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.

Monday, February 07, 2011 Page 1 of 34
Facility Information:

Georgia Power Plant McManus

1 Crispen Island

Brunswick Ga 31525

Contact: Sarah Markham

Phone: 205-257-6780

Fax:

Email: sasander@southernco.com

Testing Company:

Weston Solutions

1625 Pumphrey Ave

Auburn Al 36832

Contact:Jon Howard

Phone: 33-466-5600

Fax:

Email: j.howard@westonsolutions.com

Air Permit Number:

715

Permitted Source ID/Name:

1 McManus Unit 1

Permitted Maximum Process Rate: Max. Normal Operation Process Rate: Target Process Test Rat

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

 process flow diagram:

See attached report

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description

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 160.5 0 0 0 1200 480 2 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Carbon Monoxide Method 10 3 0

Stack Formaldehyde Method 0011 3 0

Stack 2,3,7,8-TCDD Method 23 3 0

Stack 1,2,3,7,8-PeCDD Method 23 3 0

Stack 1,2,3,4,7,8-HxCDD Method 23 3 0

Stack 1,2,3,6,7,8-HxCDD Method 23 3 0

Stack 1,2,3,7,8,9-HxCDD Method 23 3 0

Stack 1,2,3,4,6,7,8-HpCDD Method 23 3 0

Monday, February 07, 2011 Page 2 of 34
Stack OCDD Method 23 3 0

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

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

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

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

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

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

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

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

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

Stack OCDF Method 23 3 0

Stack Other TCDD Method 23 0

Stack Other PeCDD Method 23 0

Stack Other HxCDD Method 23 0

Stack Other HpCDD Method 23 0

Stack Other TCDF Method 23 0

Stack Other PeCDF Method 23 0

Stack Other HxCDF Method 23 0

Stack Other HpCDF Method 23 0

Stack 3,3',4,4'-TCB (PCB77) Method 23 3 0

Stack 3,4,4',5-TCB (PCB81) Method 23 3 0

Stack 2,3,3',4,4'-PeCB (PCB105) Method 23 3 0

Stack 2,3,4,4',5-PeCB (PCB114) Method 23 3 0

Stack 2,3',4,4',5-PeCB (PCB118) Method 23 3 0

Stack 2',3,4,4',5-PeCB (PCB123) Method 23 3 0

Stack 3,3',4,4',5-PeCB (PCB126) Method 23 3 0

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

HxCB (PCBs156/157)

Stack Method 23 3 0

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

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

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

(PCB189)

Stack Method 23 3 0

Total organic compounds 

(TOC) as Propane

Stack Method 25A 3 0

Stack Hydrogen Fluoride Method 26A 3 0

Stack Hydrogen Chloride Method 26A 3 0

Stack Filterable PM2.5 OTM - 27 3 0

Stack Total Particulate OTM - 28 3 0

Organic Condensible 

Particulate

Stack OTM - 28 3 0

Inorganic (Aqueous) 

Condensible Part.

Stack OTM - 28 3 0

Stack Cobalt Method 29 3 0

Stack Filterable Particulate Method 29 3 0

Stack Phosphorus (yellow or white) Method 29 3 0

Stack Selenium Method 29 3 0

Stack Nickel Method 29 3 0

Stack Lead Method 29 3 0

Stack Chromium Method 29 3 0

Stack Cadmium Method 29 3 0

Stack Beryllium Method 29 3 0

Stack Antimony Method 29 3 0

Stack Arsenic Method 29 3 0

Monday, February 07, 2011 Page 3 of 34
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.

See attached report

Stack Manganese Method 29 3 0

Stack O2 Method 3A O2 3 0

Stack Co2 Method 3A CO2 3 0

Stack Sulfur Dioxide Method 6C 3 0

Stack Nitrogen oxides (NOx) Method 7E 3 0

Monday, February 07, 2011 Page 4 of 34
Sampling / Stack Data Results Summary

Location Stack - Method 0011

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 9:27:00 AM 1:16:00 PM 4:55:00 PM

Run Finish Time 11:40:00 AM 3:27:00 PM 7:05:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 62.790 58.379 59.144 60.104

Moisture Content of Stack Gas, % 9.80 9.88 10.12 9.933

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

Carbon Dioxide, % 11 10.9 10.9 10.933

Oxygen, % 6.9 6.7 6.8 6.800

Average Stack Gas Temperature, °F 310.46 312.50 313.83 312.263

Dry Volumetric Flow Rate, dry scfm 161,970.0 154,945.1 158,619.7 158,511.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 261,414.3 250,961.1 258,042.3 256,805.900

Percent Isokinetic of Sampling Rate, % 103.9 101.0 99.9 101.600

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location Stack - Method 10

Average

Run Number 1 2 3

Test Date 4/6/2010 4/6/2010 4/6/2010

Run Start Time 10:02:00 AM 12:07:00 

PM

2:11:00 PM

Run Finish Time 11:56:00 AM 1:59:00 PM 4:02:00 PM

Carbon Dioxide, % 11 11.2 11.1 11.100

Oxygen, % 6.8 6.5 6.6 6.633

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 5 of 34
Location Stack - Method 23

Average

Run Number 1 2 3

Test Date 4/8/2010 4/11/2010 4/12/2010

Run Start Time 8:29:00 AM 12:05:00 

AM

6:20:00 AM

Run Finish Time 6:01:00 PM 4:00:00 PM 8:57:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 273.001 304.634 293.342 290.326

Moisture Content of Stack Gas, % 10.76 8.45 8.64 9.283

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

Carbon Dioxide, % 10.8 10.1 10.2 10.367

Oxygen, % 6.7 7.8 7.6 7.367

Average Stack Gas Temperature, °F 317.85 317.52 317.75 317.707

Dry Volumetric Flow Rate, dry scfm 154,828.3 164,040.7 166,854.3 161,907.767

Actual Wet Volumetric Flue Gas Flow Rate, acfm 255,766.2 261,498.6 267,146.7 261,470.500

Percent Isokinetic of Sampling Rate, % 98.5 100.4 95.1 98.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location Stack - Method 25A

Average

Run Number 1 2 3

Test Date 4/6/2010 4/6/2010 4/6/2010

Run Start Time 10:02:00 AM 12:07:00 

PM

2:11:00 PM

Run Finish Time 11:56:00 AM 1:59:00 PM 4:02:00 PM

Carbon Dioxide, % 11 11.2 11.1 11.100

Oxygen, % 6.8 6.5 6.6 6.633

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 6 of 34
Location Stack - Method 26A

