmium Method 29 3 180 0 Stack Exit
Nickel Method 29 3 180 0 Stack Exit
O2 Method 3A O2 3 60 0 Stack Exit
Co2 Method 3A CO2 3 60 0 Stack Exit
Total Particulate Method 5/OTM-28 3 180 0 Stack Exit
Filterable Particulate Method 5/OTM-28 3 180 0 Stack Exit Organic Condensible

Particulate Method 5/OTM-28 3 180 0 Stack Exit

Inorganic (Aqueous)

Condensible Part. Method 5/OTM-28 3 180 0 Stack Exit

Sulfur Dioxide Method 6C 3 60 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### Wednesday, February 02, 2011 Page 3 of 37

### Sampling / Stack Data Results Summary



### Location Stack Exit - Method 10
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 10 3
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



### Wednesday, February 02, 2011 Page 4 of 37

### 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



### Location Stack Exit - Method 25A 3
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



### Wednesday, February 02, 2011 Page 5 of 37

### Location Stack Exit - Method 26A
Average

Run Number CTM033-1 CTM033-2 CTM033-3

Test Date 3/17/2010 3/17/2010 3/18/2010

Run Start Time 4:50:00 PM 6:39:00 PM 8:45:00 AM

Run Finish Time 6:00:00 PM 7:44:00 PM 9:52:00 AM

Net Run Time, minutes 60 60 60
Dry Gas Meter Volume Sampled, dscf 38.093 38.173 38.999 38.422
Moisture Content of Stack Gas, % 15.71 15.76 15.69 15.720
Moisture Saturation at Stack Gas Temperature, % 14.06 13.92 13.78 13.920
Carbon Dioxide, % 13.83 13.93 13.95 13.903
Oxygen, % 5.61 5.5 5.38 5.497
Average Stack Gas Temperature, °F 126.29 125.92 126.42 126.210
Dry Volumetric Flow Rate, dry scfm 1,203,402.4 1,197,466. 8 1,218,049.6 1,206,306.26 7
Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,599,783.7 1,588,301. 0 1,576,408.3 1,588,164.33 3
Percent Isokinetic of Sampling Rate, % 102.5 103.2 103.7 103.133
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



### Wednesday, February 02, 2011 Page 6 of 37

### Location Stack Exit - Method 29
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



### 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



### Wednesday, February 02, 2011 Page 7 of 37

### Location Stack Exit - Method 3A CO2 3
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 CO2 3 6
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



### Wednesday, February 02, 2011 Page 8 of 37

### 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



### Location Stack Exit - Method 3A O2 3
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



### Wednesday, February 02, 2011 Page 9 of 37

### Location Stack Exit - Method 3A O2 3 6
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 5/OTM-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



### Wednesday, February 02, 2011 Page 10 of 37

### Location Stack Exit - Method 6C
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 6C 3
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



### Wednesday, February 02, 2011 Page 11 of 37

### Location Stack Exit - Method 7E
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 7E 3
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



### Wednesday, February 02, 2011 Page 12 of 37

### Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average
Run 1 2 3
Elb/hr 2.30E+03 2.16E+03 1.17E+03 1,876.667
lb/mmBtuO2 4.26E-01 3.82E-01 2.16E-01 0.341

ppm 4.39E+02 3.95E+02 2.21E+02 351.667 ppm@7%O2 3.99E+02 3.57E+02 2.02E+02 319.333



### Location: Stack Exit - Method 10 3 Compound: Carbon Monoxide Average
Run 4
Elb/hr 1.37E+03 1,370.000
lb/mmBtuO2 2.48E-01 0.248

ppm 2.54E+02 254.000 ppm@7%O2 2.32E+02 232.000



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average
Run 1 2 3
lb/mmBtuO2 8.77E-04 3.44E-04 4.25E-04 0.001

ppm 5.73E-01 2.26E-01 2.77E-01 0.359 ppm@7%O2 5.21E-01 2.05E-01 2.53E-01 0.326



### Location: Stack Exit - Method 25A 3 Compound: Total organic compounds (TOC) as Average
Run 4
lb/mmBtuO2 6.48E-04 0.001

ppm 4.22E-01 0.422 ppm@7%O2 3.85E-01 0.385



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average
RunNumber CTM033-1 CTM033-2 CTM033-3 Mass_mg 1.305 1.535 1.331 1.390
Elb/hr 5.45E+00 6.37E+00 5.50E+00 5.773
lb/mmBtuO2 1.01E-03 1.18E-03 9.91E-04 0.001 mg/dscm 1.21E+00 1.42E+00 1.21E+00 1.280 mg/dscm@7%O2 1.10E+00 1.28E+00 1.08E+00 1.153



