### 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.

Friday, February 11, 2011 Page 1 of 23

### Facility Information:

ENTERGY LA, ROY S. NELSON UNIT N

3500 HOUSTON RIVER RD

Westlake LA 70669
Contact: Theodore Chenet

Phone: 281-297-3313

Fax: 281-297-3013
Email: tchenet@entergy.com Testing Company:

METCO Environmental

3226 Commander Dr.

Carrollton TX 75006
Contact: Lewis Adams

Phone: 972-931-7127

Fax: 972-931-8398
Email: ladams@metcoenv.com

Air Permit Number:
1393 Permitted Source ID/Name:
Unit Number 6 Boiler ID
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: Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 110003271049 FRS #: 110003271049

SCC / Description 10100212 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous Coal - Pulverized Coal: Dry 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 296 2228 2640 4 296 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location
Carbon Monoxide Method 10 3 120 0 Stack Exit Total organic compounds

(TOC) as Propane Method 25A 3 120 0 Stack Exit

Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 360 0 Stack Exit

Filterable PM2.5 OTM - 27/28 3 360 0 Stack Exit Organic Condensible

Particulate OTM - 27/28 3 360 0 Stack Exit



### Friday, February 11, 2011 Page 2 of 23

### 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.
The modified non-isokinetic Method 26 train was used for the determination of HF, HCL, and HCN. The train was sampled at a constant rate through a five impinger train (miniture), with the first three impingers spiked with 6.0N NaOH. Total PM2.5 OTM - 27/28 3 360 0 Stack Exit Total Particulate OTM - 27/28 3 360 0 Stack Exit Selenium Method 29 3 240 0 Stack Exit Antimony Method 29 3 240 0 Stack Exit Arsenic Method 29 3 240 0 Stack Exit Beryllium Method 29 3 240 0 Stack Exit Cadmium Method 29 3 240 0 Stack Exit Chromium Method 29 3 240 0 Stack Exit Lead Method 29 3 240 0 Stack Exit Filterable Particulate Method 29 3 240 0 Stack Exit Nickel Method 29 3 240 0 Stack Exit Cobalt Method 29 3 240 0 Stack Exit Phosphorus (yellow or white) Method 29 3 240 0 Stack Exit Manganese Method 29 3 240 0 Stack Exit Mercury 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 Sulfur Dioxide Method 6C 3 120 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 120 0 Stack Exit



### Friday, February 11, 2011 Page 3 of 23

### 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 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 11, 2011 Page 4 of 23

### Location Stack Exit - Method 29 Average

Run Number 2 3 1

Test Date 5/12/2010 5/12/2010 7/13/2010

Run Start Time 9:05:00 AM 8:20:00 AM 9:50:00 AM

Run Finish Time 1:48:00 PM 12:51:00 PM 2:35:00 PM

Net Run Time, minutes 240 240 240 Dry Gas Meter Volume Sampled, dscf 140.845 139.665 139.687 140.066
Moisture Content of Stack Gas, % 13.47 14.53 13.43 13.810 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000
Carbon Dioxide, % 14.3 14.4 14.8 14.500 Oxygen, % 5.1 4.6 4.9 4.867 Average Stack Gas Temperature, °F 336.37 338.77 353.44 342.860 Dry Volumetric Flow Rate, dry scfm 1,347,884.3 1,335,369.8 1,317,285.3 1,333,513.13 3
Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,370,049.0 2,383,525.0 2,371,195.9 2,374,923.30 0 Percent Isokinetic of Sampling Rate, % 96.3 96.4 97.8 96.833
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



### 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



### Friday, February 11, 2011 Page 5 of 23

### 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 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



### Friday, February 11, 2011 Page 6 of 23

### 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 - 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 11, 2011 Page 7 of 23

### Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average
Run 1 2 3 Elb/hr 6.60E+03 3.04E+03 4.52E+03 4,720.000 lb/mmBtuO2 1.06E+00 4.92E-01 6.95E-01 0.749
ppm 1.14E+03 5.22E+02 7.62E+02 808.000 ppm@7%O2 9.92E+02 4.60E+02 6.50E+02 700.667



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average
Run 1 2 3 Elb/hr 3.50E+01 1.21E+02 2.69E+01 60.967 lb/mmBtuO2 5.61E-03 1.96E-02 4.13E-03 0.010
ppm 3.83E+00 1.32E+01 2.88E+00 6.637 ppm@7%O2 3.33E+00 1.16E+01 2.46E+00 5.797