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 11:31:00 AM 2:57:00 

AM

4:38:00 PM

Run Finish Time 1:40:00 PM 4:10:00 PM 6:32:00 PM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 36.806 35.377 35.795 35.993

Moisture Content of Stack Gas, % 15.63 15.32 15.69 15.547

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

Carbon Dioxide, % 11.5 11.5 11.4 11.467

Oxygen, % 7 7.1 7.1 7.067

Average Stack Gas Temperature, °F 311.96 313.13 314.92 313.337

Dry Volumetric Flow Rate, dry scfm 145,550.6 142,443.7 141,785.0 143,259.767

Actual Wet Volumetric Flue Gas Flow Rate, acfm 251,635.5 245,734.5 246,240.3 247,870.100

Percent Isokinetic of Sampling Rate, % 110.1 108.1 109.9 109.367

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 7 of 34
Location Stack - Method 29

Average

Run Number 1 2 3

Test Date 4/13/2010 4/14/2010 4/14/2010

Run Start Time 12:12:00 PM 6:25:00 

AM

11:50:00 AM

Run Finish Time 5:22:00 PM 9:20:00 

AM

4:00:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 149.603 146.648 145.866 147.372

Moisture Content of Stack Gas, % 8.61 8.82 9.06 8.830

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

Carbon Dioxide, % 10.5 10.8 10.7 10.667

Oxygen, % 7.3 7.1 7 7.133

Average Stack Gas Temperature, °F 335.06 318.10 330.06 327.740

Dry Volumetric Flow Rate, dry scfm 159,008.6 158,360.7 156,122.2 157,830.500

Actual Wet Volumetric Flue Gas Flow Rate, acfm 259,391.1 253,405.8 254,333.1 255,710.000

Percent Isokinetic of Sampling Rate, % 101.8 100.2 101.1 101.033

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 4/6/2010 4/6/2010 4/6/2010

Run Start Time 10:02:00 AM 12:07:00 

PM

2:11:00 PM

Run Finish Time 11:56:00 AM 1:59:00 PM 4:02:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 0 0 0 0.000

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Moisture, % 0 0 0 0.000

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Monday, February 07, 2011 Page 8 of 34
Location Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 4/6/2010 4/6/2010 4/6/2010

Run Start Time 10:02:00 AM 2:11:00 PM

Run Finish Time 11:56:00 AM 4:02:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 0 0 0 0.000

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Moisture, % 0 0 0 0.000

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack - Method 6C

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 9:27:00 AM 11:31:00 

AM

1:16:00 PM

Run Finish Time 11:23:00 AM 12:51:00 

PM

4:10:00 PM

Carbon Dioxide, % 11 11.1 11 11.033

Oxygen, % 6.9 6.7 6.8 6.800

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 9 of 34
Location Stack - Method 7E

Average

Run Number 1 2 3

Test Date 4/6/2010 4/6/2010 4/6/2010

Run Start Time 10:02:00 AM 12:07:00 

PM

2:11:00 PM

Run Finish Time 11:56:00 AM 1:59:00 PM 4:02:00 PM

Carbon Dioxide, % 11 11.2 11.1 11.100

Oxygen, % 6.8 6.5 6.6 6.633

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location Stack - OTM - 27

Average

Run Number 1 2 3

Test Date 4/8/2010 4/8/2010 4/11/2010

Run Start Time 12:50:00 PM 4:29:00 PM 6:15:00 AM

Run Finish Time 1:58:00 PM 6:50:00 PM 7:30:00 AM

Net Run Time, minutes 57.75 58.25 59.25

Dry Gas Meter Volume Sampled, dscf 20.896 21.283 21.534 21.238

Moisture Content of Stack Gas, % 11.10 11.77 9.42 10.763

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

Carbon Dioxide, % 10.9 10 10.1 10.333

Oxygen, % 6.7 7 7.6 7.100

Average Stack Gas Temperature, °F 317.69 319.46 304.21 313.787

Dry Volumetric Flow Rate, dry scfm 156,761.7 152,608.8 163,754.1 157,708.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 259,896.9 255,513.3 261,835.8 259,082.000

Percent Isokinetic of Sampling Rate, % 100.7 104.4 96.8 100.633

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 10 of 34
Location Stack - OTM - 28

Average

Run Number 1 2 3

Test Date 4/13/2010 4/14/2010 4/14/2010

Run Start Time 12:15:00 PM 6:42:00 

AM

12:19:00 PM

Run Finish Time 5:19:00 PM 11:58:00 

AM

3:01:00 PM

Net Run Time, minutes 240 240 125

Dry Gas Meter Volume Sampled, dscf 144.833 136.460 72.409 117.901

Moisture Content of Stack Gas, % 8.80 10.05 9.18 9.343

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

Carbon Dioxide, % 10.5 10.8 10.5 10.600

Oxygen, % 7.3 7.1 7.1 7.167

Average Stack Gas Temperature, °F 335.81 320.42 330.92 329.050

Dry Volumetric Flow Rate, dry scfm 159,199.4 153,427.3 158,070.3 156,899.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 260,402.7 249,528.0 258,042.3 255,991.000

Percent Isokinetic of Sampling Rate, % 101.6 99.3 98.2 99.700

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 11 of 34
Emissions Summary

Location: Stack - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.447 0.402 0.106 0.318

lb/mmBtuO2 2.15E-04 2.05E-04 5.38E-05 0.000

ppm 2.01E-01 1.95E-01 5.07E-02 0.149

ppm@7%O2 2.00E-01 1.91E-01 5.00E-02 0.147

Location: Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000

lb/mmBtuO2 1.04E-03 1.53E-03 1.03E-03 0.001

ppm 1.05E+00 1.58E+00 1.05E+00 1.227

ppm@7%O2 1.04E+00 1.53E+00 1.02E+00 1.197

Location: Stack - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000016 0.0000000016 0.0000000016 0.000

lb/mmBtuO2 1.75E-13 1.70E-13 1.74E-13 0.000

ng/dscm 2.07E-04 1.86E-04 1.93E-04 0.000

ng/dscm@7%O2 2.03E-04 1.97E-04 2.02E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000039 0.0000000098 0.0000000063 0.000

lb/mmBtuO2 4.26E-13 1.04E-12 6.84E-13 0.000

ng/dscm 5.05E-04 1.14E-03 7.59E-04 0.001

ng/dscm@7%O2 4.94E-04 1.21E-03 7.93E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000002 0.0000000021 0.0000000021 0.000

