Name: Kevin Holbrooks

Title: Director, Environmental Compliance

Company: Jacksonville Electric Authority

Sign Date:

Name: Carl Vineyard

Title: Utility MACT Program Manager

Company: Grace Consulting, Inc.

Sign Date: 9/2/2010

Permitted Facility Representative / Date Testing Company Representative / Date

JEA, Northside Station, 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.

Friday, February 04, 2011 Page 1 of 34
JEA, Northside Station, Unit 2

Facility Information:

Northside Station, Unit 2

4377 Heckscher Drive

Jacksonville FL 32226

Contact: Kevin Holbrooks

Phone: 904-665-4540

Fax: 904-665-4530

Email: Holbke@JEA.com

Testing Company:

Grace Consulting, Inc.

510 Dickson Street

Wellington OH 44090

Contact:Carl Vineyard

Phone: 440-647-6672

Fax: 440-647-6673

Email: carlvineyard@gcitest.com

Air Permit Number:

667

Permitted Source ID/Name:

JEA Northside2

Permitted Maximum Process Rate: 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:

Flow Diagram attached.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 1203100045 FRS #: 110037464106

SCC / Description 10100202 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Bituminous Coal) 

The following state and federal regulations that apply to the proposed testing:

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

Unit 2 Stack 180 0 0 0 3600 1548 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Unit 2 Stack Carbon Monoxide Method 10 3 180 0

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

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

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

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

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

Unit 2 Stack OCDD Method 23 3 480 0

Friday, February 04, 2011 Page 2 of 34
JEA, Northside Station, Unit 2

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

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

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

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

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

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

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

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

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

Unit 2 Stack Total Dioxins Method 23 3 480 0

Unit 2 Stack Total Furans Method 23 3 480 0

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

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

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

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

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

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

Unit 2 Stack 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)

Unit 2 Stack Method 23 3 480 0

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

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

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

(PCB189)

Unit 2 Stack Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Unit 2 Stack Method 25A 3 120 0

Unit 2 Stack Hydrogen Fluoride Method 26A 3 180 0

Unit 2 Stack Hydrogen Chloride Method 26A 3 180 0

Unit 2 Stack Hydrogen Chloride Method 26A 3 180 0

Unit 2 Stack Hydrogen Fluoride Method 26A 3 180 0

Unit 2 Stack Filterable Particulate OTM - 27/28 3 360 0

Inorganic (Aqueous) 

Condensible Part.

Unit 2 Stack OTM - 27/28 3 360 0

Unit 2 Stack Total PM2.5 OTM - 27/28 3 360 0

Organic Condensible 

Particulate

Unit 2 Stack OTM - 27/28 3 360 0

Unit 2 Stack Total Particulate OTM - 27/28 3 360 0

Unit 2 Stack Filterable PM2.5 OTM - 27/28 3 360 0

Unit 2 Stack Filterable Particulate Method 29 3 240 0

Unit 2 Stack Beryllium Method 29 3 240 0

Unit 2 Stack Cadmium Method 29 3 240 0

Unit 2 Stack Chromium Method 29 3 240 0

Unit 2 Stack Arsenic Method 29 3 240 0

Unit 2 Stack Cobalt Method 29 3 240 0

Unit 2 Stack Lead Method 29 3 240 0

Unit 2 Stack Manganese Method 29 3 240 0

Unit 2 Stack Nickel Method 29 3 240 0

Unit 2 Stack Selenium Method 29 3 240 0

Unit 2 Stack Antimony Method 29 3 240 0

Unit 2 Stack Phosphorus (yellow or white) Method 29 3 240 0

Unit 2 Stack Co2 Method 3A CO2 3 180 0

Unit 2 Stack O2 Method 3A O2 3 180 0

Unit 2 Stack Sulfur Dioxide Method 6C 3 180 0

Friday, February 04, 2011 Page 3 of 34
JEA, Northside Station, Unit 2

The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

The HCN was sampled using CTM 033 with 4 Normal NsOH and an additional impinger for one hour per the 

clarification given by the USEPA .

Unit 2 Stack Nitrogen oxides (NOx) Method 7E 3 180 0

Friday, February 04, 2011 Page 4 of 34
JEA, Northside Station, Unit 2

Sampling / Stack Data Results Summary

Location Unit 2 Stack - Method 10

Average

Run Number 1 2 3

Test Date 5/27/2010 5/27/2010 5/28/2010

Run Start Time 4:00:00 PM 6:30:00 PM 7:35:00 AM

Run Finish Time 6:11:00 PM 8:38:00 PM 9:45:00 AM

Carbon Dioxide, % 14.6 14.7 14.6 14.633

Oxygen, % 5.1 5 4.9 5.000

Dry Volumetric Flow Rate, dry scfm 661205 672539 661789 665,177.667

F-Factor, dscfm/MMBtu @ %O2 9966 9966 9974 9,968.667

Moisture, % 11.02 11.49 10.31 10.940

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 2 Stack - Method 23

Average

Run Number 1 2 3

Test Date 6/2/2010 6/3/2010 6/4/2010

Run Start Time 7:45:00 AM 8:10:00 

AM

7:20:00 AM

Run Finish Time 4:00:00 PM 4:25:00 PM 3:30:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 311.208 309.811 302.346 307.788

Moisture Content of Stack Gas, % 10.77 10.72 11.07 10.853

Moisture Saturation at Stack Gas Temperature, % 77.56 78.14 77.92 77.873

Carbon Dioxide, % 15.6 15.2 15.7 15.500

Oxygen, % 4.3 4.6 4.8 4.567

Average Stack Gas Temperature, °F 199.04 199.33 199.23 199.200

Dry Volumetric Flow Rate, dry scfm 583,917.6 582,599.6 584,533.0 583,683.400

Actual Wet Volumetric Flue Gas Flow Rate, acfm 824,799.6 823,951.4 829,252.8 826,001.267

Percent Isokinetic of Sampling Rate, % 105.1 104.9 102.0 104.000

F-Factor, dscfm/MMBtu @ %O2 8922 8586 8626 8,711.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 04, 2011 Page 5 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 25A

Average

Run Number 1 2 3

Test Date 5/27/2010 5/27/2010 5/28/2010

Run Start Time 4:00:00 PM 6:30:00 PM 7:35:00 AM

Run Finish Time 6:11:00 PM 8:38:00 PM 9:45:00 AM

Carbon Dioxide, % 14.6 14.7 14.6 14.633

Oxygen, % 5.1 5 4.9 5.000

Dry Volumetric Flow Rate, dry scfm 661205 672539 661789 665,177.667

F-Factor, dscfm/MMBtu @ %O2 9966 9966 9974 9,968.667

Moisture, % 11.02 11.49 10.31 10.940

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 2 Stack - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Friday, February 04, 2011 Page 6 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 29

Average

Run Number

Test Date

Run Start Time

Run Finish Time Unit 2 Stack Unit 2 

Stack

Unit 2 Stack

Net Run Time, minutes Method 29 Method 29 Method 29

Dry Gas Meter Volume Sampled, dscf 1.01 1.01 1.01 1.010

Moisture Content of Stack Gas, % 161.763 158.759 159.100 159.874

Moisture Saturation at Stack Gas Temperature, % 99.33 95.10 98.73 97.720

Carbon Dioxide, % 395.5 387.8 399 394.100

Oxygen, % 18.62 18.25 18.78 18.550

Average Stack Gas Temperature, °F 1.10 1.06 1.05 1.070

Dry Volumetric Flow Rate, dry scfm 79.91 78.66 78.19 78.920

Actual Wet Volumetric Flue Gas Flow Rate, acfm 180 180 180 180.000

Percent Isokinetic of Sampling Rate, % 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 176.715 176.715 176.715 176.715

