Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Wednesday, February 16, 2011 Page 1 of 45
Facility Information:

IP&L Eagle Valley Generating Station

4040 Blue Bluff Road

Martinsville IN 46151

Contact: Kyle Noah

Phone: 317-439-1251

Fax: 765-342-2311

Email: kyle.noah@aes.com

Testing Company:

URS Corporation

1600 Perimeter Park Drive, Suite 400

Morrisville NC 27560

Contact:Brad Justus

Phone: 919-461-1326

Fax: 919-461-1415

Email: brad_justus@urscorp.com

Air Permit Number:

991

Permitted Source ID/Name:

Boilers 1 and 2 Combined Stack

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

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

 process flow diagram:

Boilers 1 and 2 are rated at 45 MW each and fire No. 2 Distillate Fuel Oil. Both units exhaust through a common 

stack.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 110000396606 FRS #: 110000396606

SCC / Description 10100501 External Combustion Boilers - Electric Generation - Distillate Oil - Grades 1 and 2 

Oil 

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 Exit 15 0 0 0 180 50 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 180 0

Stack Exit Carbon Monoxide Method 10 3 120 0

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

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

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

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

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

Wednesday, February 16, 2011 Page 2 of 45
Stack Exit 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

Stack Exit OCDD Method 23 3 480 0

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

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

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

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

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

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

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

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

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

Stack Exit OCDF Method 23 3 480 0

Stack Exit Total Dioxins Method 23 3 480 0

Stack Exit Total Furans Method 23 3 480 0

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

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

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

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

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

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

Stack Exit 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 Exit Method 23 3 480 0

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

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

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

(PCB189)

Stack Exit Method 23 3 480 0

Stack Exit Total PCBs Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Total Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Organic Condensible 

Particulate

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Wednesday, February 16, 2011 Page 3 of 45
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.

None

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Wednesday, February 16, 2011 Page 4 of 45
Sampling / Stack Data Results Summary

Location Stack Exit - 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 Exit - Method 23

Average

Run Number 1 2 3

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

Run Start Time 12:10:00 AM 9:00:00 

AM

12:10:00 AM

Run Finish Time 8:27:00 AM 5:15:00 PM 11:35:00 PM

Net Run Time, minutes 485 480 480

Dry Gas Meter Volume Sampled, dscf 346.675 345.732 346.506 346.304

Moisture Content of Stack Gas, % 7.18 7.03 7.46 7.223

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

Carbon Dioxide, % 7.4 7.4 7.5 7.433

Oxygen, % 11.5 11.5 11.2 11.400

Average Stack Gas Temperature, °F 269.79 269.19 271.78 270.253

Dry Volumetric Flow Rate, dry scfm 1,150.3 1,156.1 1,143.3 1,149.900

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,749.2 1,753.6 1,748.5 1,750.433

Percent Isokinetic of Sampling Rate, % 96.8 97.1 98.4 97.433

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

Wednesday, February 16, 2011 Page 5 of 45
Location Stack Exit - 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 Exit - 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

Wednesday, February 16, 2011 Page 6 of 45
Location Stack Exit - 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 Exit - 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

Wednesday, February 16, 2011 Page 7 of 45
Location Stack Exit - 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 Exit - 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

Wednesday, February 16, 2011 Page 8 of 45
Location Stack Exit - Method 3A CO2 3 6 9

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 Exit - Method 3A CO2 3 6 9 12

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

Wednesday, February 16, 2011 Page 9 of 45
Location Stack Exit - 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 Exit - 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

Wednesday, February 16, 2011 Page 10 of 45
Location Stack Exit - 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 Exit - Method 3A O2 3 6 9

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

Wednesday, February 16, 2011 Page 11 of 45
Location Stack Exit - Method 3A O2 3 6 9 12

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 Exit - 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

Wednesday, February 16, 2011 Page 12 of 45
Location Stack Exit - 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 Exit - 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

