Name: Jon Hays

Title: Environmental Specialist

Company: Duke Energy

Sign Date: 9/2/2010

Name: Pat Ford

Title: project manager

Company: AECOM

Sign Date: 8/26/2010

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.

Tuesday, February 01, 2011 Page 1 of 30
9/2/2010

Facility Information:

IN_Wabash River Combined Cycle Station 

450 Bolton Road

West Terre Haute IN 47885

Contact: Jon Hays

Phone: 317-838-4445

Fax: 317-8382490

Email: jon.hays@duke.energy.com

Testing Company:

AECOM

2 Technology Park Drive

Westford MA 01886

Contact: Patrick Ford

Phone: 978-589-3427

Fax: 978-589-3100

Email: pat.ford@aecom.com

Air Permit Number:

167-26486-00147

Permitted Source ID/Name:

Unit 1 Combustion Turbine

Permitted Maximum Process Rate:

1709.1

Max. Normal Operation Process Rate:

1709.1

Target Process Test Rate

1709.1

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

 process flow diagram:

This description should describe the process and associated controls to differentiate this facility from, or document 

similarity with others of same SCC.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 1816700147 FRS #: 330015654589

SCC / Description 20100201 Internal Combustion Engines - Electric Generation - Natural Gas - 

Turbine 

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 216 0 0 0 8 2 4 16

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 60 0

Stack Exit Carbon Monoxide Method 10 3 120 0

Stack Exit 2,3,7,8-TCDD Method 23 3 416 0

Stack Exit 1,2,3,7,8-PeCDD Method 23 3 416 0

Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 416 0

Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 416 0

Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 416 0

Tuesday, February 01, 2011 Page 2 of 30
9/2/2010

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

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

of request AND approval, including dates.

Stack Exit 1,2,3,4,6,7,8-HpCDD Method 23 3 416 0

Stack Exit OCDD Method 23 3 416 0

Stack Exit 2,3,7,8-TCDF Method 23 3 416 0

Stack Exit 1,2,3,7,8-PeCDF Method 23 3 416 0

Stack Exit 2,3,4,7,8-PeCDF Method 23 3 416 0

Stack Exit 1,2,3,4,7,8-HxCDF Method 23 3 416 0

Stack Exit 1,2,3,6,7,8-HxCDF Method 23 3 416 0

Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 416 0

Stack Exit 1,2,3,7,8,9-HxCDF Method 23 3 416 0

Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 416 0

Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 416 0

Stack Exit OCDF Method 23 3 416 0

Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 416 0

Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 416 0

Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 416 0

Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 416 0

Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 416 0

Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 416 0

Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 416 0

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

HxCB (PCBs156/157)

Stack Exit Method 23 3 416 0

Stack Exit 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 416 0

Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 416 0

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

(PCB189)

Stack Exit Method 23 3 416 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26A 3 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 120 0

Total PM2.5 OTM - 27/28 3 280 0 R1 299 Min, R2 329 

Min, R3 318 Min

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 280 0 R1 299 Min, R2 329 

Min, R3 318 Min

Stack Exit

Organic Condensible 

Particulate

OTM - 27/28 3 280 0 R1 299 Min, R2 329 

Min, R3 318 Min

Stack Exit

Filterable PM2.5 OTM - 27/28 3 280 0 R1 299 Min, R2 329 

Min, R3 318 Min

Stack Exit

Stack Exit Nickel Method 29 3 160 0

Stack Exit Manganese Method 29 3 160 0

Stack Exit Filterable Particulate Method 29 3 160 0

Stack Exit Antimony Method 29 3 160 0

Stack Exit Beryllium Method 29 3 160 0

Stack Exit Arsenic Method 29 3 160 0

Stack Exit Cobalt Method 29 3 160 0

Stack Exit Chromium Method 29 3 160 0

Stack Exit Selenium Method 29 3 160 0

Stack Exit Cadmium Method 29 3 160 0

Stack Exit Lead Method 29 3 160 0

Stack Exit O2 Method 3A O2 3 60 0

Stack Exit Co2 Method 3A CO2 3 60 0

Stack Exit Sulfur Dioxide Method 6C 3 60 0

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

Tuesday, February 01, 2011 Page 3 of 30
9/2/2010 The following describes any modifications and/or deviations to the applicable test 

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

of request AND approval, including dates.