### Compound: Hydrogen Fluoride Average
RunNumber CTM033-1 CTM033-2 CTM033-3 Mass_mg 0.65 0.62 0.64 0.637
Elb/hr 2.72E+00 2.57E+00 2.64E+00 2.643



### Wednesday, February 02, 2011 Page 13 of 37lb/mmBtuO2 5.03E-04 4.75E-04 4.76E-04 0.000 mg/dscm 6.03E-01 5.74E-01 5.80E-01 0.586 mg/dscm@7%O2 5.48E-01 5.18E-01 5.19E-01 0.528



### Location: Stack Exit - Method 29 

### Compound: Antimony Average
RunNumber M29- R1 M29-R2 M29-R3 Mass_mg 0.00027 0.00041 0.00022 0.000
Elb/hr 3.08E-04 4.71E-04 2.51E-04 0.000
lb/mmBtuO2 5.61E-08 8.54E-08 4.42E-08 0.000 ug/dscm 6.69E-02 1.03E-01 5.37E-02 0.075 ug/dscm@7%O2 6.11E-02 9.30E-02 4.82E-02 0.067



### Compound: Arsenic Average
RunNumber M29- R1 M29-R2 M29-R3 Mass_mg 0.00254 0.0039 0.0042 0.004
Elb/hr 2.90E-03 4.48E-03 4.79E-03 0.004
lb/mmBtuO2 5.27E-07 8.13E-07 8.44E-07 0.000 ug/dscm 6.30E-01 9.81E-01 1.02E+00 0.877 ug/dscm@7%O2 5.75E-01 8.85E-01 9.15E-01 0.792



### Compound: Beryllium Average
RunNumber M29- R1 M29-R2 M29-R3 Mass_mg 0.00011 0.00008 0.00008 0.000
Elb/hr 1.25E-04 9.19E-05 9.13E-05 0.000
lb/mmBtuO2 2.28E-08 1.67E-08 1.61E-08 0.000 ug/dscm 2.73E-02 2.01E-02 1.95E-02 0.022 ug/dscm@7%O2 2.49E-02 1.81E-02 1.75E-02 0.020



### Compound: Cadmium Average
RunNumber M29- R1 M29-R2 M29-R3 Mass_mg 0.00058 0.00054 0.00018 0.000
Elb/hr 6.61E-04 6.20E-04 2.05E-04 0.000
lb/mmBtuO2 1.20E-07 1.13E-07 3.62E-08 0.000 ug/dscm 1.44E-01 1.36E-01 4.39E-02 0.108 ug/dscm@7%O2 1.31E-01 1.23E-01 3.94E-02 0.098



### Compound: Chromium Average
RunNumber M29- R1 M29-R2 M29-R3 Mass_mg 0.0112 0.0259 0.0137 0.017
Elb/hr 1.28E-02 2.98E-02 1.56E-02 0.019
lb/mmBtuO2 2.33E-06 5.40E-06 2.75E-06 0.000 ug/dscm 2.78E+00 6.51E+00 3.34E+00 4.210 ug/dscm@7%O2 2.54E+00 5.88E+00 3.00E+00 3.807



### Compound: Cobalt Average
RunNumber M29- R1 M29-R2 M29-R3



### Wednesday, February 02, 2011 Page 14 of 37Mass_mg 0.00055 0.00069 0.0006 0.001
Elb/hr 6.27E-04 7.93E-04 6.85E-04 0.001
lb/mmBtuO2 1.14E-07 1.44E-07 1.21E-07 0.000 ug/dscm 1.36E-01 1.74E-01 1.46E-01 0.152 ug/dscm@7%O2 1.24E-01 1.57E-01 1.31E-01 0.137



