Name: Jack Grant

Title: Plant Manager

Company: Vienna Power, LLC

Sign Date: 6/22/2010

Name: Brian Durkop

Title: Vice President

Company: Eagle Mountain Scientific, Inc.

Sign Date: 5/27/2009

Permitted Facility Representative / Date Testing Company Representative / Date

Vienna

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.

Tuesday, February 22, 2011 Page 1 of 33
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Facility Information:

Vienna Power, LLC

Power Plant Road and Chapel of Ease Roa

Vienna MD 21869-0128

Contact: Paul Straub

Phone: 302-934-3683

Fax:

Email: Paul.Straub@nrgenergy.com

Testing Company:

Eagle Mountain Scientific, Inc.

8905 Autumn Oaks Drive

Suite 2

Rockford MN 55373

Contact:Brian Durkop

Phone: 763-477-4462

Fax: 763-477-5991

Email: bdurkop@eagle-msi.com

Air Permit Number:

1564

Permitted Source ID/Name:

8 Unit 8

Permitted Maximum Process Rate:

170 MW

Max. Normal Operation Process Rate:

156 MW

Target Process Test Rate

60 MW

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

Vienna Unit 8 is a fuel oil #6 fired Combustion Engineering tangentially fired, dry bottom electric utility boiler. The 

unit provides steam to a turbine/generator with a maximum gross out put of 156 MW. The unit is equipped with a 

multiclone for dust control.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 2401900013 FRS #: 110000585260

SCC / Description 10100401 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: 

Normal Firing 

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 150.1 0 0 0 564 312 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Naphthalene** SW0010 3 120 0

Stack Exit 2-Methylnaphthalene SW0010 3 120 0

Stack Exit Acenaphthylene** SW0010 3 120 0

Stack Exit Acenaphthene** SW0010 3 120 0

Stack Exit Fluorene** SW0010 3 120 0

Stack Exit Phenanthrene** SW0010 3 120 0

Stack Exit Anthracene** SW0010 3 120 0

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Stack Exit Fluoranthene** SW0010 3 120 0

Stack Exit Pyrene** SW0010 3 120 0

Stack Exit Benzo(a)Anthracene* SW0010 3 120 0

Stack Exit Chrysene* SW0010 3 120 0

Stack Exit Benzo(b)Fluoranthene* SW0010 3 120 0

Stack Exit Benzo(k)Fluoranthene* SW0010 3 120 0

Stack Exit Benzo(e)Pyrene SW0010 3 120 0

Stack Exit Benzo(a)Pyrene* SW0010 3 120 0

Stack Exit Perylene SW0010 3 120 0

Stack Exit Indeno(1,2,3-cd)Pyrene* SW0010 3 120 0

Stack Exit Dibenzo(a,h)Anthracene* SW0010 3 120 0

Stack Exit Benzo(ghi)Perylene** SW0010 3 120 0

Stack Exit Carbon Monoxide Method 10 3 180 0

Stack Exit Formaldehyde Method 0011 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 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 0

Stack Exit Other PeCDD Method 23 0

Stack Exit Other HxCDD Method 23 0

Stack Exit Other HpCDD Method 23 0

Stack Exit Other TCDF Method 23 0

Stack Exit Other PeCDF Method 23 0

Stack Exit Other HxCDF Method 23 0

Stack Exit Other HpCDF Method 23 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

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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.

None

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 Chloride Method 26 3 180 0

Stack Exit Hydrogen Fluoride Method 26 3 180 0

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 240 0

Stack Exit Filterable Particulate OTM - 27/28 3 240 0

Stack Exit Total PM2.5 OTM - 27/28 3 240 0

Stack Exit Total Particulate OTM - 27/28 3 240 0

Stack Exit Filterable PM2.5 OTM - 27/28 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Magnesium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit Co2 Method 3A CO2 3 240 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit Filterable Particulate Method 5/OTM-28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit Method 5/OTM-28 3 240 0

Stack Exit Total Particulate Method 5/OTM-28 3 240 0

Organic Condensible 

Particulate

Stack Exit Method 5/OTM-28 3 240 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0

Tuesday, February 22, 2011 Page 4 of 33
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Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:46:00 AM 1:06:00 PM 4:40:00 PM

Run Finish Time 12:12:00 PM 3:38:00 PM 7:35:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 77.765 76.655 76.015 76.812

Moisture Content of Stack Gas, % 8.30 7.88 7.25 7.810

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Average Stack Gas Temperature, °F 380.77 389.07 381.37 383.737

Dry Volumetric Flow Rate, dry scfm 190,612.7 187,092.5 188,259.8 188,655.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 332,666.2 328,242.4 325,072.0 328,660.200

Percent Isokinetic of Sampling Rate, % 98.4 98.8 97.4 98.200

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:00:00 AM 1:15:00 PM 4:35:00 PM

Run Finish Time 12:00:00 PM 4:15:00 PM 7:35:00 PM

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Moisture, % 0 0 0 0.000

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, February 22, 2011 Page 5 of 33
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Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 2/23/2010 2/23/2010 2/24/2010

Run Start Time 6:47:00 AM 3:44:00 PM 7:56:00 AM

Run Finish Time 3:03:00 PM 11:54:00 

PM

6:26:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 310.054 308.076 319.021 312.384

Moisture Content of Stack Gas, % 8.04 7.93 7.67 7.880

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 11.4 11.5 10.9 11.267

Oxygen, % 6.3 6.4 6.9 6.533

Average Stack Gas Temperature, °F 374.38 377.74 384.49 378.870

Dry Volumetric Flow Rate, dry scfm 183,475.3 181,900.2 187,182.0 184,185.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 318,805.1 316,961.8 326,104.3 320,623.733

Percent Isokinetic of Sampling Rate, % 100.5 100.7 101.3 100.833

F-Factor, dscfm/MMBtu @ %O2 9504 9560 9518 9,527.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:50:00 AM 1:06:00 PM 4:39:00 PM

Run Finish Time 11:50:00 AM 3:06:00 PM 6:39:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 6.9 6.9 6.9 6.900

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Moisture, % 7.7 7.7 7.5 7.633

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, February 22, 2011 Page 6 of 33
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Location Stack Exit - Method 26

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 8:56:00 AM 1:09:00 PM 4:40:00 PM

Run Finish Time 11:55:00 AM 4:17:00 PM 7:39:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 125.762 126.785 126.210 126.252

Moisture Content of Stack Gas, % 0.00 0.00 0.00 0.000

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Average Stack Gas Temperature, °F 394.09 391.40 388.53 391.340

Dry Volumetric Flow Rate, dry scfm 0.0 0.0 0.0 0.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 0.0 0.0 0.0 0.000

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Fw 0 0 0.000

Fc 0 0 0.000

Location Stack Exit - Method 29 

Average

Run Number 1 2 3

Test Date 2/23/2010 2/23/2010 2/23/2010

Run Start Time 8:04:00 AM 4:18:00 PM 12:00:00 AM

Run Finish Time 2:06:00 PM 8:34:00 PM 11:59:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 147.595 154.641 157.008 153.081

Moisture Content of Stack Gas, % 9.94 9.60 9.39 9.643

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 11.4 11.4 11.4 11.400

Oxygen, % 6.3 6.4 6.5 6.400

Average Stack Gas Temperature, °F 370.41 375.72 375.08 373.737

Dry Volumetric Flow Rate, dry scfm 173,988.2 180,989.8 181,799.9 178,925.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 307,229.6 320,427.1 320,869.5 316,175.400

