Name: Tom Trickey, PE

Title: Plant Manager

Company: Lakeland Electric

Sign Date: 10/28/2010

Name: Mike Taylor

Title: President

Company: Catalyst Air Management

Sign Date: 10/28/2010

Permitted Facility Representative / Date Testing Company Representative / Date

FL676 McIntosh Unit 2

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.

Thursday, January 27, 2011 Page 1 of 23
FL676 McIntosh Unit 2

10/28/2010

Facility Information:

FL676 McIntosh Power Plant

3030 East Lake Parker Dr.

Lakeland FL 33805

Contact: Bret Galbraith

Phone: 863-834-8180

Fax: 863-834-8187

Email: bret.galbraith@lakelandelectric.com

Testing Company:

Catalyst Air Management, Inc.

2505 Byington Solway Rd.

Knoxville TN 37931

Contact:Mike Taylor

Phone: 865-531-0075

Fax: 865-531-0750

Email: mike.taylor@catalystair.com

Air Permit Number:

FL676

Permitted Source ID/Name:

2 McIntosh Power Plant

Permitted Maximum Process Rate:

1184 mmBtu/hr

Max. Normal Operation Process Rate: Target Process Test Rate

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

 process flow diagram:

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

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

FL676 Unit 2 126 0 0 0 319 268 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

FL676 Unit 2 Carbon Monoxide Method 10 3 120 0

FL676 Unit 2 2,3,7,8-TCDD Method 23 3 480 0

FL676 Unit 2 1,2,3,7,8-PeCDD Method 23 3 480 0

FL676 Unit 2 1,2,3,4,7,8-HxCDD Method 23 3 480 0

FL676 Unit 2 1,2,3,6,7,8-HxCDD Method 23 3 480 0

FL676 Unit 2 1,2,3,7,8,9-HxCDD Method 23 3 480 0

FL676 Unit 2 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

Thursday, January 27, 2011 Page 2 of 23
FL676 McIntosh Unit 2

10/28/2010

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.

FL676 Unit 2 OCDD Method 23 3 480 0

FL676 Unit 2 2,3,7,8-TCDF Method 23 3 480 0

FL676 Unit 2 1,2,3,7,8-PeCDF Method 23 3 480 0

FL676 Unit 2 2,3,4,7,8-PeCDF Method 23 3 480 0

FL676 Unit 2 1,2,3,4,7,8-HxCDF Method 23 3 480 0

FL676 Unit 2 1,2,3,6,7,8-HxCDF Method 23 3 480 0

FL676 Unit 2 2,3,4,6,7,8-HxCDF Method 23 3 480 0

FL676 Unit 2 1,2,3,7,8,9-HxCDF Method 23 3 480 0

FL676 Unit 2 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

FL676 Unit 2 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

FL676 Unit 2 OCDF Method 23 3 480 0

FL676 Unit 2 Total Dioxins Method 23 3 480 0

FL676 Unit 2 Total Furans Method 23 3 480 0

FL676 Unit 2 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

FL676 Unit 2 3,4,4',5-TCB (PCB81) Method 23 3 480 0

FL676 Unit 2 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

FL676 Unit 2 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

FL676 Unit 2 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

FL676 Unit 2 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

FL676 Unit 2 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)

FL676 Unit 2 Method 23 3 480 0

FL676 Unit 2 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

FL676 Unit 2 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

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

(PCB189)

FL676 Unit 2 Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

FL676 Unit 2 Method 25A 3 120 0

FL676 Unit 2 Chlorine Method 26A 3 180 0

FL676 Unit 2 Hydrogen Chloride Method 26A 3 180 0

FL676 Unit 2 Hydrogen Fluoride Method 26A 3 180 0

Organic Condensible 

Particulate

FL676 Unit 2 OTM - 27/28 3 330 0

FL676 Unit 2 Total PM2.5 OTM - 27/28 3 330 0

FL676 Unit 2 Filterable PM2.5 OTM - 27/28 3 330 0

Inorganic (Aqueous) 

Condensible Part.

FL676 Unit 2 OTM - 27/28 3 330 0

FL676 Unit 2 Chromium Method 29 3 240 0

FL676 Unit 2 Nickel Method 29 3 240 0

FL676 Unit 2 Cadmium Method 29 3 240 0

FL676 Unit 2 Beryllium Method 29 3 240 0

FL676 Unit 2 Cobalt Method 29 3 240 0

FL676 Unit 2 Arsenic Method 29 3 240 0

FL676 Unit 2 Filterable Particulate Method 29 3 240 0

FL676 Unit 2 Antimony Method 29 3 240 0

FL676 Unit 2 Manganese Method 29 3 240 0

FL676 Unit 2 Selenium Method 29 3 240 0

FL676 Unit 2 Lead Method 29 3 240 0

Thursday, January 27, 2011 Page 3 of 23
FL676 McIntosh Unit 2

10/28/2010

Thursday, January 27, 2011 Page 4 of 23
FL676 McIntosh Unit 2

10/28/2010

Sampling / Stack Data Results Summary

Location FL676 Unit 2 - Method 10

Average

Run Number M10-1 M10-2 M10-3

Test Date 7/20/2010 7/20/2010 7/20/2010

Run Start Time 9:00:00 AM 11:05:00 

AM

1:10:00 PM

Run Finish Time 11:00:00 AM 1:05:00 PM 3:10:00 PM

Carbon Dioxide, % 7.5 7.6 7.7 7.600

Oxygen, % 8.7 8.6 8.5 8.600

Dry Volumetric Flow Rate, dry scfm 133516 133516 133516 133,516.000

F-Factor, dscfm/MMBtu @ %O2 8798 8797 8797 8,797.333

Moisture, % 10.98 10.98 10.98 10.980

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location FL676 Unit 2 - Method 23

