### Name:

Title: Company: Sign Date: Name: Title: Company: Sign Date: Permitted Facility Representative / Date Testing Company Representative / Date 

## 10-188 Entergy Gerald Andrus 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 32

### 10-188 Entergy Gerald Andrus

Facility Information: ENTERY MS, GERALD ANDRUS PLAN
HIGHWAY 82 WEST

GREENVILLE MS 38701 Contact: TAD CHENET
Phone: 281-297-3313
Fax: 281-297-3251
Email: tchenet@entergy.com Testing Company:
METCO ENVIRONMENTAL
3226 COMMANDER BLAVD.

CARROLLTON TX 75006 Contact: NED SHAPPLEY
Phone: 972-931-7127
Fax: 972-931-8398
Email: NSHAPPLEY@METCOENV.COM

Air Permit Number: 2800-00048 Permitted Source ID/Name: UNIT NUMBER 1 STACK AA-001
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 #: 110000375781 FRS #: 110000375781

SCC / Description 10102101 External Combustion Boilers - Electric Generation - Other Oil - All

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 276.063 2364 2244 4 276.063 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 2,3,7,8-TCDD Method 23 3 480 0 Stack Exit 1,2,3,7,8-PeCDD Method 23 3 480 0 Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 480 0 Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 480 0 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



### Friday, February 11, 2011 Page 2 of 32

### 10-188 Entergy Gerald Andrus

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 3 480 0 Stack Exit Other PeCDD Method 23 3 480 0 Stack Exit Other HxCDD Method 23 3 480 0 Stack Exit Other HpCDD Method 23 3 480 0 Stack Exit Other TCDF Method 23 3 480 0 Stack Exit Other PeCDF Method 23 3 480 0 Stack Exit Other HxCDF Method 23 3 480 0 Stack Exit Other HpCDF Method 23 3 480 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 Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Filterable Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Organic Condensible

Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit



### Friday, February 11, 2011 Page 3 of 32

### 10-188 Entergy Gerald Andrus

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. Method 26A was modified to collect HCN with the HCL and HF.The concentration of the sodium hydroxide solution used was increased from 0.1 N to 6N , an additional impinger containing sodium hydroxide was added to the train (three impingers instead of two), the pH of the impinger solutions was monitored periodically throughout the sample run. This modification was addressed on the Uticility ICR website in the Frequently Asked Questions area (Question Test-025). At the time of testing, this modification was still approved.

Total Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Nickel Method 29 3 240 0 Stack Exit Antimony Method 29 3 240 0 Stack Exit Arsenic Method 29 3 240 0 Stack Exit 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 Mercury Method 29 3 240 0 Stack Exit Selenium Method 29 3 240 0 Stack Exit Phosphorus (yellow or white) Method 29 3 240 0 Stack Exit Cobalt Method 29 3 240 0 Stack Exit Manganese Method 29 3 240 0 Stack Exit Co2 Method 3A CO2 3 480 0 Stack Exit O2 Method 3A O2 3 480 0 Stack Exit Sulfur Dioxide Method 6C 3 180 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### Friday, February 11, 2011 Page 4 of 32

### 10-188 Entergy Gerald Andrus

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 23 Average Run Number 1 3 4
Test Date 5/4/2010 5/5/2010 5/6/2010
Run Start Time 10:05:00 AM 12:18:00 AM 10:10:00 AM

Run Finish Time 7:25:00 PM 11:50:00 PM 8:25:00 PM

Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 309.707 259.755 305.324 291.595 Moisture Content of Stack Gas, % 6.30 7.13 6.87 6.767 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 9 9.9 10.1 9.667 Oxygen, % 8.5 8.6 8.6 8.567 Average Stack Gas Temperature, °F 283.69 290.43 295.79 289.970 Dry Volumetric Flow Rate, dry scfm 1,317,342.9 1,199,694.2 1,285,099.7 1,267,378.93 3 Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,013,892.1 1,869,739.8 2,010,151.1 1,964,594.33 3 Percent Isokinetic of Sampling Rate, % 103.4 95.2 104.5 101.033 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Friday, February 11, 2011 Page 5 of 32

### 10-188 Entergy Gerald Andrus

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 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



### Friday, February 11, 2011 Page 6 of 32

### 10-188 Entergy Gerald Andrus

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 11, 2011 Page 7 of 32

### 10-188 Entergy Gerald Andrus

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 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



### Friday, February 11, 2011 Page 8 of 32

### 10-188 Entergy Gerald Andrus

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 9 of 32

### 10-188 Entergy Gerald Andrus

Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run 1 3 4 Elb/hr -2.86E+01 0.00E+00 0.00E+00 -9.533 lb/mmBtuO2 -5.54E-03 0.00E+00 0.00E+00 -0.002 ppm -5.09E+00 0.00E+00 0.00E+00 -1.697 ppm@7%O2 -5.52E+00 0.00E+00 0.00E+00 -1.840



### Location: Stack Exit - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 3 4 Mass_mg 0.0000000022 0.0000000029 0.0000000028 0.000 lb/mmBtuO2 2.43E-13 3.84E-13 3.16E-13 0.000 ng/dscm 2.51E-04 3.94E-04 3.24E-04 0.000 ng/dscm@7%O2 2.81E-04 4.45E-04 3.66E-04 0.000


### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 3 4 Mass_mg 0.0000000058 0.0000000029 0.0000000018 0.000 lb/mmBtuO2 6.40E-13 3.84E-13 2.03E-13 0.000 ng/dscm 6.61E-04 3.94E-04 2.08E-04 0.000 ng/dscm@7%O2 7.41E-04 4.45E-04 2.35E-04 0.000


### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 3 4 Mass_mg 0.0000000026 0.0000000028 0.0000000015 0.000 lb/mmBtuO2 2.87E-13 3.71E-13 1.69E-13 0.000 ng/dscm 2.97E-04 3.81E-04 1.74E-04 0.000 ng/dscm@7%O2 3.33E-04 4.31E-04 1.97E-04 0.000


### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 3 4 Mass_mg 0.0000000022 0.0000000021 0.0000000013 0.000 lb/mmBtuO2 2.43E-13 2.78E-13 1.47E-13 0.000 ng/dscm 2.51E-04 2.86E-04 1.50E-04 0.000 ng/dscm@7%O2 2.81E-04 3.23E-04 1.70E-04 0.000


### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 3 4 Mass_mg 0.0000000034 0.0000000053 0.0000000031 0.000 lb/mmBtuO2 3.75E-13 7.02E-13 3.50E-13 0.000 ng/dscm 3.88E-04 7.21E-04 3.59E-04 0.000 ng/dscm@7%O2 4.35E-04 8.15E-04 4.06E-04 0.001



### Friday, February 11, 2011 Page 10 of 32

### 10-188 Entergy Gerald Andrus

Compound: 1,2,3,6,7,8-HxCDD Average RunNumber 1 3 4 Mass_mg 0.0000000022 0.000000002 0.0000000012 0.000 lb/mmBtuO2 2.43E-13 2.65E-13 1.35E-13 0.000 ng/dscm 2.51E-04 2.72E-04 1.39E-04 0.000 ng/dscm@7%O2 2.81E-04 3.07E-04 1.57E-04 0.000


### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber 1 3 4 Mass_mg 0.0000000013 0.0000000013 0.00000000076 0.000 lb/mmBtuO2 1.43E-13 1.72E-13 8.57E-14 0.000 ng/dscm 1.48E-04 1.77E-04 8.79E-05 0.000 ng/dscm@7%O2 1.66E-04 2.00E-04 9.93E-05 0.000


### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 3 4 Mass_mg 0.000000016 0.0000000076 0.0000000013 0.000 lb/mmBtuO2 1.76E-12 1.01E-12 1.47E-13 0.000 ng/dscm 1.82E-03 1.03E-03 1.50E-04 0.001 ng/dscm@7%O2 2.04E-03 1.16E-03 1.70E-04 0.001


### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 3 4 Mass_mg 0.0000000014 0.0000000014 0.00000000081 0.000 lb/mmBtuO2 1.54E-13 1.86E-13 9.13E-14 0.000 ng/dscm 1.60E-04 1.90E-04 9.37E-05 0.000 ng/dscm@7%O2 1.79E-04 2.15E-04 1.06E-04 0.000


### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 3 4 Mass_mg 0.0000000022 0.0000000024 0.0000000015 0.000 lb/mmBtuO2 2.43E-13 3.18E-13 1.69E-13 0.000 ng/dscm 2.51E-04 3.26E-04 1.74E-04 0.000 ng/dscm@7%O2 2.81E-04 3.68E-04 1.97E-04 0.000


### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 3 4 Mass_mg 0.0000000017 0.0000000023 0.0000000021 0.000 lb/mmBtuO2 1.87E-13 3.05E-13 2.37E-13 0.000 ng/dscm 1.94E-04 3.13E-04 2.43E-04 0.000 ng/dscm@7%O2 2.17E-04 3.54E-04 2.75E-04 0.000


### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 1 3 4 Mass_mg 0.0000001105 0.0000002431 0.0000001051 0.000 lb/mmBtuO2 1.22E-11 3.22E-11 1.19E-11 0.000



### Friday, February 11, 2011 Page 11 of 32

### 10-188 Entergy Gerald Andrus

ng/dscm 1.26E-02 3.31E-02 1.22E-02 0.019 ng/dscm@7%O2 1.41E-02 3.74E-02 1.38E-02 0.022


### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 1 3 4 Mass_mg 0.0000004118 0.0000007122 0.0000003436 0.000 lb/mmBtuO2 4.54E-11 9.44E-11 3.87E-11 0.000 ng/dscm 4.70E-02 9.68E-02 3.97E-02 0.061 ng/dscm@7%O2 5.27E-02 1.09E-01 4.49E-02 0.069


### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber 1 3 4 Mass_mg 0.0000002437 0.0000003569 0.000001523 0.000 lb/mmBtuO2 2.69E-11 4.73E-11 1.72E-10 0.000 ng/dscm 2.78E-02 4.85E-02 1.76E-01 0.084 ng/dscm@7%O2 3.12E-02 5.48E-02 1.99E-01 0.095


### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 1 3 4 Mass_mg 0.0000001086 0.0000002204 0.0000000966 0.000 lb/mmBtuO2 1.20E-11 2.92E-11 1.09E-11 0.000 ng/dscm 1.24E-02 3.00E-02 1.12E-02 0.018 ng/dscm@7%O2 1.39E-02 3.39E-02 1.27E-02 0.020


### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber 1 3 4 Mass_mg 0.0000001246 0.000000217 0.000000137 0.000 lb/mmBtuO2 1.37E-11 2.88E-11 1.54E-11 0.000 ng/dscm 1.42E-02 2.95E-02 1.58E-02 0.020 ng/dscm@7%O2 1.59E-02 3.33E-02 1.79E-02 0.022


### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber 1 3 4 Mass_mg 0.000001838 0.000001658 0.000002697 0.000 lb/mmBtuO2 2.03E-10 2.20E-10 3.04E-10 0.000 ng/dscm 2.10E-01 2.25E-01 3.12E-01 0.249 ng/dscm@7%O2 2.35E-01 2.54E-01 3.53E-01 0.281


### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber 1 3 4 Mass_mg 0.0000001278 0.0000002435 0.0000001579 0.000 lb/mmBtuO2 1.41E-11 3.23E-11 1.78E-11 0.000 ng/dscm 1.46E-02 3.31E-02 1.83E-02 0.022 ng/dscm@7%O2 1.64E-02 3.74E-02 2.07E-02 0.025


### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber 1 3 4



### Friday, February 11, 2011 Page 12 of 32

### 10-188 Entergy Gerald Andrus

Mass_mg 0.0000000016 0.0000000016 0.00000000093 0.000 lb/mmBtuO2 1.76E-13 2.12E-13 1.05E-13 0.000 ng/dscm 1.82E-04 2.18E-04 1.08E-04 0.000 ng/dscm@7%O2 2.04E-04 2.46E-04 1.22E-04 0.000


### Compound: 2,3,4,7,8-PeCDF Average RunNumber 1 3 4 Mass_mg 0.0000000026 0.0000000023 0.0000000027 0.000 lb/mmBtuO2 2.87E-13 3.05E-13 3.04E-13 0.000 ng/dscm 2.97E-04 3.13E-04 3.12E-04 0.000 ng/dscm@7%O2 3.33E-04 3.54E-04 3.53E-04 0.000


### Compound: 2,3,7,8-TCDD Average RunNumber 1 3 4 Mass_mg 0.0000000036 0.0000000048 0.0000000026 0.000 lb/mmBtuO2 3.97E-13 6.36E-13 2.93E-13 0.000 ng/dscm 4.11E-04 6.53E-04 3.01E-04 0.000 ng/dscm@7%O2 4.61E-04 7.38E-04 3.40E-04 0.001


### Compound: 2,3,7,8-TCDF Average RunNumber 1 3 4 Mass_mg 0.0000000061 0.0000000095 0.0000000043 0.000 lb/mmBtuO2 6.73E-13 1.26E-12 4.85E-13 0.000 ng/dscm 6.96E-04 1.29E-03 4.97E-04 0.001 ng/dscm@7%O2 7.80E-04 1.46E-03 5.62E-04 0.001


### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 1 3 4 Mass_mg 0.0000001233 0.0000002212 0.0000001272 0.000 lb/mmBtuO2 1.36E-11 2.93E-11 1.43E-11 0.000 ng/dscm 1.41E-02 3.01E-02 1.47E-02 0.020 ng/dscm@7%O2 1.58E-02 3.40E-02 1.66E-02 0.022


### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber 1 3 4 Mass_mg 0.0000001366 0.0000002432 0.0000001578 0.000 lb/mmBtuO2 1.51E-11 3.22E-11 1.78E-11 0.000 ng/dscm 1.56E-02 3.31E-02 1.83E-02 0.022 ng/dscm@7%O2 1.75E-02 3.74E-02 2.07E-02 0.025


### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber 1 3 4 Mass_mg 0.0000001988 0.0000002846 0.000003423 0.000 lb/mmBtuO2 2.19E-11 3.77E-11 3.86E-10 0.000 ng/dscm 2.27E-02 3.87E-02 3.96E-01 0.152 ng/dscm@7%O2 2.54E-02 4.37E-02 4.48E-01 0.172



### Friday, February 11, 2011 Page 13 of 32

### 10-188 Entergy Gerald Andrus

Compound: 3,4,4',5-TCB (PCB81) Average RunNumber 1 3 4 Mass_mg 0.0000001364 0.0000002845 0.0000002505 0.000 lb/mmBtuO2 1.50E-11 3.77E-11 2.82E-11 0.000 ng/dscm 1.56E-02 3.87E-02 2.90E-02 0.028 ng/dscm@7%O2 1.75E-02 4.37E-02 3.28E-02 0.031


### Compound: OCDD Average RunNumber 1 3 4 Mass_mg 0.0000000066 0.000000012 0.0000000075 0.000 lb/mmBtuO2 7.28E-13 1.59E-12 8.46E-13 0.000 ng/dscm 7.53E-04 1.63E-03 8.68E-04 0.001 ng/dscm@7%O2 8.44E-04 1.84E-03 9.81E-04 0.001


### Compound: OCDF Average RunNumber 1 3 4 Mass_mg 0.0000000093 0.00000001 0.0000000037 0.000 lb/mmBtuO2 1.03E-12 1.33E-12 4.17E-13 0.000 ng/dscm 1.06E-03 1.36E-03 4.28E-04 0.001 ng/dscm@7%O2 1.19E-03 1.54E-03 4.84E-04 0.001