Wednesday, February 16, 2011 Page 13 of 45
Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run DF/30B Run 1 DF/30B Run 2 DF/30B Run 3

lb/mmBtuO2 1.01E-03 1.19E-03 3.33E-04 0.001

ppm 6.80E-01 8.04E-01 2.31E-01 0.572

ppm@7%O2 1.00E+00 1.18E+00 3.32E-01 0.837

Location: Stack Exit - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000976 0.0000000224 0.000000068 0.000

lb/mmBtuO2 1.27E-11 2.92E-12 8.57E-12 0.000

ng/dscm 9.94E-03 2.29E-03 6.93E-03 0.006

ng/dscm@7%O2 1.47E-02 3.39E-03 9.93E-03 0.009

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000931 0.00000000252 0.00000000517 0.000

lb/mmBtuO2 1.21E-12 3.28E-13 6.51E-13 0.000

ng/dscm 9.49E-04 2.57E-04 5.27E-04 0.001

ng/dscm@7%O2 1.40E-03 3.80E-04 7.55E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000594 0.0000000031 0.00000000623 0.000

lb/mmBtuO2 7.72E-13 4.04E-13 7.85E-13 0.000

ng/dscm 6.05E-04 3.17E-04 6.35E-04 0.001

ng/dscm@7%O2 8.95E-04 4.69E-04 9.10E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000351 0.00000000319 0.0000000216 0.000

lb/mmBtuO2 4.56E-12 4.16E-13 2.72E-12 0.000

ng/dscm 3.58E-03 3.26E-04 2.20E-03 0.002

ng/dscm@7%O2 5.29E-03 4.82E-04 3.15E-03 0.003

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000743 0.00000000173 0.00000000405 0.000

lb/mmBtuO2 9.65E-13 2.25E-13 5.10E-13 0.000

ng/dscm 7.57E-04 1.77E-04 4.13E-04 0.000

ng/dscm@7%O2 1.12E-03 2.62E-04 5.92E-04 0.001

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

Average

Wednesday, February 16, 2011 Page 14 of 45
RunNumber 1 2 3

Mass_mg 0.0000000411 0.00000000433 0.000000024 0.000

lb/mmBtuO2 5.34E-12 5.64E-13 3.02E-12 0.000

ng/dscm 4.19E-03 4.42E-04 2.45E-03 0.002

ng/dscm@7%O2 6.20E-03 6.54E-04 3.51E-03 0.003

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000445 0.00000000171 0.00000000297 0.000

lb/mmBtuO2 5.78E-13 2.23E-13 3.74E-13 0.000

ng/dscm 4.53E-04 1.75E-04 3.03E-04 0.000

ng/dscm@7%O2 6.70E-04 2.59E-04 4.34E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000525 0.00000000759 0.0000000294 0.000

lb/mmBtuO2 6.82E-12 9.89E-13 3.70E-12 0.000

ng/dscm 5.35E-03 7.75E-04 3.00E-03 0.003

ng/dscm@7%O2 7.91E-03 1.15E-03 4.30E-03 0.004

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000333 0.00000000154 0.00000000411 0.000

lb/mmBtuO2 4.33E-13 2.01E-13 5.18E-13 0.000

ng/dscm 3.39E-04 1.57E-04 4.19E-04 0.000

ng/dscm@7%O2 5.01E-04 2.32E-04 6.00E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000756 0.00000000424 0.0000000571 0.000

lb/mmBtuO2 9.82E-12 5.52E-13 7.19E-12 0.000

ng/dscm 7.70E-03 4.33E-04 5.82E-03 0.005

ng/dscm@7%O2 1.14E-02 6.40E-04 8.34E-03 0.007

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000104 0.0000000024 0.00000000705 0.000

lb/mmBtuO2 1.35E-12 3.13E-13 8.88E-13 0.000

ng/dscm 1.06E-03 2.45E-04 7.19E-04 0.001

ng/dscm@7%O2 1.57E-03 3.62E-04 1.03E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000391 0.0000000623 0.0000000374 0.000

lb/mmBtuO2 5.08E-12 8.12E-12 4.71E-12 0.000

ng/dscm 3.98E-03 6.36E-03 3.81E-03 0.005

ng/dscm@7%O2 5.89E-03 9.40E-03 5.46E-03 0.007

Wednesday, February 16, 2011 Page 15 of 45
Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 1 2 3