Average

Run Number M23-1 M23-2 M23-3

Test Date 7/20/2010 7/21/2010 7/22/2010

Run Start Time 12:10:00 PM 6:19:00 

AM

6:50:00 AM

Run Finish Time 8:26:00 PM 3:01:00 PM 3:32:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 264.410 264.710 321.981 283.700

Moisture Content of Stack Gas, % 10.97 11.87 11.75 11.530

Moisture Saturation at Stack Gas Temperature, % 40.16 38.34 39.70 39.400

Carbon Dioxide, % 7.6 7.2 7.5 7.433

Oxygen, % 8.8 9.1 8.4 8.767

Average Stack Gas Temperature, °F 169.27 167.17 168.67 168.370

Dry Volumetric Flow Rate, dry scfm 133,520.9 130,731.4 130,290.8 131,514.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 179,397.2 177,267.0 176,851.4 177,838.533

Percent Isokinetic of Sampling Rate, % 104.8 107.2 108.1 106.700

F-Factor, dscfm/MMBtu @ %O2 8796 8791 8795 8,794.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, January 27, 2011 Page 5 of 23
FL676 McIntosh Unit 2

10/28/2010

Location FL676 Unit 2 - Method 25A

Average

Run Number M25A-1 M25A-2 M25A-3

Test Date 7/20/2010 7/20/2010 7/20/2010

Run Start Time 9:00:00 AM 11:05:00 

AM

1:10:00 PM

Run Finish Time 11:00:00 AM 1:05:00 PM 3:10:00 PM

Carbon Dioxide, % 7.5 7.6 7.7 7.600

Oxygen, % 8.7 8.6 8.5 8.600

Dry Volumetric Flow Rate, dry scfm 133516 133516 133516 133,516.000

F-Factor, dscfm/MMBtu @ %O2 8798 8797 8797 8,797.333

Moisture, % 10.98 10.98 10.98 10.980

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location FL676 Unit 2 - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 7/23/2010 7/23/2010 7/23/2010

Run Start Time 6:46:00 AM 10:11:00 

AM

1:36:00 PM

Run Finish Time 10:00:00 AM 1:24:00 PM 4:47:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 163.608 163.026 159.636 162.090

Moisture Content of Stack Gas, % 13.94 14.07 13.61 13.873

Moisture Saturation at Stack Gas Temperature, % 49.79 56.85 44.74 50.460

Carbon Dioxide, % 9.8 9.7 9.2 9.567

Oxygen, % 5.5 5.4 5.4 5.433

Average Stack Gas Temperature, °F 178.63 184.63 173.88 179.047

Dry Volumetric Flow Rate, dry scfm 211,977.3 209,541.7 213,456.0 211,658.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 299,826.5 299,618.7 298,527.7 299,324.300

Percent Isokinetic of Sampling Rate, % 108.9 109.8 105.5 108.067

F-Factor, dscfm/MMBtu @ %O2 8803 8803 8803 8,803.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, January 27, 2011 Page 6 of 23
FL676 McIntosh Unit 2

10/28/2010

Location FL676 Unit 2 - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 6/4/2010 6/5/2010 6/5/2010

Run Start Time 10:20:00 AM 6:19:00 

AM

12:15:00 PM

Run Finish Time 2:35:00 PM 10:34:00 

AM

4:31:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 138.076 136.871 138.327 137.758

Moisture Content of Stack Gas, % 12.80 13.48 13.03 13.103

Moisture Saturation at Stack Gas Temperature, % 40.64 36.76 42.04 39.813

Carbon Dioxide, % 8.1 8.2 8.2 8.167

Oxygen, % 7.2 7 7 7.067

Average Stack Gas Temperature, °F 169.54 165.25 171.04 168.610

Dry Volumetric Flow Rate, dry scfm 128,920.9 129,181.1 129,785.9 129,295.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 177,942.5 178,358.1 179,916.7 178,739.100

Percent Isokinetic of Sampling Rate, % 106.4 105.3 105.9 105.867

F-Factor, dscfm/MMBtu @ %O2 8790 8793 8796 8,793.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, January 27, 2011 Page 7 of 23
FL676 McIntosh Unit 2

10/28/2010

Location FL676 Unit 2 - OTM - 27/28

Average

Run Number OTM27-1 OTM27-2 OTM27-3

Test Date 6/4/2010 6/5/2010 6/5/2010

Run Start Time 10:00:00 AM 6:19:00 

AM

12:49:00 PM

Run Finish Time 4:48:00 PM 12:01:00 

PM

6:36:00 PM

Net Run Time, minutes 331.25 329.75 332.5

Dry Gas Meter Volume Sampled, dscf 121.640 118.312 119.599 119.850

Moisture Content of Stack Gas, % 12.28 12.45 12.62 12.450

Moisture Saturation at Stack Gas Temperature, % 36.99 33.79 34.32 35.033

Carbon Dioxide, % 8.1 8.2 8.2 8.167

Oxygen, % 7.2 7 7 7.067

Average Stack Gas Temperature, °F 165.50 161.67 162.33 163.167

Dry Volumetric Flow Rate, dry scfm 133,392.5 134,152.5 133,864.6 133,803.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 181,787.0 181,994.9 182,150.7 181,977.533