### Compound: Lead Average
RunNumber M29- R1 M29-R2 M29-R3 Mass_mg 0.00287 0.00336 0.00146 0.003
Elb/hr 3.27E-03 3.86E-03 1.67E-03 0.003
lb/mmBtuO2 5.96E-07 7.00E-07 2.93E-07 0.000 ug/dscm 7.11E-01 8.45E-01 3.56E-01 0.637 ug/dscm@7%O2 6.49E-01 7.63E-01 3.19E-01 0.577



### Compound: Manganese Average
RunNumber M29- R1 M29-R2 M29-R3 Mass_mg 0.011 0.0141 0.0111 0.012
Elb/hr 1.25E-02 1.62E-02 1.27E-02 0.014
lb/mmBtuO2 2.28E-06 2.94E-06 2.23E-06 0.000 ug/dscm 2.73E+00 3.55E+00 2.71E+00 2.997 ug/dscm@7%O2 2.49E+00 3.20E+00 2.43E+00 2.707



### Compound: Nickel Average
RunNumber M29- R1 M29-R2 M29-R3 Mass_mg 0.0105 0.03693 0.0134 0.020
Elb/hr 1.20E-02 4.24E-02 1.53E-02 0.023
lb/mmBtuO2 2.18E-06 7.69E-06 2.69E-06 0.000 ug/dscm 2.60E+00 9.29E+00 3.27E+00 5.053 ug/dscm@7%O2 2.37E+00 8.39E+00 2.93E+00 4.563



### Compound: Selenium Average
RunNumber M29- R1 M29-R2 M29-R3 Mass_mg 0.0732 0.1426 0.1309 0.116
Elb/hr 8.35E-02 1.64E-01 1.49E-01 0.132
lb/mmBtuO2 1.52E-05 2.97E-05 2.63E-05 0.000 ug/dscm 1.81E+01 3.59E+01 3.19E+01 28.633 ug/dscm@7%O2 1.65E+01 3.24E+01 2.86E+01 25.833



### Location: Stack Exit - Method 5/OTM-28 Compound: Filterable Particulate Average
RunNumber M5-R1 M5-R2 M5-R3 Mass_mg 15.9 19.8 23.3 19.667
Elb/hr 1.93E+01 2.38E+01 2.80E+01 23.700 gr/dscf 1.77E-03 2.18E-03 2.55E-03 0.002 gr/dscf@7%O2 1.62E-03 1.97E-03 2.29E-03 0.002
lb/mmBtuO2 3.39E-03 4.13E-03 4.82E-03 0.004



### Wednesday, February 02, 2011 Page 15 of 37

### Compound: Inorganic (Aqueous) Condensible Pa Average
RunNumber M5-R1 M5-R2 M5-R3 Mass_mg 17 7.4 6.4 10.267
Elb/hr 2.07E+01 8.91E+00 7.68E+00 12.430 gr/dscf 1.89E-03 8.14E-04 7.02E-04 0.001 gr/dscf@7%O2 1.72E-03 7.35E-04 6.30E-04 0.001
lb/mmBtuO2 3.62E-03 1.54E-03 1.32E-03 0.002



### Compound: Organic Condensible Particulate Average
RunNumber M5-R1 M5-R2 M5-R3 Mass_mg 7.4 6.3 8.5 7.400
Elb/hr 9.00E+00 7.59E+00 1.02E+01 8.930 gr/dscf 8.22E-04 6.93E-04 9.32E-04 0.001 gr/dscf@7%O2 7.50E-04 6.26E-04 8.36E-04 0.001
lb/mmBtuO2 1.58E-03 1.31E-03 1.76E-03 0.002



### Compound: Total Particulate Average
RunNumber M5-R1 M5-R2 M5-R3 Mass_mg 40.3 33.5 38.2 37.333
Elb/hr 4.90E+01 4.03E+01 4.58E+01 45.033 gr/dscf 4.48E-03 3.69E-03 4.19E-03 0.004 gr/dscf@7%O2 4.09E-03 3.33E-03 3.76E-03 0.004
lb/mmBtuO2 8.58E-03 6.99E-03 7.89E-03 0.008



