Name: Jeff Walker

Title: Environmental Manager

Company: Cedar Bay Generating Company L.P.

Sign Date: 7/20/2010

Name: Stephen Webb

Title: Air Test Coordinator

Company: Coastal Air Consulting Inc.

Sign Date: 7/20/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Cedar Bay Generating Plant -CBB

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.

Saturday, January 22, 2011 Page 1 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

Facility Information:

Cedar Bay Generating Plant (ORIS Code 10

9640 Eastport Road(32218)

P.O. Box 26324

Jacksonville Fl 32226

Contact: Jeff Walker

Phone: 904-696-1547

Fax: 904-751-7320

Email: jeffwalker@cogentrix.com

Testing Company:

Coastal Air Consulting

245 West Ohio Avenue

Lake Helen Fl 32744

Contact: Stephen Webb

Phone: 386-451-0169

Fax:

Email: coastalair123@aol.com

Air Permit Number:

310337-016-AV

Permitted Source ID/Name:

CBB

Permitted Maximum Process Rate:

104000 lbs/hr

Max. Normal Operation Process Rate:

90000 lbs/hr

Target Process Test Rate

85000 lbs/hr

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

 process flow diagram:

CFB w/limestone injection for acid gas, SNCR for Nox control, baghouse with pulse air for particulates

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #: 110000362018

SCC / Description 10100218 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Atmospheric Fluidized Bed Combustion: Circulating Bed (Bitum. 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

duct after 

baghouse

0 109 126.6 117 237 117 6 24

Regulation Description Compound Limit Unit

40 CFR 60, Subpart Da Sulfur Dioxide 0.3 lb/million BTU 

using CO2

40 CFR 60, Subpart Da Nitrogen oxides (NOx) 0.17 lb/million BTU 

using CO2

40 CFR 60, Subpart Da Carbon Monoxide 0.175 lb/million BTU 

using CO2

40 CFR 60, Subpart Da Total Particulate 0.018 lb/million BTU 

using CO2

40 CFR 60, Subpart Da Total PM10 0.018 lb/million BTU 

using CO2

Saturday, January 22, 2011 Page 2 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

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.

N/A

Test Parameter Information:

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Total organic compounds 

(TOC)

duct after Method 25A 3 120 0

baghouse

duct after Hydrogen Fluoride Method 26A 3 180 0

baghouse

duct after Hydrogen Chloride Method 26A 3 180 0

baghouse

duct after Filterable PM2.5 OTM - 27/28 3 240 0

baghouse

Inorganic (Aqueous) 

Condensible Part.

duct after OTM - 27/28 3 240 0

baghouse

duct after Cobalt Method 29 3 240 0

baghouse

duct after Selenium Method 29 3 240 0

baghouse

duct after Nickel Method 29 3 240 0

baghouse

duct after Manganese Method 29 3 240 0

baghouse

duct after Lead Method 29 3 240 0

baghouse

duct after Arsenic Method 29 3 240 0

baghouse

duct after Chromium Method 29 3 240 0

baghouse

duct after Beryllium Method 29 3 240 0

baghouse

duct after Cadmium Method 29 3 240 0

baghouse

duct after Filterable Particulate Method 29 3 240 0

baghouse

duct after Antimony Method 29 3 240 0

baghouse

Saturday, January 22, 2011 Page 3 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

Sampling / Stack Data Results Summary

Location duct after baghouse - Method 25A

Average

Run Number 1 2 3

Test Date 5/11/2010 5/11/2010 5/11/2010

Run Start Time 11:15:00 AM 1:30:00 PM 3:45:00 PM

Run Finish Time 1:15:00 PM 3:30:00 PM 5:45:00 PM

Carbon Dioxide, % 14.679 14.341 14.727 14.582

Oxygen, % 4.982 4.854 4.808 4.881

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 8.6 8.6 8.1 8.433

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location duct after baghouse - Method 26A

Average

Run Number 1 2 3

Test Date 5/11/2010 5/11/2010 5/11/2010

Run Start Time 8:51:00 AM 12:22:00 

PM

3:45:00 PM

Run Finish Time 11:43:30 AM 3:14:30 PM 6:37:30 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 158.160 153.034 161.355 157.516