### Compound: Other HpCDD Average RunNumber 1 3 4 Mass_mg 0.0000000022 0.0000000029 0.0000000028 0.000 lb/mmBtuO2 2.43E-13 3.84E-13 3.16E-13 0.000 ng/dscm 2.51E-04 3.94E-04 3.24E-04 0.000 ng/dscm@7%O2 2.81E-04 4.45E-04 3.66E-04 0.000


### Compound: Other HpCDF Average RunNumber 1 3 4 Mass_mg 0.0000000084 0.0000000029 0.0000000018 0.000 lb/mmBtuO2 9.26E-13 3.84E-13 2.03E-13 0.000 ng/dscm 9.58E-04 3.94E-04 2.08E-04 0.001 ng/dscm@7%O2 1.07E-03 4.45E-04 2.35E-04 0.001


### Compound: Other HxCDD Average RunNumber 1 3 4 Mass_mg 0.000000016 0.000000001 0.00000002 0.000 lb/mmBtuO2 1.76E-12 1.33E-13 2.26E-12 0.000 ng/dscm 1.82E-03 1.36E-04 2.31E-03 0.001 ng/dscm@7%O2 2.04E-03 1.54E-04 2.61E-03 0.002


### Compound: Other HxCDF Average RunNumber 1 3 4 Mass_mg 0.000000011 0.000000012 0.000000018 0.000 lb/mmBtuO2 1.21E-12 1.59E-12 2.03E-12 0.000



### Friday, February 11, 2011 Page 14 of 32

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ng/dscm 1.25E-03 1.63E-03 2.08E-03 0.002 ng/dscm@7%O2 1.40E-03 1.84E-03 2.35E-03 0.002


### Compound: Other PeCDD Average RunNumber 1 3 4 Mass_mg 0.0000000041 0.0000000081 0.0000000051 0.000 lb/mmBtuO2 4.52E-13 1.07E-12 5.75E-13 0.000 ng/dscm 4.68E-04 1.10E-03 5.90E-04 0.001 ng/dscm@7%O2 5.25E-04 1.24E-03 6.67E-04 0.001


### Compound: Other PeCDF Average RunNumber 1 3 4 Mass_mg 0.000000027 0.000000026 0.000000024 0.000 lb/mmBtuO2 2.98E-12 3.45E-12 2.71E-12 0.000 ng/dscm 3.08E-03 3.54E-03 2.78E-03 0.003 ng/dscm@7%O2 3.45E-03 4.00E-03 3.14E-03 0.004


### Compound: Other TCDD Average RunNumber 1 3 4 Mass_mg 0.00000065 0.0000022 0.00000004 0.000 lb/mmBtuO2 7.17E-11 2.92E-10 4.51E-12 0.000 ng/dscm 7.41E-02 2.99E-01 4.63E-03 0.126 ng/dscm@7%O2 8.31E-02 3.38E-01 5.23E-03 0.142


### Compound: Other TCDF Average RunNumber 1 3 4 Mass_mg 0.00000011 0.00000038 0.000000031 0.000 lb/mmBtuO2 1.21E-11 5.04E-11 3.50E-12 0.000 ng/dscm 1.25E-02 5.17E-02 3.59E-03 0.023 ng/dscm@7%O2 1.40E-02 5.84E-02 4.06E-03 0.025


### Compound: Total Dioxins Average RunNumber 1 3 4 Mass_mg 0.0000006789 0.000002224 0.0000000754 0.000 lb/mmBtuO2 7.49E-11 2.95E-10 8.50E-12 0.000 ng/dscm 7.74E-02 3.02E-01 8.72E-03 0.129 ng/dscm@7%O2 8.68E-02 3.41E-01 9.85E-03 0.146


### Compound: Total Furans Average RunNumber 1 3 4 Mass_mg 0.0000001657 0.0000004309 0.0000000785 0.000 lb/mmBtuO2 1.83E-11 5.71E-11 8.85E-12 0.000 ng/dscm 1.89E-02 5.86E-02 9.08E-03 0.029 ng/dscm@7%O2 2.12E-02 6.62E-02 1.03E-02 0.033



### Location: Stack Exit - Method 25A



### Friday, February 11, 2011 Page 15 of 32

### 10-188 Entergy Gerald Andrus

Compound: Total organic compounds (TOC) as Average Run 1 3 4 Elb/hr 2.55E+00 6.62E-01 1.58E+00 1.597 lb/mmBtuO2 4.94E-04 1.36E-04 3.10E-04 0.000 ppm 2.88E-01 7.56E-02 1.73E-01 0.179 ppm@7%O2 3.12E-01 8.62E-02 1.96E-01 0.198



### Location: Stack Exit - Method 29 

### Compound: Antimony Average RunNumber 1 3 4 Mass_mg 0.4323 0.3172 0.4547 0.401 Elb/hr 5.42E-01 3.78E-01 5.30E-01 0.483 lb/mmBtuO2 1.10E-04 7.36E-05 1.11E-04 0.000 mg/dscm 1.14E-01 7.55E-02 1.14E-01 0.101 mg/dscm@7%O2 1.28E-01 8.53E-02 1.29E-01 0.114


