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:

AA-001 UNIT NUMBER 1 STACK

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 0 0 276.063 2364 2244 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit 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

Friday, February 11, 2011 Page 2 of 32
10-188 Entergy Gerald Andrus

Stack Exit OCDD Method 23 3 480 0

Stack Exit 2,3,7,8-TCDF Method 23 3 480 0

Stack Exit 1,2,3,7,8-PeCDF Method 23 3 480 0

Stack Exit 2,3,4,7,8-PeCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,7,8,9-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

Stack Exit OCDF Method 23 3 480 0

Stack Exit Other TCDD Method 23 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

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Stack Exit Method 23 3 480 0

Stack Exit 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Stack Exit Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

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

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

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
10-188 Entergy Gerald Andrus

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 0 RUN 1

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 0 RUN 1

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 0 RUN 1

1 Flue Gas Oxygen Content 8.52 % 0 RUN 1

1 Flue Gas Carbon Dioxide Content 9.02 % 0 RUN 1

1 Flue Gas Moisture Content 5.83 % 0 RUN 1

1 Flue Gas Sampling Point Temperature 280 Deg F 0 RUN 1

1 Flue Gas Pressure 29.43 "Hg 0 RUN 1

1 Standard Pressure 29.92 "Hg 0 RUN 1

1 Standard Temperature 68 Deg F 0 RUN 1

1 Unit Gross Electrical Output 529 Mwe 0 RUN 1

1 Unit Net Electric Generation 510 MWh 0 RUN 1

4 Average Heat Input 4726 MMBtu/hr 0 RUN 3

4 Fuel Oil Firing Rate 30607 gal/hr 0 RUN 3

4 Flue Gas Flow Rate 1E+06 0 RUN 3,DSCFM

4 Flue Gas Oxygen Content 8.62 % 0 RUN 3

4 Flue Gas Carbon Dioxide Content 9.94 % 0 RUN 3

4 Flue Gas Moisture Content 7.45 % 0 RUN 3

4 Flue Gas Sampling Point Temperature 285 Deg F 0 RUN 3

4 Flue Gas Pressure 29.38 "Hg 0 RUN 3

4 Standard Pressure 29.92 "Hg 0 RUN 3

4 Standard Temperature 68 Deg F 0 RUN 3

4 Unit Gross Electrical Output 530 Mwe 0 RUN 3

4 Unit Net Electric Generation 510 MWh 0 RUN 3

5 Average Heat Input 4718 MMBtu/hr 0 RUN 4

5 Fuel Oil Firing Rate 30560 gal/hr 0 RUN 4

5 Flue Gas Flow Rate 1E+06 0 RUN 4,SCFM

Friday, February 11, 2011 Page 20 of 32
10-188 Entergy Gerald Andrus

APCD Run Data

Process Lab Run Data

5 Flue Gas Oxygen Content 8.63 % 0 RUN 4

5 Flue Gas Carbon Dioxide Content 10.06 % 0 RUN 4

5 Flue Gas Moisture Content 6.85 % 0 RUN 4

5 Flue Gas Sampling Point Temperature 293 Deg F 0 RUN 4

5 Flue Gas Pressure 29.39 "Hg 0 RUN 4

5 Standard Pressure 29.92 "Hg 0 RUN 4

5 Standard Temperature 68 Deg F 0 RUN 4

5 Unit Gross Electrical Output 530 Mwe 0 RUN 4

5 Unit Net Electric Generation 510 MWh 0 RUN 4

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