Percent Isokinetic of Sampling Rate, % 99.4 100.1 101.2 100.233

F-Factor, dscfm/MMBtu @ %O2 9504 9560 9518 9,527.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, February 22, 2011 Page 7 of 33
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Location Stack Exit - Method 5/OTM-28

Average

Run Number 2 3

Test Date 2/23/2010 2/23/2010

Run Start Time 3:53:00 PM 9:26:00 PM

Run Finish Time 5:41:00 PM 11:04:00 

PM

Net Run Time, minutes 60 60

Dry Gas Meter Volume Sampled, dscf 37.577 38.731 38.154

Moisture Content of Stack Gas, % 8.23 8.33 8.280

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.000

Carbon Dioxide, % 11.4 11.4 11.400

Oxygen, % 6.3 6.4 6.350

Average Stack Gas Temperature, °F 362.45 359.96 361.205

Dry Volumetric Flow Rate, dry scfm 190,133.9 193,516.4 191,825.150

Actual Wet Volumetric Flue Gas Flow Rate, acfm 326,325.4 331,486.5 328,905.950

Percent Isokinetic of Sampling Rate, % 95.3 96.5 95.900

F-Factor, dscfm/MMBtu @ %O2 9560 9560 9,560.000

Fw 0 0 0.000

Fc 0 0 0.000

Location Stack Exit - Method 6C

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:00:00 AM 1:15:00 PM 4:35:00 PM

Run Finish Time 12:00:00 PM 4:15:00 PM 7:35:00 PM

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Moisture, % 0 0 0 0.000

Fuel Type Override Override Override

Fw 0 0 0.000

Fc 1420 1420 1420 1,420.000

Tuesday, February 22, 2011 Page 8 of 33
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Location Stack Exit - Method 7E

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:00:00 AM 1:15:00 PM 4:35:00 PM

Run Finish Time 12:00:00 PM 4:15:00 PM 7:35:00 PM

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Moisture, % 0 0 0 0.000

Fuel Type Override Override Oil

Fw 0 0.000

Fc 1420 1420 1420 1,420.000

Location Stack Exit - OTM - 27/28

Average

Run Number 1

Test Date 2/23/2010

Run Start Time 7:00:00 AM

Run Finish Time 10:22:00 AM

Net Run Time, minutes 214

Dry Gas Meter Volume Sampled, dscf 75.339 75.339

Moisture Content of Stack Gas, % 8.71 8.710

Moisture Saturation at Stack Gas Temperature, % 100.00 100.000

Carbon Dioxide, % 11.5 11.500

Oxygen, % 6.3 6.300

Average Stack Gas Temperature, °F 373.38 373.380

Dry Volumetric Flow Rate, dry scfm 195,219.9 195,219.900

Actual Wet Volumetric Flue Gas Flow Rate, acfm 341,292.5 341,292.500

Percent Isokinetic of Sampling Rate, % 88.7 88.700

F-Factor, dscfm/MMBtu @ %O2 9504 9,504.000

Fw 0 0.000

Fc 0 0.000

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Location Stack Exit - SW0010

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:46:00 AM 1:06:00 PM 4:40:00 PM

Run Finish Time 12:12:00 PM 3:38:00 PM 7:35:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 78.507 79.597 77.723 78.609

Moisture Content of Stack Gas, % 7.70 7.67 7.48 7.617

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Average Stack Gas Temperature, °F 393.44 393.74 391.77 392.983

Dry Volumetric Flow Rate, dry scfm 186,456.3 186,660.8 183,480.6 185,532.567

Actual Wet Volumetric Flue Gas Flow Rate, acfm 328,168.7 328,537.3 321,533.0 326,079.667

Percent Isokinetic of Sampling Rate, % 98.7 100.0 99.3 99.333

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, February 22, 2011 Page 10 of 33
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Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.006 0.002 0.002 0.003

lb/mmBtuO2 2.42E-06 8.17E-07 8.24E-07 0.000

ppm 2.18E-03 7.38E-04 7.44E-04 0.001

ppm@7%O2 2.16E-03 7.33E-04 7.39E-04 0.001

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 3.79E-02 5.43E-03 1.27E-02 0.019

ppm 3.67E+01 5.26E+00 1.23E+01 18.087

ppm@7%O2 3.64E+01 5.22E+00 1.22E+01 17.940

Location: Stack Exit - Method 23

Compound: 1,2,3,4,6,7,8-HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000068 0.000000004 0.0000000068 0.000

lb/mmBtuO2 6.58E-13 3.94E-13 6.68E-13 0.000

ng/dscm 7.75E-04 4.59E-04 7.53E-04 0.001

ng/dscm@7%O2 7.38E-04 4.40E-04 7.48E-04 0.001

Compound: 1,2,3,4,6,7,8-HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000063 0.0000000038 0.0000000094 0.000

lb/mmBtuO2 6.09E-13 3.75E-13 9.23E-13 0.000

ng/dscm 7.18E-04 4.36E-04 1.04E-03 0.001

ng/dscm@7%O2 6.84E-04 4.18E-04 1.03E-03 0.001

Compound: 1,2,3,4,7,8,9-HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000021 0.0000000021 0.000000002 0.000

lb/mmBtuO2 2.03E-13 2.07E-13 1.96E-13 0.000

ng/dscm 2.39E-04 2.41E-04 2.21E-04 0.000

ng/dscm@7%O2 2.28E-04 2.31E-04 2.19E-04 0.000

Compound: 1,2,3,4,7,8-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000017 0.0000000018 0.000

lb/mmBtuO2 1.64E-13 1.68E-13 1.77E-13 0.000

ng/dscm 1.94E-04 1.95E-04 1.99E-04 0.000

ng/dscm@7%O2 1.85E-04 1.87E-04 1.98E-04 0.000

Tuesday, February 22, 2011 Page 11 of 33
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Compound: 1,2,3,4,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000023 0.0000000021 0.0000000032 0.000

lb/mmBtuO2 2.22E-13 2.07E-13 3.14E-13 0.000

ng/dscm 2.62E-04 2.41E-04 3.54E-04 0.000

ng/dscm@7%O2 2.49E-04 2.31E-04 3.51E-04 0.000

Compound: 1,2,3,6,7,8-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000017 0.0000000017 0.000

lb/mmBtuO2 1.64E-13 1.68E-13 1.67E-13 0.000

ng/dscm 1.94E-04 1.95E-04 1.88E-04 0.000

ng/dscm@7%O2 1.85E-04 1.87E-04 1.87E-04 0.000

Compound: 1,2,3,6,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000019 0.0000000015 0.0000000029 0.000

lb/mmBtuO2 1.84E-13 1.48E-13 2.85E-13 0.000

ng/dscm 2.16E-04 1.72E-04 3.21E-04 0.000

ng/dscm@7%O2 2.06E-04 1.65E-04 3.19E-04 0.000

Compound: 1,2,3,7,8,9-HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000016 0.0000000016 0.0000000016 0.000

lb/mmBtuO2 1.55E-13 1.58E-13 1.57E-13 0.000

ng/dscm 1.82E-04 1.83E-04 1.77E-04 0.000

ng/dscm@7%O2 1.73E-04 1.75E-04 1.76E-04 0.000

Compound: 1,2,3,7,8,9-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000019 0.0000000019 0.0000000019 0.000

lb/mmBtuO2 1.84E-13 1.87E-13 1.87E-13 0.000

ng/dscm 2.16E-04 2.18E-04 2.10E-04 0.000

ng/dscm@7%O2 2.06E-04 2.09E-04 2.09E-04 0.000

Compound: 1,2,3,7,8-PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000017 0.0000000017 0.000

lb/mmBtuO2 1.64E-13 1.68E-13 1.67E-13 0.000

ng/dscm 1.94E-04 1.95E-04 1.88E-04 0.000

ng/dscm@7%O2 1.85E-04 1.87E-04 1.87E-04 0.000

Compound: 1,2,3,7,8-PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000018 0.0000000017 0.0000000036 0.000

lb/mmBtuO2 1.74E-13 1.68E-13 3.53E-13 0.000

Tuesday, February 22, 2011 Page 12 of 33
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ng/dscm 2.05E-04 1.95E-04 3.99E-04 0.000

ng/dscm@7%O2 1.95E-04 1.87E-04 3.96E-04 0.000

Compound: 2,3,3',4,4',5,5'-HpCB (PCB189)