### Compound: Arsenic Average RunNumber 1 3 4 Mass_mg 0.0173 0.01323 0.0178 0.016 Elb/hr 2.17E-02 1.58E-02 2.08E-02 0.019 lb/mmBtuO2 4.41E-06 3.07E-06 4.33E-06 0.000 mg/dscm 4.56E-03 3.15E-03 4.45E-03 0.004 mg/dscm@7%O2 5.11E-03 3.56E-03 5.03E-03 0.005


### Compound: Beryllium Average RunNumber 1 3 4 Mass_mg 0.001 0.001 0.001 0.001 Elb/hr 1.25E-03 1.19E-03 1.17E-03 0.001 lb/mmBtuO2 2.55E-07 2.32E-07 2.44E-07 0.000 mg/dscm 2.64E-04 2.38E-04 2.50E-04 0.000 mg/dscm@7%O2 2.96E-04 2.69E-04 2.83E-04 0.000


### Compound: Cadmium Average RunNumber 1 3 4 Mass_mg 0.00121 0.00107 0.00107 0.001 Elb/hr 1.52E-03 1.27E-03 1.25E-03 0.001 lb/mmBtuO2 3.08E-07 2.48E-07 2.61E-07 0.000 mg/dscm 3.19E-04 2.55E-04 2.67E-04 0.000 mg/dscm@7%O2 3.58E-04 2.88E-04 3.02E-04 0.000


### Compound: Chromium Average RunNumber 1 3 4 Mass_mg 0.02939 0.02739 0.06852 0.042 Elb/hr 3.68E-02 3.26E-02 7.99E-02 0.050 lb/mmBtuO2 7.49E-06 6.35E-06 1.67E-05 0.000 mg/dscm 7.75E-03 6.52E-03 1.71E-02 0.010 mg/dscm@7%O2 8.69E-03 7.37E-03 1.93E-02 0.012



### Friday, February 11, 2011 Page 16 of 32

### 10-188 Entergy Gerald Andrus

Compound: Cobalt Average RunNumber 1 3 4 Mass_mg 0.0612 0.0452 0.0694 0.059 Elb/hr 7.67E-02 5.39E-02 8.09E-02 0.071 lb/mmBtuO2 1.56E-05 1.05E-05 1.69E-05 0.000 mg/dscm 1.61E-02 1.08E-02 1.73E-02 0.015 mg/dscm@7%O2 1.80E-02 1.22E-02 1.96E-02 0.017


### Compound: Filterable Particulate Average RunNumber 1 3 4 Mass_mg 188.5 124 197.5 170.000 Elb/hr 2.36E+02 1.48E+02 2.30E+02 204.667 lb/mmBtuO2 4.80E-02 2.88E-02 4.81E-02 0.042 mg/dscm 4.97E+01 2.95E+01 4.93E+01 42.833 mg/dscm@7%O2 5.57E+01 3.33E+01 5.57E+01 48.233


### Compound: Lead Average RunNumber 1 3 4 Mass_mg 0.0456 0.0344 0.05674 0.046 Elb/hr 5.72E-02 4.10E-02 6.61E-02 0.055 lb/mmBtuO2 1.16E-05 7.98E-06 1.38E-05 0.000 mg/dscm 1.20E-02 8.19E-03 1.42E-02 0.011 mg/dscm@7%O2 1.35E-02 9.26E-03 1.60E-02 0.013


### Compound: Manganese Average RunNumber 1 3 4 Mass_mg 0.05198 0.0371 0.06288 0.051 Elb/hr 6.52E-02 4.42E-02 7.33E-02 0.061 lb/mmBtuO2 1.32E-05 8.60E-06 1.53E-05 0.000 mg/dscm 1.37E-02 8.83E-03 1.57E-02 0.013 mg/dscm@7%O2 1.54E-02 9.98E-03 1.77E-02 0.014


### Compound: Mercury Average RunNumber 1 3 4 Mass_mg 0.00153 0.00086 0.00113 0.001 Elb/hr 1.92E-03 1.02E-03 1.32E-03 0.001 lb/mmBtuO2 3.90E-07 1.99E-07 2.75E-07 0.000 mg/dscm 4.03E-04 2.05E-04 2.82E-04 0.000 mg/dscm@7%O2 4.52E-04 2.32E-04 3.19E-04 0.000


### Compound: Nickel Average RunNumber 1 3 4 Mass_mg 1.046 0.8394 1.2088 1.031 Elb/hr 1.31E+00 1.00E+00 1.41E+00 1.240 lb/mmBtuO2 2.67E-04 1.95E-04 2.94E-04 0.000 mg/dscm 2.76E-01 2.00E-01 3.02E-01 0.259 mg/dscm@7%O2 3.09E-01 2.26E-01 3.41E-01 0.292



### Friday, February 11, 2011 Page 17 of 32

### 10-188 Entergy Gerald Andrus

Compound: Phosphorus (yellow or white) Average RunNumber 1 3 4 Mass_mg 0.45196 0.38616 0.50125 0.446 Elb/hr 5.67E-01 4.60E-01 5.84E-01 0.537 lb/mmBtuO2 1.15E-04 8.96E-05 1.22E-04 0.000 mg/dscm 1.19E-01 9.19E-02 1.25E-01 0.112 mg/dscm@7%O2 1.33E-01 1.04E-01 1.41E-01 0.126