Fw 847,277.7 834,024.1 829,040.8 836,780.867

Fc 598,083.1 588,670.6 583,535.7 590,096.467

Location Unit 2 Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/26/2010

Run Start Time 2:40:00 PM 1:25:00 PM 4:55:00 PM

Run Finish Time 5:49:00 PM 4:35:00 PM 8:05:00 PM

Carbon Dioxide, % 15.3 15.6 15.7 15.533

Oxygen, % 4.3 4.5 4.4 4.400

Dry Volumetric Flow Rate, dry scfm 665866 649441 667962 661,089.667

F-Factor, dscfm/MMBtu @ %O2 9907 9912 9966 9,928.333

Moisture, % 11.13 11.15 10.91 11.063

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 04, 2011 Page 7 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 3A CO2 3

Average

Run Number 4 5 6

Test Date 5/25/2010 5/26/2010 5/27/2010

Run Start Time 8:30:00 AM 8:00:00 

AM

9:10:00 AM

Run Finish Time 3:24:00 PM 2:12:00 PM 3:25:00 PM

Carbon Dioxide, % 15.1 15.4 15.3 15.267

Oxygen, % 4.3 4.6 4.8 4.567

Dry Volumetric Flow Rate, dry scfm 670275 659440 656412 662,042.333

F-Factor, dscfm/MMBtu @ %O2 9906 9913 9966 9,928.333

Moisture, % 10.78 10.74 11.08 10.867

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 2 Stack - Method 3A CO2 3 6

Average

Run Number 7 8 9

Test Date 5/27/2010 5/27/2010 5/28/2010

Run Start Time 4:00:00 PM 6:30:00 PM 7:35:00 AM

Run Finish Time 6:11:00 PM 8:38:00 PM 9:45:00 AM

Carbon Dioxide, % 14.6 14.7 14.6 14.633

Oxygen, % 5.1 5 4.9 5.000

Dry Volumetric Flow Rate, dry scfm 661205 672539 661789 665,177.667

F-Factor, dscfm/MMBtu @ %O2 9966 9966 9974 9,968.667

Moisture, % 11.02 11.49 10.31 10.940

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 04, 2011 Page 8 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/26/2010

Run Start Time 2:40:00 PM 1:25:00 PM 4:55:00 PM

Run Finish Time 5:49:00 PM 4:35:00 PM 8:05:00 PM

Carbon Dioxide, % 15.3 15.6 15.7 15.533

Oxygen, % 4.3 4.5 4.4 4.400

Dry Volumetric Flow Rate, dry scfm 665866 649441 667962 661,089.667

F-Factor, dscfm/MMBtu @ %O2 9907 9912 9966 9,928.333

Moisture, % 11.13 11.15 10.91 11.063

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 2 Stack - Method 3A O2 3

Average

Run Number 4 5 6

Test Date 5/25/2010 5/26/2010 5/27/2010

Run Start Time 8:30:00 AM 8:00:00 

AM

9:10:00 AM

Run Finish Time 3:24:00 PM 2:12:00 PM 3:25:00 PM

Carbon Dioxide, % 15.1 15.4 15.3 15.267

Oxygen, % 4.3 4.6 4.8 4.567

Dry Volumetric Flow Rate, dry scfm 670275 659440 656412 662,042.333

F-Factor, dscfm/MMBtu @ %O2 9906 9913 9966 9,928.333

Moisture, % 10.78 10.74 11.08 10.867

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 04, 2011 Page 9 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 3A O2 3 6

Average

Run Number 7 8 9

Test Date 5/27/2010 5/27/2010 5/28/2010

Run Start Time 4:00:00 PM 6:30:00 PM 7:35:00 AM

Run Finish Time 6:11:00 PM 8:38:00 PM 9:45:00 AM

Carbon Dioxide, % 14.6 14.7 14.6 14.633

Oxygen, % 5.1 5 4.9 5.000

Dry Volumetric Flow Rate, dry scfm 661205 672539 661789 665,177.667

F-Factor, dscfm/MMBtu @ %O2 9966 9966 9974 9,968.667

Moisture, % 11.02 11.49 10.31 10.940

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 2 Stack - Method 6C

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/26/2010

Run Start Time 2:40:00 PM 1:25:00 PM 4:55:00 PM

Run Finish Time 5:49:00 PM 4:35:00 PM 8:05:00 PM

Carbon Dioxide, % 15.3 15.6 15.7 15.533

Oxygen, % 4.3 4.5 4.4 4.400

Dry Volumetric Flow Rate, dry scfm 665866 649441 667962 661,089.667

F-Factor, dscfm/MMBtu @ %O2 9907 9912 9966 9,928.333

Moisture, % 11.13 11.15 10.91 11.063

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 04, 2011 Page 10 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 7E

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/26/2010

Run Start Time 2:40:00 PM 1:25:00 PM 4:55:00 PM

Run Finish Time 5:49:00 PM 4:35:00 PM 8:05:00 PM

Carbon Dioxide, % 15.3 15.6 15.7 15.533

Oxygen, % 4.3 4.5 4.4 4.400

Dry Volumetric Flow Rate, dry scfm 665866 649441 667962 661,089.667

F-Factor, dscfm/MMBtu @ %O2 9907 9912 9966 9,928.333

Moisture, % 11.13 11.15 10.91 11.063

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 2 Stack - OTM - 27/28

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/27/2010

Run Start Time 8:30:00 AM 8:00:00 

AM

9:10:00 AM

Run Finish Time 3:24:00 PM 2:12:00 PM 2:42:18 PM

Net Run Time, minutes 359.8 360 360.1

Dry Gas Meter Volume Sampled, dscf 113.705 118.731 119.425 117.287

Moisture Content of Stack Gas, % 12.81 10.78 11.49 11.693

Moisture Saturation at Stack Gas Temperature, % 81.75 79.37 77.89 79.670

Carbon Dioxide, % 15.1 15.4 15.3 15.267

Oxygen, % 4.3 4.6 4.8 4.567

Average Stack Gas Temperature, °F 201.58 200.00 199.00 200.193

Dry Volumetric Flow Rate, dry scfm 612,289.7 631,890.9 635,354.6 626,511.733

Actual Wet Volumetric Flue Gas Flow Rate, acfm 888,523.0 896,687.3 909,304.7 898,171.667

Percent Isokinetic of Sampling Rate, % 87.8 88.8 88.8 88.467

F-Factor, dscfm/MMBtu @ %O2 9906 9913 9966 9,928.333

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, February 04, 2011 Page 11 of 34
JEA, Northside Station, Unit 2