Average

RunNumber 1 2 3

Mass_mg 0.0000000032 0.0000000049 0.0000000031 0.000

lb/mmBtuO2 3.10E-13 4.83E-13 3.04E-13 0.000

ng/dscm 3.65E-04 5.62E-04 3.43E-04 0.000

ng/dscm@7%O2 3.48E-04 5.39E-04 3.41E-04 0.000

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 1 2 3

Mass_mg 0.000000011 0.000000014 0.000000018 0.000

lb/mmBtuO2 1.06E-12 1.38E-12 1.77E-12 0.000

ng/dscm 1.25E-03 1.61E-03 1.99E-03 0.002

ng/dscm@7%O2 1.19E-03 1.54E-03 1.98E-03 0.002

Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber 1 2 3

Mass_mg 0.000000022 0.000000038 0.000000038 0.000

lb/mmBtuO2 2.13E-12 3.75E-12 3.73E-12 0.000

ng/dscm 2.51E-03 4.36E-03 4.21E-03 0.004

ng/dscm@7%O2 2.39E-03 4.18E-03 4.18E-03 0.004

Compound: 2,3',4,4',5,5'-HxCB (PCB167)

Average

RunNumber 1 2 3

Mass_mg 0.000000004 0.000000005 0.0000000078 0.000

lb/mmBtuO2 3.87E-13 4.93E-13 7.66E-13 0.000

ng/dscm 4.56E-04 5.73E-04 8.64E-04 0.001

ng/dscm@7%O2 4.34E-04 5.49E-04 8.58E-04 0.001

Compound: 2,3,4,4',5-PeCB (PCB114)

Average

RunNumber 1 2 3

Mass_mg 0.0000000058 0.0000000046 0.000000004 0.000

lb/mmBtuO2 5.61E-13 4.54E-13 3.93E-13 0.000

ng/dscm 6.61E-04 5.27E-04 4.43E-04 0.001

ng/dscm@7%O2 6.29E-04 5.05E-04 4.40E-04 0.001

Compound: 2,3',4,4',5-PeCB (PCB118)

Average

RunNumber 1 2 3

Mass_mg 0.000000077 0.00000011 0.00000011 0.000

lb/mmBtuO2 7.45E-12 1.08E-11 1.08E-11 0.000

ng/dscm 8.77E-03 1.26E-02 1.22E-02 0.011

ng/dscm@7%O2 8.35E-03 1.21E-02 1.21E-02 0.011

Compound: 2',3,4,4',5-PeCB (PCB123)

Average

RunNumber 1 2 3

Tuesday, February 22, 2011 Page 13 of 33
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Mass_mg 0.0000000059 0.0000000029 0.0000000035 0.000

lb/mmBtuO2 5.71E-13 2.86E-13 3.44E-13 0.000

ng/dscm 6.72E-04 3.32E-04 3.87E-04 0.000

ng/dscm@7%O2 6.40E-04 3.18E-04 3.84E-04 0.000

Compound: 2,3,4,6,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000003 0.0000000026 0.0000000045 0.000

lb/mmBtuO2 2.90E-13 2.56E-13 4.42E-13 0.000

ng/dscm 3.42E-04 2.98E-04 4.98E-04 0.000

ng/dscm@7%O2 3.26E-04 2.86E-04 4.94E-04 0.000

Compound: 2,3,4,7,8-PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000004 0.0000000038 0.0000000058 0.000

lb/mmBtuO2 3.87E-13 3.75E-13 5.70E-13 0.000

ng/dscm 4.56E-04 4.36E-04 6.42E-04 0.001

ng/dscm@7%O2 4.34E-04 4.18E-04 6.37E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000017 0.0000000016 0.000

lb/mmBtuO2 1.64E-13 1.68E-13 1.57E-13 0.000

ng/dscm 1.94E-04 1.95E-04 1.77E-04 0.000

ng/dscm@7%O2 1.85E-04 1.87E-04 1.76E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000117 0.0000000102 0.0000000146 0.000

lb/mmBtuO2 1.13E-12 1.01E-12 1.43E-12 0.000

ng/dscm 1.33E-03 1.17E-03 1.62E-03 0.001

ng/dscm@7%O2 1.27E-03 1.12E-03 1.61E-03 0.001

Compound: 3,3',4,4',5,5'-HxCB (PCB169)

Average

RunNumber 1 2 3

Mass_mg 0.0000000032 0.0000000052 0.0000000032 0.000

lb/mmBtuO2 3.10E-13 5.13E-13 3.14E-13 0.000

ng/dscm 3.65E-04 5.96E-04 3.54E-04 0.000

ng/dscm@7%O2 3.48E-04 5.71E-04 3.51E-04 0.000

Compound: 3,3',4,4',5-PeCB (PCB126)

Average

RunNumber 1 2 3

Mass_mg 0.0000000058 0.0000000029 0.0000000035 0.000

lb/mmBtuO2 5.61E-13 2.86E-13 3.44E-13 0.000

ng/dscm 6.61E-04 3.32E-04 3.87E-04 0.000

ng/dscm@7%O2 6.29E-04 3.18E-04 3.84E-04 0.000

Tuesday, February 22, 2011 Page 14 of 33
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Compound: 3,3',4,4'-TCB (PCB77)

Average

RunNumber 1 2 3

Mass_mg 0.000000017 0.000000016 0.000000015 0.000

lb/mmBtuO2 1.64E-12 1.58E-12 1.47E-12 0.000

ng/dscm 1.94E-03 1.83E-03 1.66E-03 0.002

ng/dscm@7%O2 1.85E-03 1.75E-03 1.65E-03 0.002

Compound: 3,4,4',5-TCB (PCB81)

Average

RunNumber 1 2 3

Mass_mg 0.0000000026 0.0000000052 0.0000000035 0.000

lb/mmBtuO2 2.52E-13 5.13E-13 3.44E-13 0.000

ng/dscm 2.96E-04 5.96E-04 3.87E-04 0.000

ng/dscm@7%O2 2.82E-04 5.71E-04 3.84E-04 0.000

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000343 0.0000000136 0.000000023 0.000

lb/mmBtuO2 3.32E-12 1.34E-12 2.26E-12 0.000

ng/dscm 3.91E-03 1.56E-03 2.55E-03 0.003

ng/dscm@7%O2 3.72E-03 1.50E-03 2.53E-03 0.003

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000084 0.0000000051 0.0000000065 0.000

lb/mmBtuO2 8.13E-13 5.03E-13 6.38E-13 0.000

ng/dscm 9.57E-04 5.85E-04 7.20E-04 0.001

ng/dscm@7%O2 9.11E-04 5.61E-04 7.15E-04 0.001

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000134 0.0000000074 0.0000000141 0.000