Mass_mg 0.000000237 0.000000317 0.000000144 0.000

lb/mmBtuO2 3.08E-11 4.13E-11 1.81E-11 0.000

ng/dscm 2.41E-02 3.24E-02 1.47E-02 0.024

ng/dscm@7%O2 3.56E-02 4.79E-02 2.11E-02 0.035

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

Average

RunNumber 1 2 3

Mass_mg 0.00000152 0.00000186 0.000000794 0.000

lb/mmBtuO2 1.98E-10 2.42E-10 1.00E-10 0.000

ng/dscm 1.55E-01 1.90E-01 8.09E-02 0.142

ng/dscm@7%O2 2.29E-01 2.81E-01 1.16E-01 0.209

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000753 0.000000133 0.0000000597 0.000

lb/mmBtuO2 9.78E-12 1.73E-11 7.52E-12 0.000

ng/dscm 7.67E-03 1.36E-02 6.09E-03 0.009

ng/dscm@7%O2 1.13E-02 2.01E-02 8.73E-03 0.013

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000303 0.000000131 0.0000000703 0.000

lb/mmBtuO2 3.94E-12 1.71E-11 8.86E-12 0.000

ng/dscm 3.09E-03 1.34E-02 7.17E-03 0.008

ng/dscm@7%O2 4.57E-03 1.98E-02 1.03E-02 0.012

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

Average

RunNumber 1 2 3

Mass_mg 0.0000043 0.00000547 0.00000227 0.000

lb/mmBtuO2 5.59E-10 7.13E-10 2.86E-10 0.000

ng/dscm 4.38E-01 5.59E-01 2.31E-01 0.409

ng/dscm@7%O2 6.48E-01 8.27E-01 3.31E-01 0.602

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000374 0.0000000564 0.0000000274 0.000

lb/mmBtuO2 4.86E-12 7.35E-12 3.45E-12 0.000

ng/dscm 3.81E-03 5.76E-03 2.79E-03 0.004

ng/dscm@7%O2 5.63E-03 8.52E-03 4.00E-03 0.006

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000215 0.00000000109 0.00000000277 0.000

lb/mmBtuO2 2.79E-13 1.42E-13 3.49E-13 0.000

Wednesday, February 16, 2011 Page 16 of 45
ng/dscm 2.19E-04 1.11E-04 2.82E-04 0.000

ng/dscm@7%O2 3.24E-04 1.64E-04 4.04E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000781 0.00000000156 0.00000000251 0.000

lb/mmBtuO2 1.01E-12 2.03E-13 3.16E-13 0.000

ng/dscm 7.96E-04 1.59E-04 2.56E-04 0.000

ng/dscm@7%O2 1.18E-03 2.35E-04 3.67E-04 0.001

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000311 0.00000000259 0.0000000223 0.000

lb/mmBtuO2 4.04E-12 3.37E-13 2.81E-12 0.000

ng/dscm 3.17E-03 2.65E-04 2.27E-03 0.002

ng/dscm@7%O2 4.69E-03 3.92E-04 3.25E-03 0.003

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000759 0.0000000025 0.00000000305 0.000

lb/mmBtuO2 9.86E-13 3.26E-13 3.84E-13 0.000

ng/dscm 7.73E-04 2.55E-04 3.11E-04 0.000

ng/dscm@7%O2 1.14E-03 3.77E-04 4.46E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000399 0.0000000583 0.0000000404 0.000

lb/mmBtuO2 5.18E-12 7.60E-12 5.09E-12 0.000

ng/dscm 4.07E-03 5.96E-03 4.12E-03 0.005

ng/dscm@7%O2 6.02E-03 8.81E-03 5.90E-03 0.007

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000472 0.0000000568 0.0000000399 0.000

lb/mmBtuO2 6.13E-12 7.40E-12 5.03E-12 0.000

ng/dscm 4.81E-03 5.80E-03 4.07E-03 0.005

ng/dscm@7%O2 7.11E-03 8.58E-03 5.83E-03 0.007

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

Average

RunNumber 1 2 3

Mass_mg 0.000000718 0.000000881 0.000000346 0.000

lb/mmBtuO2 9.33E-11 1.15E-10 4.36E-11 0.000

ng/dscm 7.32E-02 9.00E-02 3.53E-02 0.066

ng/dscm@7%O2 1.08E-01 1.33E-01 5.06E-02 0.097

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

Average

RunNumber 1 2 3

Wednesday, February 16, 2011 Page 17 of 45
Mass_mg 0.0000000474 0.000000074 0.00000003 0.000