Emissions Summary

Location: Unit 2 Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.99E-02 2.18E-02 2.20E-02 0.021

ppm 2.07E+01 2.29E+01 2.32E+01 22.267

ppm@7%O2 1.82E+01 2.00E+01 2.02E+01 19.467

Location: Unit 2 Stack - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000032 0.0000000036 0.0000000047 0.000

lb/mmBtuO2 2.55E-13 2.82E-13 3.84E-13 0.000

ng/dscm 3.63E-04 4.10E-04 5.49E-04 0.000

ng/dscm@7%O2 3.04E-04 3.50E-04 4.74E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000022 0.0000000025 0.0000000029 0.000

lb/mmBtuO2 1.75E-13 1.96E-13 2.37E-13 0.000

ng/dscm 2.50E-04 2.85E-04 3.39E-04 0.000

ng/dscm@7%O2 2.09E-04 2.43E-04 2.93E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000029 0.0000000033 0.0000000038 0.000

lb/mmBtuO2 2.31E-13 2.59E-13 3.10E-13 0.000

ng/dscm 3.29E-04 3.76E-04 4.44E-04 0.000

ng/dscm@7%O2 2.75E-04 3.21E-04 3.83E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000024 0.0000000032 0.0000000027 0.000

lb/mmBtuO2 1.91E-13 2.51E-13 2.20E-13 0.000

ng/dscm 2.72E-04 3.65E-04 3.15E-04 0.000

ng/dscm@7%O2 2.28E-04 3.11E-04 2.72E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000019 0.0000000021 0.0000000021 0.000

lb/mmBtuO2 1.51E-13 1.65E-13 1.71E-13 0.000

ng/dscm 2.16E-04 2.39E-04 2.45E-04 0.000

ng/dscm@7%O2 1.81E-04 2.04E-04 2.12E-04 0.000

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

Average

Friday, February 04, 2011 Page 12 of 34
JEA, Northside Station, Unit 2

RunNumber 1 2 3

Mass_mg 0.0000000023 0.0000000031 0.0000000026 0.000

lb/mmBtuO2 1.83E-13 2.43E-13 2.12E-13 0.000

ng/dscm 2.61E-04 3.53E-04 3.04E-04 0.000

ng/dscm@7%O2 2.19E-04 3.01E-04 2.62E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000017 0.0000000019 0.0000000019 0.000

lb/mmBtuO2 1.35E-13 1.49E-13 1.55E-13 0.000

ng/dscm 1.93E-04 2.17E-04 2.22E-04 0.000

ng/dscm@7%O2 1.62E-04 1.85E-04 1.92E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000024 0.0000000032 0.0000000027 0.000

lb/mmBtuO2 1.91E-13 2.51E-13 2.20E-13 0.000

ng/dscm 2.72E-04 3.65E-04 3.15E-04 0.000

ng/dscm@7%O2 2.28E-04 3.11E-04 2.72E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000021 0.0000000023 0.0000000023 0.000

lb/mmBtuO2 1.67E-13 1.80E-13 1.88E-13 0.000

ng/dscm 2.38E-04 2.62E-04 2.69E-04 0.000

ng/dscm@7%O2 1.99E-04 2.23E-04 2.32E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000003 0.0000000032 0.0000000031 0.000

lb/mmBtuO2 2.39E-13 2.51E-13 2.53E-13 0.000

ng/dscm 3.40E-04 3.65E-04 3.62E-04 0.000

ng/dscm@7%O2 2.85E-04 3.11E-04 3.13E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000024 0.0000000026 0.0000000026 0.000

lb/mmBtuO2 1.91E-13 2.04E-13 2.12E-13 0.000

ng/dscm 2.72E-04 2.96E-04 3.04E-04 0.000

ng/dscm@7%O2 2.28E-04 2.52E-04 2.62E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000017 0.000000016 0.0000000146 0.000

lb/mmBtuO2 1.35E-12 1.25E-12 1.19E-12 0.000

ng/dscm 1.93E-03 1.82E-03 1.71E-03 0.002

ng/dscm@7%O2 1.62E-03 1.55E-03 1.48E-03 0.002

Friday, February 04, 2011 Page 13 of 34
JEA, Northside Station, Unit 2

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

Average

RunNumber 1 2 3

Mass_mg 0.000000432 0.00000016 0.000000118 0.000

lb/mmBtuO2 3.44E-11 1.25E-11 9.63E-12 0.000

ng/dscm 4.90E-02 1.82E-02 1.38E-02 0.027

ng/dscm@7%O2 4.10E-02 1.55E-02 1.19E-02 0.023

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

Average

RunNumber 1 2 3

Mass_mg 0.000002033 0.00000093 0.000000878 0.000

lb/mmBtuO2 1.62E-10 7.29E-11 7.17E-11 0.000

ng/dscm 2.31E-01 1.06E-01 1.03E-01 0.147

ng/dscm@7%O2 1.93E-01 9.04E-02 8.89E-02 0.124

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

Average

RunNumber 1 2 3

Mass_mg 0.000000093 0.000000033 0.000000042 0.000

lb/mmBtuO2 7.40E-12 2.59E-12 3.43E-12 0.000

ng/dscm 1.06E-02 3.76E-03 4.91E-03 0.006

ng/dscm@7%O2 8.88E-03 3.21E-03 4.24E-03 0.005

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

Average

RunNumber 1 2 3

Mass_mg 0.000000147 0.000000055 0.000000064 0.000

lb/mmBtuO2 1.17E-11 4.31E-12 5.23E-12 0.000

ng/dscm 1.67E-02 6.27E-03 7.48E-03 0.010

ng/dscm@7%O2 1.40E-02 5.35E-03 6.46E-03 0.009

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

Average

RunNumber 1 2 3

Mass_mg 0.000007245 0.00000327 0.00000307 0.000

lb/mmBtuO2 5.77E-10 2.56E-10 2.51E-10 0.000

ng/dscm 8.22E-01 3.73E-01 3.59E-01 0.518

ng/dscm@7%O2 6.88E-01 3.18E-01 3.10E-01 0.439

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

Average

RunNumber 1 2 3

Mass_mg 0.000000098 0.000000033 0.000000061 0.000

lb/mmBtuO2 7.80E-12 2.59E-12 4.98E-12 0.000

ng/dscm 1.11E-02 3.76E-03 7.13E-03 0.007

ng/dscm@7%O2 9.29E-03 3.21E-03 6.16E-03 0.006

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000018 0.000000002 0.000000002 0.000

lb/mmBtuO2 1.43E-13 1.57E-13 1.63E-13 0.000

Friday, February 04, 2011 Page 14 of 34
JEA, Northside Station, Unit 2

ng/dscm 2.04E-04 2.28E-04 2.34E-04 0.000

ng/dscm@7%O2 1.71E-04 1.94E-04 2.02E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000025 0.0000000027 0.0000000027 0.000

lb/mmBtuO2 1.99E-13 2.12E-13 2.20E-13 0.000

ng/dscm 2.84E-04 3.08E-04 3.15E-04 0.000

ng/dscm@7%O2 2.38E-04 2.63E-04 2.72E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000037 0.0000000038 0.0000000038 0.000

lb/mmBtuO2 2.94E-13 2.98E-13 3.10E-13 0.000

ng/dscm 4.20E-04 4.33E-04 4.44E-04 0.000

ng/dscm@7%O2 3.52E-04 3.69E-04 3.83E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000083 0.000000056 0.0000000202 0.000

