### 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:
Northside 3 JEA

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 3817.5 2442.5 4 13 48 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location

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 Stack



### Friday, February 04, 2011 Page 2 of 67

### Jacksonville Electric Authority

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

HxCB (PCBs156/157) 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 Stack 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 0 Stack

Total organic compounds

(TOC) as Propane 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 Stack Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 180 0 Stack

Organic Condensible

Particulate 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 Stack



### 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.

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 Stack



### 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 67RunNumber 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 67ng/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 67Mass_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 67ppm 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