Name: Kevin Holbrooks

Title: Director Environmental Compliance

Company: Jacksonville Electric Authority

Sign Date:

Name: Carl Vineyard

Title: MACT Utility Program Manager

Company: Grace Consulting, Inc.

Sign Date: 7/6/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Jacksonville Electric Authority

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 67
Jacksonville Electric Authority

Facility Information:

Northside Station, Unit 3

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@aol.com

Air Permit Number:

667

Permitted Source ID/Name:

JEA Northside 3

Permitted Maximum Process Rate: Max. Normal Operation Process Rate:

18440

Target Process Test Rate

18440

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

Normal Firing 

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

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

Stack 468.71 0 0 13 3817.5 2442.5 4 48

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Carbon Monoxide Method 10 3 120 0

Stack 2,3,7,8-TCDD Method 23 3 480 0

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

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

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

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

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

Friday, February 04, 2011 Page 2 of 67
Jacksonville Electric Authority

Stack OCDD Method 23 3 480 0

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

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

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

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

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

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

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

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

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

Stack OCDF Method 23 3 480 0

Stack Total Dioxins Method 23 3 480 0

Stack Total Furans Method 23 3 480 0

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

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

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

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

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

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

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)

Stack Method 23 3 480 0

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

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

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

(PCB189)

Stack Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Method 25A 3 120 0

Stack Hydrogen Fluoride Method 26A 3 180 0

Stack Hydrogen Chloride Method 26A 3 180 0

Stack Filterable Particulate OTM - 27/28 3 180 0

Stack Filterable PM2.5 OTM - 27/28 3 180 0

Inorganic (Aqueous) 

Condensible Part.

Stack OTM - 27/28 3 180 0

Organic Condensible 

Particulate

Stack OTM - 27/28 3 180 0

Stack Total Particulate OTM - 27/28 3 180 0

Stack Total PM2.5 OTM - 27/28 3 180 0

Stack Chromium Method 29 3 240 0

Stack Antimony Method 29 3 240 0

Stack Arsenic Method 29 3 240 0

Stack Cadmium Method 29 3 240 0

Stack Cobalt Method 29 3 240 0

Stack Lead Method 29 3 240 0

Stack Manganese Method 29 3 240 0

Stack Nickel Method 29 3 240 0

Stack Selenium Method 29 3 240 0

Stack Filterable Particulate Method 29 3 240 0

Stack Beryllium Method 29 3 240 0

Stack Co2 Method 3A CO2 3 120 0

Stack Co2 Method 3A CO2 3 240 0

Stack O2 Method 3A O2 3 240 0

Stack O2 Method 3A O2 3 180 0

Friday, February 04, 2011 Page 3 of 67
Jacksonville Electric Authority

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 6 NaOH and an additional impinger for one hour per the clarification 

given by the USEPA in FAQ Number 10. You may use a modified Method 26A or Method 26 sampling train. The 

analysis is then with ion chromatography.

Stack O2 Method 3A O2 3 120 0

Stack Co2 Method 3A CO2 3 180 0

Stack Sulfur Dioxide Method 6C 3 180 0

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

Friday, February 04, 2011 Page 4 of 67
Jacksonville Electric Authority

Sampling / Stack Data Results Summary

Location Stack - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack - Method 23

Average

Run Number 1 2 3

Test Date 5/8/2010 5/9/2010 5/10/2010

Run Start Time 8:05:00 AM 7:45:00 

AM

7:40:00 AM

Run Finish Time 4:31:00 PM 4:06:00 PM 4:00:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 346.762 337.607 333.109 339.159

Moisture Content of Stack Gas, % 6.26 5.84 3.34 5.147

Moisture Saturation at Stack Gas Temperature, % 82.72 79.65 82.30 81.557

Carbon Dioxide, % 6 6.1 5.8 5.967

Oxygen, % 13.3 13.2 13.6 13.367

Average Stack Gas Temperature, °F 202.46 200.63 202.31 201.800

Dry Volumetric Flow Rate, dry scfm 1,623,696.2 1,585,879.7 1,598,354.2 1,602,643.36

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,180,517.1 2,114,375.5 2,076,991.1 2,123,961.23

3

Percent Isokinetic of Sampling Rate, % 99.1 98.8 96.7 98.200

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

Friday, February 04, 2011 Page 5 of 67
Jacksonville Electric Authority

Location Stack - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location 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 67
Jacksonville Electric Authority

Location Stack - Method 29

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

Location Stack - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Friday, February 04, 2011 Page 7 of 67
Jacksonville Electric Authority

Location Stack - Method 3A CO2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Friday, February 04, 2011 Page 8 of 67
Jacksonville Electric Authority

Location Stack - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack - Method 3A O2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Friday, February 04, 2011 Page 9 of 67
Jacksonville Electric Authority

Location Stack - Method 3A O2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Friday, February 04, 2011 Page 10 of 67
Jacksonville Electric Authority

Location Stack - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack - OTM - 27/28

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 11 of 67
Jacksonville Electric Authority

Emissions Summary

Location: Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.62E-03 1.64E-03 1.49E-03 0.002

ppm 8.91E-01 9.18E-01 8.33E-01 0.881

ppm@7%O2 1.61E+00 1.64E+00 1.48E+00 1.577

Location: Stack - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.000000029 0.000000033 0.000000028 0.000

lb/mmBtuO2 4.66E-12 5.38E-12 4.88E-12 0.000

ng/dscm 2.95E-03 3.45E-03 2.97E-03 0.003

ng/dscm@7%O2 5.40E-03 6.23E-03 5.66E-03 0.006

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

Average

RunNumber 1 2 3

Mass_mg 0.000000022 0.000000018 0.00000003 0.000

lb/mmBtuO2 3.53E-12 2.93E-12 5.22E-12 0.000

ng/dscm 2.24E-03 1.88E-03 3.18E-03 0.002

ng/dscm@7%O2 4.10E-03 3.39E-03 6.06E-03 0.005

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000072 0.0000000042 0.000000007 0.000