Percent Isokinetic of Sampling Rate, % 109.3 106.2 106.6 107.367

F-Factor, dscfm/MMBtu @ %O2 8790 8793 8796 8,793.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, January 27, 2011 Page 8 of 23
FL676 McIntosh Unit 2

10/28/2010

Emissions Summary

Location: FL676 Unit 2 - Method 10

Compound: Carbon Monoxide

Average

Run M10-1 M10-2 M10-3

lb/mmBtuO2 5.72E-02 5.94E-02 5.66E-02 0.058

ppm 5.22E+01 5.47E+01 5.25E+01 53.133

ppm@7%O2 5.95E+01 6.18E+01 5.89E+01 60.067

Location: FL676 Unit 2 - Method 23

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000018 0.000000003 0.000000002 0.000

lb/mmBtuO2 2.28E-13 3.89E-13 2.01E-13 0.000

ng/dscm 2.40E-04 4.00E-04 2.19E-04 0.000

ng/dscm@7%O2 2.76E-04 4.71E-04 2.44E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000026 0.0000000029 0.0000000029 0.000

lb/mmBtuO2 3.29E-13 3.76E-13 2.92E-13 0.000

ng/dscm 3.47E-04 3.87E-04 3.18E-04 0.000

ng/dscm@7%O2 3.99E-04 4.56E-04 3.54E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000018 0.0000000018 0.0000000019 0.000

lb/mmBtuO2 2.28E-13 2.33E-13 1.91E-13 0.000

ng/dscm 2.40E-04 2.40E-04 2.08E-04 0.000

ng/dscm@7%O2 2.76E-04 2.83E-04 2.31E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000015 0.0000000017 0.0000000016 0.000

lb/mmBtuO2 1.90E-13 2.20E-13 1.61E-13 0.000

ng/dscm 2.00E-04 2.27E-04 1.76E-04 0.000

ng/dscm@7%O2 2.30E-04 2.67E-04 1.96E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000016 0.0000000015 0.0000000016 0.000

lb/mmBtuO2 2.03E-13 1.95E-13 1.61E-13 0.000

ng/dscm 2.14E-04 2.00E-04 1.76E-04 0.000

ng/dscm@7%O2 2.46E-04 2.36E-04 1.96E-04 0.000

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

Average

Thursday, January 27, 2011 Page 9 of 23
FL676 McIntosh Unit 2

10/28/2010

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000016 0.0000000018 0.0000000017 0.000

lb/mmBtuO2 2.03E-13 2.33E-13 1.71E-13 0.000

ng/dscm 2.14E-04 2.40E-04 1.86E-04 0.000

ng/dscm@7%O2 2.46E-04 2.83E-04 2.07E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000015 0.0000000014 0.0000000015 0.000

lb/mmBtuO2 1.90E-13 1.82E-13 1.51E-13 0.000

ng/dscm 2.00E-04 1.87E-04 1.65E-04 0.000

ng/dscm@7%O2 2.30E-04 2.20E-04 1.83E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000015 0.0000000017 0.0000000015 0.000

lb/mmBtuO2 1.90E-13 2.20E-13 1.51E-13 0.000

ng/dscm 2.00E-04 2.27E-04 1.65E-04 0.000

ng/dscm@7%O2 2.30E-04 2.67E-04 1.83E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000002 0.0000000018 0.0000000019 0.000

lb/mmBtuO2 2.53E-13 2.33E-13 1.91E-13 0.000

ng/dscm 2.67E-04 2.40E-04 2.08E-04 0.000

ng/dscm@7%O2 3.07E-04 2.83E-04 2.31E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000017 0.0000000015 0.0000000017 0.000

lb/mmBtuO2 2.15E-13 1.95E-13 1.71E-13 0.000

ng/dscm 2.27E-04 2.00E-04 1.86E-04 0.000

ng/dscm@7%O2 2.61E-04 2.36E-04 2.07E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000016 0.0000000018 0.0000000018 0.000

lb/mmBtuO2 2.03E-13 2.33E-13 1.81E-13 0.000

ng/dscm 2.14E-04 2.40E-04 1.97E-04 0.000

ng/dscm@7%O2 2.46E-04 2.83E-04 2.19E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000011 0.00000003 0.000000024 0.000

lb/mmBtuO2 1.39E-12 3.89E-12 2.42E-12 0.000

ng/dscm 1.47E-03 4.00E-03 2.63E-03 0.003

ng/dscm@7%O2 1.69E-03 4.71E-03 2.92E-03 0.003

Thursday, January 27, 2011 Page 10 of 23
FL676 McIntosh Unit 2

10/28/2010

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.00000002 0.000000026 0.000000028 0.000

lb/mmBtuO2 2.53E-12 3.37E-12 2.82E-12 0.000

ng/dscm 2.67E-03 3.47E-03 3.07E-03 0.003

ng/dscm@7%O2 3.07E-03 4.09E-03 3.41E-03 0.004

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.00000004 0.00000003 0.00000006 0.000

lb/mmBtuO2 5.07E-12 3.89E-12 6.04E-12 0.000

ng/dscm 5.34E-03 4.00E-03 6.58E-03 0.005

ng/dscm@7%O2 6.13E-03 4.71E-03 7.32E-03 0.006

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000096 0.000000025 0.000000021 0.000

lb/mmBtuO2 1.22E-12 3.24E-12 2.11E-12 0.000

ng/dscm 1.28E-03 3.34E-03 2.30E-03 0.002

ng/dscm@7%O2 1.47E-03 3.93E-03 2.56E-03 0.003

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000007 0.000000018 0.000000019 0.000