lb/mmBtuO2 6.16E-12 9.64E-12 3.78E-12 0.000

ng/dscm 4.83E-03 7.56E-03 3.06E-03 0.005

ng/dscm@7%O2 7.14E-03 1.12E-02 4.38E-03 0.008

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000953 0.0000000401 0.0000000724 0.000

lb/mmBtuO2 1.24E-11 5.22E-12 9.12E-12 0.000

ng/dscm 9.71E-03 4.10E-03 7.38E-03 0.007

ng/dscm@7%O2 1.44E-02 6.06E-03 1.06E-02 0.010

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000195 0.00000000893 0.0000000199 0.000

lb/mmBtuO2 2.53E-12 1.16E-12 2.51E-12 0.000

ng/dscm 1.99E-03 9.12E-04 2.03E-03 0.002

ng/dscm@7%O2 2.94E-03 1.35E-03 2.91E-03 0.002

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000125 0.0000000249 0.0000000893 0.000

lb/mmBtuO2 1.62E-11 3.24E-12 1.13E-11 0.000

ng/dscm 1.27E-02 2.54E-03 9.10E-03 0.008

ng/dscm@7%O2 1.88E-02 3.76E-03 1.30E-02 0.012

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000928 0 0.00000000736 0.000

lb/mmBtuO2 1.21E-12 0.00E+00 9.27E-13 0.000

ng/dscm 9.45E-04 0.00E+00 7.50E-04 0.001

ng/dscm@7%O2 1.40E-03 0.00E+00 1.07E-03 0.001

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000491 0.0000000459 0.000000302 0.000

lb/mmBtuO2 6.38E-11 5.98E-12 3.80E-11 0.000

ng/dscm 5.00E-02 4.69E-03 3.08E-02 0.028

ng/dscm@7%O2 7.39E-02 6.94E-03 4.41E-02 0.042

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000317 0.00000000382 0.0000000174 0.000

lb/mmBtuO2 4.12E-12 4.98E-13 2.19E-12 0.000

ng/dscm 3.23E-03 3.90E-04 1.77E-03 0.002

ng/dscm@7%O2 4.78E-03 5.77E-04 2.54E-03 0.003

Wednesday, February 16, 2011 Page 18 of 45
Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000676 0.0000000424 0.000000479 0.000

lb/mmBtuO2 8.78E-11 5.52E-12 6.03E-11 0.000

ng/dscm 6.89E-02 4.33E-03 4.88E-02 0.041

ng/dscm@7%O2 1.02E-01 6.40E-03 6.99E-02 0.059

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000753 0.00000000724 0.0000000323 0.000

lb/mmBtuO2 9.78E-12 9.43E-13 4.07E-12 0.000

ng/dscm 7.67E-03 7.40E-04 3.29E-03 0.004

ng/dscm@7%O2 1.13E-02 1.09E-03 4.71E-03 0.006

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000573 0.0000000356 0.000000383 0.000

lb/mmBtuO2 7.45E-11 4.64E-12 4.83E-11 0.000

ng/dscm 5.84E-02 3.64E-03 3.90E-02 0.034

ng/dscm@7%O2 8.64E-02 5.38E-03 5.59E-02 0.049

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000103 0.0000000367 0.0000000742 0.000

lb/mmBtuO2 1.34E-11 4.78E-12 9.35E-12 0.000

ng/dscm 1.05E-02 3.75E-03 7.56E-03 0.007

ng/dscm@7%O2 1.55E-02 5.55E-03 1.08E-02 0.011

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.000002293 0.000000233 0.0000015481 0.000

lb/mmBtuO2 2.98E-10 3.04E-11 1.95E-10 0.000

ng/dscm 2.34E-01 2.38E-02 1.58E-01 0.139

ng/dscm@7%O2 3.46E-01 3.52E-02 2.26E-01 0.202

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.000000297 0.000000075 0.00000018907 0.000