Moisture Content of Stack Gas, % 9.67 9.30 9.46 9.477

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

Carbon Dioxide, % 15.5 15.5 15.5 15.500

Oxygen, % 3.4 3.4 3.4 3.400

Average Stack Gas Temperature, °F 312.83 318.79 318.42 316.680

Dry Volumetric Flow Rate, dry scfm 243,211.9 238,310.4 252,508.5 244,676.933

Actual Wet Volumetric Flue Gas Flow Rate, acfm 411,566.4 404,724.2 429,390.6 415,227.067

Percent Isokinetic of Sampling Rate, % 101.6 100.3 99.8 100.567

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

Saturday, January 22, 2011 Page 4 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

Location duct after baghouse - Method 29

Average

Run Number 1 2 M5-3

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

Run Start Time 10:37:00 AM 3:10:00 PM 9:25:00 AM

Run Finish Time 2:27:00 PM 7:00:00 PM 1:15:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 219.275 211.065 211.331 213.890

Moisture Content of Stack Gas, % 8.80 8.77 9.61 9.060

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

Carbon Dioxide, % 15.1 15.1 15 15.067

Oxygen, % 4.6 4.5 4.4 4.500

Average Stack Gas Temperature, °F 319.21 320.00 314.38 317.863

Dry Volumetric Flow Rate, dry scfm 244,258.4 249,565.4 242,207.7 245,343.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 412,773.8 422,030.9 410,416.4 415,073.700

Percent Isokinetic of Sampling Rate, % 105.2 99.1 102.2 102.167

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 duct after baghouse - OTM - 27/28

Average

Run Number 1 2 3

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

Run Start Time 9:34:00 AM 4:28:00 PM 9:52:00 AM

Run Finish Time 2:06:00 PM 9:03:00 PM 2:35:00 PM

Net Run Time, minutes 294.25 301.25 316.75

Dry Gas Meter Volume Sampled, dscf 99.394 102.574 108.084 103.351

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, % 14.5 14.5 14.5 14.500

Oxygen, % 5 5 5 5.000

Average Stack Gas Temperature, °F 319.17 320.67 318.25 319.363

Dry Volumetric Flow Rate, dry scfm 300,173.2 307,136.7 306,508.8 304,606.233

Actual Wet Volumetric Flue Gas Flow Rate, acfm 461,474.1 473,088.6 471,478.7 468,680.467

Percent Isokinetic of Sampling Rate, % 76.3 75.1 75.5 75.633

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

Saturday, January 22, 2011 Page 5 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

Emissions Summary

Location: duct after baghouse - Method 25A

Compound: Total organic compounds (TOC)

Average

Run 1 2 3

ppm 7.39E-01 6.39E-01 9.67E-04 0.460

ppm@7%O2 6.45E-01 5.54E-01 8.35E-04 0.400

Location: duct after baghouse - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 312.613 238.567 367.184 306.121

lb/mmBtuCO2 5.06E-02 3.99E-02 5.83E-02 0.050

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.324 0.336 0.352 0.337

lb/mmBtuCO2 5.24E-05 5.62E-05 5.59E-05 0.000

Location: duct after baghouse - Method 29

Compound: Antimony

Average

RunNumber 1 2 M5-3

Mass_mg 0.0002 0.000283 0.000301 0.000

lb/mmBtuCO2 2.40E-08 3.52E-08 3.77E-08 0.000

Compound: Arsenic

Average

RunNumber 1 2 M5-3

Mass_mg 0.0006 0.001193 0.001119 0.001

lb/mmBtuCO2 7.19E-08 1.49E-07 1.40E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 M5-3

Mass_mg 0.00005 0.00007 0.000076 0.000

lb/mmBtuCO2 5.99E-09 8.72E-09 9.51E-09 0.000

Compound: Cadmium

Average

RunNumber 1 2 M5-3

Mass_mg 0.002657 0.000813 0.000682 0.001

lb/mmBtuCO2 3.18E-07 1.01E-07 8.54E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 M5-3

Mass_mg 0.00585 0.00586 0.0112 0.008

lb/mmBtuCO2 7.01E-07 7.30E-07 1.40E-06 0.000

Saturday, January 22, 2011 Page 6 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