lb/mmBtuO2 8.87E-13 2.33E-12 1.91E-12 0.000

ng/dscm 9.35E-04 2.40E-03 2.08E-03 0.002

ng/dscm@7%O2 1.07E-03 2.83E-03 2.31E-03 0.002

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.00000014 0.00000009 0.00000021 0.000

lb/mmBtuO2 1.77E-11 1.17E-11 2.11E-11 0.000

ng/dscm 1.87E-02 1.20E-02 2.30E-02 0.018

ng/dscm@7%O2 2.15E-02 1.41E-02 2.56E-02 0.020

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000071 0.000000018 0.000000019 0.000

lb/mmBtuO2 8.99E-13 2.33E-12 1.91E-12 0.000

ng/dscm 9.48E-04 2.40E-03 2.08E-03 0.002

ng/dscm@7%O2 1.09E-03 2.83E-03 2.31E-03 0.002

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000018 0.0000000017 0.0000000018 0.000

lb/mmBtuO2 2.28E-13 2.20E-13 1.81E-13 0.000

Thursday, January 27, 2011 Page 11 of 23
FL676 McIntosh Unit 2

10/28/2010

ng/dscm 2.40E-04 2.27E-04 1.97E-04 0.000

ng/dscm@7%O2 2.76E-04 2.67E-04 2.19E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000016 0.000000002 0.0000000023 0.000

lb/mmBtuO2 2.03E-13 2.59E-13 2.32E-13 0.000

ng/dscm 2.14E-04 2.67E-04 2.52E-04 0.000

ng/dscm@7%O2 2.46E-04 3.15E-04 2.80E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000018 0.0000000018 0.0000000016 0.000

lb/mmBtuO2 2.28E-13 2.33E-13 1.61E-13 0.000

ng/dscm 2.40E-04 2.40E-04 1.76E-04 0.000

ng/dscm@7%O2 2.76E-04 2.83E-04 1.96E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000002 0.0000000024 0.000000004 0.000

lb/mmBtuO2 2.53E-13 3.11E-13 4.03E-13 0.000

ng/dscm 2.67E-04 3.20E-04 4.39E-04 0.000

ng/dscm@7%O2 3.07E-04 3.77E-04 4.88E-04 0.000

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000099 0.000000026 0.000000022 0.000

lb/mmBtuO2 1.25E-12 3.37E-12 2.22E-12 0.000

ng/dscm 1.32E-03 3.47E-03 2.41E-03 0.002

ng/dscm@7%O2 1.52E-03 4.09E-03 2.68E-03 0.003

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

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000071 0.000000018 0.000000019 0.000

lb/mmBtuO2 8.99E-13 2.33E-12 1.91E-12 0.000

ng/dscm 9.48E-04 2.40E-03 2.08E-03 0.002

ng/dscm@7%O2 1.09E-03 2.83E-03 2.31E-03 0.002

Compound: 3,3',4,4'-TCB (PCB77)

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.00000001 0.000000023 0.00000002 0.000

lb/mmBtuO2 1.27E-12 2.98E-12 2.01E-12 0.000

ng/dscm 1.34E-03 3.07E-03 2.19E-03 0.002

ng/dscm@7%O2 1.54E-03 3.62E-03 2.44E-03 0.003

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

Average

RunNumber M23-1 M23-2 M23-3

Thursday, January 27, 2011 Page 12 of 23
FL676 McIntosh Unit 2

10/28/2010

Mass_mg 0.000000012 0.000000023 0.000000021 0.000

lb/mmBtuO2 1.52E-12 2.98E-12 2.11E-12 0.000

ng/dscm 1.60E-03 3.07E-03 2.30E-03 0.002

ng/dscm@7%O2 1.84E-03 3.62E-03 2.56E-03 0.003

Compound: OCDD

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000009 0.0000000081 0.000000012 0.000

lb/mmBtuO2 1.14E-12 1.05E-12 1.21E-12 0.000

ng/dscm 1.20E-03 1.08E-03 1.32E-03 0.001

ng/dscm@7%O2 1.38E-03 1.27E-03 1.47E-03 0.001

Compound: OCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000034 0.0000000032 0.0000000039 0.000

lb/mmBtuO2 4.31E-13 4.15E-13 3.93E-13 0.000

ng/dscm 4.54E-04 4.27E-04 4.28E-04 0.000

ng/dscm@7%O2 5.22E-04 5.03E-04 4.76E-04 0.001

Compound: Total Dioxins

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000189 0.0000000186 0.0000000211 0.000

lb/mmBtuO2 2.39E-12 2.41E-12 2.12E-12 0.000

ng/dscm 2.52E-03 2.48E-03 2.31E-03 0.002

ng/dscm@7%O2 2.89E-03 2.92E-03 2.57E-03 0.003

Compound: Total Furans

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000189 0.0000000175 0.0000000216 0.000

lb/mmBtuO2 2.39E-12 2.27E-12 2.17E-12 0.000

ng/dscm 2.52E-03 2.34E-03 2.37E-03 0.002

ng/dscm@7%O2 2.89E-03 2.76E-03 2.64E-03 0.003

Location: FL676 Unit 2 - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run M25A-1 M25A-2 M25A-3