lb/mmBtuO2 1.30E-12 7.30E-13 1.38E-12 0.000

ng/dscm 1.53E-03 8.48E-04 1.56E-03 0.001

ng/dscm@7%O2 1.46E-03 8.13E-04 1.55E-03 0.001

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000073 0.0000000044 0.000000011 0.000

lb/mmBtuO2 7.06E-13 4.34E-13 1.08E-12 0.000

ng/dscm 8.32E-04 5.04E-04 1.22E-03 0.001

ng/dscm@7%O2 7.92E-04 4.83E-04 1.21E-03 0.001

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000002 0.0000000028 0.0000000021 0.000

lb/mmBtuO2 1.93E-13 2.76E-13 2.06E-13 0.000

Tuesday, February 22, 2011 Page 15 of 33
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ng/dscm 2.28E-04 3.21E-04 2.32E-04 0.000

ng/dscm@7%O2 2.17E-04 3.08E-04 2.30E-04 0.000

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000136 0.0000000081 0.0000000236 0.000

lb/mmBtuO2 1.32E-12 7.99E-13 2.32E-12 0.000

ng/dscm 1.55E-03 9.29E-04 2.61E-03 0.002

ng/dscm@7%O2 1.48E-03 8.91E-04 2.59E-03 0.002

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000017 0.0000000019 0.000

lb/mmBtuO2 1.64E-13 1.68E-13 1.87E-13 0.000

ng/dscm 1.94E-04 1.95E-04 2.10E-04 0.000

ng/dscm@7%O2 1.85E-04 1.87E-04 2.09E-04 0.000

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000174 0.0000000074 0.000000044 0.000

lb/mmBtuO2 1.68E-12 7.30E-13 4.32E-12 0.000

ng/dscm 1.98E-03 8.48E-04 4.87E-03 0.003

ng/dscm@7%O2 1.89E-03 8.13E-04 4.84E-03 0.003

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000018 0.0000000023 0.0000000088 0.000

lb/mmBtuO2 1.74E-13 2.27E-13 8.64E-13 0.000

ng/dscm 2.05E-04 2.64E-04 9.74E-04 0.000

ng/dscm@7%O2 1.95E-04 2.53E-04 9.67E-04 0.000

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000231 0.000000035 0.000000067 0.000

lb/mmBtuO2 2.23E-12 3.45E-12 6.58E-12 0.000

ng/dscm 2.63E-03 4.01E-03 7.42E-03 0.005

ng/dscm@7%O2 2.50E-03 3.84E-03 7.37E-03 0.005

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.000000053 0.000000028 0.00000005 0.000

lb/mmBtuO2 5.13E-12 2.76E-12 4.91E-12 0.000

ng/dscm 6.04E-03 3.21E-03 5.54E-03 0.005

ng/dscm@7%O2 5.75E-03 3.08E-03 5.50E-03 0.005

Compound: Total Furans

Average

RunNumber 1 2 3

Tuesday, February 22, 2011 Page 16 of 33
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Process Run Data

Mass_mg 0.00000007 0.00000006 0.000000152 0.000

lb/mmBtuO2 6.77E-12 5.92E-12 1.49E-11 0.000

ng/dscm 7.97E-03 6.88E-03 1.68E-02 0.011

ng/dscm@7%O2 7.59E-03 6.60E-03 1.67E-02 0.010

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 2.56E-02 1.74E-02 1.36E-02 0.019

ppm 1.58E+01 1.07E+01 8.38E+00 11.627

ppm@7%O2 1.57E+01 1.06E+01 8.32E+00 11.540

Location: Stack Exit - Method 26

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 5.6 5.8 5.7 5.700

lb/mmBtuO2 1.39E-03 1.43E-03 1.41E-03 0.001

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 1.1 0.98 0.93 1.003

lb/mmBtuO2 2.74E-04 2.42E-04 2.31E-04 0.000

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.198 0.185 0.188 0.190

lb/mmBtuO2 4.02E-05 3.63E-05 3.65E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0255 0.0203 0.0211 0.022

lb/mmBtuO2 5.18E-06 3.99E-06 4.09E-06 0.000

Compound: Beryllium

Average

RunNumber

Mass_mg #Num!

lb/mmBtuO2 #Num!

Tuesday, February 22, 2011 Page 17 of 33
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6/22/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Average Heat Input 701.9 MMBtu/hr 0

10 Average Heat Input 688.6 MMBtu/hr 0

11 Average Heat Input 692.1 MMBtu/hr 0

12 Average Heat Input 693.7 MMBtu/hr 0

2 Average Heat Input 691.2 MMBtu/hr 0

3 Average Heat Input 692.6 MMBtu/hr 0

4 Average Heat Input 693.7 MMBtu/hr 0

5 Average Heat Input 692.1 MMBtu/hr 0

6 Average Heat Input 688.6 MMBtu/hr 0

7 Average Heat Input 702.7 MMBtu/hr 0

8 Average Heat Input 691.1 MMBtu/hr 0

9 Average Heat Input 691.8 MMBtu/hr 0

1 Fuel Oil Firing Rate 77.581 gal/min 0

10 Fuel Oil Firing Rate 76.111 gal/min 0

11 Fuel Oil Firing Rate 76.492 gal/min 0

12 Fuel Oil Firing Rate 76.666 gal/min 0

2 Fuel Oil Firing Rate 76.395 gal/min 0

3 Fuel Oil Firing Rate 76.548 gal/min 0

4 Fuel Oil Firing Rate 76.666 gal/min 0

5 Fuel Oil Firing Rate 76.492 gal/min 0

6 Fuel Oil Firing Rate 76.111 gal/min 0

7 Fuel Oil Firing Rate 77.67 gal/min 0

8 Fuel Oil Firing Rate 76.384 gal/min 0

9 Fuel Oil Firing Rate 76.462 gal/min 0

1 Unit Gross Electrical Output 60.5 Mwe 0 Run 1

10 Unit Gross Electrical Output 60.2 Mwe 0 Run 3

11 Unit Gross Electrical Output 60.2 Mwe 0 Run 2

12 Unit Gross Electrical Output 60.3 Mwe 0 Run 1

2 Unit Gross Electrical Output 60.1 Mwe 0 Run 2

3 Unit Gross Electrical Output 60.3 Mwe 0 Run 3

4 Unit Gross Electrical Output 60.3 Mwe 0 Run 1

5 Unit Gross Electrical Output 60.2 Mwe 0 Run 2

6 Unit Gross Electrical Output 60.2 Mwe 0 Run 3

Tuesday, February 22, 2011 Page 18 of 33
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APCD Run Data

7 Unit Gross Electrical Output 60.5 Mwe 0 Run 1

8 Unit Gross Electrical Output 60.2 Mwe 0 Run 2

9 Unit Gross Electrical Output 60.1 Mwe 0 Run 3

1 Opacity 2.5 % Dioxin/Furan 

Organic HAP 

Group

0

10 Opacity 4.45 % Acid Gas HAP 

Group

0

11 Opacity 3.54 % Acid Gas HAP 

Group

0

12 Opacity 3.9 % Acid Gas HAP 

Group

0

2 Opacity 2.8 % Dioxin/Furan 

Organic HAP 

Group

0

3 Opacity 4 % Dioxin/Furan 

Organic HAP 

Group

0

4 Opacity 3.9 % Non-Dioxin 

Organic HAP 

Group

0

5 Opacity 3.54 % Non-Dioxin 

Organic HAP 

Group

0

6 Opacity 4.45 % Non-Dioxin 

Organic HAP 

Group

0

7 Opacity 2.6 % Mercury and 

Metallic HAP 

Group

0

8 Opacity 2.7 % Mercury and 

Metallic HAP 

Group

0

9 Opacity 2.9 % Mercury and 

Metallic HAP 

Group

0

Run Name Value UOM Comments

Target

Value

1 MULTIPLE CYCLONES 0.8801 Delta P 0

10 MULTIPLE CYCLONES 0.839 Delta P 0

11 MULTIPLE CYCLONES 0.8438 Delta P 0

12 MULTIPLE CYCLONES 0.8522 Delta P 0

2 MULTIPLE CYCLONES 0.8546 Delta P 0

Tuesday, February 22, 2011 Page 19 of 33
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3 MULTIPLE CYCLONES 0.7857 Delta P 0