lb/mmBtuO2 1.16E-12 6.84E-13 1.22E-12 0.000

ng/dscm 7.33E-04 4.39E-04 7.42E-04 0.001

ng/dscm@7%O2 1.34E-03 7.92E-04 1.41E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000023 0.0000000037 0.0000000043 0.000

lb/mmBtuO2 3.70E-13 6.03E-13 7.49E-13 0.000

ng/dscm 2.34E-04 3.87E-04 4.56E-04 0.000

ng/dscm@7%O2 4.28E-04 6.99E-04 8.68E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000016 0.000000016 0.000000031 0.000

lb/mmBtuO2 2.57E-12 2.61E-12 5.40E-12 0.000

ng/dscm 1.63E-03 1.67E-03 3.29E-03 0.002

ng/dscm@7%O2 2.98E-03 3.01E-03 6.26E-03 0.004

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

Average

Friday, February 04, 2011 Page 12 of 67
Jacksonville Electric Authority

RunNumber 1 2 3

Mass_mg 0.0000000046 0.0000000049 0.0000000042 0.000

lb/mmBtuO2 7.39E-13 7.98E-13 7.31E-13 0.000

ng/dscm 4.69E-04 5.13E-04 4.45E-04 0.000

ng/dscm@7%O2 8.58E-04 9.26E-04 8.47E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000015 0.000000018 0.000000022 0.000

lb/mmBtuO2 2.41E-12 2.93E-12 3.83E-12 0.000

ng/dscm 1.53E-03 1.88E-03 2.33E-03 0.002

ng/dscm@7%O2 2.80E-03 3.39E-03 4.44E-03 0.004

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000039 0.0000000044 0.0000000042 0.000

lb/mmBtuO2 6.27E-13 7.17E-13 7.31E-13 0.000

ng/dscm 3.97E-04 4.60E-04 4.45E-04 0.000

ng/dscm@7%O2 7.26E-04 8.30E-04 8.47E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000025 0.0000000047 0.0000000038 0.000

lb/mmBtuO2 4.02E-13 7.66E-13 6.62E-13 0.000

ng/dscm 2.55E-04 4.92E-04 4.03E-04 0.000

ng/dscm@7%O2 4.66E-04 8.88E-04 7.67E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000063 0.0000000085 0.0000000093 0.000

lb/mmBtuO2 1.01E-12 1.38E-12 1.62E-12 0.000

ng/dscm 6.42E-04 8.89E-04 9.86E-04 0.001

ng/dscm@7%O2 1.17E-03 1.60E-03 1.88E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.000000028 0.000000036 0.000000041 0.000

lb/mmBtuO2 4.50E-12 5.86E-12 7.14E-12 0.000

ng/dscm 2.85E-03 3.77E-03 4.35E-03 0.004

ng/dscm@7%O2 5.21E-03 6.81E-03 8.28E-03 0.007

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

Average

RunNumber 1 2 3

Mass_mg 0.000000031 0.000000041 0.0000000364 0.000

lb/mmBtuO2 4.98E-12 6.68E-12 6.34E-12 0.000

ng/dscm 3.16E-03 4.29E-03 3.86E-03 0.004

ng/dscm@7%O2 5.78E-03 7.74E-03 7.35E-03 0.007

Friday, February 04, 2011 Page 13 of 67
Jacksonville Electric Authority

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

Average

RunNumber 1 2 3

Mass_mg 0.0000008712 0.000001494 0.000000962 0.000

lb/mmBtuO2 1.40E-10 2.43E-10 1.68E-10 0.000

ng/dscm 8.87E-02 1.56E-01 1.02E-01 0.116

ng/dscm@7%O2 1.62E-01 2.82E-01 1.94E-01 0.213

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

Average

RunNumber 1 2 3

Mass_mg 0.000002137 0.00000639 0.00000385 0.000

lb/mmBtuO2 3.43E-10 1.04E-09 6.70E-10 0.000

ng/dscm 2.18E-01 6.69E-01 4.08E-01 0.432

ng/dscm@7%O2 3.99E-01 1.21E+00 7.77E-01 0.795

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

Average

RunNumber 1 2 3

Mass_mg 0.0000001163 0.000000357 0.000000186 0.000

lb/mmBtuO2 1.87E-11 5.82E-11 3.24E-11 0.000

ng/dscm 1.18E-02 3.73E-02 1.97E-02 0.023

ng/dscm@7%O2 2.16E-02 6.73E-02 3.75E-02 0.042

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

Average

RunNumber 1 2 3

Mass_mg 0.0000001085 0.00000054 0.000000275 0.000

lb/mmBtuO2 1.74E-11 8.80E-11 4.79E-11 0.000

ng/dscm 1.11E-02 5.65E-02 2.92E-02 0.032

ng/dscm@7%O2 2.03E-02 1.02E-01 5.56E-02 0.059

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

Average

RunNumber 1 2 3

Mass_mg 0.000006662 0.0000244 0.0000143 0.000

lb/mmBtuO2 1.07E-09 3.97E-09 2.49E-09 0.000

ng/dscm 6.79E-01 2.55E+00 1.52E+00 1.583

ng/dscm@7%O2 1.24E+00 4.60E+00 2.89E+00 2.910

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000909 0.000000317 0.000000203 0.000

lb/mmBtuO2 1.46E-11 5.16E-11 3.53E-11 0.000

ng/dscm 9.26E-03 3.32E-02 2.15E-02 0.021

ng/dscm@7%O2 1.69E-02 5.99E-02 4.09E-02 0.039

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000022 0.0000000078 0.0000000033 0.000

lb/mmBtuO2 3.53E-13 1.27E-12 5.75E-13 0.000

Friday, February 04, 2011 Page 14 of 67
Jacksonville Electric Authority

ng/dscm 2.24E-04 8.16E-04 3.50E-04 0.000

ng/dscm@7%O2 4.10E-04 1.47E-03 6.66E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000024 0.000000013 0.0000000093 0.000

lb/mmBtuO2 3.86E-12 2.12E-12 1.62E-12 0.000

ng/dscm 2.44E-03 1.36E-03 9.86E-04 0.002

ng/dscm@7%O2 4.46E-03 2.46E-03 1.88E-03 0.003

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000063 0.0000000064 0.000000007 0.000