lb/mmBtuO2 2.18E-13 2.23E-13 2.28E-13 0.000

ng/dscm 2.59E-04 2.43E-04 2.53E-04 0.000

ng/dscm@7%O2 2.54E-04 2.58E-04 2.64E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000016 0.0000000018 0.000

lb/mmBtuO2 1.86E-13 1.70E-13 1.95E-13 0.000

ng/dscm 2.20E-04 1.86E-04 2.17E-04 0.000

ng/dscm@7%O2 2.15E-04 1.97E-04 2.27E-04 0.000

Monday, February 07, 2011 Page 12 of 34
Compound: 1,2,3,4,7,8-HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000018 0.0000000015 0.0000000015 0.000

lb/mmBtuO2 1.97E-13 1.59E-13 1.63E-13 0.000

ng/dscm 2.33E-04 1.74E-04 1.81E-04 0.000

ng/dscm@7%O2 2.28E-04 1.85E-04 1.89E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000016 0.0000000017 0.000

lb/mmBtuO2 1.86E-13 1.70E-13 1.85E-13 0.000

ng/dscm 2.20E-04 1.86E-04 2.05E-04 0.000

ng/dscm@7%O2 2.15E-04 1.97E-04 2.14E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000016 0.0000000016 0.0000000014 0.000

lb/mmBtuO2 1.75E-13 1.70E-13 1.52E-13 0.000

ng/dscm 2.07E-04 1.86E-04 1.69E-04 0.000

ng/dscm@7%O2 2.03E-04 1.97E-04 1.77E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000016 0.0000000015 0.0000000017 0.000

lb/mmBtuO2 1.75E-13 1.59E-13 1.85E-13 0.000

ng/dscm 2.07E-04 1.74E-04 2.05E-04 0.000

ng/dscm@7%O2 2.03E-04 1.85E-04 2.14E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000022 0.0000000021 0.0000000018 0.000

lb/mmBtuO2 2.40E-13 2.23E-13 1.95E-13 0.000

ng/dscm 2.85E-04 2.43E-04 2.17E-04 0.000

ng/dscm@7%O2 2.79E-04 2.58E-04 2.27E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000015 0.0000000021 0.0000000016 0.000

lb/mmBtuO2 1.64E-13 2.23E-13 1.74E-13 0.000

ng/dscm 1.94E-04 2.43E-04 1.93E-04 0.000

ng/dscm@7%O2 1.90E-04 2.58E-04 2.02E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000017 0.0000000016 0.000

lb/mmBtuO2 1.86E-13 1.80E-13 1.74E-13 0.000

Monday, February 07, 2011 Page 13 of 34
ng/dscm 2.20E-04 1.97E-04 1.93E-04 0.000

ng/dscm@7%O2 2.15E-04 2.09E-04 2.02E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000014 0.000000013 0.000000024 0.000

lb/mmBtuO2 1.53E-12 1.38E-12 2.60E-12 0.000

ng/dscm 1.81E-03 1.51E-03 2.89E-03 0.002

ng/dscm@7%O2 1.77E-03 1.60E-03 3.02E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.000000095 0.00000005 0.000000048 0.000

lb/mmBtuO2 1.04E-11 5.31E-12 5.21E-12 0.000

ng/dscm 1.23E-02 5.80E-03 5.78E-03 0.008

ng/dscm@7%O2 1.20E-02 6.15E-03 6.04E-03 0.008

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

Average

RunNumber 1 2 3

Mass_mg 0.00000043 0.00000033 0.00000027 0.000

lb/mmBtuO2 4.70E-11 3.50E-11 2.93E-11 0.000

ng/dscm 5.56E-02 3.83E-02 3.25E-02 0.042

ng/dscm@7%O2 5.44E-02 4.06E-02 3.40E-02 0.043

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

Average

RunNumber 1 2 3

Mass_mg 0.000000027 0.000000015 0.00000002 0.000

lb/mmBtuO2 2.95E-12 1.59E-12 2.17E-12 0.000

ng/dscm 3.49E-03 1.74E-03 2.41E-03 0.003

ng/dscm@7%O2 3.42E-03 1.85E-03 2.52E-03 0.003

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

Average

RunNumber 1 2 3

Mass_mg 0.000000024 0.00000002 0.000000016 0.000

lb/mmBtuO2 2.62E-12 2.12E-12 1.74E-12 0.000

ng/dscm 3.11E-03 2.32E-03 1.93E-03 0.002

ng/dscm@7%O2 3.04E-03 2.46E-03 2.02E-03 0.003

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

Average

RunNumber 1 2 3

Mass_mg 0.0000012 0.00000089 0.0000007 0.000

lb/mmBtuO2 1.31E-10 9.44E-11 7.60E-11 0.000

ng/dscm 1.55E-01 1.03E-01 8.43E-02 0.114

ng/dscm@7%O2 1.52E-01 1.09E-01 8.81E-02 0.116

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

Average

RunNumber 1 2 3

Monday, February 07, 2011 Page 14 of 34
Mass_mg 0.0000000094 0.00000002 0.000000014 0.000

lb/mmBtuO2 1.03E-12 2.12E-12 1.52E-12 0.000

ng/dscm 1.22E-03 2.32E-03 1.69E-03 0.002

ng/dscm@7%O2 1.19E-03 2.46E-03 1.77E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.000000002 0.0000000021 0.0000000017 0.000

lb/mmBtuO2 2.18E-13 2.23E-13 1.85E-13 0.000

ng/dscm 2.59E-04 2.43E-04 2.05E-04 0.000

ng/dscm@7%O2 2.54E-04 2.58E-04 2.14E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000016 0.0000000016 0.0000000015 0.000

lb/mmBtuO2 1.75E-13 1.70E-13 1.63E-13 0.000

ng/dscm 2.07E-04 1.86E-04 1.81E-04 0.000

ng/dscm@7%O2 2.03E-04 1.97E-04 1.89E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000016 0.0000000024 0.0000000021 0.000

lb/mmBtuO2 1.75E-13 2.55E-13 2.28E-13 0.000

ng/dscm 2.07E-04 2.78E-04 2.53E-04 0.000

ng/dscm@7%O2 2.03E-04 2.95E-04 2.64E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000015 0.0000000016 0.0000000075 0.000

lb/mmBtuO2 1.64E-13 1.70E-13 8.14E-13 0.000

ng/dscm 1.94E-04 1.86E-04 9.03E-04 0.000

ng/dscm@7%O2 1.90E-04 1.97E-04 9.44E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000073 0.000000014 0.000000014 0.000

lb/mmBtuO2 7.97E-13 1.49E-12 1.52E-12 0.000

ng/dscm 9.44E-04 1.62E-03 1.69E-03 0.001

ng/dscm@7%O2 9.24E-04 1.72E-03 1.77E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000092 0.00000002 0.000000014 0.000

lb/mmBtuO2 1.00E-12 2.12E-12 1.52E-12 0.000

ng/dscm 1.19E-03 2.32E-03 1.69E-03 0.002

ng/dscm@7%O2 1.16E-03 2.46E-03 1.77E-03 0.002

Monday, February 07, 2011 Page 15 of 34
Compound: 3,3',4,4'-TCB (PCB77)