4 MULTIPLE CYCLONES 0.8522 Delta P 0

5 MULTIPLE CYCLONES 0.8546 Delta P 0

6 MULTIPLE CYCLONES 0.7857 Delta P 0

7 MULTIPLE CYCLONES 0.8843 Delta P 0

8 MULTIPLE CYCLONES 0.8284 Delta P 0

9 MULTIPLE CYCLONES 0.8777 Delta P 0

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

provide detailed

0 0

10 drop down lists. If not on list add description and 

provide detailed

0 0

11 drop down lists. If not on list add description and 

provide detailed

0 0

12 drop down lists. If not on list add description and 

provide detailed

0 0

2 drop down lists. If not on list add description and 

provide detailed

0 0

3 drop down lists. If not on list add description and 

provide detailed

0 0

4 drop down lists. If not on list add description and 

provide detailed

0 0

5 drop down lists. If not on list add description and 

provide detailed

0 0

6 drop down lists. If not on list add description and 

provide detailed

0 0

7 drop down lists. If not on list add description and 

provide detailed

0 0

8 drop down lists. If not on list add description and 

provide detailed

0 0

9 drop down lists. If not on list add description and 

provide detailed

0 0

1 desription in section 5a. 0 0

10 desription in section 5a. 0 0

11 desription in section 5a. 0 0

12 desription in section 5a. 0 0

2 desription in section 5a. 0 0

3 desription in section 5a. 0 0

4 desription in section 5a. 0 0

5 desription in section 5a. 0 0

6 desription in section 5a. 0 0

7 desription in section 5a. 0 0

Tuesday, February 22, 2011 Page 20 of 33
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Process Lab Run Data

8 desription in section 5a. 0 0

9 desription in section 5a. 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 18310 Btu/lb

2 Fuel Higher Heating Value 18240 Btu/lb

3 Fuel Higher Heating Value 18330 Btu/lb

1 Fuel Moisture 0 %

2 Fuel Moisture 0 %

3 Fuel Moisture 0 %

1 Fuel Mercury Content 0.1 mg/Kg

2 Fuel Mercury Content 0.1 mg/Kg

3 Fuel Mercury Content 0.1 mg/Kg

1 Fuel Cadmium Content 1 mg/Kg

2 Fuel Cadmium Content 1 mg/Kg

3 Fuel Cadmium Content 1 mg/Kg

1 Fuel Nickel Content 1.84 mg/Kg

2 Fuel Nickel Content 2.9 mg/Kg

3 Fuel Nickel Content 2.89 mg/Kg

1 Fuel Arsenic Content 2 mg/Kg

2 Fuel Arsenic Content 2 mg/Kg

3 Fuel Arsenic Content 2 mg/Kg

1 Fuel Chromium Content 1 mg/Kg

2 Fuel Chromium Content 1.14 mg/Kg

3 Fuel Chromium Content 1 mg/Kg

1 Fuel Beryllium Content 1 mg/Kg

2 Fuel Beryllium Content 1 mg/Kg

3 Fuel Beryllium Content 1 mg/Kg

1 Fuel Lead Content 1 mg/Kg

2 Fuel Lead Content 1.39 mg/Kg

3 Fuel Lead Content 1 mg/Kg

1 Fuel Manganese Content 1.58 mg/Kg

2 Fuel Manganese Content 1.52 mg/Kg

3 Fuel Manganese Content 1.41 mg/Kg

1 Fuel Chlorine Content 0.02 %

2 Fuel Chlorine Content 0.03 %

3 Fuel Chlorine Content 0.02 %

1 Fuel Fluorine Content 13 mg/Kg

2 Fuel Fluorine Content 17 mg/Kg

3 Fuel Fluorine Content 15 mg/Kg

1 Fuel Antimony Content 3 mg/Kg

Tuesday, February 22, 2011 Page 21 of 33
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6/22/2010

2 Fuel Antimony Content 3 mg/Kg

3 Fuel Antimony Content 3 mg/Kg

1 Fuel Selenium Content 2 mg/Kg

2 Fuel Selenium Content 2 mg/Kg

3 Fuel Selenium Content 2 mg/Kg

1 Fuel Ash Content 0.15 %

2 Fuel Ash Content 0.08 %

3 Fuel Ash Content 0.08 %

1 Fuel Carbon Content 86.6 %

2 Fuel Carbon Content 86.4 %

3 Fuel Carbon Content 86.6 %

1 Fuel Hydrogen Content 11.2 %

2 Fuel Hydrogen Content 11.4 %

3 Fuel Hydrogen Content 11.3 %

1 Fuel Nitrogen Content 0.45 %

2 Fuel Nitrogen Content 0.44 %

3 Fuel Nitrogen Content 0.46 %

1 Fuel Oxygen Content 0.19 %

2 Fuel Oxygen Content 0.36 %

3 Fuel Oxygen Content 0.15 %

1 Fuel Sulfur Content 1.35 %

2 Fuel Sulfur Content 1.4 %

3 Fuel Sulfur Content 1.46 %

1 Fuel Cobalt Content 0.1 mg/Kg

2 Fuel Cobalt Content 0.1 mg/Kg

3 Fuel Cobalt Content 0.1 mg/Kg

Tuesday, February 22, 2011 Page 22 of 33
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6/22/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:46:00 AM 1:06:00 PM 4:40:00 PM

Run Finish Time 12:12:00 PM 3:38:00 PM 7:35:00 PM

Net Traversing Points 120 120 120

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.279 0.279 0.279 0.279

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.972 0.972 0.972 0.972

Barometric Pressure, inches of Mercury 29.81 29.81 29.81 29.810

Average Orifice Meter Differential, inches H2O 1.51 1.46 1.41 1.460

Dry Gas Meter Volume Sampled, cubic feet 81.510 80.220 78.501 80.077

Average Dry Gas Meter Temperature, °F 77.95 77.04 69.89 74.960

Dry Gas Meter Volume Sampled, dscf 77.765 76.655 76.015 76.812

Total Moisture Liquid collected, g 149.6 139.3 126.1 138.333

Volume of Water Vapor, standard cubic feet 7.04 6.56 5.94 6.513

Moisture Content of Stack Gas, % 8.30 7.88 7.25 7.810

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.917 0.9212 0.9275 0.922

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Carbon Monoxide & Nitrogen, % 82.2 82.2 82.1 82.167

Fuel Factor 1.28 1.28 1.27

Dry Molecular Weight, lb/lb-Mole 30.02 30.02 30.04 30.027

Wet Molecular weight, lb/lb-Mole 29.02 29.07 29.17 29.087

Flue Gas Static Pressure, inches of H2O -0.55 -0.55 -0.55 -0.550

Absolute Flue Gas Pressure, inches of Mercury 29.77 29.77 29.77 29.770

Average Stack Gas Temperature, °F 380.77 389.07 381.37 383.737

Average Velocity Head, inches of H2O 0.4056317970

50468

0.391818329

577015

0.389071862

633476

0.396

Average Stack Gas Velocity, feet/second 45.12 44.52 44.09 44.577

Stack Cross-Sectional Area, square feet 122.882 122.882 122.882 122.882

Dry Volumetric Flow Rate, dry scfm 190,612.7 187,092.5 188,259.8 188,655.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 332,666.2 328,242.4 325,072.0 328,660.200