### Compound: Selenium Average RunNumber 1 3 4 Mass_mg 0.0082 0.0053 0.0069 0.007 Elb/hr 1.03E-02 6.31E-03 8.04E-03 0.008 lb/mmBtuO2 2.09E-06 1.23E-06 1.68E-06 0.000 mg/dscm 2.16E-03 1.26E-03 1.72E-03 0.002 mg/dscm@7%O2 2.42E-03 1.42E-03 1.94E-03 0.002



### Location: Stack Exit - Method 6C Compound: Sulfur Dioxide Average Run 1 3 4 Elb/hr 5.22E+03 5.03E+03 5.25E+03 5,166.667 lb/mmBtuO2 1.04E+00 1.03E+00 1.06E+00 1.043 ppm 4.03E+02 3.95E+02 4.09E+02 402.333 ppm@7%O2 4.52E+02 4.47E+02 4.63E+02 454.000



### Location: Stack Exit - Method 7E Compound: Nitrogen oxides (NOx) Average Run 1 3 4 Elb/hr 2.54E+03 2.66E+03 2.78E+03 2,660.000 lb/mmBtuO2 5.06E-01 5.42E-01 5.74E-01 0.541 ppm 2.73E+02 2.90E+02 3.02E+02 288.333 ppm@7%O2 3.07E+02 3.28E+02 3.49E+02 328.000



### Location: Stack Exit - OTM - 27/28 Compound: Filterable Particulate Average RunNumber 1 3 4 Mass_mg 112.1 124.7 143.8 126.867 Elb/hr 1.46E+02 1.79E+02 1.91E+02 172.000 gr/dscf 1.31E-02 1.61E-02 1.70E-02 0.015 lb/mmBtuO2 2.90E-02 3.60E-02 3.78E-02 0.034


### Compound: Filterable PM2.5 Average RunNumber 1 3 4 Mass_mg 62 123.1 142.1 109.067 Elb/hr 8.07E+01 1.76E+02 1.89E+02 148.567 gr/dscf 7.24E-03 1.59E-02 1.68E-02 0.013



### Friday, February 11, 2011 Page 18 of 32

### 10-188 Entergy Gerald Andrus

Process Run Data lb/mmBtuO2 1.60E-02 3.56E-02 3.74E-02 0.030


### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 3 4 Mass_mg 85.4 126.2 132.9 114.833 Elb/hr 1.11E+02 1.81E+02 1.77E+02 156.333 gr/dscf 9.97E-03 1.63E-02 1.57E-02 0.014 lb/mmBtuO2 2.21E-02 3.65E-02 3.49E-02 0.031


### Compound: Organic Condensible Particulate Average RunNumber 1 3 4 Mass_mg 11.7 24.1 28 21.267 Elb/hr 1.52E+01 3.45E+01 3.73E+01 29.000 gr/dscf 1.37E-03 3.12E-03 3.30E-03 0.003 lb/mmBtuO2 3.02E-03 6.96E-03 7.36E-03 0.006


### Compound: Total Particulate Average RunNumber 1 3 4 Mass_mg 207.2 273 302.7 260.967 Elb/hr 2.70E+02 3.91E+02 4.03E+02 354.667 gr/dscf 2.42E-02 3.53E-02 3.57E-02 0.032 lb/mmBtuO2 5.36E-02 7.89E-02 7.96E-02 0.071


### Compound: Total PM2.5 Average RunNumber 1 3 4 Mass_mg 157.1 271.4 301 243.167 Elb/hr 2.04E+02 3.89E+02 4.01E+02 331.333 gr/dscf 1.83E-02 3.51E-02 3.55E-02 0.030 lb/mmBtuO2 4.06E-02 7.84E-02 7.92E-02 0.066



### Friday, February 11, 2011 Page 19 of 32

### 10-188 Entergy Gerald Andrus

Process Run Data



### Run Name Value UOM Comments Target Value 1 Average Heat Input 4699 MMBtu/hr RUN 1 0


### 2 Average Heat Input 0 MMBtu/hr 0
3 Average Heat Input 0 MMBtu/hr 0
2 Steam Output 0 1000 lb steam/hr 0


### 3 Steam Output 0 1000 lb steam/hr 0
1 Fuel Oil Firing Rate 30428 gal/hr RUN 1 0
2 Fuel Oil Firing Rate 0 gal/hr 0


### 3 Fuel Oil Firing Rate 0 gal/hr 0
1 Flue Gas Flow Rate 1E+06 RUN 1 0
1 Flue Gas Oxygen Content 8.52 % RUN 1 0


### 1 Flue Gas Carbon Dioxide Content 9.02 % RUN 1 0
1 Flue Gas Moisture Content 5.83 % RUN 1 0
1 Flue Gas Sampling Point Temperature 280 Deg F RUN 1 0


### 1 Flue Gas Pressure 29.43 "Hg RUN 1 0
1 Standard Pressure 29.92 "Hg RUN 1 0
1 Standard Temperature 68 Deg F RUN 1 0


### 1 Unit Gross Electrical Output 529 Mwe RUN 1 0
1 Unit Net Electric Generation 510 MWh RUN 1 0
4 Average Heat Input 4726 MMBtu/hr RUN 3 0