Average

RunNumber 1 2 3

Mass_mg 0.000000083 0.00000014 0.000000063 0.000

lb/mmBtuO2 9.07E-12 1.49E-11 6.84E-12 0.000

ng/dscm 1.07E-02 1.62E-02 7.59E-03 0.011

ng/dscm@7%O2 1.05E-02 1.72E-02 7.93E-03 0.012

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000053 0.000000013 0.0000000097 0.000

lb/mmBtuO2 5.79E-13 1.38E-12 1.05E-12 0.000

ng/dscm 6.86E-04 1.51E-03 1.17E-03 0.001

ng/dscm@7%O2 6.72E-04 1.60E-03 1.22E-03 0.001

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000031 0.000000016 0.0000000035 0.000

lb/mmBtuO2 3.39E-13 1.70E-12 3.80E-13 0.000

ng/dscm 4.01E-04 1.86E-03 4.21E-04 0.001

ng/dscm@7%O2 3.93E-04 1.97E-03 4.40E-04 0.001

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000033 0.0000000033 0.0000000036 0.000

lb/mmBtuO2 3.60E-13 3.50E-13 3.91E-13 0.000

ng/dscm 4.27E-04 3.83E-04 4.33E-04 0.000

ng/dscm@7%O2 4.18E-04 4.06E-04 4.53E-04 0.000

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

Monday, February 07, 2011 Page 16 of 34
ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000055 0.00000005 0.00000004 0.000

lb/mmBtuO2 6.01E-12 5.31E-12 4.34E-12 0.000

ng/dscm 7.12E-03 5.80E-03 4.82E-03 0.006

ng/dscm@7%O2 6.97E-03 6.15E-03 5.04E-03 0.006

Location: Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000

lb/mmBtuO2 1.07E-03 1.05E-03 9.08E-04 0.001

ppm 6.89E-01 6.89E-01 5.90E-01 0.656

ppm@7%O2 6.79E-01 6.65E-01 5.73E-01 0.639

Location: Stack - Method 26A

Monday, February 07, 2011 Page 17 of 34
Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 1.53 1.2 1.07 1.267

lb/mmBtuO2 1.27E-03 1.04E-03 9.17E-04 0.001

ppm 9.68E-01 7.90E-01 6.96E-01 0.818

ppm@7%O2 9.68E-01 7.96E-01 7.01E-01 0.822

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.236 0.434 0.373 0.348

lb/mmBtuO2 1.95E-04 3.76E-04 3.20E-04 0.000

ppm 2.72E-01 5.21E-01 4.42E-01 0.412

ppm@7%O2 2.72E-01 5.25E-01 4.45E-01 0.414

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0748 0.0756 0.0765 0.076

lb/mmBtuO2 1.56E-05 1.58E-05 1.60E-05 0.000

mg/dscm 1.77E-02 1.82E-02 1.85E-02 0.018

mg/dscm@7%O2 1.81E-02 1.83E-02 1.85E-02 0.018

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.01263 0.01293 0.01263 0.013

lb/mmBtuO2 2.63E-06 2.71E-06 2.64E-06 0.000

mg/dscm 2.98E-03 3.11E-03 3.06E-03 0.003

mg/dscm@7%O2 3.05E-03 3.13E-03 3.06E-03 0.003

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.0015 0.0015 0.0015 0.002

lb/mmBtuO2 3.12E-07 3.14E-07 3.13E-07 0.000

mg/dscm 3.54E-04 3.61E-04 3.63E-04 0.000

mg/dscm@7%O2 3.62E-04 3.64E-04 3.63E-04 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0021 0.0015 0.00205 0.002

lb/mmBtuO2 4.37E-07 3.14E-07 4.28E-07 0.000

mg/dscm 4.96E-04 3.61E-04 4.96E-04 0.000

mg/dscm@7%O2 5.07E-04 3.64E-04 4.96E-04 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.02067 0.01647 0.01677 0.018

Monday, February 07, 2011 Page 18 of 34
lb/mmBtuO2 4.30E-06 3.45E-06 3.50E-06 0.000

mg/dscm 4.88E-03 3.97E-03 4.06E-03 0.004

mg/dscm@7%O2 4.99E-03 4.00E-03 4.06E-03 0.004

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.119 0.114 0.117 0.117

lb/mmBtuO2 2.48E-05 2.39E-05 2.44E-05 0.000

mg/dscm 2.81E-02 2.75E-02 2.83E-02 0.028

mg/dscm@7%O2 2.87E-02 2.77E-02 2.83E-02 0.028

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 273 231 228 244.000

lb/mmBtuO2 5.68E-02 4.83E-02 4.76E-02 0.051

mg/dscm 6.45E+01 5.56E+01 5.52E+01 58.433

mg/dscm@7%O2 6.59E+01 5.60E+01 5.52E+01 59.033

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.02229 0.02139 0.02179 0.022

lb/mmBtuO2 4.64E-06 4.48E-06 4.55E-06 0.000

mg/dscm 5.26E-03 5.15E-03 5.28E-03 0.005

mg/dscm@7%O2 5.38E-03 5.19E-03 5.28E-03 0.005

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.593 0.565 0.577 0.578

lb/mmBtuO2 1.23E-04 1.18E-04 1.21E-04 0.000

mg/dscm 1.40E-01 1.36E-01 1.40E-01 0.139

mg/dscm@7%O2 1.43E-01 1.37E-01 1.40E-01 0.140

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 4.76209 4.53209 4.63209 4.642

lb/mmBtuO2 9.91E-04 9.48E-04 9.67E-04 0.001

mg/dscm 1.12E+00 1.09E+00 1.12E+00 1.110

mg/dscm@7%O2 1.14E+00 1.10E+00 1.12E+00 1.120

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Mass_mg 0.9176 0.8936 0.91295 0.908