lb/mmBtuO2 6.60E-12 4.39E-12 1.65E-12 0.000

ng/dscm 9.42E-03 6.38E-03 2.36E-03 0.006

ng/dscm@7%O2 7.89E-03 5.44E-03 2.04E-03 0.005

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

Average

RunNumber 1 2 3

Mass_mg 0.000000146 0.000000066 0.000000059 0.000

lb/mmBtuO2 1.16E-11 5.17E-12 4.82E-12 0.000

ng/dscm 1.66E-02 7.52E-03 6.89E-03 0.010

ng/dscm@7%O2 1.39E-02 6.41E-03 5.95E-03 0.009

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

Average

RunNumber 1 2 3

Mass_mg 0.000001244 0.000000488 0.000000454 0.000

lb/mmBtuO2 9.90E-11 3.82E-11 3.71E-11 0.000

ng/dscm 1.41E-01 5.56E-02 5.30E-02 0.083

ng/dscm@7%O2 1.18E-01 4.74E-02 4.58E-02 0.070

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

Average

RunNumber 1 2 3

Mass_mg 0.000000078 0.00000003 0.00000003 0.000

lb/mmBtuO2 6.21E-12 2.35E-12 2.45E-12 0.000

ng/dscm 8.85E-03 3.42E-03 3.50E-03 0.005

ng/dscm@7%O2 7.41E-03 2.92E-03 3.02E-03 0.004

Compound: OCDD

Average

RunNumber 1 2 3

Friday, February 04, 2011 Page 15 of 34
JEA, Northside Station, Unit 2

Mass_mg 0.0000000064 0.0000000076 0.000000006 0.000

lb/mmBtuO2 5.09E-13 5.95E-13 4.90E-13 0.000

ng/dscm 7.26E-04 8.66E-04 7.01E-04 0.001

ng/dscm@7%O2 6.08E-04 7.38E-04 6.05E-04 0.001

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.0000000251 0.0000000299 0.0000000275 0.000

lb/mmBtuO2 2.00E-12 2.34E-12 2.25E-12 0.000

ng/dscm 2.85E-03 3.41E-03 3.21E-03 0.003

ng/dscm@7%O2 2.39E-03 2.91E-03 2.77E-03 0.003

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.0000000498 0.0000000568 0.0000000551 0.000

lb/mmBtuO2 3.96E-12 4.45E-12 4.50E-12 0.000

ng/dscm 5.65E-03 6.48E-03 6.44E-03 0.006

ng/dscm@7%O2 4.73E-03 5.53E-03 5.56E-03 0.005

Location: Unit 2 Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 5.90E-04 6.60E-04 5.60E-04 0.001

ppm 3.91E-01 4.40E-01 3.76E-01 0.402

ppm@7%O2 3.44E-01 3.85E-01 3.27E-01 0.352

Location: Unit 2 Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.35 0.39 0.38 0.373

lb/mmBtuO2 8.40E-05 9.70E-05 9.18E-05 0.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.21 0.24 0.23 0.227

lb/mmBtuO2 5.04E-05 5.97E-05 5.56E-05 0.000

Location: Unit 2 Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0002 0.0001 0.0005 0.000

lb/mmBtuO2 3.57E-08 1.85E-08 9.46E-08 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Friday, February 04, 2011 Page 16 of 34
JEA, Northside Station, Unit 2

Mass_mg 0.00033 0.00033 0.00033 0.000

lb/mmBtuO2 5.89E-08 6.10E-08 6.24E-08 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00032 0.00032 0.00032 0.000

lb/mmBtuO2 5.72E-08 5.91E-08 6.05E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00195 0.001063 0.00272 0.002

lb/mmBtuO2 3.48E-07 1.96E-07 5.15E-07 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00062 0.00132 0.00034 0.001

lb/mmBtuO2 1.11E-07 2.44E-07 6.43E-08 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.001 0.001 0.001 0.001

lb/mmBtuO2 1.79E-07 1.85E-07 1.89E-07 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 2.2 1.75 4.25 2.733

lb/mmBtuO2 3.93E-04 3.23E-04 8.04E-04 0.001

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.0599 0.0258 0.0877 0.058

lb/mmBtuO2 1.07E-05 4.77E-06 1.66E-05 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.00101 0.00127 0.00113 0.001

lb/mmBtuO2 1.80E-07 2.35E-07 2.14E-07 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.02884 0.00074 0.02364 0.018

lb/mmBtuO2 5.15E-06 1.37E-07 4.47E-06 0.000

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Friday, February 04, 2011 Page 17 of 34
JEA, Northside Station, Unit 2

Mass_mg 0.021 0.0092 0.0074 0.013

lb/mmBtuO2 3.75E-06 1.70E-06 1.40E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.00043 0.00043 0.00043 0.000

lb/mmBtuO2 7.68E-08 7.94E-08 8.14E-08 0.000

Location: Unit 2 Stack - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 1.63E-01 1.78E-01 1.72E-01 0.171

ppm 7.88E+01 8.47E+01 8.22E+01 81.900

ppm@7%O2 6.60E+01 7.18E+01 6.92E+01 69.000

Location: Unit 2 Stack - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 1.15E-01 1.06E-01 9.89E-02 0.107

ppm 7.72E+01 7.02E+01 6.56E+01 71.000

ppm@7%O2 6.46E+01 5.95E+01 5.53E+01 59.800

Location: Unit 2 Stack - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 10.4 8.5 9.5 9.467