lb/mmBtuO2 8.06E-04 1.15E-03 1.50E-03 0.001

ppm 4.67E-01 6.71E-01 8.84E-01 0.674

ppm@7%O2 5.32E-01 7.58E-01 9.91E-01 0.760

Location: FL676 Unit 2 - Method 26A

Compound: Chlorine

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 3.9 3.5 3.2 3.533

lb/mmBtuO2 6.28E-04 5.62E-04 5.25E-04 0.001

Thursday, January 27, 2011 Page 13 of 23
FL676 McIntosh Unit 2

10/28/2010

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 0.95 0.85 1.1 0.967

lb/mmBtuO2 1.53E-04 1.36E-04 1.80E-04 0.000

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 0.38 0.35 0.33 0.353

lb/mmBtuO2 6.12E-05 5.62E-05 5.41E-05 0.000

Location: FL676 Unit 2 - Method 29

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0092 0.0073 0.0073 0.008

lb/mmBtuO2 1.97E-06 1.55E-06 1.54E-06 0.000

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0039 0.003 0.0035 0.003

lb/mmBtuO2 8.35E-07 6.39E-07 7.38E-07 0.000

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00075 0.00075 0.00075 0.001

lb/mmBtuO2 1.61E-07 1.60E-07 1.58E-07 0.000

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00315 0.00078 0.00075 0.002

lb/mmBtuO2 6.74E-07 1.66E-07 1.58E-07 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.12385 0.02921 0.01775 0.057

lb/mmBtuO2 2.65E-05 6.22E-06 3.74E-06 0.000

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.01485 0.01469 0.01415 0.015

lb/mmBtuO2 3.18E-06 3.13E-06 2.98E-06 0.000

Compound: Filterable Particulate

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 339.2 362.4 337.6 346.400

Thursday, January 27, 2011 Page 14 of 23
FL676 McIntosh Unit 2

10/28/2010

Process Run Data

lb/mmBtuO2 7.26E-02 7.72E-02 7.12E-02 0.074

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.11422 1.36502 0.09582 0.525

lb/mmBtuO2 2.45E-05 2.91E-04 2.02E-05 0.000

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0372 0.02854 0.0267 0.031

lb/mmBtuO2 7.96E-06 6.08E-06 5.63E-06 0.000

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.76965 0.73165 0.67555 0.726

lb/mmBtuO2 1.65E-04 1.56E-04 1.42E-04 0.000

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0075 0.0088 0.0075 0.008

lb/mmBtuO2 1.61E-06 1.87E-06 1.58E-06 0.000

Location: FL676 Unit 2 - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 19.53 25.23 25.33 23.363

lb/mmBtuO2 4.75E-03 6.22E-03 6.18E-03 0.006

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 26 15 12 17.667

lb/mmBtuO2 6.32E-03 3.70E-03 2.93E-03 0.004

Compound: Organic Condensible Particulate

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 1.8 1 1.1 1.300

lb/mmBtuO2 4.37E-04 2.46E-04 2.68E-04 0.000

Compound: Total PM2.5

Average

RunNumber OTM27-1 OTM27-2 OTM27-3

Mass_mg 47.33 41.23 38.43 42.330

lb/mmBtuO2 1.15E-02 1.02E-02 9.37E-03 0.010

Thursday, January 27, 2011 Page 15 of 23
FL676 McIntosh Unit 2

10/28/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Residual Oil (No. 6) Burned 94.8 mmBtu/hr Daily Avg. June 4, 