lb/mmBtuO2 3.86E-11 9.77E-12 2.38E-11 0.000

ng/dscm 3.03E-02 7.66E-03 1.93E-02 0.019

ng/dscm@7%O2 4.48E-02 1.13E-02 2.77E-02 0.028

Compound: Total PCBs

Average

RunNumber 1 2 3

Mass_mg 0.000007092 0.0000091 0.000003859 0.000

lb/mmBtuO2 9.22E-10 1.19E-09 4.86E-10 0.000

Wednesday, February 16, 2011 Page 19 of 45
ng/dscm 7.23E-01 9.30E-01 3.93E-01 0.682

ng/dscm@7%O2 1.07E+00 1.38E+00 5.63E-01 1.004

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run DF/30B Run 1 DF/30B Run 2 DF/30B Run 3

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

ppm 0.00E+00 0.00E+00 0.00E+00 0.000

ppm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.253 0.282 0.279 0.271

Elb/hr 2.85E-04 3.19E-04 3.21E-04 0.000

lb/mmBtuO2 8.76E-05 9.52E-05 9.76E-05 0.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.26 0.289 0.286 0.278

Elb/hr 2.93E-04 3.27E-04 3.29E-04 0.000

lb/mmBtuO2 9.00E-05 9.76E-05 1.00E-04 0.000

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0003 0.0003 0.0015 0.001

Elb/hr 1.74E-07 1.65E-07 8.48E-07 0.000

lb/mmBtuO2 5.40E-08 4.78E-08 2.43E-07 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0017 0.0019 0.0167 0.007

Elb/hr 9.84E-07 1.05E-06 9.44E-06 0.000

lb/mmBtuO2 3.06E-07 3.03E-07 2.70E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.0001 0.0001 0.0006 0.000

Elb/hr 5.79E-08 5.51E-08 3.39E-07 0.000

lb/mmBtuO2 1.80E-08 1.59E-08 9.70E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0003 0.0004 0.0003 0.000

Wednesday, February 16, 2011 Page 20 of 45
Elb/hr 1.74E-07 2.20E-07 1.70E-07 0.000

lb/mmBtuO2 5.40E-08 6.38E-08 4.85E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0058 0.0055 0.0065 0.006

Elb/hr 3.36E-06 3.03E-06 3.67E-06 0.000

lb/mmBtuO2 1.04E-06 8.77E-07 1.05E-06 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 13 16.8 11.7 13.833

Elb/hr 7.53E-03 9.26E-03 6.61E-03 0.008

lb/mmBtuO2 2.34E-03 2.68E-03 1.89E-03 0.002

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.0395 0.0434 0.0468 0.043

Elb/hr 2.29E-05 2.39E-05 2.64E-05 0.000

lb/mmBtuO2 7.11E-06 6.92E-06 7.57E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.009 0.0098 0.0079 0.009

Elb/hr 5.21E-06 5.40E-06 4.46E-06 0.000

lb/mmBtuO2 1.62E-06 1.56E-06 1.28E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0058 0.0067 0.009 0.007

Elb/hr 3.36E-06 3.69E-06 5.09E-06 0.000

lb/mmBtuO2 1.04E-06 1.07E-06 1.46E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0012 0.0009 0.0093 0.004

Elb/hr 6.95E-07 4.96E-07 5.26E-06 0.000

lb/mmBtuO2 2.16E-07 1.43E-07 1.50E-06 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run Acid Gas R1 Acid Gas R2 Acid Gas R3

lb/mmBtuO2 2.53E-02 2.10E-02 1.87E-02 0.022

ppm 7.68E+00 6.39E+00 5.72E+00 6.597

ppm@7%O2 1.10E+01 9.14E+00 8.14E+00 9.427

Wednesday, February 16, 2011 Page 21 of 45
Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run Acid Gas R1 Acid Gas R2 Acid Gas R3