lb/mmBtuO2 1.91E-04 1.87E-04 1.91E-04 0.000

mg/dscm 2.17E-01 2.15E-01 2.21E-01 0.218

mg/dscm@7%O2 2.22E-01 2.17E-01 2.21E-01 0.220

Compound: Selenium

Average

Monday, February 07, 2011 Page 19 of 34
RunNumber 1 2 3

Mass_mg 0.0374 0.015 0.019 0.024

lb/mmBtuO2 7.78E-06 3.14E-06 3.97E-06 0.000

mg/dscm 8.83E-03 3.61E-03 4.60E-03 0.006

mg/dscm@7%O2 9.02E-03 3.64E-03 4.60E-03 0.006

Location: Stack - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 2.04E+00 2.02E+00 2.02E+00 2.027

ppm 8.92E+02 8.96E+02 8.91E+02 893.000

ppm@7%O2 8.86E+02 8.77E+02 8.78E+02 880.333

Location: Stack - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 4.65E-01 4.94E-01 4.64E-01 0.474

ppm 2.86E+02 3.10E+02 2.89E+02 295.000

ppm@7%O2 2.82E+02 2.99E+02 2.81E+02 287.333

Location: Stack - OTM - 27

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 26.8 27.1 10.1 21.333

Elb/hr 2.66E+01 2.57E+01 1.02E+01 20.833

lb/mmBtuO2 3.82E-02 3.88E-02 1.49E-02 0.031

Location: Stack - OTM - 28

Compound: Inorganic (Aqueous) Condensible P

Average

RunNumber 1 2 3

Mass_mg 176 137 88 133.667

Elb/hr 2.56E+01 2.04E+01 2.54E+01 23.800

lb/mmBtuO2 3.78E-02 3.08E-02 3.73E-02 0.035

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 6 3 2 3.667

Elb/hr 8.72E-01 4.46E-01 5.78E-01 0.632

lb/mmBtuO2 1.29E-03 6.75E-04 8.48E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 182 140 90 137.333

Elb/hr 2.65E+01 2.08E+01 2.60E+01 24.433

lb/mmBtuO2 3.91E-02 3.15E-02 3.81E-02 0.036

Monday, February 07, 2011 Page 20 of 34
Process Run Data

Monday, February 07, 2011 Page 21 of 34
Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Total power output 0 0

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 0

Monday, February 07, 2011 Page 22 of 34
Sampling / Stack Data Results Detail

Location Stack - Method 0011

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 9:27:00 AM 1:16:00 PM 4:55:00 PM

Run Finish Time 11:40:00 AM 3:27:00 PM 7:05:00 PM

Net Traversing Points 24 24 24

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 1.005 1.005 1.005 1.005

Barometric Pressure, inches of Mercury 30 30 30 30.000

Average Orifice Meter Differential, inches H2O 0.97 0.86 0.89 0.907

Dry Gas Meter Volume Sampled, cubic feet 62.561 59.195 59.572 60.443

Average Dry Gas Meter Temperature, °F 71.38 80.63 77.08 76.363

Dry Gas Meter Volume Sampled, dscf 62.790 58.379 59.144 60.104

Total Moisture Liquid collected, g 144.9 135.9 141.5 140.767

Volume of Water Vapor, standard cubic feet 6.82 6.40 6.66 6.627

Moisture Content of Stack Gas, % 9.80 9.88 10.12 9.933

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

Dry Mole Fraction 0.902 0.9012 0.8988 0.901

Carbon Dioxide, % 11 10.9 10.9 10.933

Oxygen, % 6.9 6.7 6.8 6.800

Carbon Monoxide & Nitrogen, % 82.1 82.4 82.3 82.267

Fuel Factor 1.27 1.30 1.29

Dry Molecular Weight, lb/lb-Mole 30.04 30.01 30.02 30.023

Wet Molecular weight, lb/lb-Mole 28.86 28.82 28.80 28.827

Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200

Absolute Flue Gas Pressure, inches of Mercury 29.99 29.99 29.99 29.990

Average Stack Gas Temperature, °F 310.46 312.50 313.83 312.263

Average Velocity Head, inches of H2O 0.2094136920

08481

0.192303839

916199

0.202744974

270916

0.201

Average Stack Gas Velocity, feet/second 31.01 29.77 30.61 30.463

Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500

Dry Volumetric Flow Rate, dry scfm 161,970.0 154,945.1 158,619.7 158,511.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 261,414.3 250,961.1 258,042.3 256,805.900

Percent Isokinetic of Sampling Rate, % 103.9 101.0 99.9 101.600

Percent Excess Air, % 46.7 44.5 45.6 45.600

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Round Duct Diameter, inches 160.5 160.5 160.5

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 23 of 34
Location Stack - Method 10

Average

Run Number 1 2 3

Test Date 4/6/2010 4/6/2010 4/6/2010

Run Start Time 10:02:00 AM 12:07:00 PM 2:11:00 PM

Run Finish Time 11:56:00 AM 1:59:00 PM 4:02:00 PM

Carbon Dioxide, % 11 11.2 11.1 11.100

Oxygen, % 6.8 6.5 6.6 6.633

Fuel Factor 1.28 1.29 1.29

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 852 852 852 852.000

Operating Units ppm ppm ppm

No. Readings/Avg.

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B

Calibration Pre Zero Cylinder Instrument Response 9 5 8 7.333

Calibration Pre Zero Cylinder Bias 0.35 -0.12 0.23 0.153

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC119377 CC119377 CC119377

Calibration Pre High Cylinder Instrument Response 440 439 438 439.000

Calibration Pre High Cylinder Bias -0.12 -0.23 -0.35 -0.233

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID XC01167B XC01167B XC01167B

Calibration Post Zero Cylinder Instrument Response 5 8 8 7.000

Calibration Post Zero Cylinder Bias -0.12 0.23 0.23 0.113

Calibration Post Zero Cylinder Drift 0.47 0.35 0 0.273

Calibration Post High Cylinder ID CC119377 CC119377 CC119377

Calibration Post High Cylinder Instrument Response 439 438 439 438.667

Calibration Post High Cylinder Bias -0.23 -0.35 -0.23 -0.270

Calibration Post High Cylinder Drift 0.11 0.12 0.12 0.117

Cavg 8 8 9 8.333

Cavg Units ppmvd ppmvd ppmvd

Cgas 1.0497 1.5764 1.0546 1.227

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Monday, February 07, 2011 Page 24 of 34
Location Stack - Method 23