lb/mmBtuO2 1.01E-12 1.04E-12 1.22E-12 0.000

ng/dscm 6.42E-04 6.70E-04 7.42E-04 0.001

ng/dscm@7%O2 1.17E-03 1.21E-03 1.41E-03 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000018 0.000000018 0.000000012 0.000

lb/mmBtuO2 2.89E-12 2.93E-12 2.09E-12 0.000

ng/dscm 1.83E-03 1.88E-03 1.27E-03 0.002

ng/dscm@7%O2 3.35E-03 3.39E-03 2.42E-03 0.003

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000385 0.000000082 0.0000000562 0.000

lb/mmBtuO2 6.19E-12 1.34E-11 9.79E-12 0.000

ng/dscm 3.92E-03 8.58E-03 5.96E-03 0.006

ng/dscm@7%O2 7.17E-03 1.55E-02 1.13E-02 0.011

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000396 0.000000092 0.000000055 0.000

lb/mmBtuO2 6.36E-12 1.50E-11 9.58E-12 0.000

ng/dscm 4.03E-03 9.62E-03 5.83E-03 0.006

ng/dscm@7%O2 7.37E-03 1.74E-02 1.11E-02 0.012

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

Average

RunNumber 1 2 3

Mass_mg 0.0000003659 0.00000193 0.000000718 0.000

lb/mmBtuO2 5.88E-11 3.14E-10 1.25E-10 0.000

ng/dscm 3.73E-02 2.02E-01 7.61E-02 0.105

ng/dscm@7%O2 6.82E-02 3.65E-01 1.45E-01 0.193

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

Average

RunNumber 1 2 3

Friday, February 04, 2011 Page 15 of 67
Jacksonville Electric Authority

Mass_mg 0.0000000407 0.000000103 0.000000076 0.000

lb/mmBtuO2 6.54E-12 1.68E-11 1.32E-11 0.000

ng/dscm 4.15E-03 1.08E-02 8.06E-03 0.008

ng/dscm@7%O2 7.59E-03 1.95E-02 1.53E-02 0.014

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000067 0.000000083 0.000000084 0.000

lb/mmBtuO2 1.08E-11 1.35E-11 1.46E-11 0.000

ng/dscm 6.82E-03 8.68E-03 8.91E-03 0.008

ng/dscm@7%O2 1.25E-02 1.57E-02 1.70E-02 0.015

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000047 0.000000012 0.000000019 0.000

lb/mmBtuO2 7.55E-13 1.95E-12 3.31E-12 0.000

ng/dscm 4.79E-04 1.26E-03 2.01E-03 0.001

ng/dscm@7%O2 8.76E-04 2.27E-03 3.83E-03 0.002

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.0000001194 0.0000001439 0.000000141 0.000

lb/mmBtuO2 1.92E-11 2.34E-11 2.46E-11 0.000

ng/dscm 1.22E-02 1.51E-02 1.50E-02 0.014

ng/dscm@7%O2 2.23E-02 2.73E-02 2.86E-02 0.026

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.0000001396 0.0000001477 0.0000001784 0.000

lb/mmBtuO2 2.24E-11 2.41E-11 3.11E-11 0.000

ng/dscm 1.42E-02 1.55E-02 1.89E-02 0.016

ng/dscm@7%O2 2.60E-02 2.80E-02 3.60E-02 0.030

Compound: Total HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000065 0.00000008 0.000000066 0.000

lb/mmBtuO2 1.04E-11 1.30E-11 1.15E-11 0.000

ng/dscm 6.62E-03 8.37E-03 7.00E-03 0.007

ng/dscm@7%O2 1.21E-02 1.51E-02 1.33E-02 0.014

Compound: Total HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000004 0.000000032 0.000000053 0.000

lb/mmBtuO2 6.43E-12 5.21E-12 9.23E-12 0.000

ng/dscm 4.07E-03 3.35E-03 5.62E-03 0.004

ng/dscm@7%O2 7.44E-03 6.05E-03 1.07E-02 0.008

Friday, February 04, 2011 Page 16 of 67
Jacksonville Electric Authority

Compound: Total HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000063 0.000000075 0.000000092 0.000

lb/mmBtuO2 1.01E-11 1.22E-11 1.60E-11 0.000

ng/dscm 6.42E-03 7.85E-03 9.75E-03 0.008

ng/dscm@7%O2 1.17E-02 1.42E-02 1.86E-02 0.015

Compound: Total HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000015 0.00000023 0.00000022 0.000

lb/mmBtuO2 2.41E-11 3.75E-11 3.83E-11 0.000

ng/dscm 1.53E-02 2.41E-02 2.33E-02 0.021

ng/dscm@7%O2 2.80E-02 4.35E-02 4.44E-02 0.039

Compound: Total PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000061 0.000000093 0.0000001 0.000

lb/mmBtuO2 9.80E-12 1.51E-11 1.74E-11 0.000

ng/dscm 6.21E-03 9.73E-03 1.06E-02 0.009

ng/dscm@7%O2 1.14E-02 1.76E-02 2.02E-02 0.016

Compound: Total PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000056 0.0000004 0.0000004 0.000

lb/mmBtuO2 9.00E-11 6.52E-11 6.97E-11 0.000

ng/dscm 5.70E-02 4.18E-02 4.24E-02 0.047

ng/dscm@7%O2 1.04E-01 7.55E-02 8.07E-02 0.087

Compound: Total TCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000093 0.00000007 0.00000011 0.000

lb/mmBtuO2 1.49E-11 1.14E-11 1.92E-11 0.000

ng/dscm 9.47E-03 7.32E-03 1.17E-02 0.009

ng/dscm@7%O2 1.73E-02 1.32E-02 2.23E-02 0.018

Compound: Total TCDF 

Average

RunNumber 1 2 3

Mass_mg 0.00000077 0.00000065 0.00000043 0.000

lb/mmBtuO2 1.24E-10 1.06E-10 7.49E-11 0.000

ng/dscm 7.84E-02 6.80E-02 4.56E-02 0.064

ng/dscm@7%O2 1.43E-01 1.23E-01 8.68E-02 0.118

Location: Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 3.43E-05 1.23E-04 -5.38E-05 0.000