Percent Isokinetic of Sampling Rate, % 98.4 98.8 97.4 98.200

Percent Excess Air, % 46.6 46.6 46.7 46.633

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Round Duct Diameter, inches 150.1 150.1 150.1

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, February 22, 2011 Page 23 of 33
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Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:00:00 AM 1:15:00 PM 4:35:00 PM

Run Finish Time 12:00:00 PM 4:15:00 PM 7:35:00 PM

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Fuel Factor 0 0 1.27

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 203 203 203 203.000

Operating Units ppm PPM PPM

No. Readings/Avg. 3 3 3 3.000

Calibration Set 123 123 123 123.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.2 2.25 2.43 1.627

Calibration Pre Zero Cylinder Bias -0.09 0.92 1.01 0.613

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM058516-

CO

ALM058516

-CO

ALM058516-

CO

Calibration Pre High Cylinder Instrument Response 98.2 100.4 100.2 99.600

Calibration Pre High Cylinder Bias -0.79 0.3 0.2 -0.097

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 2.25 2.43 1 1.893

Calibration Post Zero Cylinder Bias 0.92 1.01 0.31 0.747

Calibration Post Zero Cylinder Drift 1.01 0.09 0.7 0.600

Calibration Post High Cylinder ID ALM058516-

CO

ALM058516

-CO

ALM058516-

CO

Calibration Post High Cylinder Instrument Response 100.4 100.2 97.8 99.467

Calibration Post High Cylinder Bias 0.3 0.2 -0.99 -0.163

Calibration Post High Cylinder Drift 1.09 0.1 1.19 0.793

Cavg 37.3 7.5 13.7 19.500

Cavg Units ppmvd ppmvd ppmvd

Cgas 36.7095 5.2569 12.2948 18.087

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, February 22, 2011 Page 24 of 33
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6/22/2010

Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 2/23/2010 2/23/2010 2/24/2010

Run Start Time 6:47:00 AM 3:44:00 PM 7:56:00 AM

Run Finish Time 3:03:00 PM 11:54:00 PM 6:26:00 PM

Net Traversing Points 479 480 478

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.281 0.281 0.281 0.281

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.98 0.98 0.98 0.980

Barometric Pressure, inches of Mercury 29.63 29.63 29.79 29.683

Average Orifice Meter Differential, inches H2O 1.54 1.53 1.61 1.560

Dry Gas Meter Volume Sampled, cubic feet 325.778 327.044 337.278 330.033

Average Dry Gas Meter Temperature, °F 80.47 86.04 86.84 84.450

Dry Gas Meter Volume Sampled, dscf 310.054 308.076 319.021 312.384

Total Moisture Liquid collected, g 576 564 563.5 567.833

Volume of Water Vapor, standard cubic feet 27.11 26.55 26.52 26.727

Moisture Content of Stack Gas, % 8.04 7.93 7.67 7.880

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.9196 0.9207 0.9233 0.921

Carbon Dioxide, % 11.4 11.5 10.9 11.267

Oxygen, % 6.3 6.4 6.9 6.533

Carbon Monoxide & Nitrogen, % 82.3 82.1 82.2 82.200

Fuel Factor 1.28 1.26 1.28

Dry Molecular Weight, lb/lb-Mole 30.08 30.10 30.02 30.067

Wet Molecular weight, lb/lb-Mole 29.11 29.14 29.10 29.117

Flue Gas Static Pressure, inches of H2O -0.55 -0.55 -0.55 -0.550

Absolute Flue Gas Pressure, inches of Mercury 29.59 29.59 29.75 29.643

Average Stack Gas Temperature, °F 374.38 377.74 384.49 378.870

Average Velocity Head, inches of H2O 0.3743668664

03901

0.368829074

420694

0.388966079

541166

0.377

Average Stack Gas Velocity, feet/second 43.24 42.99 44.23 43.487

Stack Cross-Sectional Area, square feet 122.882 122.882 122.882 122.882

Dry Volumetric Flow Rate, dry scfm 183,475.3 181,900.2 187,182.0 184,185.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 318,805.1 316,961.8 326,104.3 320,623.733

Percent Isokinetic of Sampling Rate, % 100.5 100.7 101.3 100.833

Percent Excess Air, % 40.8 41.9 46.6 43.100

F-Factor, dscfm/MMBtu @ %O2 9504 9560 9518 9,527.333

Round Duct Diameter, inches 150.1 150.1 150.1

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, February 22, 2011 Page 25 of 33
Vienna

6/22/2010

Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:50:00 AM 1:06:00 PM 4:39:00 PM

Run Finish Time 11:50:00 AM 3:06:00 PM 6:39:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 6.9 6.9 6.9 6.900

Fuel Factor 0 0 0

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Moisture, % 7.7 7.7 7.5 7.633

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 45 45 45 45.000

Operating Units ppm ppm ppm

No. Readings/Avg. 3 3 3 3.000

Calibration Set 999 999 999 999.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.2 0.26 0.16 0.207

Calibration Pre Zero Cylinder Bias 0 0.13 -0.09 0.013

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC312673-

PRO

CC312673-

PRO

CC312673-

PRO

Calibration Pre High Cylinder Instrument Response 15.46 15.3 15.14 15.300

Calibration Pre High Cylinder Bias 0 -0.36 -0.71 -0.357

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.26 0.16 0.52 0.313

Calibration Post Zero Cylinder Bias 0.13 -0.09 0.71 0.250

Calibration Post Zero Cylinder Drift 0.13 0.22 0.8 0.383

Calibration Post High Cylinder ID CC312673-

PRO

CC312673-

PRO

CC312673-

PRO

Calibration Post High Cylinder Instrument Response 15.3 15.14 15.03 15.157

Calibration Post High Cylinder Bias -0.36 -0.71 -0.96 -0.677

Calibration Post High Cylinder Drift 0.36 0.35 0.25 0.320

Cavg 14.8 10 7.9 10.900

Cavg Units ppmvw ppmvw ppmvw

Cgas 15.7542 10.6844 8.3808 11.606

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 14.541148514

8515

9.861745502

998

7.752268565

61546

10.718

Cgasw Units ppmvw ppmvw ppmvw

Tuesday, February 22, 2011 Page 26 of 33
Vienna

6/22/2010

Location Stack Exit - Method 26

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 8:56:00 AM 1:09:00 PM 4:40:00 PM

Run Finish Time 11:55:00 AM 4:17:00 PM 7:39:00 PM

Net Traversing Points 180 179 180

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0 0 0 0.000

Pitot Tube Coefficient 0 0 0 0.000

Dry Gas Meter Calibration Factor 1.011 1.011 1.011 1.011

Barometric Pressure, inches of Mercury 29.79 29.79 29.79 29.790

Average Orifice Meter Differential, inches H2O 1.78 1.80 1.79 1.790

Dry Gas Meter Volume Sampled, cubic feet 127.403 127.780 128.594 127.926

Average Dry Gas Meter Temperature, °F 80.79 78.04 83.92 80.917

Dry Gas Meter Volume Sampled, dscf 125.762 126.785 126.210 126.252

Total Moisture Liquid collected, g 0 0 0 0.000

Volume of Water Vapor, standard cubic feet 0.00 0.00 0.00 0.000

Moisture Content of Stack Gas, % 0.00 0.00 0.00 0.000

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 1 1 1 1.000

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Carbon Monoxide & Nitrogen, % 82.2 82.2 82.1 82.167