Tuesday, February 01, 2011 Page 4 of 30
9/2/2010

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 6/28/2010 6/29/2010 6/30/2010

Run Start Time 9:08:00 AM 7:45:00 

AM

7:43:00 AM

Run Finish Time 4:32:00 PM 2:51:00 

PM

2:51:00 PM

Net Run Time, minutes 416 416 416

Dry Gas Meter Volume Sampled, dscf 299.239 296.408 299.996 298.548

Moisture Content of Stack Gas, % 14.62 13.48 12.03 13.377

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

Carbon Dioxide, % 8.3 9 9.3 8.867

Oxygen, % 14.1 13.5 13.5 13.700

Average Stack Gas Temperature, °F 381.38 380.73 380.42 380.843

Dry Volumetric Flow Rate, dry scfm 743,525.9 743,678.1 756,916.2 748,040.067

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,424,364.8 1,398,561.

6

1,390,927.6 1,404,618.00

0

Percent Isokinetic of Sampling Rate, % 102.4 101.4 100.8 101.533

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc 2341 2341 2341 2,341.000

Tuesday, February 01, 2011 Page 5 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 6 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 7 of 30
9/2/2010

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 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

Tuesday, February 01, 2011 Page 8 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 9 of 30
9/2/2010

Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 3.27E+00 2.95E+00 2.76E+00 2.993

lb/mmBtuCO2 1.85E-03 1.65E-03 1.54E-03 0.002

ppm 1.01E+00 9.02E-01 8.37E-01 0.916

ppm@7%O2 1.99E+00 1.78E+00 1.65E+00 1.807

Location: Stack Exit - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000037 0.0000000039 0.0000000056 0.000

Elb/hr 1.22E-09 1.29E-09 1.87E-09 0.000

lb/mmBtuCO2 7.69E-13 7.55E-13 1.04E-12 0.000

ug/dscm 4.37E-07 4.65E-07 6.59E-07 0.000

ug/dscm@7%O2 8.93E-07 8.73E-07 1.24E-06 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000022 0.0000000044 0.0000000026 0.000

Elb/hr 7.23E-10 1.46E-09 8.68E-10 0.000

lb/mmBtuCO2 4.57E-13 8.51E-13 4.81E-13 0.000

ug/dscm 2.60E-07 5.24E-07 3.06E-07 0.000

ug/dscm@7%O2 5.31E-07 9.84E-07 5.75E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000029 0.0000000025 0.0000000035 0.000

Elb/hr 9.53E-10 8.30E-10 1.17E-09 0.000

lb/mmBtuCO2 6.03E-13 4.84E-13 6.47E-13 0.000

ug/dscm 3.42E-07 2.98E-07 4.12E-07 0.000

ug/dscm@7%O2 6.99E-07 5.60E-07 7.74E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000023 0.0000000022 0.0000000031 0.000

Elb/hr 7.56E-10 7.30E-10 1.03E-09 0.000

lb/mmBtuCO2 4.78E-13 4.26E-13 5.73E-13 0.000

ug/dscm 2.71E-07 2.62E-07 3.65E-07 0.000

ug/dscm@7%O2 5.54E-07 4.92E-07 6.86E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000022 0.0000000012 0.0000000016 0.000

Elb/hr 7.23E-10 3.98E-10 5.34E-10 0.000

Tuesday, February 01, 2011 Page 10 of 30
9/2/2010

lb/mmBtuCO2 4.57E-13 2.32E-13 2.96E-13 0.000

ug/dscm 2.60E-07 1.43E-07 1.88E-07 0.000

ug/dscm@7%O2 5.31E-07 2.69E-07 3.53E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000023 0.0000000021 0.000000003 0.000

Elb/hr 7.56E-10 6.97E-10 1.00E-09 0.000

lb/mmBtuCO2 4.78E-13 4.06E-13 5.55E-13 0.000

ug/dscm 2.71E-07 2.50E-07 3.53E-07 0.000

ug/dscm@7%O2 5.54E-07 4.70E-07 6.63E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000011 0.0000000011 0.0000000014 0.000