### Location: Stack Exit - Method 29 Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.0064 0.0064 0.0064 0.006 Elb/hr 7.98E-03 8.10E-03 8.09E-03 0.008 lb/mmBtuO2 1.29E-06 1.30E-06 1.27E-06 0.000 ug/dscm 1.62E+00 1.60E+00 1.62E+00 1.613


### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.00151 0.00186 0.00186 0.002 Elb/hr 1.88E-03 2.35E-03 2.35E-03 0.002 lb/mmBtuO2 3.04E-07 3.77E-07 3.68E-07 0.000 ug/dscm 3.82E-01 4.66E-01 4.70E-01 0.439


### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.001 0.001 0.001 0.001 Elb/hr 1.25E-03 1.27E-03 1.26E-03 0.001 lb/mmBtuO2 2.02E-07 2.02E-07 1.98E-07 0.000 ug/dscm 2.53E-01 2.51E-01 2.53E-01 0.252


### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.0013 0.00156 0.00154 0.001 Elb/hr 1.62E-03 1.97E-03 1.95E-03 0.002 lb/mmBtuO2 2.62E-07 3.16E-07 3.05E-07 0.000 ug/dscm 3.29E-01 3.91E-01 3.89E-01 0.370



### Friday, February 11, 2011 Page 8 of 23

### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.00341 0.00351 0.00321 0.003 Elb/hr 4.25E-03 4.44E-03 4.06E-03 0.004 lb/mmBtuO2 6.88E-07 7.11E-07 6.35E-07 0.000 ug/dscm 8.62E-01 8.80E-01 8.12E-01 0.851


### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.01 0.01 0.01 0.010 Elb/hr 1.25E-02 1.27E-02 1.26E-02 0.013 lb/mmBtuO2 2.02E-06 2.02E-06 1.98E-06 0.000 ug/dscm 2.53E+00 2.51E+00 2.53E+00 2.523


### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 64.3 54.3 50.3 56.300 Elb/hr 8.02E+01 6.87E+01 6.36E+01 70.833 lb/mmBtuO2 1.30E-02 1.10E-02 9.96E-03 0.011 ug/dscm 1.63E+04 1.36E+04 1.27E+04 14,200.000


### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.00243 0.00249 0.00222 0.002 Elb/hr 3.03E-03 3.15E-03 2.81E-03 0.003 lb/mmBtuO2 4.90E-07 5.04E-07 4.39E-07 0.000 ug/dscm 6.14E-01 6.24E-01 5.61E-01 0.600


### Compound: Manganese Average RunNumber 1 2 3 Mass_mg 0.00387 0.00397 0.00312 0.004 Elb/hr 4.83E-03 5.03E-03 3.95E-03 0.005 lb/mmBtuO2 7.80E-07 8.04E-07 6.18E-07 0.000 ug/dscm 9.79E-01 9.96E-01 7.89E-01 0.921


### Compound: Mercury Average RunNumber 1 2 3 Mass_mg 0.03291 0.03258 0.04328 0.036 Elb/hr 4.11E-02 4.12E-02 5.47E-02 0.046 lb/mmBtuO2 6.64E-06 6.60E-06 8.57E-06 0.000 ug/dscm 8.32E+00 8.17E+00 1.09E+01 9.130


### Compound: Nickel Average RunNumber 1 2 3 Mass_mg 0.0157 0.0078 0.0047 0.009 Elb/hr 1.96E-02 9.87E-03 5.94E-03 0.012



### Friday, February 11, 2011 Page 9 of 23lb/mmBtuO2 3.17E-06 1.58E-06 9.30E-07 0.000 ug/dscm 3.97E+00 1.96E+00 1.19E+00 2.373


### Compound: Phosphorus (yellow or white) Average RunNumber 1 2 3 Mass_mg 0.995 0.97355 1.0109 0.993 Elb/hr 1.24E+00 1.23E+00 1.28E+00 1.250 lb/mmBtuO2 2.01E-04 1.97E-04 2.00E-04 0.000 ug/dscm 2.52E+02 2.44E+02 2.56E+02 250.667


### Compound: Selenium Average RunNumber 1 2 3 Mass_mg 0.1136 0.1045 0.1836 0.134 Elb/hr 1.42E-01 1.32E-01 2.32E-01 0.169 lb/mmBtuO2 2.29E-05 2.12E-05 3.63E-05 0.000 ug/dscm 2.87E+01 2.62E+01 4.64E+01 33.767