lb/mmBtuO2 1.17E-01 1.16E-01 1.14E-01 0.116

ppm 4.96E+01 4.94E+01 4.74E+01 48.800

ppm@7%O2 7.11E+01 7.06E+01 6.94E+01 70.367

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 5.3 13.6 11.7 10.200

Elb/hr 5.50E-03 1.42E-02 1.19E-02 0.011

gr/dscf 5.92E-04 1.50E-03 1.18E-03 0.001

lb/mmBtuO2 1.71E-03 4.27E-03 2.43E-03 0.003

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 2.2 8.6 5.7 5.500

Elb/hr 2.28E-03 8.97E-03 5.79E-03 0.006

gr/dscf 2.46E-04 9.46E-04 5.74E-04 0.001

lb/mmBtuO2 7.10E-04 2.70E-03 1.18E-03 0.002

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 1 7.6 5 4.533

Elb/hr 1.04E-03 7.93E-03 5.08E-03 0.005

gr/dscf 1.12E-04 8.36E-04 5.03E-04 0.000

lb/mmBtuO2 3.23E-04 2.39E-03 1.04E-03 0.001

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 5.7 3.9 2.8 4.133

Elb/hr 5.92E-03 4.07E-03 2.85E-03 0.004

gr/dscf 6.37E-04 4.29E-04 2.82E-04 0.000

lb/mmBtuO2 1.84E-03 1.23E-03 5.81E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 12 25.1 19.5 18.867

Elb/hr 1.25E-02 2.62E-02 1.98E-02 0.020

gr/dscf 1.34E-03 2.76E-03 1.96E-03 0.002

lb/mmBtuO2 3.87E-03 7.89E-03 4.05E-03 0.005

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 9.8 16.5 13.8 13.367

Wednesday, February 16, 2011 Page 22 of 45
Process Run Data

Elb/hr 1.02E-02 1.72E-02 1.40E-02 0.014

gr/dscf 1.10E-03 1.81E-03 1.39E-03 0.001

lb/mmBtuO2 3.16E-03 5.19E-03 2.87E-03 0.004

Wednesday, February 16, 2011 Page 23 of 45
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 418 Million Btus/hr 0