Elb/hr 3.62E-10 3.65E-10 4.67E-10 0.000

lb/mmBtuCO2 2.29E-13 2.13E-13 2.59E-13 0.000

ug/dscm 1.30E-07 1.31E-07 1.65E-07 0.000

ug/dscm@7%O2 2.66E-07 2.46E-07 3.10E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000023 0.0000000022 0.000000003 0.000

Elb/hr 7.56E-10 7.30E-10 1.00E-09 0.000

lb/mmBtuCO2 4.78E-13 4.26E-13 5.55E-13 0.000

ug/dscm 2.71E-07 2.62E-07 3.53E-07 0.000

ug/dscm@7%O2 5.54E-07 4.92E-07 6.63E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000014 0.0000000013 0.0000000017 0.000

Elb/hr 4.60E-10 4.31E-10 5.67E-10 0.000

lb/mmBtuCO2 2.91E-13 2.52E-13 3.14E-13 0.000

ug/dscm 1.65E-07 1.55E-07 2.00E-07 0.000

ug/dscm@7%O2 3.37E-07 2.91E-07 3.76E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000024 0.0000000021 0.0000000027 0.000

Elb/hr 7.89E-10 6.97E-10 9.01E-10 0.000

lb/mmBtuCO2 4.99E-13 4.06E-13 4.99E-13 0.000

ug/dscm 2.83E-07 2.50E-07 3.18E-07 0.000

ug/dscm@7%O2 5.78E-07 4.70E-07 5.97E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000018 0.0000000018 0.0000000023 0.000

Elb/hr 5.92E-10 5.97E-10 7.68E-10 0.000

Tuesday, February 01, 2011 Page 11 of 30
9/2/2010

lb/mmBtuCO2 3.74E-13 3.48E-13 4.25E-13 0.000

ug/dscm 2.12E-07 2.14E-07 2.71E-07 0.000

ug/dscm@7%O2 4.33E-07 4.02E-07 5.09E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000109 0.0000000111 0.0000000154 0.000

Elb/hr 3.58E-09 3.68E-09 5.14E-09 0.000

lb/mmBtuCO2 2.26E-12 2.15E-12 2.85E-12 0.000

ug/dscm 1.29E-06 1.32E-06 1.81E-06 0.000

ug/dscm@7%O2 2.64E-06 2.48E-06 3.40E-06 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000007 0.000000054 0.00000033 0.000

Elb/hr 2.30E-08 1.79E-08 1.10E-07 0.000

lb/mmBtuCO2 1.45E-11 1.04E-11 6.10E-11 0.000

ug/dscm 8.26E-06 6.43E-06 3.89E-05 0.000

ug/dscm@7%O2 1.69E-05 1.21E-05 7.31E-05 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000015 0.000000131 0.00000092 0.000

Elb/hr 4.93E-08 4.35E-08 3.07E-07 0.000

lb/mmBtuCO2 3.12E-11 2.53E-11 1.70E-10 0.000

ug/dscm 1.77E-05 1.56E-05 1.08E-04 0.000

ug/dscm@7%O2 3.62E-05 2.93E-05 2.03E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000014 0.000000015 0.0000000579 0.000

Elb/hr 4.60E-09 4.98E-09 1.93E-08 0.000

lb/mmBtuCO2 2.91E-12 2.90E-12 1.07E-11 0.000

ug/dscm 1.65E-06 1.79E-06 6.82E-06 0.000

ug/dscm@7%O2 3.37E-06 3.36E-06 1.28E-05 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000114 0.0000000109 0.0000000469 0.000

Elb/hr 3.75E-09 3.62E-09 1.57E-08 0.000

lb/mmBtuCO2 2.37E-12 2.11E-12 8.68E-12 0.000

ug/dscm 1.35E-06 1.30E-06 5.52E-06 0.000

ug/dscm@7%O2 2.76E-06 2.44E-06 1.04E-05 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000364 0.000000288 0.00000191 0.000