Average

Run Number 1 2 3

Test Date 4/8/2010 4/11/2010 4/12/2010

Run Start Time 8:29:00 AM 12:05:00 AM 6:20:00 AM

Run Finish Time 6:01:00 PM 4:00:00 PM 8:57:00 PM

Net Traversing Points 97 96 96

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.31 0.315 0.315 0.313

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.981 0.981 0.981 0.981

Barometric Pressure, inches of Mercury 29.91 30.21 30.15 30.090

Average Orifice Meter Differential, inches H2O 1.26 1.60 1.48 1.447

Dry Gas Meter Volume Sampled, cubic feet 287.272 317.245 305.833 303.450

Average Dry Gas Meter Temperature, °F 86.55 86.76 86.14 86.483

Dry Gas Meter Volume Sampled, dscf 273.001 304.634 293.342 290.326

Total Moisture Liquid collected, g 698.9 597.5 589.6 628.667

Volume of Water Vapor, standard cubic feet 32.90 28.12 27.75 29.590

Moisture Content of Stack Gas, % 10.76 8.45 8.64 9.283

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

Dry Mole Fraction 0.8924 0.9155 0.9136 0.907

Carbon Dioxide, % 10.8 10.1 10.2 10.367

Oxygen, % 6.7 7.8 7.6 7.367

Carbon Monoxide & Nitrogen, % 82.5 82.1 82.2 82.267

Fuel Factor 1.31 1.30 1.30

Dry Molecular Weight, lb/lb-Mole 30.00 29.93 29.94 29.957

Wet Molecular weight, lb/lb-Mole 28.71 28.92 28.91 28.847

Flue Gas Static Pressure, inches of H2O -0.2 -0.21 -0.21 -0.207

Absolute Flue Gas Pressure, inches of Mercury 29.90 30.19 30.13 30.073

Average Stack Gas Temperature, °F 317.85 317.52 317.75 317.707

Average Velocity Head, inches of H2O 0.1970434433

2353

0.209480704

64025

0.218076660

192309

0.208

Average Stack Gas Velocity, feet/second 30.34 31.02 31.69 31.017

Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500

Dry Volumetric Flow Rate, dry scfm 154,828.3 164,040.7 166,854.3 161,907.767

Actual Wet Volumetric Flue Gas Flow Rate, acfm 255,766.2 261,498.6 267,146.7 261,470.500

Percent Isokinetic of Sampling Rate, % 98.5 100.4 95.1 98.000

Percent Excess Air, % 44.4 56.2 53.9 51.500

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Round Duct Diameter, inches 160.5 160.5 160.5

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 25 of 34
Location Stack - Method 25A

Average

Run Number 1 2 3

Test Date 4/6/2010 4/6/2010 4/6/2010

Run Start Time 10:02:00 AM 12:07:00 PM 2:11:00 PM

Run Finish Time 11:56:00 AM 1:59:00 PM 4:02:00 PM

Carbon Dioxide, % 11 11.2 11.1 11.100

Oxygen, % 6.8 6.5 6.6 6.633

Fuel Factor 1.28 1.29 1.29

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 100 100 100 100.000

Operating Units ppm ppm ppm

No. Readings/Avg.

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B

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 CC23540 CC23540 CC23540

Calibration Pre High Cylinder Instrument Response 12.6 12.6 12.6 12.600

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 XC01167B XC01167B XC01167B

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID CC23540 CC23540 CC23540

Calibration Post High Cylinder Instrument Response 12.6 12.6 12.6 12.600

Calibration Post High Cylinder Bias 0 0 0 0.000

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 0.7 0.7 0.6 0.667

Cavg Units ppmvd ppmvd ppmvd

Cgas 0.6889 0.6889 0.5905 0.656

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Monday, February 07, 2011 Page 26 of 34
Location Stack - Method 26A

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 11:31:00 AM 2:57:00 AM 4:38:00 PM

Run Finish Time 1:40:00 PM 4:10:00 PM 6:32:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 60 60 60

Nozzle Diameter, inches 0.314 0.314 0.314 0.314

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 30 30 30 30.000

Average Orifice Meter Differential, inches H2O 1.22 1.17 1.17 1.187

Dry Gas Meter Volume Sampled, cubic feet 38.324 36.907 37.242 37.491

Average Dry Gas Meter Temperature, °F 77.42 78.38 76.92 77.573

Dry Gas Meter Volume Sampled, dscf 36.806 35.377 35.795 35.993

Total Moisture Liquid collected, g 144.9 135.9 141.5 140.767

Volume of Water Vapor, standard cubic feet 6.82 6.40 6.66 6.627

Moisture Content of Stack Gas, % 15.63 15.32 15.69 15.547

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

Dry Mole Fraction 0.8437 0.8468 0.8431 0.845

Carbon Dioxide, % 11.5 11.5 11.4 11.467

Oxygen, % 7 7.1 7.1 7.067

Carbon Monoxide & Nitrogen, % 81.5 81.4 81.5 81.467

Fuel Factor 1.21 1.20 1.21

Dry Molecular Weight, lb/lb-Mole 30.12 30.12 30.11 30.117

Wet Molecular weight, lb/lb-Mole 28.23 28.26 28.21 28.233

Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200

Absolute Flue Gas Pressure, inches of Mercury 29.99 29.99 29.99 29.990

Average Stack Gas Temperature, °F 311.96 313.13 314.92 313.337

Average Velocity Head, inches of H2O 0.1895385365

66323

0.180603066

146483

0.180609454

802809

0.184

Average Stack Gas Velocity, feet/second 29.85 29.15 29.21 29.403

Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500

Dry Volumetric Flow Rate, dry scfm 145,550.6 142,443.7 141,785.0 143,259.767

Actual Wet Volumetric Flue Gas Flow Rate, acfm 251,635.5 245,734.5 246,240.3 247,870.100

Percent Isokinetic of Sampling Rate, % 110.1 108.1 109.9 109.367

Percent Excess Air, % 48.2 49.3 49.3 48.933

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Round Duct Diameter, inches 160.5 160.5 160.5

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 27 of 34
Location Stack - Method 29

Average

Run Number 1 2 3

Test Date 4/13/2010 4/14/2010 4/14/2010

Run Start Time 12:12:00 PM 6:25:00 AM 11:50:00 AM

Run Finish Time 5:22:00 PM 9:20:00 AM 4:00:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.315 0.315 0.315 0.315