2010

0

2 Residual Oil (No. 6) Burned 137.2 mmBtu/hr Daily Avg. June 5, 

2010

0

3 Residual Oil (No. 6) Burned 145.4 mmBtu/hr Daily Avg. July 

20, 2010

0

4 Residual Oil (No. 6) Burned 120.3 mmBtu/hr Daily Avg. July 

21, 2010

0

5 Residual Oil (No. 6) Burned 135.2 mmBtu/hr Daily Avg. July 

22, 2010

0

6 Residual Oil (No. 6) Burned 257.9 mmBtu/hr Daily Avg. July 

23, 2010

0

1 Pipeline Natural Gas 389.1 mmBtu/hr Daily Avg. June 4, 

2010

0

2 Pipeline Natural Gas 353 mmBtu/hr Daily Avg. June 5, 

2010

0

3 Pipeline Natural Gas 324.7 mmBtu/hr Daily Avg. July 

20, 2010

0

4 Pipeline Natural Gas 364.9 mmBtu/hr Daily Avg. July 

21, 2010

0

5 Pipeline Natural Gas 355.4 mmBtu/hr Daily Avg. July 

22, 2010

0

6 Pipeline Natural Gas 608.5 mmBtu/hr Daily Avg. July 

23, 2010

0

1 Unit Load 47.2 MW Daily Avg. June 4, 

2010

0

2 Unit Load 48.2 MW Daily Avg. June 5, 

2010

0

3 Unit Load 48.5 MW Daily Avg. July 

20, 2010

0

4 Unit Load 46.1 MW Daily Avg. July 

21, 2010

0

5 Unit Load 47 MW Daily Avg. July 

22, 2010

0

6 Unit Load 90.9 MW Daily Avg. July 

23, 2010

0

1 Heat Input 483.9 mmBtu/hr Daily Avg. June 4, 

2010

0

2 Heat Input 490.2 mmBtu/hr Daily Avg. June 5, 

2010

0

3 Heat Input 470.1 mmBtu/hr Daily Avg. July 

20, 2010

0

Thursday, January 27, 2011 Page 16 of 23
FL676 McIntosh Unit 2

10/28/2010

APCD Run Data

Process Lab Run Data

4 Heat Input 485.2 mmBtu/hr Daily Avg. July 

21, 2010

0

5 Heat Input 490.6 mmBtu/hr Daily Avg. July 

22, 2010

0

6 Heat Input 866.4 mmBtu/hr Daily Avg. July 

23, 2010

0

Thursday, January 27, 2011 Page 17 of 23
FL676 McIntosh Unit 2

10/28/2010

Sampling / Stack Data Results Detail

Location FL676 Unit 2 - Method 10

Average

Run Number M10-1 M10-2 M10-3

Test Date 7/20/2010 7/20/2010 7/20/2010

Run Start Time 9:00:00 AM 11:05:00 AM 1:10:00 PM

Run Finish Time 11:00:00 AM 1:05:00 PM 3:10:00 PM

Carbon Dioxide, % 7.5 7.6 7.7 7.600

Oxygen, % 8.7 8.6 8.5 8.600

Fuel Factor 1.63 1.62 1.61

Dry Volumetric Flow Rate, dry scfm 133516 133516 133516 133,516.000

F-Factor, dscfm/MMBtu @ %O2 8798 8797 8797 8,797.333

Moisture, % 10.98 10.98 10.98 10.980

Analyzer Make TEI TEI TEI

Analyzer Model 48C 48C 48C

Analyzer Serial Number 48C-71529-

369

48C-71529-

369

48C-71529-

369

Operating Range 200 200 200 200.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 111 111 111 111.000

Calibration Pre Zero Cylinder ID CC242679 CC242679 CC242679

Calibration Pre Zero Cylinder Instrument Response 0.03 0.2 0.33 0.187

Calibration Pre Zero Cylinder Bias -0.01 0.08 0.15 0.073

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC307483 CC307483 CC307483

Calibration Pre High Cylinder Instrument Response 99.55 99.5 99.52 99.523

Calibration Pre High Cylinder Bias 2.09 2.06 2.07 2.073

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC242679 CC242679 CC242679

Calibration Post Zero Cylinder Instrument Response 0.2 0.33 0.66 0.397

Calibration Post Zero Cylinder Bias 0.08 0.15 0.32 0.183

Calibration Post Zero Cylinder Drift 0.09 0.07 0.17 0.110

Calibration Post High Cylinder ID CC307483 CC307483 CC307483

Calibration Post High Cylinder Instrument Response 99.5 99.52 99.59 99.537

Calibration Post High Cylinder Bias 2.06 2.07 2.11 2.080

Calibration Post High Cylinder Drift 2.9999999999

9998E-02

9.999999999

99979E-03

0.04 0.027

Cavg 55.13 57.72 55.57 56.140

Cavg Units ppmvd ppmvd ppmvd

Cgas 52.2424 54.6501 52.4842 53.126

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

Thursday, January 27, 2011 Page 18 of 23
FL676 McIntosh Unit 2

10/28/2010

Location FL676 Unit 2 - Method 23

Average

Run Number M23-1 M23-2 M23-3

Test Date 7/20/2010 7/21/2010 7/22/2010

Run Start Time 12:10:00 PM 6:19:00 AM 6:50:00 AM

Run Finish Time 8:26:00 PM 3:01:00 PM 3:32:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.25 0.25 0.275 0.258

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.01 1.01 1.01 1.010

Barometric Pressure, inches of Mercury 29.82 29.75 29.75 29.773

Average Orifice Meter Differential, inches H2O 0.91 0.88 1.29 1.027

Dry Gas Meter Volume Sampled, cubic feet 280.795 275.339 336.368 297.501

Average Dry Gas Meter Temperature, °F 105.70 92.74 95.71 98.050

Dry Gas Meter Volume Sampled, dscf 264.410 264.710 321.981 283.700

Total Moisture Liquid collected, g 692.3 757.6 910.8 786.900

Volume of Water Vapor, standard cubic feet 32.59 35.66 42.87 37.040

Moisture Content of Stack Gas, % 10.97 11.87 11.75 11.530

Moisture Saturation at Stack Gas Temperature, % 40.16 38.34 39.70 39.400

Dry Mole Fraction 0.8903 0.8813 0.8825 0.885

Carbon Dioxide, % 7.6 7.2 7.5 7.433

Oxygen, % 8.8 9.1 8.4 8.767

Carbon Monoxide & Nitrogen, % 83.6 83.7 84.1 83.800

Fuel Factor 1.59 1.64 1.67

Dry Molecular Weight, lb/lb-Mole 29.57 29.52 29.54 29.543

Wet Molecular weight, lb/lb-Mole 28.30 28.15 28.18 28.210

Flue Gas Static Pressure, inches of H2O -0.17 -0.2 -0.2 -0.190

Absolute Flue Gas Pressure, inches of Mercury 29.81 29.74 29.74 29.763

Average Stack Gas Temperature, °F 169.27 167.17 168.67 168.370

Average Velocity Head, inches of H2O 0.3100475627

9388

0.301313586

603872

0.299619221

910039

0.304

Average Stack Gas Velocity, feet/second 34.53 34.12 34.04 34.230

Stack Cross-Sectional Area, square feet 86.590 86.590 86.590 86.590

Dry Volumetric Flow Rate, dry scfm 133,520.9 130,731.4 130,290.8 131,514.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 179,397.2 177,267.0 176,851.4 177,838.533