Elb/hr 1.20E-07 9.56E-08 6.37E-07 0.000

Tuesday, February 01, 2011 Page 12 of 30
9/2/2010

lb/mmBtuCO2 7.56E-11 5.57E-11 3.53E-10 0.000

ug/dscm 4.30E-05 3.43E-05 2.25E-04 0.000

ug/dscm@7%O2 8.79E-05 6.44E-05 4.23E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000129 0.0000000121 0.0000000314 0.000

Elb/hr 4.24E-09 4.02E-09 1.05E-08 0.000

lb/mmBtuCO2 2.68E-12 2.34E-12 5.81E-12 0.000

ug/dscm 1.52E-06 1.44E-06 3.70E-06 0.000

ug/dscm@7%O2 3.11E-06 2.70E-06 6.95E-06 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000012 0.0000000011 0.0000000015 0.000

Elb/hr 3.94E-10 3.65E-10 5.01E-10 0.000

lb/mmBtuCO2 2.49E-13 2.13E-13 2.77E-13 0.000

ug/dscm 1.42E-07 1.31E-07 1.77E-07 0.000

ug/dscm@7%O2 2.90E-07 2.46E-07 3.32E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000002 0.0000000018 0.0000000023 0.000

Elb/hr 6.57E-10 5.97E-10 7.68E-10 0.000

lb/mmBtuCO2 4.16E-13 3.48E-13 4.25E-13 0.000

ug/dscm 2.36E-07 2.14E-07 2.71E-07 0.000

ug/dscm@7%O2 4.82E-07 4.02E-07 5.09E-07 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000045 0.0000000052 0.000000006 0.000

Elb/hr 1.48E-09 1.73E-09 2.00E-09 0.000

lb/mmBtuCO2 9.35E-13 1.01E-12 1.11E-12 0.000

ug/dscm 5.31E-07 6.20E-07 7.06E-07 0.000

ug/dscm@7%O2 1.09E-06 1.16E-06 1.33E-06 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000094 0.0000000031 0.0000000036 0.000

Elb/hr 3.09E-09 1.03E-09 1.20E-09 0.000

lb/mmBtuCO2 1.95E-12 6.00E-13 6.66E-13 0.000

ug/dscm 1.11E-06 3.69E-07 4.24E-07 0.000

ug/dscm@7%O2 2.27E-06 6.93E-07 7.96E-07 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000075 0.0000000173 0.000000025 0.000

Elb/hr 2.47E-08 5.74E-09 8.34E-09 0.000

Tuesday, February 01, 2011 Page 13 of 30
9/2/2010

lb/mmBtuCO2 1.56E-11 3.35E-12 4.62E-12 0.000

ug/dscm 8.85E-06 2.06E-06 2.94E-06 0.000

ug/dscm@7%O2 1.81E-05 3.87E-06 5.52E-06 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000013 0.0000000125 0.0000000206 0.000

Elb/hr 4.27E-09 4.15E-09 6.88E-09 0.000

lb/mmBtuCO2 2.70E-12 2.42E-12 3.81E-12 0.000

ug/dscm 1.53E-06 1.49E-06 2.43E-06 0.000

ug/dscm@7%O2 3.13E-06 2.80E-06 4.56E-06 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000068 0.0000000283 0.000000122 0.000

Elb/hr 2.23E-08 9.39E-09 4.07E-08 0.000

lb/mmBtuCO2 1.41E-11 5.48E-12 2.26E-11 0.000

ug/dscm 8.03E-06 3.37E-06 1.44E-05 0.000

ug/dscm@7%O2 1.64E-05 6.33E-06 2.70E-05 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000203 0.0000000165 0.0000000264 0.000

Elb/hr 6.67E-09 5.48E-09 8.81E-09 0.000

lb/mmBtuCO2 4.22E-12 3.19E-12 4.88E-12 0.000

ug/dscm 2.40E-06 1.97E-06 3.11E-06 0.000

ug/dscm@7%O2 4.91E-06 3.70E-06 5.84E-06 0.000

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000008 0.0000000078 0.000000015 0.000