Friday, February 04, 2011 Page 17 of 67
Jacksonville Electric Authority

ppm 1.20E-02 4.37E-02 -1.91E-02 0.012

ppm@7%O2 2.17E-02 7.79E-02 -3.40E-02 0.022

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 2.28 2.47 2.18 2.310

lb/mmBtuO2 9.32E-04 1.02E-03 9.52E-04 0.001

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.19 0.21 0.21 0.203

lb/mmBtuO2 7.77E-05 8.67E-05 9.17E-05 0.000

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0892 0.08485 0.08475 0.086

lb/mmBtuO2 2.89E-05 3.20E-05 2.77E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.01396 0.01163 0.01173 0.012

lb/mmBtuO2 4.52E-06 4.38E-06 3.83E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00032 0.00032 0.00032 0.000

lb/mmBtuO2 1.04E-07 1.21E-07 1.05E-07 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00107 0.00133 0.001063 0.001

lb/mmBtuO2 3.47E-07 5.01E-07 3.47E-07 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0734 0.025 0.02044 0.040

lb/mmBtuO2 2.38E-05 9.42E-06 6.68E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.0845 0.0798 0.0756 0.080

lb/mmBtuO2 2.74E-05 3.01E-05 2.47E-05 0.000

Friday, February 04, 2011 Page 18 of 67
Jacksonville Electric Authority

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 88 110.8 103.3 100.700

lb/mmBtuO2 2.85E-02 4.17E-02 3.37E-02 0.035

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.01154 0.02044 0.00754 0.013

lb/mmBtuO2 3.74E-06 7.70E-06 2.46E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.04997 0.02607 0.01967 0.032

lb/mmBtuO2 1.62E-05 9.82E-06 6.42E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 3.8562 3.6273 3.5761 3.687

lb/mmBtuO2 1.25E-03 1.37E-03 1.17E-03 0.001

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0357 0.0248 0.0146 0.025

lb/mmBtuO2 1.16E-05 9.34E-06 4.77E-06 0.000

Location: Stack - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 1.68E+00 1.66E+00 1.63E+00 1.657

ppm 4.22E+02 4.11E+02 3.99E+02 410.667

ppm@7%O2 7.33E+02 7.23E+02 7.11E+02 722.333

Location: Stack - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 3.52E-01 3.55E-01 3.56E-01 0.354

ppm 1.23E+02 1.22E+02 1.21E+02 122.000

ppm@7%O2 2.14E+02 2.15E+02 2.16E+02 215.000

Location: Stack - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 73.26 68.4 67.4 69.687

lb/mmBtuO2 3.45E-02 6.72E-02 6.02E-02 0.054

Friday, February 04, 2011 Page 19 of 67
Jacksonville Electric Authority

Process Run Data

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 66.66 68.2 66.6 67.153

lb/mmBtuO2 3.14E-02 6.70E-02 5.95E-02 0.053

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 22.6 15.3 10 15.967

lb/mmBtuO2 1.06E-02 1.50E-02 8.94E-03 0.012

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 10.3 5.3 10.8 8.800

lb/mmBtuO2 4.85E-03 5.21E-03 9.65E-03 0.007

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 106.16 89 88.2 94.453

lb/mmBtuO2 5.00E-02 8.74E-02 7.88E-02 0.072

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 99.56 88.8 87.4 91.920

lb/mmBtuO2 4.68E-02 8.72E-02 7.81E-02 0.071

Friday, February 04, 2011 Page 20 of 67
Jacksonville Electric Authority

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 18460 MMBtu 18440

2 Heat Input 18460 MMBtu 18440

3 Heat Input 18460 MMBtu 18440

1 Steam Flow 1008.7 Klb/hr 1000

2 Steam Flow 1010.1 Klb/hr 1000

3 Steam Flow 1011.3 Klb/hr 1000

1 Gross Mwe 124.82 Mwe 124

2 Gross Mwe 124.88 Mwe 124

3 Gross Mwe 125.04 Mwe 124

Friday, February 04, 2011 Page 21 of 67
Jacksonville Electric Authority

Sampling / Stack Data Results Detail

Location Stack - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 22 of 67
Jacksonville Electric Authority

Location Stack - Method 23

Average

Run Number 1 2 3

Test Date 5/8/2010 5/9/2010 5/10/2010

Run Start Time 8:05:00 AM 7:45:00 AM 7:40:00 AM

Run Finish Time 4:31:00 PM 4:06:00 PM 4:00:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 480 480 480

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 1.014 1.014 1.014 1.014

Barometric Pressure, inches of Mercury 29.85 29.85 29.91 29.870

Average Orifice Meter Differential, inches H2O 1.78 1.64 1.63 1.683

Dry Gas Meter Volume Sampled, cubic feet 352.940 339.283 337.462 343.228

Average Dry Gas Meter Temperature, °F 86.04 78.96 84.38 83.127

Dry Gas Meter Volume Sampled, dscf 346.762 337.607 333.109 339.159

Total Moisture Liquid collected, g 491.8 445.1 244.8 393.900

Volume of Water Vapor, standard cubic feet 23.15 20.95 11.52 18.540

Moisture Content of Stack Gas, % 6.26 5.84 3.34 5.147

Moisture Saturation at Stack Gas Temperature, % 82.72 79.65 82.30 81.557

Dry Mole Fraction 0.9374 0.9416 0.9666 0.949

Carbon Dioxide, % 6 6.1 5.8 5.967

Oxygen, % 13.3 13.2 13.6 13.367

Carbon Monoxide & Nitrogen, % 80.7 80.7 80.6 80.667

Fuel Factor 1.27 1.26 1.26

Dry Molecular Weight, lb/lb-Mole 29.49 29.50 29.47 29.487

Wet Molecular weight, lb/lb-Mole 28.77 28.83 29.09 28.897

Flue Gas Static Pressure, inches of H2O -0.45 -0.36 -0.36 -0.390

Absolute Flue Gas Pressure, inches of Mercury 29.82 29.82 29.88 29.840

Average Stack Gas Temperature, °F 202.46 200.63 202.31 201.800

Average Velocity Head, inches of H2O 0.2310115562

88141

0.218206190

029089

0.212467664

58375

0.221

Average Stack Gas Velocity, feet/second 30.33 29.41 28.89 29.543

Stack Cross-Sectional Area, square feet 1,198.218 1,198.218 1,198.218 1,198.218

Dry Volumetric Flow Rate, dry scfm 1,623,696.2 1,585,879.7 1,598,354.2 1,602,643.3