Process Run Data

Compound: Cobalt

Average

RunNumber 1 2 M5-3

Mass_mg 0.000838 0.000532 0.000835 0.001

lb/mmBtuCO2 1.00E-07 6.62E-08 1.05E-07 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 M5-3

Mass_mg 19.8 16.8 81.6 39.400

lb/mmBtuCO2 2.37E-03 2.09E-03 1.02E-02 0.005

Compound: Lead

Average

RunNumber 1 2 M5-3

Mass_mg 0.00285 0.00289 0.002043 0.003

lb/mmBtuCO2 3.42E-07 3.60E-07 2.56E-07 0.000

Compound: Manganese

Average

RunNumber 1 2 M5-3

Mass_mg 0.00265 0.003038 0.00393 0.003

lb/mmBtuCO2 3.18E-07 3.78E-07 4.92E-07 0.000

Compound: Nickel

Average

RunNumber 1 2 M5-3

Mass_mg 0.0075 0.00526 0.00516 0.006

lb/mmBtuCO2 8.99E-07 6.55E-07 6.46E-07 0.000

Compound: Selenium

Average

RunNumber 1 2 M5-3

Mass_mg 0.000612 0.00793 0.00311 0.004

lb/mmBtuCO2 7.33E-08 9.87E-07 3.89E-07 0.000

Location: duct after baghouse - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 0.014 0 0.001 0.005

lb/mmBtuCO2 3.85E-06 0.00E+00 2.53E-07 0.000

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 5.7 5.5 6 5.733

lb/mmBtuCO2 1.57E-03 1.47E-03 1.52E-03 0.002

Saturday, January 22, 2011 Page 7 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 43.5 Tons/hr 45

2 Bituminous Coal Burned 44 Tons/hr 45

3 Bituminous Coal Burned 43 Tons/hr 45

1 heat input 1090 lbs/mmBtu 1000

2 heat input 1090 lbs/mmBtu 1000

3 heat input 1080 lbs/mmBtu 1000

1 steam output 798 llbs/hr 750

2 steam output 802 llbs/hr 750

3 steam output 782 llbs/hr 750

Run Name Value UOM Comments

Target

Value

1 FLUID BED DRY SCRUBBER 0.24 lbs/mmBtu 0.25

2 FLUID BED DRY SCRUBBER 0.23 lbs/mmBtu 0.25

3 FLUID BED DRY SCRUBBER 0 lbs/mmBtu 0.25

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0.16 lbs/mmBtu 0.16

2 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0.16 lbs/mmBtu 0.16

3 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 lbs/mmBtu 0.16

1 BAGHOUSE 3 per cent 10

2 BAGHOUSE 2 per cent 10

3 BAGHOUSE 0 per cent 10

Run Name Value UOM Comments

1 btu value of coal 12394 btu/lb

Saturday, January 22, 2011 Page 8 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

Sampling / Stack Data Results Detail

Location duct after baghouse - Method 25A

Average

Run Number 1 2 3

Test Date 5/11/2010 5/11/2010 5/11/2010

Run Start Time 11:15:00 AM 1:30:00 PM 3:45:00 PM

Run Finish Time 1:15:00 PM 3:30:00 PM 5:45:00 PM

Carbon Dioxide, % 14.679 14.341 14.727 14.582

Oxygen, % 4.982 4.854 4.808 4.881

Fuel Factor 1.08 1.12 1.09

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 8.6 8.6 8.1 8.433

Analyzer Make Vig Vig Vig

Analyzer Model 20 20 20 20.000

Analyzer Serial Number 1591203 1591203 1591203 1,591,203.0

00

Operating Range 20 20 20 20.000

Operating Units ppm ppm ppm

No. Readings/Avg. 120 120 120 120.000

Calibration Set 0 0 0 0.000

Calibration Pre Zero Cylinder ID CC-231298 CC-231298 CC-231298

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB-0017527 EB-0017527 EB-0017527

Calibration Pre High Cylinder Instrument Response 6 6 6 6.000

Calibration Pre High Cylinder Bias 0 0 0 0.000

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC-231298 CC-231298 CC-231298