### Location: Stack Exit - Method 6C Compound: Sulfur Dioxide Average
Run CTM033-1 CTM033-2 CTM033-3
Elb/hr 7.20E+02 7.28E+02 7.21E+02 723.000
lb/mmBtuO2 1.32E-01 1.33E-01 1.29E-01 0.131

ppm 5.96E+01 6.04E+01 5.89E+01 59.633 ppm@7%O2 5.42E+01 5.45E+01 5.28E+01 53.833



### Location: Stack Exit - Method 6C 3 Compound: Sulfur Dioxide Average
Run Organic-1 Organic-2 Organic-3
Elb/hr 3.42E+02 4.41E+02 2.69E+02 350.667
lb/mmBtuO2 6.09E-02 7.85E-02 4.82E-02 0.063

ppm 2.74E+01 3.55E+01 2.16E+01 28.167 ppm@7%O2 2.49E+01 3.21E+01 1.97E+01 25.567



### Location: Stack Exit - Method 7E Compound: Nitrogen oxides (NOx) Average
Run CTM033-1 CTM033-2 CTM033-3
Elb/hr 9.04E+02 9.02E+02 9.35E+02 913.667
lb/mmBtuO2 1.66E-01 1.65E-01 1.67E-01 0.166

ppm 1.04E+02 1.04E+02 1.06E+02 104.667



### Wednesday, February 02, 2011 Page 16 of 37

### Process Run Data ppm@7%O2 9.45E+01 9.39E+01 9.49E+01 94.433



### Location: Stack Exit - Method 7E 3 Compound: Nitrogen oxides (NOx) Average
Run Organic-1 Organic-2 Organic-3
Elb/hr 9.64E+02 9.61E+02 9.62E+02 962.333
lb/mmBtuO2 1.72E-01 1.71E-01 1.73E-01 0.172

ppm 1.07E+02 1.08E+02 1.08E+02 107.667 ppm@7%O2 9.73E+01 9.77E+01 9.86E+01 97.867