### Location: Stack Exit - Method 6C Compound: Sulfur Dioxide Average
Run 1 2 3 Elb/hr 4.16E+03 3.62E+02 4.35E+03 2,957.333 lb/mmBtuO2 6.67E-01 5.86E-01 6.69E-01 0.641
ppm 3.14E+02 2.72E+02 3.21E+02 302.333 ppm@7%O2 2.73E+02 2.40E+02 2.74E+02 262.333



### Location: Stack Exit - Method 7E Compound: Nitrogen oxides (NOx) Average
Run 1 2 3 Elb/hr 1.07E+03 1.12E+03 9.73E+06 3,244,063.333 lb/mmBtuO2 1.71E-01 1.81E-01 1.50E+03 500.117
ppm 1.12E+02 1.17E+02 9.99E+05 333,076.333 ppm@7%O2 9.74E+01 1.03E+02 8.52E+05 284,066.800



### Location: Stack Exit - OTM - 27/28 Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 3.1 12.5 5.8 7.133 Elb/hr 4.46E+00 1.78E+01 8.82E+00 10.360 gr/dscf 3.64E-04 1.50E-03 7.22E-04 0.001 lb/mmBtuO2 6.65E-04 2.77E-03 1.29E-03 0.002


### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 33.7 69 80.1 60.933 Elb/hr 4.85E+01 9.82E+01 1.22E+02 89.567 gr/dscf 3.96E-03 8.27E-03 9.97E-03 0.007



### Friday, February 11, 2011 Page 10 of 23

### Process Run Data lb/mmBtuO2 7.23E-03 1.53E-02 1.79E-02 0.013


### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 21.7 3.9 2.5 9.367 Elb/hr 3.12E+01 5.55E+00 3.80E+00 13.517 gr/dscf 2.55E-03 4.67E-04 3.11E-04 0.001 lb/mmBtuO2 4.66E-03 8.63E-04 5.58E-04 0.002


### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 59.2 94.2 93.6 82.333 Elb/hr 8.52E+01 1.34E+02 1.42E+02 120.400 gr/dscf 6.96E-03 1.13E-02 1.17E-02 0.010 lb/mmBtuO2 1.27E-02 2.09E-02 2.09E-02 0.018


### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 56.5 88.8 86.4 77.233 Elb/hr 8.14E+01 1.26E+02 1.31E+02 112.800 gr/dscf 6.64E-03 1.06E-02 1.08E-02 0.009 lb/mmBtuO2 1.21E-02 1.97E-02 1.93E-02 0.017



### Friday, February 11, 2011 Page 11 of 23

### Process Run Data



### Run Name Value UOM Comments Target Value
1 Bituminous Coal Burned 0.35 1000 Tons/hr Average during Run 3 test period 0