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,180,517.1 2,114,375.5 2,076,991.1 2,123,961.2

33

Percent Isokinetic of Sampling Rate, % 99.1 98.8 96.7 98.200

Percent Excess Air, % 166.2 162.9 177.1 168.733

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

Round Duct Diameter, inches 468.71 468.71 468.71

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

Friday, February 04, 2011 Page 23 of 67
Jacksonville Electric Authority

Location Stack - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 24 of 67
Jacksonville Electric Authority

Location 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 25 of 67
Jacksonville Electric Authority

Location Stack - Method 29

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 26 of 67
Jacksonville Electric Authority

Location Stack - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 27 of 67
Jacksonville Electric Authority

Location Stack - Method 3A CO2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 28 of 67
Jacksonville Electric Authority

Location Stack - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 29 of 67
Jacksonville Electric Authority

Location Stack - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 30 of 67
Jacksonville Electric Authority

Location Stack - Method 3A O2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 31 of 67
Jacksonville Electric Authority

Location Stack - Method 3A O2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 32 of 67
Jacksonville Electric Authority

Location Stack - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 33 of 67
Jacksonville Electric Authority

Location Stack - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 34 of 67
Jacksonville Electric Authority

Location Stack - OTM - 27/28

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 35 of 67
Facility Information:

Contact:

Phone:

Fax:

Email:

Testing Company:

Contact:

Phone:

Fax:

Email:

Air Permit Number: Permitted Source ID/Name:

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:

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.

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:

Friday, February 04, 2011 Page 36 of 67
Sampling / Stack Data Results Summary

Location Stack - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack - Method 23

Average

Run Number 1 2 3

Test Date 5/8/2010 5/9/2010 5/10/2010

Run Start Time 8:05:00 AM 7:45:00 

AM

7:40:00 AM

Run Finish Time 4:31:00 PM 4:06:00 PM 4:00:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 346.762 337.607 333.109 339.159

Moisture Content of Stack Gas, % 6.26 5.84 3.34 5.147

Moisture Saturation at Stack Gas Temperature, % 82.72 79.65 82.30 81.557

Carbon Dioxide, % 6 6.1 5.8 5.967

Oxygen, % 13.3 13.2 13.6 13.367

Average Stack Gas Temperature, °F 202.46 200.63 202.31 201.800

Dry Volumetric Flow Rate, dry scfm 1,623,696.2 1,585,879.7 1,598,354.2 1,602,643.36

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,180,517.1 2,114,375.5 2,076,991.1 2,123,961.23

3

Percent Isokinetic of Sampling Rate, % 99.1 98.8 96.7 98.200

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

Friday, February 04, 2011 Page 37 of 67
Location Stack - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location 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 38 of 67
Location Stack - Method 29

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

Location Stack - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Friday, February 04, 2011 Page 39 of 67
Location Stack - Method 3A CO2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Friday, February 04, 2011 Page 40 of 67
Location Stack - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack - Method 3A O2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Friday, February 04, 2011 Page 41 of 67
Location Stack - Method 3A O2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Friday, February 04, 2011 Page 42 of 67
Location Stack - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack - OTM - 27/28

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 43 of 67
Emissions Summary

Location: Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.62E-03 1.64E-03 1.49E-03 0.002

ppm 8.91E-01 9.18E-01 8.33E-01 0.881

ppm@7%O2 1.61E+00 1.64E+00 1.48E+00 1.577

Location: Stack - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.000000029 0.000000033 0.000000028 0.000

lb/mmBtuO2 4.66E-12 5.38E-12 4.88E-12 0.000

ng/dscm 2.95E-03 3.45E-03 2.97E-03 0.003

ng/dscm@7%O2 5.40E-03 6.23E-03 5.66E-03 0.006

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

Average

RunNumber 1 2 3

Mass_mg 0.000000022 0.000000018 0.00000003 0.000

lb/mmBtuO2 3.53E-12 2.93E-12 5.22E-12 0.000

ng/dscm 2.24E-03 1.88E-03 3.18E-03 0.002

ng/dscm@7%O2 4.10E-03 3.39E-03 6.06E-03 0.005

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000072 0.0000000042 0.000000007 0.000

lb/mmBtuO2 1.16E-12 6.84E-13 1.22E-12 0.000

ng/dscm 7.33E-04 4.39E-04 7.42E-04 0.001

ng/dscm@7%O2 1.34E-03 7.92E-04 1.41E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000023 0.0000000037 0.0000000043 0.000

lb/mmBtuO2 3.70E-13 6.03E-13 7.49E-13 0.000

ng/dscm 2.34E-04 3.87E-04 4.56E-04 0.000

ng/dscm@7%O2 4.28E-04 6.99E-04 8.68E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000016 0.000000016 0.000000031 0.000

lb/mmBtuO2 2.57E-12 2.61E-12 5.40E-12 0.000

ng/dscm 1.63E-03 1.67E-03 3.29E-03 0.002

ng/dscm@7%O2 2.98E-03 3.01E-03 6.26E-03 0.004

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

Average

Friday, February 04, 2011 Page 44 of 67
RunNumber 1 2 3

Mass_mg 0.0000000046 0.0000000049 0.0000000042 0.000

lb/mmBtuO2 7.39E-13 7.98E-13 7.31E-13 0.000

ng/dscm 4.69E-04 5.13E-04 4.45E-04 0.000

ng/dscm@7%O2 8.58E-04 9.26E-04 8.47E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000015 0.000000018 0.000000022 0.000