10 Heat Input 415.9 Million Btus/hr 0

11 Heat Input 419.4 Million Btus/hr 0

12 Heat Input 401.8 Million Btus/hr 0

13 Heat Input 400.3 Million Btus/hr 0

14 Heat Input 407.6 Million Btus/hr 0

15 Heat Input 399.6 Million Btus/hr 0

2 Heat Input 383.5 Million Btus/hr 0

3 Heat Input 391.3 Million Btus/hr 0

4 Heat Input 406.6 Million Btus/hr 0

5 Heat Input 395.5 Million Btus/hr 0

6 Heat Input 389.1 Million Btus/hr 0

7 Heat Input 415.3 Million Btus/hr 0

8 Heat Input 409.9 Million Btus/hr 0

9 Heat Input 412.8 Million Btus/hr 0

1 Average Heat Input 0 MMBtu/hr 0

10 Average Heat Input 0 MMBtu/hr 0

11 Average Heat Input 0 MMBtu/hr 0

12 Average Heat Input 0 MMBtu/hr 0

13 Average Heat Input 0 MMBtu/hr 0

14 Average Heat Input 0 MMBtu/hr 0

15 Average Heat Input 0 MMBtu/hr 0

2 Average Heat Input 0 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0

4 Average Heat Input 0 MMBtu/hr 0

5 Average Heat Input 0 MMBtu/hr 0

6 Average Heat Input 0 MMBtu/hr 0

7 Average Heat Input 0 MMBtu/hr 0

8 Average Heat Input 0 MMBtu/hr 0

9 Average Heat Input 0 MMBtu/hr 0

1 Steam Output 0 1000 lb steam/hr 0

10 Steam Output 0 1000 lb steam/hr 0

11 Steam Output 0 1000 lb steam/hr 0

Wednesday, February 16, 2011 Page 24 of 45
12 Steam Output 0 1000 lb steam/hr 0

13 Steam Output 0 1000 lb steam/hr 0

14 Steam Output 0 1000 lb steam/hr 0

15 Steam Output 0 1000 lb steam/hr 0

2 Steam Output 0 1000 lb steam/hr 0

3 Steam Output 0 1000 lb steam/hr 0

4 Steam Output 0 1000 lb steam/hr 0

5 Steam Output 0 1000 lb steam/hr 0

6 Steam Output 0 1000 lb steam/hr 0

7 Steam Output 0 1000 lb steam/hr 0

8 Steam Output 0 1000 lb steam/hr 0

9 Steam Output 0 1000 lb steam/hr 0

1 Fuel Oil Firing Rate 0 0

10 Fuel Oil Firing Rate 0 0

11 Fuel Oil Firing Rate 0 0

12 Fuel Oil Firing Rate 0 0

13 Fuel Oil Firing Rate 0 0

14 Fuel Oil Firing Rate 0 0

15 Fuel Oil Firing Rate 0 0

2 Fuel Oil Firing Rate 0 0

3 Fuel Oil Firing Rate 0 0

4 Fuel Oil Firing Rate 0 0

5 Fuel Oil Firing Rate 0 0

6 Fuel Oil Firing Rate 0 0

7 Fuel Oil Firing Rate 0 0

8 Fuel Oil Firing Rate 0 0

9 Fuel Oil Firing Rate 0 0

1 Standard Pressure 1 atm 0

10 Standard Pressure 0 atm 0

11 Standard Pressure 0 atm 0

12 Standard Pressure 0 atm 0

13 Standard Pressure 0 atm 0

14 Standard Pressure 0 atm 0

15 Standard Pressure 0 atm 0

2 Standard Pressure 0 atm 0

3 Standard Pressure 0 atm 0

Wednesday, February 16, 2011 Page 25 of 45
4 Standard Pressure 0 atm 0

5 Standard Pressure 0 atm 0

6 Standard Pressure 0 atm 0

7 Standard Pressure 0 atm 0

8 Standard Pressure 0 atm 0

9 Standard Pressure 0 atm 0

1 Standard Temperature 68 Deg F 0

10 Standard Temperature 0 Deg F 0

11 Standard Temperature 0 Deg F 0

12 Standard Temperature 0 Deg F 0

13 Standard Temperature 0 Deg F 0

14 Standard Temperature 0 Deg F 0

15 Standard Temperature 0 Deg F 0

2 Standard Temperature 0 Deg F 0

3 Standard Temperature 0 Deg F 0

4 Standard Temperature 0 Deg F 0

5 Standard Temperature 0 Deg F 0

6 Standard Temperature 0 Deg F 0

7 Standard Temperature 0 Deg F 0

8 Standard Temperature 0 Deg F 0

9 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 32 MW 0

10 Unit Gross Electrical Output 31.9 MW 0

11 Unit Gross Electrical Output 32.1 MW 0

12 Unit Gross Electrical Output 30.3 MW 0

13 Unit Gross Electrical Output 30.1 MW 0

14 Unit Gross Electrical Output 30.5 MW 0

15 Unit Gross Electrical Output 30 MW 0

2 Unit Gross Electrical Output 28.2 MW 0

3 Unit Gross Electrical Output 28.9 MW 0

4 Unit Gross Electrical Output 30.7 MW 0

5 Unit Gross Electrical Output 29.8 MW 0

6 Unit Gross Electrical Output 29 MW 0

7 Unit Gross Electrical Output 31.8 MW 0

8 Unit Gross Electrical Output 31 MW 0

9 Unit Gross Electrical Output 31.1 MW 0

Wednesday, February 16, 2011 Page 26 of 45
APCD Run Data

Process Lab Run Data

1 Unit Net Electric Generation 29.9 MWh 0

10 Unit Net Electric Generation 29.7 MWh 0

11 Unit Net Electric Generation 29.9 MWh 0

12 Unit Net Electric Generation 28.1 MWh 0

13 Unit Net Electric Generation 27.9 MWh 0

14 Unit Net Electric Generation 28.3 MWh 0

15 Unit Net Electric Generation 27.8 MWh 0

2 Unit Net Electric Generation 26 MWh 0

3 Unit Net Electric Generation 26.7 MWh 0

4 Unit Net Electric Generation 28.6 MWh 0

5 Unit Net Electric Generation 27.6 MWh 0