### 4 Fuel Oil Firing Rate 30607 gal/hr RUN 3 0
4 Flue Gas Flow Rate 1E+06 RUN 3,DSCFM 0
4 Flue Gas Oxygen Content 8.62 % RUN 3 0


### 4 Flue Gas Carbon Dioxide Content 9.94 % RUN 3 0
4 Flue Gas Moisture Content 7.45 % RUN 3 0


### 4 Flue Gas Sampling Point Temperature 285 Deg F RUN 3 0
4 Flue Gas Pressure 29.38 "Hg RUN 3 0
4 Standard Pressure 29.92 "Hg RUN 3 0


### 4 Standard Temperature 68 Deg F RUN 3 0
4 Unit Gross Electrical Output 530 Mwe RUN 3 0
4 Unit Net Electric Generation 510 MWh RUN 3 0


### 5 Average Heat Input 4718 MMBtu/hr RUN 4 0
5 Fuel Oil Firing Rate 30560 gal/hr RUN 4 0
5 Flue Gas Flow Rate 1E+06 RUN 4,SCFM 0



### Friday, February 11, 2011 Page 20 of 32

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APCD Run Data

Process Lab Run Data 5 Flue Gas Oxygen Content 8.63 % RUN 4 0


### 5 Flue Gas Carbon Dioxide Content 10.06 % RUN 4 0
5 Flue Gas Moisture Content 6.85 % RUN 4 0
5 Flue Gas Sampling Point Temperature 293 Deg F RUN 4 0


### 5 Flue Gas Pressure 29.39 "Hg RUN 4 0
5 Standard Pressure 29.92 "Hg RUN 4 0
5 Standard Temperature 68 Deg F RUN 4 0


### 5 Unit Gross Electrical Output 530 Mwe RUN 4 0
5 Unit Net Electric Generation 510 MWh RUN 4 0



### Run Name Value UOM Comments 1 Fuel Higher Heating Value 17700 Btu/lb 

### 1 Fuel Moisture 0.283 % 1 Fuel Mercury Content 0.03 ppm 1 Fuel Cadmium Content 0.5 ppm 

### 1 Fuel Nickel Content 4.3 ppm 1 Fuel Arsenic Content 2 ppm 1 Fuel Chromium Content 1.5 ppm 1 Fuel Beryllium Content 1 ppm 

### 1 Fuel Lead Content 0.37 ppm 1 Fuel Manganese Content 1.5 ppm 1 Fuel Chlorine Content 266 ppm 

### 1 Fuel Fluorine Content 200 ppm 1 Fuel Antimony Content 6 ppm 1 Fuel Cobalt Content 0.26 ppm 1 Fuel Phosphorous Content 6 ppm 

### 2 Fuel Higher Heating Value 17800 Btu/lb 2 Fuel Moisture 0.124 % 2 Fuel Mercury Content 0.03 ppm 

### 2 Fuel Cadmium Content 0.49 ppm 2 Fuel Nickel Content 4.4 ppm 2 Fuel Arsenic Content 2 ppm 2 Fuel Chromium Content 1.5 ppm 

### 2 Fuel Beryllium Content 0.98 ppm 2 Fuel Lead Content 0.45 ppm 2 Fuel Manganese Content 0.21 ppm



### Friday, February 11, 2011 Page 21 of 32

### 10-188 Entergy Gerald Andrus

2 Fuel Chlorine Content 264 ppm 

### 2 Fuel Fluorine Content 198 ppm 2 Fuel Antimony Content 5.9 ppm 2 Fuel Cobalt Content 0.23 ppm 2 Fuel Phosphorous Content 5.8 ppm 

### 3 Fuel Higher Heating Value 17800 Btu/lb 3 Fuel Moisture 0.272 % 3 Fuel Mercury Content 0.031 ppm 

### 3 Fuel Cadmium Content 0.48 ppm 3 Fuel Nickel Content 4.4 ppm 3 Fuel Arsenic Content 1.9 ppm 3 Fuel Chromium Content 1.4 ppm 

### 3 Fuel Beryllium Content 0.96 ppm 3 Fuel Lead Content 0.42 ppm 3 Fuel Manganese Content 1.4 ppm 

### 3 Fuel Chlorine Content 262 ppm 3 Fuel Fluorine Content 196 ppm 3 Fuel Antimony Content 5.8 ppm 3 Fuel Cobalt Content 0.3 ppm 

### 3 Fuel Phosphorous Content 6 ppm 4 Fuel Higher Heating Value 17700 Btu/lb 4 Fuel Moisture 0.216 % 

### 4 Fuel Mercury Content 0.029 ppm 4 Fuel Cadmium Content 0.46 ppm 4 Fuel Nickel Content 4.5 ppm 4 Fuel Arsenic Content 1.9 ppm 

### 4 Fuel Chromium Content 0.37 ppm 4 Fuel Beryllium Content 0.93 ppm 4 Fuel Lead Content 0.36 ppm 

### 4 Fuel Manganese Content 0.58 ppm 4 Fuel Chlorine Content 110 ppm 4 Fuel Fluorine Content 196 ppm 4 Fuel Antimony Content 5.6 ppm 