Elb/hr 2.63E-09 2.59E-09 5.01E-09 0.000

lb/mmBtuCO2 1.66E-12 1.51E-12 2.77E-12 0.000

ug/dscm 9.44E-07 9.29E-07 1.77E-06 0.000

ug/dscm@7%O2 1.93E-06 1.75E-06 3.32E-06 0.000

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000042 0.0000000057 0.0000000048 0.000

Elb/hr 1.38E-09 1.89E-09 1.60E-09 0.000

lb/mmBtuCO2 8.73E-13 1.10E-12 8.88E-13 0.000

ug/dscm 4.96E-07 6.79E-07 5.65E-07 0.000

ug/dscm@7%O2 1.01E-06 1.28E-06 1.06E-06 0.000

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Tuesday, February 01, 2011 Page 14 of 30
9/2/2010

Elb/hr 5.86E-01 4.42E-01 1.40E+00 0.809

lb/mmBtuCO2 3.32E-04 2.48E-04 7.85E-04 0.000

ppm 1.15E-01 8.59E-02 2.71E-01 0.157

ppm@7%O2 2.26E-01 1.70E-01 5.34E-01 0.310

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.51 0.52 0.43 0.487

Elb/hr 5.20E-01 5.30E-01 4.44E-01 0.498

lb/mmBtuCO2 2.94E-04 3.08E-04 2.49E-04 0.000

mg/dscm 1.88E-01 1.95E-01 1.57E-01 0.180

mg/dscm@7%O2 3.71E-01 3.86E-01 3.10E-01 0.356

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.31 0.31 0.26 0.293

Elb/hr 3.16E-01 3.16E-01 2.68E-01 0.300

lb/mmBtuCO2 1.79E-04 1.83E-04 1.50E-04 0.000

mg/dscm 1.14E-01 1.16E-01 9.48E-02 0.108

mg/dscm@7%O2 2.25E-01 2.29E-01 1.87E-01 0.214

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00003 0 0.00021 0.000

Elb/hr 2.31E-05 0.00E+00 1.65E-04 0.000

gr/dscf 3.57E-09 0.00E+00 2.51E-08 0.000

gr/dscf@7%O2 6.94E-09 0.00E+00 4.91E-08 0.000

lb/mmBtuCO2 1.32E-08 0.00E+00 9.21E-08 0.000

ug/dscm 8.16E-03 0.00E+00 5.74E-02 0.022

ug/dscm@7%O2 1.59E-02 0.00E+00 1.12E-01 0.043

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00045 0.00089 0.00119 0.001

Elb/hr 3.47E-04 6.97E-04 9.34E-04 0.001

gr/dscf 5.35E-08 1.08E-07 1.42E-07 0.000

gr/dscf@7%O2 1.04E-07 2.09E-07 2.78E-07 0.000

lb/mmBtuCO2 1.98E-07 3.96E-07 5.22E-07 0.000

ug/dscm 1.22E-01 2.48E-01 3.25E-01 0.232

ug/dscm@7%O2 2.37E-01 4.79E-01 6.36E-01 0.451

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00001 0.000017 0.000014 0.000