lb/mmBtuO2 2.41E-12 2.93E-12 3.83E-12 0.000

ng/dscm 1.53E-03 1.88E-03 2.33E-03 0.002

ng/dscm@7%O2 2.80E-03 3.39E-03 4.44E-03 0.004

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000039 0.0000000044 0.0000000042 0.000

lb/mmBtuO2 6.27E-13 7.17E-13 7.31E-13 0.000

ng/dscm 3.97E-04 4.60E-04 4.45E-04 0.000

ng/dscm@7%O2 7.26E-04 8.30E-04 8.47E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000025 0.0000000047 0.0000000038 0.000

lb/mmBtuO2 4.02E-13 7.66E-13 6.62E-13 0.000

ng/dscm 2.55E-04 4.92E-04 4.03E-04 0.000

ng/dscm@7%O2 4.66E-04 8.88E-04 7.67E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000063 0.0000000085 0.0000000093 0.000

lb/mmBtuO2 1.01E-12 1.38E-12 1.62E-12 0.000

ng/dscm 6.42E-04 8.89E-04 9.86E-04 0.001

ng/dscm@7%O2 1.17E-03 1.60E-03 1.88E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.000000028 0.000000036 0.000000041 0.000

lb/mmBtuO2 4.50E-12 5.86E-12 7.14E-12 0.000

ng/dscm 2.85E-03 3.77E-03 4.35E-03 0.004

ng/dscm@7%O2 5.21E-03 6.81E-03 8.28E-03 0.007

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

Average

RunNumber 1 2 3

Mass_mg 0.000000031 0.000000041 0.0000000364 0.000

lb/mmBtuO2 4.98E-12 6.68E-12 6.34E-12 0.000

ng/dscm 3.16E-03 4.29E-03 3.86E-03 0.004

ng/dscm@7%O2 5.78E-03 7.74E-03 7.35E-03 0.007

Friday, February 04, 2011 Page 45 of 67
Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 1 2 3

Mass_mg 0.0000008712 0.000001494 0.000000962 0.000

lb/mmBtuO2 1.40E-10 2.43E-10 1.68E-10 0.000

ng/dscm 8.87E-02 1.56E-01 1.02E-01 0.116

ng/dscm@7%O2 1.62E-01 2.82E-01 1.94E-01 0.213

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

Average

RunNumber 1 2 3

Mass_mg 0.000002137 0.00000639 0.00000385 0.000

lb/mmBtuO2 3.43E-10 1.04E-09 6.70E-10 0.000

ng/dscm 2.18E-01 6.69E-01 4.08E-01 0.432

ng/dscm@7%O2 3.99E-01 1.21E+00 7.77E-01 0.795

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

Average

RunNumber 1 2 3

Mass_mg 0.0000001163 0.000000357 0.000000186 0.000

lb/mmBtuO2 1.87E-11 5.82E-11 3.24E-11 0.000

ng/dscm 1.18E-02 3.73E-02 1.97E-02 0.023

ng/dscm@7%O2 2.16E-02 6.73E-02 3.75E-02 0.042

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

Average

RunNumber 1 2 3

Mass_mg 0.0000001085 0.00000054 0.000000275 0.000

lb/mmBtuO2 1.74E-11 8.80E-11 4.79E-11 0.000

ng/dscm 1.11E-02 5.65E-02 2.92E-02 0.032

ng/dscm@7%O2 2.03E-02 1.02E-01 5.56E-02 0.059

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

Average

RunNumber 1 2 3

Mass_mg 0.000006662 0.0000244 0.0000143 0.000

lb/mmBtuO2 1.07E-09 3.97E-09 2.49E-09 0.000

ng/dscm 6.79E-01 2.55E+00 1.52E+00 1.583

ng/dscm@7%O2 1.24E+00 4.60E+00 2.89E+00 2.910

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000909 0.000000317 0.000000203 0.000

lb/mmBtuO2 1.46E-11 5.16E-11 3.53E-11 0.000

ng/dscm 9.26E-03 3.32E-02 2.15E-02 0.021

ng/dscm@7%O2 1.69E-02 5.99E-02 4.09E-02 0.039

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000022 0.0000000078 0.0000000033 0.000

lb/mmBtuO2 3.53E-13 1.27E-12 5.75E-13 0.000

Friday, February 04, 2011 Page 46 of 67
ng/dscm 2.24E-04 8.16E-04 3.50E-04 0.000

ng/dscm@7%O2 4.10E-04 1.47E-03 6.66E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000024 0.000000013 0.0000000093 0.000

lb/mmBtuO2 3.86E-12 2.12E-12 1.62E-12 0.000

ng/dscm 2.44E-03 1.36E-03 9.86E-04 0.002

ng/dscm@7%O2 4.46E-03 2.46E-03 1.88E-03 0.003

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000063 0.0000000064 0.000000007 0.000

lb/mmBtuO2 1.01E-12 1.04E-12 1.22E-12 0.000

ng/dscm 6.42E-04 6.70E-04 7.42E-04 0.001

ng/dscm@7%O2 1.17E-03 1.21E-03 1.41E-03 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000018 0.000000018 0.000000012 0.000

lb/mmBtuO2 2.89E-12 2.93E-12 2.09E-12 0.000

ng/dscm 1.83E-03 1.88E-03 1.27E-03 0.002

ng/dscm@7%O2 3.35E-03 3.39E-03 2.42E-03 0.003

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000385 0.000000082 0.0000000562 0.000

lb/mmBtuO2 6.19E-12 1.34E-11 9.79E-12 0.000

ng/dscm 3.92E-03 8.58E-03 5.96E-03 0.006

ng/dscm@7%O2 7.17E-03 1.55E-02 1.13E-02 0.011

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000396 0.000000092 0.000000055 0.000

