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:

Boiler ID Unit Number 6

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 0 0 296 2228 2640 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

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 360 0

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

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 360 0

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.

Stack Exit 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

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 23
lb/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 with 

the OTM27/OTM_28 

sampling train

0

1 Flue Gas Oxygen Content 4.88 % Provided by 

METCO 

Environmental, 

data collected with 

the OTM27/OTM_28 

sampling train

0

1 Flue Gas Carbon Dioxide Content 14.78 % Provided by 

METCO 

Environmental, 

data collected with 

the OTM27/OTM_28 

sampling train

0

1 Flue Gas Sampling Point Temperature 332 Deg F Provided by 

METCO 

Environmental, 

data collected with 

the OTM27/OTM_28 

sampling train

0

1 Flue Gas Pressure 29.55 "Hg Provided by 

METCO 

Environmental, 

data collected with 

the OTM27/OTM_28 

sampling train

0

1 Standard Pressure 29.92 "Hg Provided by 

METCO 

Environmental, 

data collected with 

the 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 with 

the 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 with 

the OTM27/OTM_28 

sampling train

0

2 Flue Gas Oxygen Content 5.13 % Provided by 

METCO 

Environmental, 

data collected with 

the OTM27/OTM_28 

sampling train

0

2 Flue Gas Carbon Dioxide Content 14.32 % Provided by 

METCO 

Environmental, 

data collected with 

the OTM27/OTM_28 

sampling train

0

2 Flue Gas Sampling Point Temperature 332 Deg F Provided by 

METCO 

Environmental, 

data collected with 

the OTM27/OTM_28 

sampling train

0

2 Flue Gas Pressure 29.65 "Hg Provided by 

METCO 

Environmental, 

data collected with 

the 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 with 

the OTM27/OTM_28 

sampling train

0

2 Standard Temperature 68 Deg F Provided by 

METCO 

Environmental, 

data collected with 

the 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 with 

the OTM27/OTM_28 

sampling train

0

3 Flue Gas Oxygen Content 4.55 % Provided by 

METCO 

Environmental, 

data collected with 

the OTM27/OTM_28 

sampling train

0

3 Flue Gas Carbon Dioxide Content 14.4 % Provided by 

METCO 

Environmental, 

data collected with 

the OTM27/OTM_28 

sampling train

0

3 Flue Gas Sampling Point Temperature 324 Deg F Provided by 

METCO 

Environmental, 

data collected with 

the 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 with 

the OTM27/OTM_28 

sampling train

0

3 Standard Pressure 29.92 "Hg Provided by 

METCO 

Environmental, 

data collected with 

the OTM27/OTM_28 

sampling train

0

3 Standard Temperature 68 Deg F Provided by 

METCO 

Environmental, 

data collected with 

the 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