lb/mmBtuO2 2.51E-03 2.01E-03 2.27E-03 0.002

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 4.9 4.8 4.7 4.800

lb/mmBtuO2 1.18E-03 1.13E-03 1.12E-03 0.001

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 5.5 11.1 5.5 7.367

lb/mmBtuO2 1.33E-03 2.62E-03 1.31E-03 0.002

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 9 3.6 6.3 6.300

lb/mmBtuO2 2.18E-03 8.50E-04 1.50E-03 0.002

Compound: Total Particulate

Average

Friday, February 04, 2011 Page 18 of 34
JEA, Northside Station, Unit 2

Process Run Data

RunNumber 1 2 3

Mass_mg 24.9 23.2 21.3 23.133

lb/mmBtuO2 6.02E-03 5.48E-03 5.09E-03 0.006

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 19.4 19.5 16.5 18.467

lb/mmBtuO2 4.69E-03 4.60E-03 3.94E-03 0.004

Friday, February 04, 2011 Page 19 of 34
JEA, Northside Station, Unit 2

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 0 mmBtu/hr 18000

1 Steam Flow 0 Klb/hr 1000

1 Gross Mwe 0 Mwe 124

Friday, February 04, 2011 Page 20 of 34
JEA, Northside Station, Unit 2

Sampling / Stack Data Results Detail

Location Unit 2 Stack - Method 10

Average

Run Number 1 2 3

Test Date 5/27/2010 5/27/2010 5/28/2010

Run Start Time 4:00:00 PM 6:30:00 PM 7:35:00 AM

Run Finish Time 6:11:00 PM 8:38:00 PM 9:45:00 AM

Carbon Dioxide, % 14.6 14.7 14.6 14.633

Oxygen, % 5.1 5 4.9 5.000

Fuel Factor 1.08 1.08 1.1

Dry Volumetric Flow Rate, dry scfm 661205 672539 661789 665,177.667

F-Factor, dscfm/MMBtu @ %O2 9966 9966 9974 9,968.667

Moisture, % 11.02 11.49 10.31 10.940

Analyzer Make Horiba Horiba Horiba

Analyzer Model VIA-510 VIA-510 VIA-510

Analyzer Serial Number 570124044 570124044 570124044 570,124,044

.000

Operating Range 90 90 90 90.000

Operating Units ppm ppm ppm

No. Readings/Avg. 120 120 120 120.000

Calibration Set 19 19 20 19.333

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.33 0.39 0.29 0.337

Calibration Pre Zero Cylinder Bias -0.04 0.02 0.09 0.023

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC239299 CC239299 CC239299

Calibration Pre High Cylinder Instrument Response 44.99 45.58 44.25 44.940

Calibration Pre High Cylinder Bias -0.44 0.21 -0.78 -0.337

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.39 0.52 0.39 0.433

Calibration Post Zero Cylinder Bias 0.02 0.17 0.2 0.130

Calibration Post Zero Cylinder Drift 0.06 0.15 0.11 0.107

Calibration Post High Cylinder ID CC239299 CC239299 CC239299

Calibration Post High Cylinder Instrument Response 45.58 46.24 44.68 45.500

Calibration Post High Cylinder Bias 0.21 0.94 -0.3 0.283

Calibration Post High Cylinder Drift 0.65 0.73 0.48 0.620

Cavg 20.91 23.42 22.95 22.427

Cavg Units ppmvd ppmvd ppmvd

Cgas 20.7215 22.8867 23.2121 22.273

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

Friday, February 04, 2011 Page 21 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 23

Average

Run Number 1 2 3

Test Date 6/2/2010 6/3/2010 6/4/2010

Run Start Time 7:45:00 AM 8:10:00 AM 7:20:00 AM

Run Finish Time 4:00:00 PM 4:25:00 PM 3:30:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.185 0.185 0.185 0.185

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.014 1.014 1.014 1.014

Barometric Pressure, inches of Mercury 29.71 29.66 29.7 29.690

Average Orifice Meter Differential, inches H2O 1.42 1.43 1.44 1.430

Dry Gas Meter Volume Sampled, cubic feet 326.869 326.720 317.913 323.834

Average Dry Gas Meter Temperature, °F 100.35 101.69 100.81 100.950

Dry Gas Meter Volume Sampled, dscf 311.208 309.811 302.346 307.788

Total Moisture Liquid collected, g 797.8 790.5 799.5 795.933

Volume of Water Vapor, standard cubic feet 37.55 37.21 37.63 37.463

Moisture Content of Stack Gas, % 10.77 10.72 11.07 10.853

Moisture Saturation at Stack Gas Temperature, % 77.56 78.14 77.92 77.873

Dry Mole Fraction 0.8923 0.8928 0.8893 0.891

Carbon Dioxide, % 15.6 15.2 15.7 15.500

Oxygen, % 4.3 4.6 4.8 4.567

Carbon Monoxide & Nitrogen, % 80.1 80.2 79.5 79.933

Fuel Factor 1.06 1.07 1.03

Dry Molecular Weight, lb/lb-Mole 30.67 30.62 30.70 30.663

Wet Molecular weight, lb/lb-Mole 29.31 29.27 29.29 29.290

Flue Gas Static Pressure, inches of H2O -1.1 -0.96 -1.2 -1.087

Absolute Flue Gas Pressure, inches of Mercury 29.63 29.59 29.61 29.610

Average Stack Gas Temperature, °F 199.04 199.33 199.23 199.200

Average Velocity Head, inches of H2O 1.5464024629

1405

1.538353335

67357

1.560666862

02415

1.548

Average Stack Gas Velocity, feet/second 77.79 77.71 78.21 77.903

Stack Cross-Sectional Area, square feet 176.715 176.715 176.715 176.715

Dry Volumetric Flow Rate, dry scfm 583,917.6 582,599.6 584,533.0 583,683.400

Actual Wet Volumetric Flue Gas Flow Rate, acfm 824,799.6 823,951.4 829,252.8 826,001.267

Percent Isokinetic of Sampling Rate, % 105.1 104.9 102.0 104.000

Percent Excess Air, % 25.5 27.8 29.7 27.667

F-Factor, dscfm/MMBtu @ %O2 8922 8586 8626 8,711.333

Round Duct Diameter, inches 180 180 180

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

Friday, February 04, 2011 Page 22 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 25A

Average

Run Number 1 2 3

Test Date 5/27/2010 5/27/2010 5/28/2010

Run Start Time 4:00:00 PM 6:30:00 PM 7:35:00 AM

Run Finish Time 6:11:00 PM 8:38:00 PM 9:45:00 AM

Carbon Dioxide, % 14.6 14.7 14.6 14.633

Oxygen, % 5.1 5 4.9 5.000

Fuel Factor 1.08 1.08 1.1

Dry Volumetric Flow Rate, dry scfm 661205 672539 661789 665,177.667

F-Factor, dscfm/MMBtu @ %O2 9966 9966 9974 9,968.667

Moisture, % 11.02 11.49 10.31 10.940

Analyzer Make Thermo Env. Thermo Env. Thermo Env.

Analyzer Model 51 51 51 51.000

Analyzer Serial Number 4723 4723 4723 4,723.000

Operating Range 9.03 9.03 9.03 9.030

Operating Units ppm ppm ppm

No. Readings/Avg. 120 120 120 120.000

Calibration Set 21 21 22 21.333

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.17 0.19 0.15 0.170

Calibration Pre Zero Cylinder Bias 0.55 0.78 -0.33 0.333

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC243371 CC243371 CC243371

Calibration Pre High Cylinder Instrument Response 5.45 5.31 5.51 5.423

Calibration Pre High Cylinder Bias 0.66 -0.89 0.78 0.183

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.19 0.12 0.17 0.160

Calibration Post Zero Cylinder Bias 0.78 0 -0.11 0.223

Calibration Post Zero Cylinder Drift 0.23 0.78 0.22 0.410

Calibration Post High Cylinder ID CC243371 CC243371 CC243371

Calibration Post High Cylinder Instrument Response 5.31 5.24 5.55 5.367

Calibration Post High Cylinder Bias -0.89 -1.66 1.22 -0.443

Calibration Post High Cylinder Drift 1.55 0.77 0.44 0.920

Cavg 0.52 0.53 0.5 0.517

Cavg Units ppmvw ppmvw ppmvw

Cgas 0.3909 0.4402 0.3756 0.402

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0.3478461538

46154

0.389648437

5

0.336834264

43203

0.358

Cgasw Units ppmvw ppmvw ppmvw

Friday, February 04, 2011 Page 23 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Friday, February 04, 2011 Page 24 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 29