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 30.24 30.24 30.24 30.240

Average Orifice Meter Differential, inches H2O 1.33 1.31 1.28 1.307

Dry Gas Meter Volume Sampled, cubic feet 152.122 149.077 148.287 149.829

Average Dry Gas Meter Temperature, °F 73.50 73.33 73.31 73.380

Dry Gas Meter Volume Sampled, dscf 149.603 146.648 145.866 147.372

Total Moisture Liquid collected, g 299.3 301.3 308.6 303.067

Volume of Water Vapor, standard cubic feet 14.09 14.18 14.53 14.267

Moisture Content of Stack Gas, % 8.61 8.82 9.06 8.830

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

Dry Mole Fraction 0.9139 0.9118 0.9094 0.912

Carbon Dioxide, % 10.5 10.8 10.7 10.667

Oxygen, % 7.3 7.1 7 7.133

Carbon Monoxide & Nitrogen, % 82.2 82.1 82.3 82.200

Fuel Factor 1.30 1.28 1.30

Dry Molecular Weight, lb/lb-Mole 29.97 30.01 29.99 29.990

Wet Molecular weight, lb/lb-Mole 28.94 28.95 28.90 28.930

Flue Gas Static Pressure, inches of H2O -0.26 -0.26 -0.26 -0.260

Absolute Flue Gas Pressure, inches of Mercury 30.22 30.22 30.22 30.220

Average Stack Gas Temperature, °F 335.06 318.10 330.06 327.740

Average Velocity Head, inches of H2O 0.2019992131

23387

0.197032018

373523

0.195084372

688685

0.198

Average Stack Gas Velocity, feet/second 30.77 30.06 30.17 30.333

Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500

Dry Volumetric Flow Rate, dry scfm 159,008.6 158,360.7 156,122.2 157,830.500

Actual Wet Volumetric Flue Gas Flow Rate, acfm 259,391.1 253,405.8 254,333.1 255,710.000

Percent Isokinetic of Sampling Rate, % 101.8 100.2 101.1 101.033

Percent Excess Air, % 50.7 48.7 47.5 48.967

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Round Duct Diameter, inches 160.5 160.5 160.5

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 28 of 34
Location Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 4/6/2010 4/6/2010 4/6/2010

Run Start Time 10:02:00 AM 12:07:00 PM 2:11:00 PM

Run Finish Time 11:56:00 AM 1:59:00 PM 4:02:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 0 0 0 0.000

Fuel Factor 0 0 0

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 20.1 20.1 20.1 20.100

Operating Units % % %

No. Readings/Avg.

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B

Calibration Pre Zero Cylinder Instrument Response 0 0 0.1 0.033

Calibration Pre Zero Cylinder Bias 0 0 0.5 0.167

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC112251 

CO2

CC112251 

CO2

CC112251 

CO2

Calibration Pre High Cylinder Instrument Response 10 10 10 10.000

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 XC01167B XC01167B XC01167B

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 0.167

Calibration Post High Cylinder ID CC112251 

CO2

CC112251 

CO2

CC112251 

CO2

Calibration Post High Cylinder Instrument Response 10 10 10 10.000

Calibration Post High Cylinder Bias 0 0 0 0.000

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 10.9 11.1 11 11.000

Cavg Units %vd %vd %vd

Cgas 11.009 11.2166 11.1202 11.115

Cgas Units %vd %vd %vd

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Monday, February 07, 2011 Page 29 of 34
Location Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 4/6/2010 4/6/2010 4/6/2010

Run Start Time 10:02:00 AM 2:11:00 PM

Run Finish Time 11:56:00 AM 4:02:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 0 0 0 0.000

Fuel Factor 0 0 0

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 20.1 20.1 20.1 20.100

Operating Units % % %

No. Readings/Avg.

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B

Calibration Pre Zero Cylinder Instrument Response 0 0 0.1 0.033

Calibration Pre Zero Cylinder Bias 0 0 0.5 0.167

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC112251 O2 CC112251 

O2

CC112251 

O2

Calibration Pre High Cylinder Instrument Response 10 10 10 10.000

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 XC01167B XC01167B XC01167B

Calibration Post Zero Cylinder Instrument Response 0 0.1 0 0.033

Calibration Post Zero Cylinder Bias 0 0.5 0 0.167

Calibration Post Zero Cylinder Drift 0 0.5 0.5 0.333

Calibration Post High Cylinder ID CC112251 O2 CC112251 

O2

CC112251 

O2

Calibration Post High Cylinder Instrument Response 10 10 10 10.000

Calibration Post High Cylinder Bias 0 0 0 0.000

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 6.8 6.5 6.6 6.633

Cavg Units %vd %vd %vd

Cgas 6.8 6.4824 6.5829 6.622

Cgas Units %vd %vd %vd

Fuel Type

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Monday, February 07, 2011 Page 30 of 34
Location Stack - Method 6C

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 9:27:00 AM 11:31:00 AM 1:16:00 PM

Run Finish Time 11:23:00 AM 12:51:00 PM 4:10:00 PM

Carbon Dioxide, % 11 11.1 11 11.033

Oxygen, % 6.9 6.7 6.8 6.800

Fuel Factor 1.27 1.28 1.28

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 2414 2414 2414 2,414.000

Operating Units ppm ppm ppm

No. Readings/Avg.

Calibration Set 6 6 6 6.000

Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B

Calibration Pre Zero Cylinder Instrument Response 3 6 9 6.000

Calibration Pre Zero Cylinder Bias 0.04 0.17 0.29 0.167

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID SG9121056B

AL

SG9121056B

AL

SG9121056B

AL

Calibration Pre High Cylinder Instrument Response 1219 1225 1225 1,223.000

Calibration Pre High Cylinder Bias -1.41 -1.16 -1.16 -1.243

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID XC01167B XC01167B XC01167B

Calibration Post Zero Cylinder Instrument Response 6 9 12 9.000

Calibration Post Zero Cylinder Bias 0.17 0.29 0.41 0.290

Calibration Post Zero Cylinder Drift 0.13 0.12 0.12 0.123

Calibration Post High Cylinder ID SG9121056B

AL

SG9121056B

AL

SG9121056B

AL

Calibration Post High Cylinder Instrument Response 1225 1225 1221 1,223.667

Calibration Post High Cylinder Bias -1.16 -1.16 -1.33 -1.217

Calibration Post High Cylinder Drift 0.25 0 0.17 0.140

Cavg 868 875 869 870.667

Cavg Units ppmvd ppmvd ppmvd

Cgas 892.2242 896.3573 890.7159 893.099

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Monday, February 07, 2011 Page 31 of 34
Location Stack - Method 7E

Average

Run Number 1 2 3

Test Date 4/6/2010 4/6/2010 4/6/2010

Run Start Time 10:02:00 AM 12:07:00 PM 2:11:00 PM

Run Finish Time 11:56:00 AM 1:59:00 PM 4:02:00 PM

Carbon Dioxide, % 11 11.2 11.1 11.100

Oxygen, % 6.8 6.5 6.6 6.633

Fuel Factor 1.28 1.29 1.29

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 441 441 441 441.000

Operating Units ppm ppm ppm

No. Readings/Avg.