Calibration Post Zero Cylinder Instrument Response 0 0.1 0.1 0.067

Calibration Post Zero Cylinder Bias 0 0.5 0.5 0.333

Calibration Post Zero Cylinder Drift 0 0.5 0.5 0.333

Calibration Post High Cylinder ID EB-0017527 EB-0017527 EB-0017527

Calibration Post High Cylinder Instrument Response 6 6.1 6 6.033

Calibration Post High Cylinder Bias 0 0.5 0 0.167

Calibration Post High Cylinder Drift 0 0.5 0 0.167

Cavg 0.74 0.69 1.01 0.813

Cavg Units ppmvd ppmvd ppbvd

Cgas 0.7388 0.6389 0.9665 0.781

Cgas Units ppmvd ppmvd ppbvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units ppmvw

Saturday, January 22, 2011 Page 9 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

Location duct after baghouse - Method 26A

Average

Run Number 1 2 3

Test Date 5/11/2010 5/11/2010 5/11/2010

Run Start Time 8:51:00 AM 12:22:00 PM 3:45:00 PM

Run Finish Time 11:43:30 AM 3:14:30 PM 6:37:30 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.25 0.25 0.25 0.250

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.925 0.925 0.925 0.925

Barometric Pressure, inches of Mercury 30.19 30.19 30.19 30.190

Average Orifice Meter Differential, inches H2O 2.59 2.50 2.81 2.633

Dry Gas Meter Volume Sampled, cubic feet 174.159 171.536 183.546 176.414

Average Dry Gas Meter Temperature, °F 86.08 95.75 104.42 95.417

Dry Gas Meter Volume Sampled, dscf 158.160 153.034 161.355 157.516

Total Moisture Liquid collected, g 359.8 333.5 358.1 350.467

Volume of Water Vapor, standard cubic feet 16.94 15.70 16.86 16.500

Moisture Content of Stack Gas, % 9.67 9.30 9.46 9.477

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

Dry Mole Fraction 0.9033 0.907 0.9054 0.905

Carbon Dioxide, % 15.5 15.5 15.5 15.500

Oxygen, % 3.4 3.4 3.4 3.400

Carbon Monoxide & Nitrogen, % 81.1 81.1 81.1 81.100

Fuel Factor 1.13 1.13 1.13

Dry Molecular Weight, lb/lb-Mole 30.62 30.62 30.62 30.620

Wet Molecular weight, lb/lb-Mole 29.40 29.45 29.43 29.427

Flue Gas Static Pressure, inches of H2O -21 -21 -21 -21.000

Absolute Flue Gas Pressure, inches of Mercury 28.65 28.65 28.65 28.650

Average Stack Gas Temperature, °F 312.83 318.79 318.42 316.680

Average Velocity Head, inches of H2O 1.0827382124

7391

1.040833561

54751

1.171359211

61541

1.098

Average Stack Gas Velocity, feet/second 71.58 70.39 74.68 72.217

Stack Cross-Sectional Area, square feet 95.829 95.829 95.829 95.829

Dry Volumetric Flow Rate, dry scfm 243,211.9 238,310.4 252,508.5 244,676.933

Actual Wet Volumetric Flue Gas Flow Rate, acfm 411,566.4 404,724.2 429,390.6 415,227.067

Percent Isokinetic of Sampling Rate, % 101.6 100.3 99.8 100.567

Percent Excess Air, % 18.9 18.9 18.9 18.900

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 126.6 126.6 126.6

Rectangular Duct Length, inches 109 109 109

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, January 22, 2011 Page 10 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

Location duct after baghouse - Method 29

Average

Run Number 1 2 M5-3

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

Run Start Time 10:37:00 AM 3:10:00 PM 9:25:00 AM

Run Finish Time 2:27:00 PM 7:00:00 PM 1:15:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.25 0.25 0.25 0.250