Average

Run Number

Test Date

Run Start Time

Run Finish Time Unit 2 Stack Unit 2 Stack Unit 2 Stack

Net Traversing Points 5/25/2010 5/26/2010 5/27/2010

Net Run Time, minutes Method 29 Method 29 Method 29

Nozzle Diameter, inches 1 2 3 2.000

Pitot Tube Coefficient 8:30:00 AM 8:00:00 AM 9:10:00 AM

Dry Gas Meter Calibration Factor 1:34:00 PM 12:09:00 PM 1:19:00 PM

Barometric Pressure, inches of Mercury 49 48 48 48.333

Average Orifice Meter Differential, inches H2O 240 240 240 240.000

Dry Gas Meter Volume Sampled, cubic feet 0.185 0.185 0.185 0.185

Average Dry Gas Meter Temperature, °F 0.84 0.84 0.84 0.840

Dry Gas Meter Volume Sampled, dscf 1.01 1.01 1.01 1.010

Total Moisture Liquid collected, g 29.75 29.66 29.6 29.670

Volume of Water Vapor, standard cubic feet 1.44 1.38 1.39 1.403

Moisture Content of Stack Gas, % 161.763 158.759 159.100 159.874

Moisture Saturation at Stack Gas Temperature, % 99.33 95.10 98.73 97.720

Dry Mole Fraction 153.899 151.710 150.748 152.119

Carbon Dioxide, % 395.5 387.8 399 394.100

Oxygen, % 18.62 18.25 18.78 18.550

Carbon Monoxide & Nitrogen, % 10.79 10.74 11.08 10.870

Fuel Factor 81.86 78.80 76.68

Dry Molecular Weight, lb/lb-Mole 0.8921 0.8926 0.8892 0.891

Wet Molecular weight, lb/lb-Mole 15.1 15.4 15.3 15.267

Flue Gas Static Pressure, inches of H2O 4.3 4.6 4.8 4.567

Absolute Flue Gas Pressure, inches of Mercury 80.6 80 79.9 80.167

Average Stack Gas Temperature, °F 1.10 1.06 1.05 1.070

Average Velocity Head, inches of H2O 30.59 30.65 30.64 30.627

Average Stack Gas Velocity, feet/second 29.23 29.29 29.24 29.253

Stack Cross-Sectional Area, square feet 1.6230302291

9554

1.574851465

59514

1.554950964

01749

1.584

Dry Volumetric Flow Rate, dry scfm 79.91 78.66 78.19 78.920

Actual Wet Volumetric Flue Gas Flow Rate, acfm 180 180 180 180.000

Percent Isokinetic of Sampling Rate, % 0 0 0 0.000

Percent Excess Air, % 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 176.715 176.715 176.715 176.715

Round Duct Diameter, inches -1.1 -1.3 -0.96

Rectangular Duct Width, inches 29.67 29.56 29.53

Rectangular Duct Length, inches 201.71 199.69 198.33

Fw 847,277.7 834,024.1 829,040.8 836,780.867

Fc 598,083.1 588,670.6 583,535.7 590,096.467

Friday, February 04, 2011 Page 25 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/26/2010

Run Start Time 2:40:00 PM 1:25:00 PM 4:55:00 PM

Run Finish Time 5:49:00 PM 4:35:00 PM 8:05:00 PM

Carbon Dioxide, % 15.3 15.6 15.7 15.533

Oxygen, % 4.3 4.5 4.4 4.400

Fuel Factor 1.08 1.05 1.05

Dry Volumetric Flow Rate, dry scfm 665866 649441 667962 661,089.667

F-Factor, dscfm/MMBtu @ %O2 9907 9912 9966 9,928.333

Moisture, % 11.13 11.15 10.91 11.063

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 18 18 18 18.000

Operating Units % % %

No. Readings/Avg. 180 180 180 180.000

Calibration Set 5 6 6 5.667

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.11 0.15 0.15 0.137

Calibration Pre Zero Cylinder Bias -0.06 0.11 0.11 0.053

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC275906_C

O2

CC275906_

CO2

CC275906_C

O2

Calibration Pre High Cylinder Instrument Response 9.11 9.06 8.91 9.027

Calibration Pre High Cylinder Bias 0.72 0.56 -0.28 0.333

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.12 0.15 0.1 0.123

Calibration Post Zero Cylinder Bias 0 0.11 -0.17 -0.020

Calibration Post Zero Cylinder Drift 0.06 0 0.28 0.113

Calibration Post High Cylinder ID CC275906_C

O2

CC275906_

CO2

CC275906_C

O2

Calibration Post High Cylinder Instrument Response 8.95 8.91 9.03 8.963

Calibration Post High Cylinder Bias -0.17 -0.28 0.39 -0.020

Calibration Post High Cylinder Drift 0.89 0.84 0.67 0.800

Cavg 15.21 15.4 15.55 15.387

Cavg Units %vd %vd %vd

Cgas 15.2559 15.5521 15.7127 15.507

Cgas Units %vd %vd %vd

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

Friday, February 04, 2011 Page 26 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 3A CO2 3

Average

Run Number 4 5 6

Test Date 5/25/2010 5/26/2010 5/27/2010

Run Start Time 8:30:00 AM 8:00:00 AM 9:10:00 AM

Run Finish Time 3:24:00 PM 2:12:00 PM 3:25:00 PM

Carbon Dioxide, % 15.1 15.4 15.3 15.267

Oxygen, % 4.3 4.6 4.8 4.567

Fuel Factor 1.1 1.06 1.05

Dry Volumetric Flow Rate, dry scfm 670275 659440 656412 662,042.333

F-Factor, dscfm/MMBtu @ %O2 9906 9913 9966 9,928.333

Moisture, % 10.78 10.74 11.08 10.867

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 18 18 18 18.000

Operating Units % % %

No. Readings/Avg. 360 360 360 360.000

Calibration Set 9 10 11 10.000

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.15 0.11 0.13 0.130

Calibration Pre Zero Cylinder Bias 0.17 -0.11 0 0.020

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC275906_C

O2

CC275906_

CO2

CC275906_C

O2

Calibration Pre High Cylinder Instrument Response 8.96 8.9 8.99 8.950

Calibration Pre High Cylinder Bias -0.11 -0.33 -0.44 -0.293

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.1 0.14 0.18 0.140

Calibration Post Zero Cylinder Bias -0.11 0.06 0.28 0.077

Calibration Post Zero Cylinder Drift 0.28 0.17 0.28 0.243

Calibration Post High Cylinder ID CC275906_C

O2

CC275906_

CO2

CC275906_C

O2

Calibration Post High Cylinder Instrument Response 8.93 8.92 8.87 8.907

Calibration Post High Cylinder Bias -0.28 -0.22 -1.11 -0.537

Calibration Post High Cylinder Drift 0.17 0.11 0.67 0.317

Cavg 14.91 15.18 15.02 15.037

Cavg Units %vd %vd %vd

Cgas 15.1035 15.4406 15.2631 15.269

Cgas Units %vd %vd %vd

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

Friday, February 04, 2011 Page 27 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 3A CO2 3 6