lb/mmBtuO2 6.36E-12 1.50E-11 9.58E-12 0.000

ng/dscm 4.03E-03 9.62E-03 5.83E-03 0.006

ng/dscm@7%O2 7.37E-03 1.74E-02 1.11E-02 0.012

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

Average

RunNumber 1 2 3

Mass_mg 0.0000003659 0.00000193 0.000000718 0.000

lb/mmBtuO2 5.88E-11 3.14E-10 1.25E-10 0.000

ng/dscm 3.73E-02 2.02E-01 7.61E-02 0.105

ng/dscm@7%O2 6.82E-02 3.65E-01 1.45E-01 0.193

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

Average

RunNumber 1 2 3

Friday, February 04, 2011 Page 47 of 67
Mass_mg 0.0000000407 0.000000103 0.000000076 0.000

lb/mmBtuO2 6.54E-12 1.68E-11 1.32E-11 0.000

ng/dscm 4.15E-03 1.08E-02 8.06E-03 0.008

ng/dscm@7%O2 7.59E-03 1.95E-02 1.53E-02 0.014

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000067 0.000000083 0.000000084 0.000

lb/mmBtuO2 1.08E-11 1.35E-11 1.46E-11 0.000

ng/dscm 6.82E-03 8.68E-03 8.91E-03 0.008

ng/dscm@7%O2 1.25E-02 1.57E-02 1.70E-02 0.015

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000047 0.000000012 0.000000019 0.000

lb/mmBtuO2 7.55E-13 1.95E-12 3.31E-12 0.000

ng/dscm 4.79E-04 1.26E-03 2.01E-03 0.001

ng/dscm@7%O2 8.76E-04 2.27E-03 3.83E-03 0.002

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.0000001194 0.0000001439 0.000000141 0.000

lb/mmBtuO2 1.92E-11 2.34E-11 2.46E-11 0.000

ng/dscm 1.22E-02 1.51E-02 1.50E-02 0.014

ng/dscm@7%O2 2.23E-02 2.73E-02 2.86E-02 0.026

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.0000001396 0.0000001477 0.0000001784 0.000

lb/mmBtuO2 2.24E-11 2.41E-11 3.11E-11 0.000

ng/dscm 1.42E-02 1.55E-02 1.89E-02 0.016

ng/dscm@7%O2 2.60E-02 2.80E-02 3.60E-02 0.030

Compound: Total HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000065 0.00000008 0.000000066 0.000

lb/mmBtuO2 1.04E-11 1.30E-11 1.15E-11 0.000

ng/dscm 6.62E-03 8.37E-03 7.00E-03 0.007

ng/dscm@7%O2 1.21E-02 1.51E-02 1.33E-02 0.014

Compound: Total HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000004 0.000000032 0.000000053 0.000

lb/mmBtuO2 6.43E-12 5.21E-12 9.23E-12 0.000

ng/dscm 4.07E-03 3.35E-03 5.62E-03 0.004

ng/dscm@7%O2 7.44E-03 6.05E-03 1.07E-02 0.008

Friday, February 04, 2011 Page 48 of 67
Compound: Total HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000063 0.000000075 0.000000092 0.000

lb/mmBtuO2 1.01E-11 1.22E-11 1.60E-11 0.000

ng/dscm 6.42E-03 7.85E-03 9.75E-03 0.008

ng/dscm@7%O2 1.17E-02 1.42E-02 1.86E-02 0.015

Compound: Total HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000015 0.00000023 0.00000022 0.000

lb/mmBtuO2 2.41E-11 3.75E-11 3.83E-11 0.000

ng/dscm 1.53E-02 2.41E-02 2.33E-02 0.021

ng/dscm@7%O2 2.80E-02 4.35E-02 4.44E-02 0.039

Compound: Total PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000061 0.000000093 0.0000001 0.000

lb/mmBtuO2 9.80E-12 1.51E-11 1.74E-11 0.000

ng/dscm 6.21E-03 9.73E-03 1.06E-02 0.009

ng/dscm@7%O2 1.14E-02 1.76E-02 2.02E-02 0.016

Compound: Total PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000056 0.0000004 0.0000004 0.000

lb/mmBtuO2 9.00E-11 6.52E-11 6.97E-11 0.000

ng/dscm 5.70E-02 4.18E-02 4.24E-02 0.047

ng/dscm@7%O2 1.04E-01 7.55E-02 8.07E-02 0.087

Compound: Total TCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000093 0.00000007 0.00000011 0.000

lb/mmBtuO2 1.49E-11 1.14E-11 1.92E-11 0.000

ng/dscm 9.47E-03 7.32E-03 1.17E-02 0.009

ng/dscm@7%O2 1.73E-02 1.32E-02 2.23E-02 0.018

Compound: Total TCDF 

Average

RunNumber 1 2 3

Mass_mg 0.00000077 0.00000065 0.00000043 0.000

lb/mmBtuO2 1.24E-10 1.06E-10 7.49E-11 0.000

ng/dscm 7.84E-02 6.80E-02 4.56E-02 0.064

ng/dscm@7%O2 1.43E-01 1.23E-01 8.68E-02 0.118

Location: Stack - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 3.43E-05 1.23E-04 -5.38E-05 0.000

Friday, February 04, 2011 Page 49 of 67
ppm 1.20E-02 4.37E-02 -1.91E-02 0.012

ppm@7%O2 2.17E-02 7.79E-02 -3.40E-02 0.022

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 2.28 2.47 2.18 2.310

lb/mmBtuO2 9.32E-04 1.02E-03 9.52E-04 0.001

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.19 0.21 0.21 0.203

lb/mmBtuO2 7.77E-05 8.67E-05 9.17E-05 0.000

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0892 0.08485 0.08475 0.086

lb/mmBtuO2 2.89E-05 3.20E-05 2.77E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.01396 0.01163 0.01173 0.012

lb/mmBtuO2 4.52E-06 4.38E-06 3.83E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00032 0.00032 0.00032 0.000

lb/mmBtuO2 1.04E-07 1.21E-07 1.05E-07 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00107 0.00133 0.001063 0.001

lb/mmBtuO2 3.47E-07 5.01E-07 3.47E-07 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0734 0.025 0.02044 0.040

lb/mmBtuO2 2.38E-05 9.42E-06 6.68E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.0845 0.0798 0.0756 0.080