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.925 0.925 0.925 0.925

Barometric Pressure, inches of Mercury 30.19 30.19 30.19 30.190

Average Orifice Meter Differential, inches H2O 2.60 2.71 2.58 2.630

Dry Gas Meter Volume Sampled, cubic feet 244.655 238.926 234.312 239.298

Average Dry Gas Meter Temperature, °F 93.33 101.54 89.83 94.900

Dry Gas Meter Volume Sampled, dscf 219.275 211.065 211.331 213.890

Total Moisture Liquid collected, g 449.3 430.8 477.3 452.467

Volume of Water Vapor, standard cubic feet 21.15 20.28 22.47 21.300

Moisture Content of Stack Gas, % 8.80 8.77 9.61 9.060

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

Dry Mole Fraction 0.912 0.9123 0.9039 0.909

Carbon Dioxide, % 15.1 15.1 15 15.067

Oxygen, % 4.6 4.5 4.4 4.500

Carbon Monoxide & Nitrogen, % 80.3 80.4 80.6 80.433

Fuel Factor 1.08 1.09 1.10

Dry Molecular Weight, lb/lb-Mole 30.60 30.60 30.58 30.593

Wet Molecular weight, lb/lb-Mole 29.49 29.49 29.37 29.450

Flue Gas Static Pressure, inches of H2O -21 -21 -21 -21.000

Absolute Flue Gas Pressure, inches of Mercury 28.65 28.65 28.65 28.650

Average Stack Gas Temperature, °F 319.21 320.00 314.38 317.863

Average Velocity Head, inches of H2O 1.0837202309

1279

1.131764993

21124

1.073478164

92964

1.096

Average Stack Gas Velocity, feet/second 71.79 73.40 71.38 72.190

Stack Cross-Sectional Area, square feet 95.829 95.829 95.829 95.829

Dry Volumetric Flow Rate, dry scfm 244,258.4 249,565.4 242,207.7 245,343.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 412,773.8 422,030.9 410,416.4 415,073.700

Percent Isokinetic of Sampling Rate, % 105.2 99.1 102.2 102.167

Percent Excess Air, % 27.7 26.9 26.1 26.900

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 126.6 126.6 126.6

Rectangular Duct Length, inches 109 109 109

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, January 22, 2011 Page 11 of 12
Cedar Bay Generating Plant -CBB

7/20/2010

Location duct after baghouse - OTM - 27/28

Average

Run Number 1 2 3

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

Run Start Time 9:34:00 AM 4:28:00 PM 9:52:00 AM

Run Finish Time 2:06:00 PM 9:03:00 PM 2:35:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 294.25 301.25 316.75

Nozzle Diameter, inches 0.161 0.161 0.161 0.161

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.948 0.948 0.948 0.948

Barometric Pressure, inches of Mercury 30.19 30.19 30.21 30.197

Average Orifice Meter Differential, inches H2O 0.47 0.50 0.47 0.480

Dry Gas Meter Volume Sampled, cubic feet 107.656 113.035 117.329 112.673

Average Dry Gas Meter Temperature, °F 87.67 97.25 89.25 91.390

Dry Gas Meter Volume Sampled, dscf 99.394 102.574 108.084 103.351

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, % 14.5 14.5 14.5 14.500

Oxygen, % 5 5 5 5.000

Carbon Monoxide & Nitrogen, % 80.5 80.5 80.5 80.500

Fuel Factor 1.10 1.10 1.10

Dry Molecular Weight, lb/lb-Mole 30.52 30.52 30.52 30.520

Wet Molecular weight, lb/lb-Mole 30.52 30.52 30.52 30.520

Flue Gas Static Pressure, inches of H2O -20 -20 -21 -20.333

Absolute Flue Gas Pressure, inches of Mercury 28.72 28.72 28.67 28.703

Average Stack Gas Temperature, °F 319.17 320.67 318.25 319.363

Average Velocity Head, inches of H2O 1.4052786577

494

1.474125066

63054

1.466008403

37519

1.448

Average Stack Gas Velocity, feet/second 80.26 82.28 82.00 81.513

Stack Cross-Sectional Area, square feet 95.829 95.829 95.829 95.829

Dry Volumetric Flow Rate, dry scfm 300,173.2 307,136.7 306,508.8 304,606.233

Actual Wet Volumetric Flue Gas Flow Rate, acfm 461,474.1 473,088.6 471,478.7 468,680.467

Percent Isokinetic of Sampling Rate, % 76.3 75.1 75.5 75.633

Percent Excess Air, % 30.8 30.8 30.8 30.800

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 126.6 126.6 126.6

Rectangular Duct Length, inches 109 109 109

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, January 22, 2011 Page 12 of 12