Average

Run Number 7 8 9

Test Date 5/27/2010 5/27/2010 5/28/2010

Run Start Time 4:00:00 PM 6:30:00 PM 7:35:00 AM

Run Finish Time 6:11:00 PM 8:38:00 PM 9:45:00 AM

Carbon Dioxide, % 14.6 14.7 14.6 14.633

Oxygen, % 5.1 5 4.9 5.000

Fuel Factor 1.08 1.08 1.1

Dry Volumetric Flow Rate, dry scfm 661205 672539 661789 665,177.667

F-Factor, dscfm/MMBtu @ %O2 9966 9966 9974 9,968.667

Moisture, % 11.02 11.49 10.31 10.940

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 18 18 18 18.000

Operating Units % % %

No. Readings/Avg. 120 120 120 120.000

Calibration Set 16 15 16 15.667

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.12 0.14 0.14 0.133

Calibration Pre Zero Cylinder Bias -0.12 -0.07 -0.1 -0.097

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC275906_C

O2

CC275906_

CO2

CC275906_C

O2

Calibration Pre High Cylinder Instrument Response 9.12 9.17 9 9.097

Calibration Pre High Cylinder Bias -0.06 0.09 -0.19 -0.053

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.14 0.11 0.18 0.143

Calibration Post Zero Cylinder Bias -0.1 -0.1 -0.06 -0.087

Calibration Post Zero Cylinder Drift 0.02 0.03 0.04 0.030

Calibration Post High Cylinder ID CC275906_C

O2

CC275906_

CO2

CC275906_C

O2

Calibration Post High Cylinder Instrument Response 9.17 9.1 9.24 9.170

Calibration Post High Cylinder Bias 0 0.01 0.08 0.030

Calibration Post High Cylinder Drift 0.06 0.08 0.27 0.137

Cavg 14.78 14.8 14.68 14.753

Cavg Units %vd %vd %vd

Cgas 14.6419 14.675 14.601 14.639

Cgas Units %vd %vd %vd

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

Friday, February 04, 2011 Page 28 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/26/2010

Run Start Time 2:40:00 PM 1:25:00 PM 4:55:00 PM

Run Finish Time 5:49:00 PM 4:35:00 PM 8:05:00 PM

Carbon Dioxide, % 15.3 15.6 15.7 15.533

Oxygen, % 4.3 4.5 4.4 4.400

Fuel Factor 1.08 1.05 1.05

Dry Volumetric Flow Rate, dry scfm 665866 649441 667962 661,089.667

F-Factor, dscfm/MMBtu @ %O2 9907 9912 9966 9,928.333

Moisture, % 11.13 11.15 10.91 11.063

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 22.4 22.4 22.4 22.400

Operating Units % % %

No. Readings/Avg. 180 180 180 180.000

Calibration Set 7 8 8 7.667

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.18 0.12 0.18 0.160

Calibration Pre Zero Cylinder Bias 0.22 -0.22 0.04 0.013

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC275906 CC275906 CC275906

Calibration Pre High Cylinder Instrument Response 11.05 10.95 10.91 10.970

Calibration Pre High Cylinder Bias -0.09 -0.76 -0.94 -0.597

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.1 0.18 0.1 0.127

Calibration Post Zero Cylinder Bias -0.13 0.04 -0.31 -0.133

Calibration Post Zero Cylinder Drift 0.35 0.26 0.35 0.320

Calibration Post High Cylinder ID CC275906 CC275906 CC275906

Calibration Post High Cylinder Instrument Response 11.11 10.91 10.99 11.003

Calibration Post High Cylinder Bias 0.18 -0.94 -0.58 -0.447

Calibration Post High Cylinder Drift 0.27 0.18 0.36 0.270

Cavg 4.42 4.59 4.45 4.487

Cavg Units %vd %vd %vd

Cgas 4.3035 4.5306 4.3858 4.407

Cgas Units %vd %vd %vd

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

Friday, February 04, 2011 Page 29 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 3A O2 3

Average

Run Number 4 5 6

Test Date 5/25/2010 5/26/2010 5/27/2010

Run Start Time 8:30:00 AM 8:00:00 AM 9:10:00 AM

Run Finish Time 3:24:00 PM 2:12:00 PM 3:25:00 PM

Carbon Dioxide, % 15.1 15.4 15.3 15.267

Oxygen, % 4.3 4.6 4.8 4.567

Fuel Factor 1.1 1.06 1.05

Dry Volumetric Flow Rate, dry scfm 670275 659440 656412 662,042.333

F-Factor, dscfm/MMBtu @ %O2 9906 9913 9966 9,928.333

Moisture, % 10.78 10.74 11.08 10.867

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 22.4 22.4 22.4 22.400

Operating Units % % %

No. Readings/Avg. 360 360 360 360.000

Calibration Set 12 13 14 13.000

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.1 0.16 0.08 0.113

Calibration Pre Zero Cylinder Bias -0.13 -0.04 -0.31 -0.160

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC275906 CC275906 CC275906

Calibration Pre High Cylinder Instrument Response 11.11 11.19 11 11.100

Calibration Pre High Cylinder Bias 0.18 0.31 0.18 0.223

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.14 0.19 0.13 0.153

Calibration Post Zero Cylinder Bias 0.04 0.09 -0.09 0.013

Calibration Post Zero Cylinder Drift 0.17 0.13 0.22 0.173

Calibration Post High Cylinder ID CC275906 CC275906 CC275906

Calibration Post High Cylinder Instrument Response 11.08 11.02 10.93 11.010

Calibration Post High Cylinder Bias 0.04 -0.45 -0.13 -0.180

Calibration Post High Cylinder Drift 0.14 0.76 0.31 0.403

Cavg 4.39 4.75 4.89 4.677

Cavg Units %vd %vd %vd

Cgas 4.2797 4.6043 4.8467 4.577

Cgas Units %vd %vd %vd

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

Friday, February 04, 2011 Page 30 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 3A O2 3 6

Average

Run Number 7 8 9

Test Date 5/27/2010 5/27/2010 5/28/2010

Run Start Time 4:00:00 PM 6:30:00 PM 7:35:00 AM

Run Finish Time 6:11:00 PM 8:38:00 PM 9:45:00 AM

Carbon Dioxide, % 14.6 14.7 14.6 14.633

Oxygen, % 5.1 5 4.9 5.000

Fuel Factor 1.08 1.08 1.1

Dry Volumetric Flow Rate, dry scfm 661205 672539 661789 665,177.667

F-Factor, dscfm/MMBtu @ %O2 9966 9966 9974 9,968.667

Moisture, % 11.02 11.49 10.31 10.940

Analyzer Make Calif. 

Analytical

Calif. 

Analytical

Calif. 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 22.4 22.4 22.4 22.400

Operating Units % % %

No. Readings/Avg. 120 120 120 120.000

Calibration Set 17 17 18 17.333

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.17 0.12 0.17 0.153

Calibration Pre Zero Cylinder Bias -0.36 -0.58 0.09 -0.283

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC275906 CC275906 CC275906

Calibration Pre High Cylinder Instrument Response 10.93 10.97 11 10.967

Calibration Pre High Cylinder Bias -0.18 0 -0.36 -0.180

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.12 0.1 0.18 0.133

Calibration Post Zero Cylinder Bias -0.58 -0.67 0.13 -0.373

Calibration Post Zero Cylinder Drift 0.22 9.000000000

00001E-02

0.04 0.117

Calibration Post High Cylinder ID CC275906 CC275906 CC275906

Calibration Post High Cylinder Instrument Response 10.97 10.81 11.18 10.987

Calibration Post High Cylinder Bias 0 -0.71 0.45 -0.087

Calibration Post High Cylinder Drift 0.18 0.71 0.81 0.567

Cavg 5.11 5.05 4.99 5.050

Cavg Units %vd %vd %vd

Cgas 5.0546 5.0408 4.8525 4.983

Cgas Units %vd %vd %vd

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

Friday, February 04, 2011 Page 31 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 6C