6 Unit Net Electric Generation 26.8 MWh 0

7 Unit Net Electric Generation 29.6 MWh 0

8 Unit Net Electric Generation 28.9 MWh 0

9 Unit Net Electric Generation 29 MWh 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 19509 Btu/lb

1 Fuel Moisture 0 %

1 Fuel Mercury Content 8E-06 ppm

1 Fuel Cadmium Content 0 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 0.003 ppm

1 Fuel Arsenic Content 0.0006 ppm

1 Fuel Chromium Content 0.0008 ppm

1 Fuel Beryllium Content 0.0002 ppm

1 Fuel Lead Content 0.001 ppm

1 Fuel Manganese Content 0.002 ppm

1 Fuel Chlorine Content 0.008 ppm

1 Fuel Fluorine Content 0 ppm

Wednesday, February 16, 2011 Page 27 of 45
Sampling / Stack Data Results Detail

Location Stack Exit - 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

Wednesday, February 16, 2011 Page 28 of 45
Location Stack Exit - Method 23

Average

Run Number 1 2 3

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

Run Start Time 12:10:00 AM 9:00:00 AM 12:10:00 AM

Run Finish Time 8:27:00 AM 5:15:00 PM 11:35:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 485 480 480

Nozzle Diameter, inches 0.38 0.38 0.38 0.380

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 29.3 29.3 29.3 29.300

Average Orifice Meter Differential, inches H2O 1.56 1.57 1.56 1.563

Dry Gas Meter Volume Sampled, cubic feet 345.588 353.310 350.034 349.644

Average Dry Gas Meter Temperature, °F 64.70 77.90 71.71 71.437

Dry Gas Meter Volume Sampled, dscf 346.675 345.732 346.506 346.304

Total Moisture Liquid collected, g 569.6 555.4 593.2 572.733

Volume of Water Vapor, standard cubic feet 26.81 26.14 27.92 26.957

Moisture Content of Stack Gas, % 7.18 7.03 7.46 7.223

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

Dry Mole Fraction 0.9282 0.9297 0.9254 0.928

Carbon Dioxide, % 7.4 7.4 7.5 7.433

Oxygen, % 11.5 11.5 11.2 11.400

Carbon Monoxide & Nitrogen, % 81.1 81.1 81.3 81.167

Fuel Factor 1.27 1.27 1.29

Dry Molecular Weight, lb/lb-Mole 29.64 29.64 29.65 29.643

Wet Molecular weight, lb/lb-Mole 28.80 28.82 28.78 28.800

Flue Gas Static Pressure, inches of H2O -0.05 -0.05 -0.05 -0.050

Absolute Flue Gas Pressure, inches of Mercury 29.30 29.30 29.30 29.300

Average Stack Gas Temperature, °F 269.79 269.19 271.78 270.253

Average Velocity Head, inches of H2O 0.1265522425

96508

0.127398901

322278

0.126048984

321641

0.127

Average Stack Gas Velocity, feet/second 23.76 23.82 23.75 23.777

Stack Cross-Sectional Area, square feet 1.227 1.227 1.227 1.227

Dry Volumetric Flow Rate, dry scfm 1,150.3 1,156.1 1,143.3 1,149.900

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,749.2 1,753.6 1,748.5 1,750.433

Percent Isokinetic of Sampling Rate, % 96.8 97.1 98.4 97.433

Percent Excess Air, % 116.0 116.0 109.1 113.700

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

Round Duct Diameter, inches 15 15 15

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

Wednesday, February 16, 2011 Page 29 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 30 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 31 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 32 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 33 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 34 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 35 of 45
Location Stack Exit - Method 3A CO2 3 6 9

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

Wednesday, February 16, 2011 Page 36 of 45
Location Stack Exit - Method 3A CO2 3 6 9 12

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

Wednesday, February 16, 2011 Page 37 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 38 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 39 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 40 of 45
Location Stack Exit - Method 3A O2 3 6 9

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

Wednesday, February 16, 2011 Page 41 of 45
Location Stack Exit - Method 3A O2 3 6 9 12

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

Wednesday, February 16, 2011 Page 42 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 43 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 44 of 45
Location Stack Exit - 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

Wednesday, February 16, 2011 Page 45 of 45