Fuel Factor 1.28 1.28 1.27

Dry Molecular Weight, lb/lb-Mole 30.02 30.02 30.04 30.027

Wet Molecular weight, lb/lb-Mole 30.02 30.02 30.04 30.027

Flue Gas Static Pressure, inches of H2O -0.55 -0.55 -0.55 -0.550

Absolute Flue Gas Pressure, inches of Mercury 29.75 29.75 29.75 29.750

Average Stack Gas Temperature, °F 394.09 391.40 388.53 391.340

Average Velocity Head, inches of H2O 0.4342186647

47912

0.424115365

024771

0.425457705

97298

0.428

Average Stack Gas Velocity, feet/second 0.00 0.00 0.00 0.000

Stack Cross-Sectional Area, square feet 122.882 122.882 122.882 122.882

Dry Volumetric Flow Rate, dry scfm 0.0 0.0 0.0 0.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 0.0 0.0 0.0 0.000

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, % 46.6 46.6 46.7 46.633

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Round Duct Diameter, inches 150.1 150.1 150.1

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0.000

Fc 0 0 0.000

Tuesday, February 22, 2011 Page 27 of 33
Vienna

6/22/2010

Location Stack Exit - Method 29 

Average

Run Number 1 2 3

Test Date 2/23/2010 2/23/2010 2/23/2010

Run Start Time 8:04:00 AM 4:18:00 PM 12:00:00 AM

Run Finish Time 2:06:00 PM 8:34:00 PM 11:59:00 PM

Net Traversing Points 240 240 240

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.283 0.283 0.283 0.283

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.006 0.988 0.988 0.994

Barometric Pressure, inches of Mercury 29.63 29.63 29.63 29.630

Average Orifice Meter Differential, inches H2O 1.40 1.53 1.57 1.500

Dry Gas Meter Volume Sampled, cubic feet 150.507 161.244 164.719 158.823

Average Dry Gas Meter Temperature, °F 78.26 80.71 84.09 81.020

Dry Gas Meter Volume Sampled, dscf 147.595 154.641 157.008 153.081

Total Moisture Liquid collected, g 346 348.9 345.9 346.933

Volume of Water Vapor, standard cubic feet 16.29 16.42 16.28 16.330

Moisture Content of Stack Gas, % 9.94 9.60 9.39 9.643

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.9006 0.904 0.9061 0.904

Carbon Dioxide, % 11.4 11.4 11.4 11.400

Oxygen, % 6.3 6.4 6.5 6.400

Carbon Monoxide & Nitrogen, % 82.3 82.2 82.1 82.200

Fuel Factor 1.28 1.27 1.26

Dry Molecular Weight, lb/lb-Mole 30.08 30.08 30.08 30.080

Wet Molecular weight, lb/lb-Mole 28.88 28.92 28.95 28.917

Flue Gas Static Pressure, inches of H2O -0.55 -0.55 -0.55 -0.550

Absolute Flue Gas Pressure, inches of Mercury 29.59 29.59 29.59 29.590

Average Stack Gas Temperature, °F 370.41 375.72 375.08 373.737

Average Velocity Head, inches of H2O 0.3465725377

52369

0.374962944

211529

0.376819331

124507

0.366

Average Stack Gas Velocity, feet/second 41.67 43.46 43.52 42.883

Stack Cross-Sectional Area, square feet 122.882 122.882 122.882 122.882

Dry Volumetric Flow Rate, dry scfm 173,988.2 180,989.8 181,799.9 178,925.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 307,229.6 320,427.1 320,869.5 316,175.400

Percent Isokinetic of Sampling Rate, % 99.4 100.1 101.2 100.233

Percent Excess Air, % 40.8 41.8 42.8 41.800

F-Factor, dscfm/MMBtu @ %O2 9504 9560 9518 9,527.333

Round Duct Diameter, inches 150.1 150.1 150.1

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, February 22, 2011 Page 28 of 33
Vienna

6/22/2010

Location Stack Exit - Method 5/OTM-28

Average

Run Number 2 3

Test Date 2/23/2010 2/23/2010

Run Start Time 3:53:00 PM 9:26:00 PM

Run Finish Time 5:41:00 PM 11:04:00 PM

Net Traversing Points 61 60

Net Run Time, minutes 60 60

Nozzle Diameter, inches 0.279 0.279 0.279

Pitot Tube Coefficient 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.98 0.98 0.980

Barometric Pressure, inches of Mercury 29.63 29.63 29.630

Average Orifice Meter Differential, inches H2O 1.53 1.62 1.575

Dry Gas Meter Volume Sampled, cubic feet 39.006 40.007 39.507

Average Dry Gas Meter Temperature, °F 73.93 71.44 72.685

Dry Gas Meter Volume Sampled, dscf 37.577 38.731 38.154

Total Moisture Liquid collected, g 71.7 74.8 73.250

Volume of Water Vapor, standard cubic feet 3.37 3.52 3.445

Moisture Content of Stack Gas, % 8.23 8.33 8.280

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.000

Dry Mole Fraction 0.9177 0.9167 0.917

Carbon Dioxide, % 11.4 11.4 11.400

Oxygen, % 6.3 6.4 6.350

Carbon Monoxide & Nitrogen, % 82.3 82.2 82.250

Fuel Factor 1.28 1.27

Dry Molecular Weight, lb/lb-Mole 30.08 30.08 30.080

Wet Molecular weight, lb/lb-Mole 29.09 29.07 29.080

Flue Gas Static Pressure, inches of H2O -0.55 -0.55 -0.550

Absolute Flue Gas Pressure, inches of Mercury 29.59 29.59 29.590

Average Stack Gas Temperature, °F 362.45 359.96 361.205

Average Velocity Head, inches of H2O 0.3975462458

70846

0.411245885

040992

0.404

Average Stack Gas Velocity, feet/second 44.26 44.96 44.610

Stack Cross-Sectional Area, square feet 122.882 122.882 122.882

Dry Volumetric Flow Rate, dry scfm 190,133.9 193,516.4 191,825.150

Actual Wet Volumetric Flue Gas Flow Rate, acfm 326,325.4 331,486.5 328,905.950

Percent Isokinetic of Sampling Rate, % 95.3 96.5 95.900

Percent Excess Air, % 40.8 41.8 41.300

F-Factor, dscfm/MMBtu @ %O2 9560 9560 9,560.000

Round Duct Diameter, inches 150.1 150.1

Rectangular Duct Width, inches 0 0

Rectangular Duct Length, inches 0 0

Fw 0 0 0.000

Fc 0 0 0.000

Tuesday, February 22, 2011 Page 29 of 33
Vienna

6/22/2010

Location Stack Exit - Method 6C

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:00:00 AM 1:15:00 PM 4:35:00 PM

Run Finish Time 12:00:00 PM 4:15:00 PM 7:35:00 PM

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Fuel Factor 0 1.28 1.27

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 800.3 800.3 800.3 800.300

Operating Units ppm ppm ppm

No. Readings/Avg. 3 3 3 3.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 5.4 1 3.3 3.233