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/26/2010

Run Start Time 2:40:00 PM 1:25:00 PM 4:55:00 PM

Run Finish Time 5:49:00 PM 4:35:00 PM 8:05:00 PM

Carbon Dioxide, % 15.3 15.6 15.7 15.533

Oxygen, % 4.3 4.5 4.4 4.400

Fuel Factor 1.08 1.05 1.05

Dry Volumetric Flow Rate, dry scfm 665866 649441 667962 661,089.667

F-Factor, dscfm/MMBtu @ %O2 9907 9912 9966 9,928.333

Moisture, % 11.13 11.15 10.91 11.063

Analyzer Make Western 

Research

Western 

Research

Western 

Research

Analyzer Model 721M 721M 721M

Analyzer Serial Number 93-721M8062-693-721M8062-693-721M8062-6

Operating Range 100 100 100 100.000

Operating Units ppm ppm ppm

No. Readings/Avg. 180 180 180 180.000

Calibration Set 3 4 4 3.667

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.32 0.57 0.69 0.527

Calibration Pre Zero Cylinder Bias -0.2 0.24 0.36 0.133

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0002329 EB0002329 EB0002329

Calibration Pre High Cylinder Instrument Response 50.51 50.89 50.24 50.547

Calibration Pre High Cylinder Bias -0.11 0.38 -0.27 0.000

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.39 0.69 0.41 0.497

Calibration Post Zero Cylinder Bias -0.13 0.36 0.08 0.103

Calibration Post Zero Cylinder Drift 0.07 0.12 0.28 0.157

Calibration Post High Cylinder ID EB0002329 EB0002329 EB0002329

Calibration Post High Cylinder Instrument Response 50.44 50.24 50.42 50.367

Calibration Post High Cylinder Bias -0.18 -0.27 -0.09 -0.180

Calibration Post High Cylinder Drift 0.07 0.65 0.18 0.300

Cavg 78.28 84.09 81.23 81.200

Cavg Units ppmvd ppmvd ppmvd

Cgas 78.8268 84.7386 82.1711 81.912

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

Friday, February 04, 2011 Page 32 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - Method 7E

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/26/2010

Run Start Time 2:40:00 PM 1:25:00 PM 4:55:00 PM

Run Finish Time 5:49:00 PM 4:35:00 PM 8:05:00 PM

Carbon Dioxide, % 15.3 15.6 15.7 15.533

Oxygen, % 4.3 4.5 4.4 4.400

Fuel Factor 1.08 1.05 1.05

Dry Volumetric Flow Rate, dry scfm 665866 649441 667962 661,089.667

F-Factor, dscfm/MMBtu @ %O2 9907 9912 9966 9,928.333

Moisture, % 11.13 11.15 10.91 11.063

Analyzer Make Thermo Env. Thermo Env. Thermo Env.

Analyzer Model 42C 42C 42C

Analyzer Serial Number 42CHL_67507

_357

42CHL_675

07_357

42CHL_6750

7_357

Operating Range 125 125 125 125.000

Operating Units ppm ppm ppm

No. Readings/Avg. 180 180 180 180.000

Calibration Set 1 2 2 1.667

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.52 0.45 0.39 0.453

Calibration Pre Zero Cylinder Bias 0.09 -0.1 -0.15 -0.053

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC308924 CC308924 CC308924

Calibration Pre High Cylinder Instrument Response 50.55 50.33 50.68 50.520

Calibration Pre High Cylinder Bias -0.14 -0.48 -0.2 -0.273

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.69 0.39 0.48 0.520

Calibration Post Zero Cylinder Bias 0.22 -0.15 -0.08 -0.003

Calibration Post Zero Cylinder Drift 0.13 0.05 0.07 0.083

Calibration Post High Cylinder ID CC308924 CC308924 CC308924

Calibration Post High Cylinder Instrument Response 50.21 50.68 50.75 50.547

Calibration Post High Cylinder Bias -0.42 -0.2 -0.14 -0.253

Calibration Post High Cylinder Drift 0.28 0.28 0.06 0.207

Cavg 76.52 69.9 65.62 70.680

Cavg Units ppmvd ppmvd ppmvd

Cgas 77.1733 70.1944 65.5999 70.989

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

Friday, February 04, 2011 Page 33 of 34
JEA, Northside Station, Unit 2

Location Unit 2 Stack - OTM - 27/28

Average

Run Number 1 2 3

Test Date 5/25/2010 5/26/2010 5/27/2010

Run Start Time 8:30:00 AM 8:00:00 AM 9:10:00 AM

Run Finish Time 3:24:00 PM 2:12:00 PM 2:42:18 PM

Net Traversing Points 13 13 13

Net Run Time, minutes 359.8 360 360.1

Nozzle Diameter, inches 0.138 0.138 0.138 0.138

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.014 1.014 1.014 1.014

Barometric Pressure, inches of Mercury 29.75 29.66 29.6 29.670

Average Orifice Meter Differential, inches H2O 0.38 0.38 0.38 0.380

Dry Gas Meter Volume Sampled, cubic feet 118.201 122.980 125.057 122.079

Average Dry Gas Meter Temperature, °F 93.92 90.25 95.17 93.113

Dry Gas Meter Volume Sampled, dscf 113.705 118.731 119.425 117.287

Total Moisture Liquid collected, g 354.9 304.6 329.4 329.633

Volume of Water Vapor, standard cubic feet 16.71 14.34 15.50 15.517

Moisture Content of Stack Gas, % 12.81 10.78 11.49 11.693

Moisture Saturation at Stack Gas Temperature, % 81.75 79.37 77.89 79.670

Dry Mole Fraction 0.8719 0.8922 0.8851 0.883

Carbon Dioxide, % 15.1 15.4 15.3 15.267

Oxygen, % 4.3 4.6 4.8 4.567

Carbon Monoxide & Nitrogen, % 80.6 80 79.9 80.167

Fuel Factor 1.10 1.06 1.05

Dry Molecular Weight, lb/lb-Mole 30.59 30.65 30.64 30.627

Wet Molecular weight, lb/lb-Mole 28.98 29.29 29.19 29.153

Flue Gas Static Pressure, inches of H2O -1.6 -1.7 -1.7 -1.667

Absolute Flue Gas Pressure, inches of Mercury 29.63 29.54 29.48 29.550

Average Stack Gas Temperature, °F 201.58 200.00 199.00 200.193

Average Velocity Head, inches of H2O 1.7676476233

927

1.818126744

17175

1.862124744

77762

1.816

Average Stack Gas Velocity, feet/second 83.80 84.57 85.76 84.710

Stack Cross-Sectional Area, square feet 176.715 176.715 176.715 176.715

Dry Volumetric Flow Rate, dry scfm 612,289.7 631,890.9 635,354.6 626,511.733

Actual Wet Volumetric Flue Gas Flow Rate, acfm 888,523.0 896,687.3 909,304.7 898,171.667

Percent Isokinetic of Sampling Rate, % 87.8 88.8 88.8 88.467

Percent Excess Air, % 25.3 27.8 29.5 27.533

F-Factor, dscfm/MMBtu @ %O2 9906 9913 9966 9,928.333

Round Duct Diameter, inches 180 180 180

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

Friday, February 04, 2011 Page 34 of 34