Elb/hr 7.70E-06 1.33E-05 1.10E-05 0.000

gr/dscf 1.19E-09 2.07E-09 1.67E-09 0.000

Tuesday, February 01, 2011 Page 15 of 30
9/2/2010

gr/dscf@7%O2 2.31E-09 4.00E-09 3.27E-09 0.000

lb/mmBtuCO2 4.39E-09 7.56E-09 6.14E-09 0.000

ug/dscm 2.72E-03 4.74E-03 3.82E-03 0.004

ug/dscm@7%O2 5.29E-03 9.15E-03 7.48E-03 0.007

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0001 0.00011 0.00002 0.000

Elb/hr 7.70E-05 8.62E-05 1.57E-05 0.000

gr/dscf 1.19E-08 1.34E-08 2.39E-09 0.000

gr/dscf@7%O2 2.31E-08 2.59E-08 4.68E-09 0.000

lb/mmBtuCO2 4.39E-08 4.89E-08 8.77E-09 0.000

ug/dscm 2.72E-02 3.07E-02 5.46E-03 0.021

ug/dscm@7%O2 5.29E-02 5.93E-02 1.07E-02 0.041

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0037 0.0041 0.0043 0.004

Elb/hr 2.85E-03 3.21E-03 3.38E-03 0.003

gr/dscf 4.40E-07 4.99E-07 5.13E-07 0.000

gr/dscf@7%O2 8.55E-07 9.63E-07 1.00E-06 0.000

lb/mmBtuCO2 1.63E-06 1.82E-06 1.89E-06 0.000

ug/dscm 1.01E+00 1.14E+00 1.17E+00 1.107

ug/dscm@7%O2 1.96E+00 2.20E+00 2.29E+00 2.150

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00115 0.00002 0.00006 0.000

Elb/hr 8.86E-04 1.57E-05 4.71E-05 0.000

gr/dscf 1.37E-07 2.43E-09 7.16E-09 0.000

gr/dscf@7%O2 2.66E-07 4.69E-09 1.40E-08 0.000

lb/mmBtuCO2 5.05E-07 8.90E-09 2.63E-08 0.000

ug/dscm 3.13E-01 5.57E-03 1.64E-02 0.112

ug/dscm@7%O2 6.08E-01 1.08E-02 3.21E-02 0.217

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 42.7 40.8 52.4 45.300

Elb/hr 3.29E+01 3.20E+01 4.11E+01 35.333

gr/dscf 5.08E-03 4.97E-03 6.26E-03 0.005

gr/dscf@7%O2 9.88E-03 9.59E-03 1.23E-02 0.011

lb/mmBtuCO2 1.88E-02 1.82E-02 2.30E-02 0.020

ug/dscm 1.16E+04 1.14E+04 1.43E+04 12,433.333

ug/dscm@7%O2 2.26E+04 2.20E+04 2.80E+04 24,200.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.0005 0.0003 0.0008 0.001

Elb/hr 3.85E-04 2.35E-04 6.28E-04 0.000

Tuesday, February 01, 2011 Page 16 of 30
9/2/2010

gr/dscf 5.94E-08 3.65E-08 9.55E-08 0.000

gr/dscf@7%O2 1.15E-07 7.05E-08 1.87E-07 0.000

lb/mmBtuCO2 2.20E-07 1.33E-07 3.51E-07 0.000

ug/dscm 1.36E-01 8.36E-02 2.19E-01 0.146

ug/dscm@7%O2 2.64E-01 1.61E-01 4.29E-01 0.285

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0038 0.0032 0.0034 0.003

Elb/hr 2.93E-03 2.51E-03 2.67E-03 0.003

gr/dscf 4.52E-07 3.90E-07 4.06E-07 0.000

gr/dscf@7%O2 8.79E-07 7.53E-07 7.95E-07 0.000

lb/mmBtuCO2 1.67E-06 1.42E-06 1.49E-06 0.000

ug/dscm 1.03E+00 8.92E-01 9.29E-01 0.950

ug/dscm@7%O2 2.00E+00 1.72E+00 1.82E+00 1.847

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.00368 0.00328 0.0027 0.003

Elb/hr 2.84E-03 2.57E-03 2.12E-03 0.003

gr/dscf 4.38E-07 3.99E-07 3.22E-07 0.000

gr/dscf@7%O2 8.51E-07 7.70E-07 6.30E-07 0.000

lb/mmBtuCO2 1.62E-06 1.46E-06 1.18E-06 0.000

ug/dscm 1.00E+00 9.14E-01 7.38E-01 0.884

ug/dscm@7%O2 1.94E+00 1.76E+00 1.44E+00 1.713

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0305 0.0402 0.02859 0.033

Elb/hr 2.35E-02 3.15E-02 2.24E-02 0.026

gr/dscf 3.63E-06 4.89E-06 3.41E-06 0.000

gr/dscf@7%O2 7.06E-06 9.44E-06 6.68E-06 0.000

lb/mmBtuCO2 1.34E-05 1.79E-05 1.25E-05 0.000

ug/dscm 8.30E+00 1.12E+01 7.81E+00 9.103

ug/dscm@7%O2 1.61E+01 2.16E+01 1.53E+01 17.667

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 1.81E+02 1.63E+02 1.61E+02 168.333

lb/mmBtuCO2 1.02E-01 9.40E-02 9.13E-02 0.096

ppm 2.46E+01 2.24E+01 2.16E+01 22.867

ppm@7%O2 4.85E+01 4.43E+01 4.27E+01 45.167

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 1.22E+02 1.27E+02 1.27E+02 125.333