### 1 Average Heat Input 6408.8 MMBtu/hr Average during Run 3 test period 0

1 Flue Gas Flow Rate 1E+06 dscfm Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

1 Flue Gas Oxygen Content 4.88 % Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0



### 1 Flue Gas Carbon Dioxide Content 14.78 % Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

1 Flue Gas Sampling Point Temperature 332 Deg F Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

1 Flue Gas Pressure 29.55 "Hg Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0



### 1 Standard Pressure 29.92 "Hg Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

Friday, February 11, 2011 Page 12 of 23

### 1 Standard Temperature 68 Deg F Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

1 Unit Gross Electrical Output 585 MW Average during Run 3 test period 0



### 1 Unit Net Electric Generation 552 MWh Average during Run 3 test period 0

2 Bituminous Coal Burned 0.35 1000 Tons/hr Average during Run 3 test period 0



### 2 Average Heat Input 6442.1 MMBtu/hr Average during Run 3 test period 0

2 Flue Gas Flow Rate 1E+06 dscfm Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0



### 2 Flue Gas Oxygen Content 5.13 % Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

2 Flue Gas Carbon Dioxide Content 14.32 % Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

2 Flue Gas Sampling Point Temperature 332 Deg F Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0



### 2 Flue Gas Pressure 29.65 "Hg Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

Friday, February 11, 2011 Page 13 of 23

### 2 Standard Pressure 29.92 "Hg Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

2 Standard Temperature 68 Deg F Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0



### 2 Unit Gross Electrical Output 585 MW Average during Run 3 test period 0

2 Unit Net Electric Generation 552 MWh Average during Run 3 test period 0



### 3 Bituminous Coal Burned 0.357 1000 Tons/hr Average during Run 3 test period 0

3 Average Heat Input 6422.5 MMBtu/hr Average during Run 3 test period 0



### 3 Flue Gas Flow Rate 1E+06 dscfm Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

3 Flue Gas Oxygen Content 4.55 % Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

3 Flue Gas Carbon Dioxide Content 14.4 % Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0



### 3 Flue Gas Sampling Point Temperature 324 Deg F Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

Friday, February 11, 2011 Page 14 of 23

### APCD Run Data

Process Lab Run Data 3 Flue Gas Pressure 29.67 "Hg Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

3 Standard Pressure 29.92 "Hg Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0



### 3 Standard Temperature 68 Deg F Provided by METCO Environmental, data collected withthe OTM27/OTM_28 sampling train 0

3 Unit Gross Electrical Output 585 MW Average during Run 3 test period 0



### 3 Unit Net Electric Generation 553 MWh Average during Run 3 test period 0

Run Name Value UOM Comments
1 See 4b Comments. 0



### Friday, February 11, 2011 Page 15 of 23

### 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



### Friday, February 11, 2011 Page 16 of 23

### 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 11, 2011 Page 17 of 23

### Location Stack Exit - Method 29 Average

Run Number 2 3 1
Test Date 5/12/2010 5/12/2010 7/13/2010 Run Start Time 9:05:00 AM 8:20:00 AM 9:50:00 AM Run Finish Time 1:48:00 PM 12:51:00 PM 2:35:00 PM Net Traversing Points 48 48 48 Net Run Time, minutes 240 240 240 Nozzle Diameter, inches 0.199 0.199 0.199 0.199 Pitot Tube Coefficient 0.805 0.805 0.805 0.805 Dry Gas Meter Calibration Factor 0.982 0.982 0.986 0.983 Barometric Pressure, inches of Mercury 29.71 29.72 29.7 29.710 Average Orifice Meter Differential, inches H2O 1.33 1.34 1.31 1.327 Dry Gas Meter Volume Sampled, cubic feet 151.915 150.418 151.063 151.132 Average Dry Gas Meter Temperature, °F 97.15 96.52 100.68 98.117 Dry Gas Meter Volume Sampled, dscf 140.845 139.665 139.687 140.066 Total Moisture Liquid collected, g 465.7 504.3 460.4 476.800 Volume of Water Vapor, standard cubic feet 21.92 23.74 21.67 22.443 Moisture Content of Stack Gas, % 13.47 14.53 13.43 13.810 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8653 0.8547 0.8657 0.862 Carbon Dioxide, % 14.3 14.4 14.8 14.500 Oxygen, % 5.1 4.6 4.9 4.867 Carbon Monoxide & Nitrogen, % 80.6 81 80.3 80.633 Fuel Factor 1.10 1.13 1.08 Dry Molecular Weight, lb/lb-Mole 30.49 30.49 30.56 30.513 Wet Molecular weight, lb/lb-Mole 28.81 28.68 28.87 28.787 Flue Gas Static Pressure, inches of H2O -0.7 -0.7 -1.6 -1.000 Absolute Flue Gas Pressure, inches of Mercury 29.66 29.67 29.58 29.637 Average Stack Gas Temperature, °F 336.37 338.77 353.44 342.860 Average Velocity Head, inches of H2O 1.5481506019 4247 1.554314073

29851 1.515951714

72946 1.539

Average Stack Gas Velocity, feet/second 82.66 83.13 82.70 82.830 Stack Cross-Sectional Area, square feet 477.871 477.871 477.871 477.871 Dry Volumetric Flow Rate, dry scfm 1,347,884.3 1,335,369.8 1,317,285.3 1,333,513.1 33 Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,370,049.0 2,383,525.0 2,371,195.9 2,374,923.3 00 Percent Isokinetic of Sampling Rate, % 96.3 96.4 97.8 96.833 Percent Excess Air, % 31.5 27.4 30.1 29.667 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Round Duct Diameter, inches 296 296 296 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



### Friday, February 11, 2011 Page 18 of 23

### 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 11, 2011 Page 19 of 23

### 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 11, 2011 Page 20 of 23

### 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



### Friday, February 11, 2011 Page 21 of 23

### 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



### Friday, February 11, 2011 Page 22 of 23

### 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 11, 2011 Page 23 of 23