Percent Isokinetic of Sampling Rate, % 104.8 107.2 108.1 106.700

Percent Excess Air, % 66.3 70.0 60.9 65.733

F-Factor, dscfm/MMBtu @ %O2 8796 8791 8795 8,794.000

Round Duct Diameter, inches 126 126 126

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

Thursday, January 27, 2011 Page 19 of 23
FL676 McIntosh Unit 2

10/28/2010

Location FL676 Unit 2 - Method 25A

Average

Run Number M25A-1 M25A-2 M25A-3

Test Date 7/20/2010 7/20/2010 7/20/2010

Run Start Time 9:00:00 AM 11:05:00 AM 1:10:00 PM

Run Finish Time 11:00:00 AM 1:05:00 PM 3:10:00 PM

Carbon Dioxide, % 7.5 7.6 7.7 7.600

Oxygen, % 8.7 8.6 8.5 8.600

Fuel Factor 1.63 1.62 1.61

Dry Volumetric Flow Rate, dry scfm 133516 133516 133516 133,516.000

F-Factor, dscfm/MMBtu @ %O2 8798 8797 8797 8,797.333

Moisture, % 10.98 10.98 10.98 10.980

Analyzer Make CAI CAI CAI

Analyzer Model 300M FID 300M FID 300M FID

Analyzer Serial Number 5011002 5011002 5011002 5,011,002.0

00

Operating Range 100 100 100 100.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 112 112 112 112.000

Calibration Pre Zero Cylinder ID CC242679 CC242679 CC242679

Calibration Pre Zero Cylinder Instrument Response 0.03 0 0.03 0.020

Calibration Pre Zero Cylinder Bias -0.03 0 -0.03 -0.020

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC101331 CC101331 CC101331

Calibration Pre High Cylinder Instrument Response 9.55 9.5 9.52 9.523

Calibration Pre High Cylinder Bias 0 -0.17 -0.1 -0.090

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC242679 CC242679 CC242679

Calibration Post Zero Cylinder Instrument Response 0 0.03 0.06 0.030

Calibration Post Zero Cylinder Bias -0.13 -0.03 0.07 -0.030

Calibration Post Zero Cylinder Drift 0.1 0.03 0.1 0.077

Calibration Post High Cylinder ID CC101331 CC101331 CC101331

Calibration Post High Cylinder Instrument Response 9.5 9.52 9.59 9.537

Calibration Post High Cylinder Bias -0.17 -0.1 0.1 -0.057

Calibration Post High Cylinder Drift 0.17 0.07 0.2 0.147

Cavg 0.43 0.61 0.83 0.623

Cavg Units ppmvw ppmvw ppmvw

Cgas 0.4672 0.6709 0.8841 0.674

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0.4158727655

09989

0.597193259

610321

0.787064702

788006

0.600

Cgasw Units ppmvw ppmvw ppmvw

Thursday, January 27, 2011 Page 20 of 23
FL676 McIntosh Unit 2

10/28/2010

Location FL676 Unit 2 - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 7/23/2010 7/23/2010 7/23/2010

Run Start Time 6:46:00 AM 10:11:00 AM 1:36:00 PM

Run Finish Time 10:00:00 AM 1:24:00 PM 4:47:00 PM

Net Traversing Points 24 24 24

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 1.01 1.01 1.01 1.010

Barometric Pressure, inches of Mercury 29.75 29.75 29.75 29.750

Average Orifice Meter Differential, inches H2O 2.47 2.43 2.46 2.453

Dry Gas Meter Volume Sampled, cubic feet 166.525 168.205 163.740 166.157

Average Dry Gas Meter Temperature, °F 83.00 90.38 87.19 86.857

Dry Gas Meter Volume Sampled, dscf 163.608 163.026 159.636 162.090

Total Moisture Liquid collected, g 563.2 567.1 534.3 554.867

Volume of Water Vapor, standard cubic feet 26.51 26.69 25.15 26.117

Moisture Content of Stack Gas, % 13.94 14.07 13.61 13.873

Moisture Saturation at Stack Gas Temperature, % 49.79 56.85 44.74 50.460

Dry Mole Fraction 0.8606 0.8593 0.8639 0.861

Carbon Dioxide, % 9.8 9.7 9.2 9.567

Oxygen, % 5.5 5.4 5.4 5.433

Carbon Monoxide & Nitrogen, % 84.7 84.9 85.4 85.000

Fuel Factor 1.57 1.60 1.68

Dry Molecular Weight, lb/lb-Mole 29.79 29.77 29.69 29.750

Wet Molecular weight, lb/lb-Mole 28.15 28.11 28.10 28.120

Flue Gas Static Pressure, inches of H2O -0.25 -0.25 -0.25 -0.250

Absolute Flue Gas Pressure, inches of Mercury 29.73 29.73 29.73 29.730

Average Stack Gas Temperature, °F 178.63 184.63 173.88 179.047

Average Velocity Head, inches of H2O 0.8462796610

42321

0.836015872

228706

0.843751436

625755

0.842

Average Stack Gas Velocity, feet/second 57.71 57.67 57.46 57.613

Stack Cross-Sectional Area, square feet 86.590 86.590 86.590 86.590

Dry Volumetric Flow Rate, dry scfm 211,977.3 209,541.7 213,456.0 211,658.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 299,826.5 299,618.7 298,527.7 299,324.300

Percent Isokinetic of Sampling Rate, % 108.9 109.8 105.5 108.067

Percent Excess Air, % 32.6 31.7 31.5 31.933

F-Factor, dscfm/MMBtu @ %O2 8803 8803 8803 8,803.000

Round Duct Diameter, inches 126 126 126

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

Thursday, January 27, 2011 Page 21 of 23
FL676 McIntosh Unit 2

10/28/2010

Location FL676 Unit 2 - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 6/4/2010 6/5/2010 6/5/2010