Calibration Set 5 5 5 5.000

Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B

Calibration Pre Zero Cylinder Instrument Response 2 2 2 2.000

Calibration Pre Zero Cylinder Bias 0.45 0.45 0.45 0.450

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC111553 CC111553 CC111553

Calibration Pre High Cylinder Instrument Response 248 245 241 244.667

Calibration Pre High Cylinder Bias 0.45 -0.23 -1.13 -0.303

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID XC01167B XC01167B XC01167B

Calibration Post Zero Cylinder Instrument Response 2 2 2 2.000

Calibration Post Zero Cylinder Bias 0.45 0.45 0.45 0.450

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID CC111553 CC111553 CC111553

Calibration Post High Cylinder Instrument Response 245 241 241 242.333

Calibration Post High Cylinder Bias -0.23 -1.13 -1.13 -0.830

Calibration Post High Cylinder Drift 0.68 0.9 0 0.527

Cavg 286 306 283 291.667

Cavg Units ppmvd ppmvd ppmvd

Cgas 285.7423 310.3071 289.2301 295.093

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Monday, February 07, 2011 Page 32 of 34
Location Stack - OTM - 27

Average

Run Number 1 2 3

Test Date 4/8/2010 4/8/2010 4/11/2010

Run Start Time 12:50:00 PM 4:29:00 PM 6:15:00 AM

Run Finish Time 1:58:00 PM 6:50:00 PM 7:30:00 AM

Net Traversing Points 13 13 14

Net Run Time, minutes 57.75 58.25 59.25

Nozzle Diameter, inches 0.243 0.243 0.243 0.243

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 29.91 29.91 29.91 29.910

Average Orifice Meter Differential, inches H2O 0.42 0.42 0.42 0.420

Dry Gas Meter Volume Sampled, cubic feet 21.768 22.062 22.519 22.116

Average Dry Gas Meter Temperature, °F 75.00 72.38 77.07 74.817

Dry Gas Meter Volume Sampled, dscf 20.896 21.283 21.534 21.238

Total Moisture Liquid collected, g 55.4 60.4 47.6 54.467

Volume of Water Vapor, standard cubic feet 2.61 2.84 2.24 2.563

Moisture Content of Stack Gas, % 11.10 11.77 9.42 10.763

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

Dry Mole Fraction 0.889 0.8823 0.9058 0.892

Carbon Dioxide, % 10.9 10 10.1 10.333

Oxygen, % 6.7 7 7.6 7.100

Carbon Monoxide & Nitrogen, % 82.4 83 82.3 82.567

Fuel Factor 1.30 1.39 1.32

Dry Molecular Weight, lb/lb-Mole 30.01 29.88 29.92 29.937

Wet Molecular weight, lb/lb-Mole 28.68 28.48 28.80 28.653

Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200

Absolute Flue Gas Pressure, inches of Mercury 29.90 29.90 29.90 29.900

Average Stack Gas Temperature, °F 317.69 319.46 304.21 313.787

Average Velocity Head, inches of H2O 0.2032665672

13948

0.194654446

547487

0.210829116

831624

0.203

Average Stack Gas Velocity, feet/second 30.83 30.31 31.06 30.733

Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500

Dry Volumetric Flow Rate, dry scfm 156,761.7 152,608.8 163,754.1 157,708.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 259,896.9 255,513.3 261,835.8 259,082.000

Percent Isokinetic of Sampling Rate, % 100.7 104.4 96.8 100.633

Percent Excess Air, % 44.5 46.9 53.8 48.400

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Round Duct Diameter, inches 160.5 160.5 160.5

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 33 of 34
Location Stack - OTM - 28

Average

Run Number 1 2 3

Test Date 4/13/2010 4/14/2010 4/14/2010

Run Start Time 12:15:00 PM 6:42:00 AM 12:19:00 PM

Run Finish Time 5:19:00 PM 11:58:00 AM 3:01:00 PM

Net Traversing Points 48 48 25

Net Run Time, minutes 240 240 125

Nozzle Diameter, inches 0.31 0.31 0.31 0.310

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 30.24 30.24 30.24 30.240

Average Orifice Meter Differential, inches H2O 1.26 1.18 1.24 1.227

Dry Gas Meter Volume Sampled, cubic feet 151.251 142.149 75.439 122.946

Average Dry Gas Meter Temperature, °F 83.35 81.88 82.04 82.423

Dry Gas Meter Volume Sampled, dscf 144.833 136.460 72.409 117.901

Total Moisture Liquid collected, g 296.8 323.7 155.6 258.700

Volume of Water Vapor, standard cubic feet 13.97 15.24 7.32 12.177

Moisture Content of Stack Gas, % 8.80 10.05 9.18 9.343

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

Dry Mole Fraction 0.912 0.8995 0.9082 0.907

Carbon Dioxide, % 10.5 10.8 10.5 10.600

Oxygen, % 7.3 7.1 7.1 7.167

Carbon Monoxide & Nitrogen, % 82.2 82.1 82.4 82.233

Fuel Factor 1.30 1.28 1.31

Dry Molecular Weight, lb/lb-Mole 29.97 30.01 29.96 29.980

Wet Molecular weight, lb/lb-Mole 28.92 28.80 28.86 28.860

Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200

Absolute Flue Gas Pressure, inches of Mercury 30.23 30.23 30.23 30.230

Average Stack Gas Temperature, °F 335.81 320.42 330.92 329.050

Average Velocity Head, inches of H2O 0.2032818342

00627

0.189553260

151069

0.200363552

027636

0.198

Average Stack Gas Velocity, feet/second 30.89 29.60 30.61 30.367

Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500

Dry Volumetric Flow Rate, dry scfm 159,199.4 153,427.3 158,070.3 156,899.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 260,402.7 249,528.0 258,042.3 255,991.000

Percent Isokinetic of Sampling Rate, % 101.6 99.3 98.2 99.700

Percent Excess Air, % 50.7 48.7 48.5 49.300

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Round Duct Diameter, inches 160.5 160.5 160.5

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 07, 2011 Page 34 of 34