lb/mmBtuO2 2.74E-05 3.01E-05 2.47E-05 0.000

Friday, February 04, 2011 Page 50 of 67
Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 88 110.8 103.3 100.700

lb/mmBtuO2 2.85E-02 4.17E-02 3.37E-02 0.035

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.01154 0.02044 0.00754 0.013

lb/mmBtuO2 3.74E-06 7.70E-06 2.46E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.04997 0.02607 0.01967 0.032

lb/mmBtuO2 1.62E-05 9.82E-06 6.42E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 3.8562 3.6273 3.5761 3.687

lb/mmBtuO2 1.25E-03 1.37E-03 1.17E-03 0.001

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0357 0.0248 0.0146 0.025

lb/mmBtuO2 1.16E-05 9.34E-06 4.77E-06 0.000

Location: Stack - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 1.68E+00 1.66E+00 1.63E+00 1.657

ppm 4.22E+02 4.11E+02 3.99E+02 410.667

ppm@7%O2 7.33E+02 7.23E+02 7.11E+02 722.333

Location: Stack - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 3.52E-01 3.55E-01 3.56E-01 0.354

ppm 1.23E+02 1.22E+02 1.21E+02 122.000

ppm@7%O2 2.14E+02 2.15E+02 2.16E+02 215.000

Location: Stack - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 73.26 68.4 67.4 69.687

lb/mmBtuO2 3.45E-02 6.72E-02 6.02E-02 0.054

Friday, February 04, 2011 Page 51 of 67
Process Run Data

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 66.66 68.2 66.6 67.153

lb/mmBtuO2 3.14E-02 6.70E-02 5.95E-02 0.053

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 22.6 15.3 10 15.967

lb/mmBtuO2 1.06E-02 1.50E-02 8.94E-03 0.012

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 10.3 5.3 10.8 8.800

lb/mmBtuO2 4.85E-03 5.21E-03 9.65E-03 0.007

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 106.16 89 88.2 94.453

lb/mmBtuO2 5.00E-02 8.74E-02 7.88E-02 0.072

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 99.56 88.8 87.4 91.920

lb/mmBtuO2 4.68E-02 8.72E-02 7.81E-02 0.071

Friday, February 04, 2011 Page 52 of 67
Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 18460 MMBtu 18440

2 Heat Input 18460 MMBtu 18440

3 Heat Input 18460 MMBtu 18440

1 Steam Flow 1008.7 Klb/hr 1000

2 Steam Flow 1010.1 Klb/hr 1000

3 Steam Flow 1011.3 Klb/hr 1000

1 Gross Mwe 124.82 Mwe 124

2 Gross Mwe 124.88 Mwe 124

3 Gross Mwe 125.04 Mwe 124

Friday, February 04, 2011 Page 53 of 67
Sampling / Stack Data Results Detail

Location Stack - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 54 of 67
Location Stack - Method 23

Average

Run Number 1 2 3

Test Date 5/8/2010 5/9/2010 5/10/2010

Run Start Time 8:05:00 AM 7:45:00 AM 7:40:00 AM

Run Finish Time 4:31:00 PM 4:06:00 PM 4:00:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 480 480 480

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 1.014 1.014 1.014 1.014

Barometric Pressure, inches of Mercury 29.85 29.85 29.91 29.870

Average Orifice Meter Differential, inches H2O 1.78 1.64 1.63 1.683

Dry Gas Meter Volume Sampled, cubic feet 352.940 339.283 337.462 343.228

Average Dry Gas Meter Temperature, °F 86.04 78.96 84.38 83.127

Dry Gas Meter Volume Sampled, dscf 346.762 337.607 333.109 339.159

Total Moisture Liquid collected, g 491.8 445.1 244.8 393.900

Volume of Water Vapor, standard cubic feet 23.15 20.95 11.52 18.540

Moisture Content of Stack Gas, % 6.26 5.84 3.34 5.147

Moisture Saturation at Stack Gas Temperature, % 82.72 79.65 82.30 81.557

Dry Mole Fraction 0.9374 0.9416 0.9666 0.949

Carbon Dioxide, % 6 6.1 5.8 5.967

Oxygen, % 13.3 13.2 13.6 13.367

Carbon Monoxide & Nitrogen, % 80.7 80.7 80.6 80.667

Fuel Factor 1.27 1.26 1.26

Dry Molecular Weight, lb/lb-Mole 29.49 29.50 29.47 29.487

Wet Molecular weight, lb/lb-Mole 28.77 28.83 29.09 28.897

Flue Gas Static Pressure, inches of H2O -0.45 -0.36 -0.36 -0.390

Absolute Flue Gas Pressure, inches of Mercury 29.82 29.82 29.88 29.840

Average Stack Gas Temperature, °F 202.46 200.63 202.31 201.800

Average Velocity Head, inches of H2O 0.2310115562

88141

0.218206190

029089

0.212467664

58375

0.221

Average Stack Gas Velocity, feet/second 30.33 29.41 28.89 29.543

Stack Cross-Sectional Area, square feet 1,198.218 1,198.218 1,198.218 1,198.218

Dry Volumetric Flow Rate, dry scfm 1,623,696.2 1,585,879.7 1,598,354.2 1,602,643.3

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,180,517.1 2,114,375.5 2,076,991.1 2,123,961.2

33

Percent Isokinetic of Sampling Rate, % 99.1 98.8 96.7 98.200

Percent Excess Air, % 166.2 162.9 177.1 168.733

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

Round Duct Diameter, inches 468.71 468.71 468.71

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

Friday, February 04, 2011 Page 55 of 67
Location Stack - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 56 of 67
Location 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 57 of 67
Location Stack - Method 29

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 58 of 67
Location Stack - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 59 of 67
Location Stack - Method 3A CO2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 60 of 67
Location Stack - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 61 of 67
Location Stack - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 62 of 67
Location Stack - Method 3A O2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 63 of 67
Location Stack - Method 3A O2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 64 of 67
Location Stack - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 65 of 67
Location Stack - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, February 04, 2011 Page 66 of 67
Location Stack - OTM - 27/28

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 67 of 67