Calibration Pre Zero Cylinder Bias 0.65 0.1 0.39 0.380

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0013036-

SO2

EB0013036-

SO2

EB0013036-

SO2

Calibration Pre High Cylinder Instrument Response 401 402.8 400.5 401.433

Calibration Pre High Cylinder Bias 0.05 0.27 -0.01 0.103

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 1 3.3 4.7 3.000

Calibration Post Zero Cylinder Bias 0.1 0.39 0.56 0.350

Calibration Post Zero Cylinder Drift 0.55 0.29 0.17 0.337

Calibration Post High Cylinder ID EB0013036-

SO2

EB0013036-

SO2

EB0013036-

SO2

Calibration Post High Cylinder Instrument Response 402.8 400.5 399.75 401.017

Calibration Post High Cylinder Bias 0.27 -0.01 -0.11 0.050

Calibration Post High Cylinder Drift 0.22 0.28 0.1 0.200

Cavg 639.1 667.1 664.2 656.800

Cavg Units ppmvd ppmvd ppmvd

Cgas 637.1759 664.95 665.8249 655.984

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, February 22, 2011 Page 30 of 33
Vienna

6/22/2010

Location Stack Exit - Method 7E

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:00:00 AM 1:15:00 PM 4:35:00 PM

Run Finish Time 12:00:00 PM 4:15:00 PM 7:35:00 PM

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Fuel Factor 1.28 1.27 1.26

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 400.3 400.3 400.3 400.300

Operating Units ppm ppm ppm

No. Readings/Avg. 3 3 3 3.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.9 0.6 0.7 0.733

Calibration Pre Zero Cylinder Bias 0.15 0.07 0.1 0.107

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID AAL6503-

NOx

AAL6503-

NOx

AAL6503-

NOx

Calibration Pre High Cylinder Instrument Response 202.6 202.9 202.2 202.567

Calibration Pre High Cylinder Bias -0.1 -0.02 -0.2 -0.107

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.6 0.7 0.5 0.600

Calibration Post Zero Cylinder Bias 0.07 0.1 0.05 0.073

Calibration Post Zero Cylinder Drift 0.08 0.03 0.05 0.053

Calibration Post High Cylinder ID AAL6503-

NOx

AAL6503-

NOx

AAL6503-

NOx

Calibration Post High Cylinder Instrument Response 202.9 202.2 203.3 202.800

Calibration Post High Cylinder Bias -0.02 -0.2 0.07 -0.050

Calibration Post High Cylinder Drift 0.02 0.18 0.27 0.157

Cavg 204.7 208 199.7 204.133

Cavg Units ppmvd ppmvd ppmvd

Cgas 204.9597 208.4797 199.9372 204.459

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Oil

Fw 0 0.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units ppmvw

Tuesday, February 22, 2011 Page 31 of 33
Vienna

6/22/2010

Location Stack Exit - OTM - 27/28

Average

Run Number 1

Test Date 2/23/2010

Run Start Time 7:00:00 AM

Run Finish Time 10:22:00 AM

Net Traversing Points 8

Net Run Time, minutes 214

Nozzle Diameter, inches 0.214 0.214

Pitot Tube Coefficient 0.84 0.840

Dry Gas Meter Calibration Factor 1.011 1.011

Barometric Pressure, inches of Mercury 29.63 29.630

Average Orifice Meter Differential, inches H2O 0.48 0.480

Dry Gas Meter Volume Sampled, cubic feet 76.022 76.022

Average Dry Gas Meter Temperature, °F 74.06 74.060

Dry Gas Meter Volume Sampled, dscf 75.339 75.339

Total Moisture Liquid collected, g 152.7 152.700

Volume of Water Vapor, standard cubic feet 7.19 7.190

Moisture Content of Stack Gas, % 8.71 8.710

Moisture Saturation at Stack Gas Temperature, % 100.00 100.000

Dry Mole Fraction 0.9129 0.913

Carbon Dioxide, % 11.5 11.500

Oxygen, % 6.3 6.300

Carbon Monoxide & Nitrogen, % 82.2 82.200

Fuel Factor 1.27

Dry Molecular Weight, lb/lb-Mole 30.09 30.090

Wet Molecular weight, lb/lb-Mole 29.04 29.040

Flue Gas Static Pressure, inches of H2O -0.55 -0.550

Absolute Flue Gas Pressure, inches of Mercury 29.59 29.590

Average Stack Gas Temperature, °F 373.38 373.380

Average Velocity Head, inches of H2O 0.4283418687

27785

0.428

Average Stack Gas Velocity, feet/second 46.29 46.290

Stack Cross-Sectional Area, square feet 122.882 122.882

Dry Volumetric Flow Rate, dry scfm 195,219.9 195,219.900

Actual Wet Volumetric Flue Gas Flow Rate, acfm 341,292.5 341,292.500

Percent Isokinetic of Sampling Rate, % 88.7 88.700

Percent Excess Air, % 40.9 40.900

F-Factor, dscfm/MMBtu @ %O2 9504 9,504.000

Round Duct Diameter, inches 150.1

Rectangular Duct Width, inches 0

Rectangular Duct Length, inches 0

Fw 0 0.000

Fc 0 0.000

Tuesday, February 22, 2011 Page 32 of 33
Vienna

6/22/2010

Location Stack Exit - SW0010

Average

Run Number 1 2 3

Test Date 2/24/2010 2/24/2010 2/24/2010

Run Start Time 9:46:00 AM 1:06:00 PM 4:40:00 PM

Run Finish Time 12:12:00 PM 3:38:00 PM 7:35:00 PM

Net Traversing Points 120 120 120

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.283 0.283 0.283 0.283

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.988 0.988 0.988 0.988

Barometric Pressure, inches of Mercury 29.81 29.81 29.81 29.810

Average Orifice Meter Differential, inches H2O 1.58 1.60 1.51 1.563

Dry Gas Meter Volume Sampled, cubic feet 82.494 83.626 80.598 82.239

Average Dry Gas Meter Temperature, °F 88.27 88.21 80.98 85.820

Dry Gas Meter Volume Sampled, dscf 78.507 79.597 77.723 78.609

Total Moisture Liquid collected, g 139.1 140.4 133.5 137.667

Volume of Water Vapor, standard cubic feet 6.55 6.61 6.28 6.480

Moisture Content of Stack Gas, % 7.70 7.67 7.48 7.617

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.923 0.9233 0.9252 0.924

Carbon Dioxide, % 10.9 10.9 11 10.933

Oxygen, % 6.9 6.9 6.9 6.900

Carbon Monoxide & Nitrogen, % 82.2 82.2 82.1 82.167

Fuel Factor 1.28 1.28 1.27

Dry Molecular Weight, lb/lb-Mole 30.02 30.02 30.04 30.027

Wet Molecular weight, lb/lb-Mole 29.09 29.10 29.14 29.110

Flue Gas Static Pressure, inches of H2O -0.55 -0.55 -0.55 -0.550

Absolute Flue Gas Pressure, inches of Mercury 29.77 29.77 29.77 29.770

Average Stack Gas Temperature, °F 393.44 393.74 391.77 392.983

Average Velocity Head, inches of H2O 0.3898992836

31904

0.390746566

504129

0.375581663

308381

0.385

Average Stack Gas Velocity, feet/second 44.51 44.56 43.61 44.227

Stack Cross-Sectional Area, square feet 122.882 122.882 122.882 122.882

Dry Volumetric Flow Rate, dry scfm 186,456.3 186,660.8 183,480.6 185,532.567

Actual Wet Volumetric Flue Gas Flow Rate, acfm 328,168.7 328,537.3 321,533.0 326,079.667

Percent Isokinetic of Sampling Rate, % 98.7 100.0 99.3 99.333

Percent Excess Air, % 46.6 46.6 46.7 46.633

F-Factor, dscfm/MMBtu @ %O2 9518 9518 9518 9,518.000

Round Duct Diameter, inches 150.1 150.1 150.1

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, February 22, 2011 Page 33 of 33