### 4 Fuel Cobalt Content 0.25 ppm 4 Fuel Phosphorous Content 5.8 ppm 5 Fuel Higher Heating Value 17800 Btu/lb 

### 5 Fuel Moisture 0.325 % 5 Fuel Mercury Content 0.033 ppm 5 Fuel Cadmium Content 0.44 ppm 5 Fuel Nickel Content 4.5 ppm 

### 5 Fuel Arsenic Content 0.33 ppm 5 Fuel Chromium Content 1.3 ppm 5 Fuel Beryllium Content 0.88 ppm



### Friday, February 11, 2011 Page 22 of 32

### 10-188 Entergy Gerald Andrus

5 Fuel Lead Content 0.47 ppm 

### 5 Fuel Manganese Content 0.58 ppm 5 Fuel Chlorine Content 262 ppm 5 Fuel Fluorine Content 196 ppm 5 Fuel Antimony Content 0.99 ppm 

### 5 Fuel Cobalt Content 0.25 ppm 5 Fuel Phosphorous Content 6.1 ppm 6 Fuel Higher Heating Value 17800 Btu/lb 

### 6 Fuel Moisture 0.114 % 6 Fuel Mercury Content 0.029 ppm 6 Fuel Cadmium Content 0.5 ppm 6 Fuel Nickel Content 4.3 ppm 

### 6 Fuel Arsenic Content 2 ppm 6 Fuel Chromium Content 1.5 ppm 6 Fuel Beryllium Content 1 ppm 

### 6 Fuel Lead Content 0.42 ppm 6 Fuel Manganese Content 0.93 ppm 6 Fuel Chlorine Content 264 ppm 6 Fuel Fluorine Content 198 ppm 

### 6 Fuel Antimony Content 6 ppm 6 Fuel Cobalt Content 0.24 ppm 6 Fuel Phosphorous Content 6.1 ppm



### Friday, February 11, 2011 Page 23 of 32

### 10-188 Entergy Gerald Andrus

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 24 of 32

### 10-188 Entergy Gerald Andrus

Location Stack Exit - Method 23 Average Run Number 1 3 4 Test Date 5/4/2010 5/5/2010 5/6/2010 Run Start Time 10:05:00 AM 12:18:00 AM 10:10:00 AM Run Finish Time 7:25:00 PM 11:50:00 PM 8:25:00 PM Net Traversing Points 49 50 49 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.19 0.19 0.19 0.190 Pitot Tube Coefficient 0.81 0.81 0.81 0.810 Dry Gas Meter Calibration Factor 1.003 1.003 1.003 1.003 Barometric Pressure, inches of Mercury 29.53 29.49 29.51 29.510 Average Orifice Meter Differential, inches H2O 1.61 1.34 1.64 1.530 Dry Gas Meter Volume Sampled, cubic feet 329.970 280.112 326.735 312.272 Average Dry Gas Meter Temperature, °F 99.11 104.76 101.24 101.703 Dry Gas Meter Volume Sampled, dscf 309.707 259.755 305.324 291.595 Total Moisture Liquid collected, g 442.3 423.8 478.3 448.133 Volume of Water Vapor, standard cubic feet 20.82 19.95 22.51 21.093 Moisture Content of Stack Gas, % 6.30 7.13 6.87 6.767 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.937 0.9287 0.9313 0.932 Carbon Dioxide, % 9 9.9 10.1 9.667 Oxygen, % 8.5 8.6 8.6 8.567 Carbon Monoxide & Nitrogen, % 82.5 81.5 81.3 81.767 Fuel Factor 1.38 1.24 1.22 Dry Molecular Weight, lb/lb-Mole 29.78 29.93 29.96 29.890 Wet Molecular weight, lb/lb-Mole 29.04 29.08 29.14 29.087 Flue Gas Static Pressure, inches of H2O -1.5 -1.5 -1.5 -1.500 Absolute Flue Gas Pressure, inches of Mercury 29.42 29.38 29.40 29.400 Average Stack Gas Temperature, °F 283.69 290.43 295.79 289.970 Average Velocity Head, inches of H2O 1.5620306808 2682 1.334349460

22767 1.535827294

60741 1.477

Average Stack Gas Velocity, feet/second 80.75 74.97 80.60 78.773 Stack Cross-Sectional Area, square feet 415.664 415.664 415.664 415.664 Dry Volumetric Flow Rate, dry scfm 1,317,342.9 1,199,694.2 1,285,099.7 1,267,378.9 33 Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,013,892.1 1,869,739.8 2,010,151.1 1,964,594.3 33 Percent Isokinetic of Sampling Rate, % 103.4 95.2 104.5 101.033 Percent Excess Air, % 64.0 66.6 66.9 65.833 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Round Duct Diameter, inches 276.0625 276.0625 276.0625 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Friday, February 11, 2011 Page 25 of 32

### 10-188 Entergy Gerald Andrus

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 26 of 32

### 10-188 Entergy Gerald Andrus

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



### Friday, February 11, 2011 Page 27 of 32

### 10-188 Entergy Gerald Andrus

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 28 of 32

### 10-188 Entergy Gerald Andrus

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 29 of 32

### 10-188 Entergy Gerald Andrus

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 30 of 32

### 10-188 Entergy Gerald Andrus

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 31 of 32

### 10-188 Entergy Gerald Andrus

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 32 of 32