Run Start Time 10:20:00 AM 6:19:00 AM 12:15:00 PM

Run Finish Time 2:35:00 PM 10:34:00 AM 4:31:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.258 0.258 0.258 0.258

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.99 0.99 0.99 0.990

Barometric Pressure, inches of Mercury 29.66 29.68 29.68 29.673

Average Orifice Meter Differential, inches H2O 0.89 0.89 0.92 0.900

Dry Gas Meter Volume Sampled, cubic feet 146.089 143.648 147.449 145.729

Average Dry Gas Meter Temperature, °F 89.46 85.40 93.98 89.613

Dry Gas Meter Volume Sampled, dscf 138.076 136.871 138.327 137.758

Total Moisture Liquid collected, g 430.5 453.2 440.2 441.300

Volume of Water Vapor, standard cubic feet 20.26 21.33 20.72 20.770

Moisture Content of Stack Gas, % 12.80 13.48 13.03 13.103

Moisture Saturation at Stack Gas Temperature, % 40.64 36.76 42.04 39.813

Dry Mole Fraction 0.872 0.8652 0.8697 0.869

Carbon Dioxide, % 8.1 8.2 8.2 8.167

Oxygen, % 7.2 7 7 7.067

Carbon Monoxide & Nitrogen, % 84.7 84.8 84.8 84.767

Fuel Factor 1.69 1.70 1.70

Dry Molecular Weight, lb/lb-Mole 29.58 29.59 29.59 29.587

Wet Molecular weight, lb/lb-Mole 28.10 28.03 28.08 28.070

Flue Gas Static Pressure, inches of H2O -0.21 -0.22 -0.22 -0.217

Absolute Flue Gas Pressure, inches of Mercury 29.64 29.66 29.66 29.653

Average Stack Gas Temperature, °F 169.54 165.25 171.04 168.610

Average Velocity Head, inches of H2O 0.3009054923

06756

0.303837253

334503

0.306842480

62535

0.304

Average Stack Gas Velocity, feet/second 34.25 34.33 34.63 34.403

Stack Cross-Sectional Area, square feet 86.590 86.590 86.590 86.590

Dry Volumetric Flow Rate, dry scfm 128,920.9 129,181.1 129,785.9 129,295.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 177,942.5 178,358.1 179,916.7 178,739.100

Percent Isokinetic of Sampling Rate, % 106.4 105.3 105.9 105.867

Percent Excess Air, % 47.5 45.5 45.5 46.167

F-Factor, dscfm/MMBtu @ %O2 8790 8793 8796 8,793.000

Round Duct Diameter, inches 126 126 126

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

Thursday, January 27, 2011 Page 22 of 23
FL676 McIntosh Unit 2

10/28/2010

Location FL676 Unit 2 - OTM - 27/28

Average

Run Number OTM27-1 OTM27-2 OTM27-3

Test Date 6/4/2010 6/5/2010 6/5/2010

Run Start Time 10:00:00 AM 6:19:00 AM 12:49:00 PM

Run Finish Time 4:48:00 PM 12:01:00 PM 6:36:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 331.25 329.75 332.5

Nozzle Diameter, inches 0.2 0.2 0.2 0.200

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.01 1.01 1.01 1.010

Barometric Pressure, inches of Mercury 29.66 29.68 29.68 29.673

Average Orifice Meter Differential, inches H2O 0.35 0.35 0.35 0.350

Dry Gas Meter Volume Sampled, cubic feet 125.812 121.702 126.007 124.507

Average Dry Gas Meter Temperature, °F 87.25 84.63 97.83 89.903

Dry Gas Meter Volume Sampled, dscf 121.640 118.312 119.599 119.850

Total Moisture Liquid collected, g 361.8 357.4 367 362.067

Volume of Water Vapor, standard cubic feet 17.03 16.82 17.27 17.040

Moisture Content of Stack Gas, % 12.28 12.45 12.62 12.450

Moisture Saturation at Stack Gas Temperature, % 36.99 33.79 34.32 35.033

Dry Mole Fraction 0.8772 0.8755 0.8738 0.876

Carbon Dioxide, % 8.1 8.2 8.2 8.167

Oxygen, % 7.2 7 7 7.067

Carbon Monoxide & Nitrogen, % 84.7 84.8 84.8 84.767

Fuel Factor 1.69 1.70 1.70

Dry Molecular Weight, lb/lb-Mole 29.58 29.59 29.59 29.587

Wet Molecular weight, lb/lb-Mole 28.16 28.15 28.13 28.147

Flue Gas Static Pressure, inches of H2O -0.2 -0.22 -0.22 -0.213

Absolute Flue Gas Pressure, inches of Mercury 29.65 29.66 29.66 29.657

Average Stack Gas Temperature, °F 165.50 161.67 162.33 163.167

Average Velocity Head, inches of H2O 0.3169740958

91863

0.319527511

431723

0.319535866

075862

0.319

Average Stack Gas Velocity, feet/second 34.99 35.03 35.06 35.027

Stack Cross-Sectional Area, square feet 86.590 86.590 86.590 86.590

Dry Volumetric Flow Rate, dry scfm 133,392.5 134,152.5 133,864.6 133,803.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 181,787.0 181,994.9 182,150.7 181,977.533

Percent Isokinetic of Sampling Rate, % 109.3 106.2 106.6 107.367

Percent Excess Air, % 47.5 45.5 45.5 46.167

F-Factor, dscfm/MMBtu @ %O2 8790 8793 8796 8,793.000

Round Duct Diameter, inches 126 126 126

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

Thursday, January 27, 2011 Page 23 of 23