Tuesday, February 01, 2011 Page 17 of 30
9/2/2010

Process Run Data

lb/mmBtuCO2 6.90E-02 7.35E-02 7.18E-02 0.071

ppm 2.31E+01 2.44E+01 2.37E+01 23.733

ppm@7%O2 4.55E+01 4.82E+01 4.69E+01 46.867

Location: Stack Exit - OTM - 27/28

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 9.8 11.2 9 10.000

Elb/hr 8.47E+00 9.21E+00 7.46E+00 8.380

gr/dscf 1.32E-03 1.37E-03 1.16E-03 0.001

gr/dscf@7%O2 2.57E-03 2.64E-03 2.27E-03 0.002

lb/mmBtuCO2 4.86E-03 5.02E-03 4.25E-03 0.005

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 13.4 15.3 5.7 11.467

Elb/hr 1.16E+01 1.26E+01 4.73E+00 9.643

gr/dscf 1.80E-03 1.88E-03 7.33E-04 0.001

gr/dscf@7%O2 3.50E-03 3.63E-03 1.44E-03 0.003

lb/mmBtuCO2 6.65E-03 6.85E-03 2.69E-03 0.005

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 17.2 19.5 16.6 17.767

Elb/hr 1.49E+01 1.60E+01 1.38E+01 14.900

gr/dscf 2.31E-03 2.39E-03 2.13E-03 0.002

gr/dscf@7%O2 4.49E-03 4.61E-03 4.17E-03 0.004

lb/mmBtuCO2 8.54E-03 8.73E-03 7.84E-03 0.008

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 38.4 44 29.3 37.233

Elb/hr 3.32E+01 3.62E+01 2.43E+01 31.233

gr/dscf 5.16E-03 5.39E-03 3.77E-03 0.005

gr/dscf@7%O2 1.00E-02 1.04E-02 7.38E-03 0.009

lb/mmBtuCO2 1.91E-02 1.97E-02 1.38E-02 0.018

Tuesday, February 01, 2011 Page 18 of 30
9/2/2010

Process Run Data

APCD Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 1772 Million Btus/hr 0 Run 1 PM/Metals