### Wednesday, February 02, 2011 Page 17 of 37

### Process Run Data



### Run Name Value UOM Comments Target Value

1 Bituminous Coal Burned 0 Tons/million BTU using O2 0



### 2 Bituminous Coal Burned 0 Tons/million BTU using O2 0

3 Bituminous Coal Burned 0 Tons/million BTU using O2 0

4 Bituminous Coal Burned 0 Tons/million BTU using O2 0



### 1 Average Heat Input 0 MMBtu/hr 0

2 Average Heat Input 0 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0



### 4 Average Heat Input 0 MMBtu/hr 0

1 Steam Output 0 1000 lb steam/hr 0

2 Steam Output 0 1000 lb steam/hr 0



### 3 Steam Output 0 1000 lb steam/hr 0

4 Steam Output 0 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

4 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



### 4 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

4 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



### 4 Fuel Oil Firing Rate 0 gal/hr 0

1 Flue Gas Flow Rate 0 0

4 Flue Gas Flow Rate 0 0



### 1 Pressure Drop Across FGD (if applicable) 0 in H20 0

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

1 FGD Scrubber Liquor pH 0 pH 0



### Wednesday, February 02, 2011 Page 18 of 37

### APCD Run Data

Process Lab Run Data 4 FGD Scrubber Liquor pH 0 pH 0



### 1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 4 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0



### 4 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0



### 1 Flue Gas Moisture Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0



### 4 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0



### 4 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

4 Standard Pressure 0 atm 0



### 1 Standard Temperature 0 Deg F 0

4 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 0 Mwe 0



### 4 Unit Gross Electrical Output 0 Mwe 0

1 Unit Net Electric Generation 0 MWh 0

4 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments Target Value



### 1 List all emissions control devices in order of process flow. Choose from 0 0

1 drop down lists. If not on list add description and provide detailed 0 0



### 1 desription in section 5a. 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %



### Wednesday, February 02, 2011 Page 19 of 37

### 1 Ultimate/Proximate Analysis 0



### 1 Fuel Chlorine Content 0 mg/kg

1 Fuel Fluorine Content 0 mg/kg

1 Metals Content 0 mg/kg



### Wednesday, February 02, 2011 Page 20 of 37

### Sampling / Stack Data Results Detail



### Location Stack Exit - Method 10 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



### Wednesday, February 02, 2011 Page 21 of 37

### Location Stack Exit - Method 10 3 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



### Wednesday, February 02, 2011 Page 22 of 37

### 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



### Wednesday, February 02, 2011 Page 23 of 37

### Location Stack Exit - Method 25A 3 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



### Wednesday, February 02, 2011 Page 24 of 37

### Location Stack Exit - Method 26A Average

Run Number CTM033-1 CTM033-2 CTM033-3
Test Date 3/17/2010 3/17/2010 3/18/2010
Run Start Time 4:50:00 PM 6:39:00 PM 8:45:00 AM
Run Finish Time 6:00:00 PM 7:44:00 PM 9:52:00 AM Net Traversing Points 24 24 24 Net Run Time, minutes 60 60 60 Nozzle Diameter, inches 0.254 0.254 0.254 0.254
Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.004 1.004 1.004 1.004 Barometric Pressure, inches of Mercury 29.1 29.1 29.8 29.333 Average Orifice Meter Differential, inches H2O 1.44 1.43 1.43 1.433 Dry Gas Meter Volume Sampled, cubic feet 40.273 40.783 40.077 40.378 Average Dry Gas Meter Temperature, °F 87.08 92.83 84.50 88.137 Dry Gas Meter Volume Sampled, dscf 38.093 38.173 38.999 38.422 Total Moisture Liquid collected, g 150.8 151.7 154.2 152.233 Volume of Water Vapor, standard cubic feet 7.10 7.14 7.26 7.167 Moisture Content of Stack Gas, % 15.71 15.76 15.69 15.720 Moisture Saturation at Stack Gas Temperature, % 14.06 13.92 13.78 13.920 Dry Mole Fraction 0.8594 0.8608 0.8622 0.861 Carbon Dioxide, % 13.83 13.93 13.95 13.903 Oxygen, % 5.61 5.5 5.38 5.497 Carbon Monoxide & Nitrogen, % 80.56 80.57 80.67 80.600
Fuel Factor 1.11 1.11 1.11 Dry Molecular Weight, lb/lb-Mole 30.44 30.45 30.45 30.447 Wet Molecular weight, lb/lb-Mole 28.99 29.05 29.08 29.040 Flue Gas Static Pressure, inches of H2O -0.26 -0.26 -0.25 -0.257 Absolute Flue Gas Pressure, inches of Mercury 29.08 29.08 29.78 29.313 Average Stack Gas Temperature, °F 126.29 125.92 126.42 126.210 Average Velocity Head, inches of H2O 0.4242966609 68342 0.419467178

61162 0.423242929

711302 0.422

Average Stack Gas Velocity, feet/second 39.01 38.73 38.44 38.727 Stack Cross-Sectional Area, square feet 683.493 683.493 683.493 683.493 Dry Volumetric Flow Rate, dry scfm 1,203,402.4 1,197,466.8 1,218,049.6 1,206,306.2 67 Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,599,783.7 1,588,301.0 1,576,408.3 1,588,164.3 33 Percent Isokinetic of Sampling Rate, % 102.5 103.2 103.7 103.133 Percent Excess Air, % 35.8 34.9 33.8 34.833 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Round Duct Diameter, inches 354 354 354 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Wednesday, February 02, 2011 Page 25 of 37

### Location Stack Exit - Method 29 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



### Wednesday, February 02, 2011 Page 26 of 37

### 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



### Wednesday, February 02, 2011 Page 27 of 37

### Location Stack Exit - Method 3A CO2 3 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



### Wednesday, February 02, 2011 Page 28 of 37

### Location Stack Exit - Method 3A CO2 3 6 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



### Wednesday, February 02, 2011 Page 29 of 37

### 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



### Wednesday, February 02, 2011 Page 30 of 37

### Location Stack Exit - Method 3A O2 3 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



### Wednesday, February 02, 2011 Page 31 of 37

### Location Stack Exit - Method 3A O2 3 6 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



### Wednesday, February 02, 2011 Page 32 of 37

### Location Stack Exit - Method 5/OTM-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



### Wednesday, February 02, 2011 Page 33 of 37

### Location Stack Exit - Method 6C 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



### Wednesday, February 02, 2011 Page 34 of 37

### Location Stack Exit - Method 6C 3 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



### Wednesday, February 02, 2011 Page 35 of 37

### Location Stack Exit - Method 7E 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



### Wednesday, February 02, 2011 Page 36 of 37

### Location Stack Exit - Method 7E 3 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



### Wednesday, February 02, 2011 Page 37 of 37