2 Heat Input 0 Million Btus/hr 0

3 Heat Input 0 Million Btus/hr 0

4 Heat Input 1753.9 Million Btus/hr 0 Run 2 PM/Metals

1 Unit Gross Electrical Output 166 MW 0 Run 1 PM/Metals

4 Unit Gross Electrical Output 165 MW 0 Run 2 PM/Metals

5 Heat Input 1724.6 Million Btus/hr 0 Run 3 PM/Metals

5 Unit Gross Electrical Output 160 MW 0 Run 3 PM/Metals

6 Heat Input 1828.1 Million Btus/hr 0 Run 1 Acid Gases

6 Unit Gross Electrical Output 164 MW 0 Run 1 Acid Gases

7 Heat Input 1801.8 Million Btus/hr 0 Run 2 Acid Gases

7 Unit Gross Electrical Output 164 MW 0 Run 2 Acid Gases

8 Heat Input 1922.7 Million Btus/hr 0 Run 3 Acid Gases

8 Unit Gross Electrical Output 164 MW 0 Run 3 Acid Gases

9 Heat Input 1737.7 Million Btus/hr Run 1 Non-Dioxin 

Organics

0

9 Unit Gross Electrical Output 163 MW Run 1 Non-Dioxin 

Organics

0

10 Heat Input 1725.9 Million Btus/hr Run 2 Non-Dioxin 

Organics

0

10 Unit Gross Electrical Output 164 MW Run 2 Non-Dioxin 

Organics

0

11 Heat Input 1780.8 Million Btus/hr Run 3 Non-Dioxin 

Organics

0

11 Unit Gross Electrical Output 163 MW Run 3 Non-Dioxin 

Organics

0

12 Heat Input 1718.5 Million Btus/hr Run 1 Dioxin 

Organics

0

12 Unit Gross Electrical Output 167 MW Run 1 Dioxin 

Organics

0

13 Heat Input 1784.6 Million Btus/hr Run 2 Dioxin 

Organics

0

13 Unit Gross Electrical Output 168 MW Run 2 Dioxin 

Organics

0

14 Heat Input 1706.6 Million Btus/hr Run 3 Dioxin 

Organics

0

14 Unit Gross Electrical Output 168 MW Run 3 Dioxin 

Organics

0

Tuesday, February 01, 2011 Page 19 of 30
9/2/2010

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 List all emissions control devices in order of 

process flow. Choose from

0 0

1 drop down lists. If not on list add description and 

provide detailed

0 0

1 desription in section 5a. 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %

1 Ultimate/Proximate Analysis 0

1 Fuel Chlorine Content 0 mg/kg

1 Fuel Fluorine Content 0 mg/kg

1 Metals Content 0 mg/kg

Tuesday, February 01, 2011 Page 20 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 21 of 30
9/2/2010

Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 6/28/2010 6/29/2010 6/30/2010

Run Start Time 9:08:00 AM 7:45:00 AM 7:43:00 AM

Run Finish Time 4:32:00 PM 2:51:00 PM 2:51:00 PM

Net Traversing Points 64 64 64

Net Run Time, minutes 416 416 416

Nozzle Diameter, inches 0.21 0.21 0.21 0.210

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.016 1.016 1.016 1.016

Barometric Pressure, inches of Mercury 29.22 29.35 29.52 29.363

Average Orifice Meter Differential, inches H2O 1.82 1.78 1.77 1.790

Dry Gas Meter Volume Sampled, cubic feet 315.940 311.254 305.278 310.824

Average Dry Gas Meter Temperature, °F 95.67 95.05 80.97 90.563

Dry Gas Meter Volume Sampled, dscf 299.239 296.408 299.996 298.548

Total Moisture Liquid collected, g 1088.1 981.5 871.5 980.367

Volume of Water Vapor, standard cubic feet 51.22 46.20 41.02 46.147

Moisture Content of Stack Gas, % 14.62 13.48 12.03 13.377

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

Dry Mole Fraction 0.8538 0.8652 0.8797 0.866

Carbon Dioxide, % 8.3 9 9.3 8.867

Oxygen, % 14.1 13.5 13.5 13.700

Carbon Monoxide & Nitrogen, % 77.6 77.5 77.2 77.433

Fuel Factor 0.82 0.82 0.80

Dry Molecular Weight, lb/lb-Mole 29.89 29.98 30.03 29.967

Wet Molecular weight, lb/lb-Mole 28.15 28.37 28.58 28.367

Flue Gas Static Pressure, inches of H2O -0.97 -0.89 -0.76 -0.873

Absolute Flue Gas Pressure, inches of Mercury 29.15 29.28 29.46 29.297

Average Stack Gas Temperature, °F 381.38 380.73 380.42 380.843

Average Velocity Head, inches of H2O 1.6459382121

7781

1.607547958

94231

1.612445120

10911

1.622

Average Stack Gas Velocity, feet/second 93.29 91.60 91.10 91.997

Stack Cross-Sectional Area, square feet 254.469 254.469 254.469 254.469

Dry Volumetric Flow Rate, dry scfm 743,525.9 743,678.1 756,916.2 748,040.067

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,424,364.8 1,398,561.6 1,390,927.6 1,404,618.0

00

Percent Isokinetic of Sampling Rate, % 102.4 101.4 100.8 101.533

Percent Excess Air, % 220.8 194.0 196.2 203.667

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches 216 216 216

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw

Fc 2341 2341 2341 2,341.000

Tuesday, February 01, 2011 Page 22 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 23 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 24 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 25 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 26 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 27 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 28 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 29 of 30
9/2/2010

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

Tuesday, February 01, 2011 Page 30 of 30