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.

Tuesday, February 15, 2011 Page 1 of 48
Facility Information:

Harding Street

3700 S. Harding Street

Indianapolis IN 46217

Contact: Angelique Oliger

Phone: (317) 261-5852

Fax:

Email: angelique.oliger@aes.com

Testing Company:

URS Corporation

1600 Perimeter Park Dr.

Morrisville

Contact:Brad Justus

Phone: 919-461-1326

Fax: 919-461-1415

Email: Brad_Justus@urscorp.com

Air Permit Number:

990

Permitted Source ID/Name:

09 09

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:

Concentric firing, Dry Bottom, 527 MMBtu/hr

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 1809700033 FRS #: 110000396991

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 90.5 0 0 0 181 724 2 6

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 Formaldehyde Method 0011 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

Tuesday, February 15, 2011 Page 2 of 48
Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 480 0

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 Other TCDD Method 23 0

Stack Exit Other PeCDD Method 23 0

Stack Exit Other HxCDD Method 23 0

Stack Exit Other HpCDD Method 23 0

Stack Exit Other TCDF Method 23 0

Stack Exit Other PeCDF Method 23 0

Stack Exit Other HxCDF Method 23 0

Stack Exit Other HpCDF Method 23 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

Stack Exit Total TEQ Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26 3 180 0

Stack Exit Hydrogen Fluoride Method 26 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

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

Organic Condensible 

Particulate

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Tuesday, February 15, 2011 Page 3 of 48
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.

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total Particulate 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 Beryllium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Mercury Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Magnesium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Cobalt Method 29 3 360 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit Co2 Method 3A CO2 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Organic Condensible 

Particulate

Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Total Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Filterable Particulate Method 5 3 240 0

Filterable Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Tuesday, February 15, 2011 Page 4 of 48
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 3/9/2010 3/9/2010 3/10/2010

Run Start Time 4:05:00 AM 3:10:00 PM 12:00:00 AM

Run Finish Time 1:10:00 PM 11:30:00 

PM

3:15:00 AM

Net Run Time, minutes 485 480 195

Dry Gas Meter Volume Sampled, dscf 341.173 345.685 139.022 275.293

Moisture Content of Stack Gas, % 6.87 7.29 7.68 7.280

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

Carbon Dioxide, % 7.3 7.3 6.8 7.133

Oxygen, % 11.2 11.1 11.6 11.300

Average Stack Gas Temperature, °F 283.08 287.28 288.95 286.437

Dry Volumetric Flow Rate, dry scfm 95,190.6 95,338.9 94,463.4 94,997.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 148,004.0 148,674.0 149,076.1 148,584.700

Percent Isokinetic of Sampling Rate, % 94.6 96.7 98.9 96.733

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

Tuesday, February 15, 2011 Page 5 of 48
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 15, 2011 Page 6 of 48
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 15, 2011 Page 7 of 48
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

Tuesday, February 15, 2011 Page 8 of 48
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 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

Tuesday, February 15, 2011 Page 9 of 48
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

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

Tuesday, February 15, 2011 Page 10 of 48
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

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 15, 2011 Page 11 of 48
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 15, 2011 Page 12 of 48
Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 0.00E+00 -5.92E-04 5.26E-03 0.002

ppm 0.00E+00 -4.21E-01 3.56E+00 1.046

ppm@7%O2 0.00E+00 -5.89E-01 5.24E+00 1.550

Location: Stack Exit - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000111 0.00000000999 0.00000000504 0.000

lb/mmBtuO2 1.42E-12 1.25E-12 1.65E-12 0.000

ng/dscm 1.15E-03 1.02E-03 1.28E-03 0.001

ng/dscm@7%O2 1.65E-03 1.45E-03 1.91E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000397 0.00000000789 0.00000000209 0.000

lb/mmBtuO2 5.08E-13 9.86E-13 6.85E-13 0.000

ng/dscm 4.11E-04 8.06E-04 5.31E-04 0.001

ng/dscm@7%O2 5.89E-04 1.14E-03 7.94E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000024 0.00000000228 0.00000000291 0.000

lb/mmBtuO2 3.07E-13 2.85E-13 9.53E-13 0.000

ng/dscm 2.48E-04 2.33E-04 7.39E-04 0.000

ng/dscm@7%O2 3.55E-04 3.30E-04 1.10E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000022 0.00000000219 0.00000000191 0.000

lb/mmBtuO2 2.81E-13 2.74E-13 6.26E-13 0.000

ng/dscm 2.28E-04 2.24E-04 4.85E-04 0.000

ng/dscm@7%O2 3.27E-04 3.18E-04 7.25E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000152 0.00000000706 0.00000000171 0.000

lb/mmBtuO2 1.94E-13 8.82E-13 5.60E-13 0.000

ng/dscm 1.57E-04 7.21E-04 4.34E-04 0.000

ng/dscm@7%O2 2.25E-04 1.02E-03 6.49E-04 0.001

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

Average

Tuesday, February 15, 2011 Page 13 of 48
RunNumber 1 2 3

Mass_mg 0.00000000224 0.00000000232 0.00000000203 0.000

lb/mmBtuO2 2.87E-13 2.90E-13 6.65E-13 0.000

ng/dscm 2.32E-04 2.37E-04 5.16E-04 0.000

ng/dscm@7%O2 3.32E-04 3.36E-04 7.71E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000136 0.0000000112 0.00000000171 0.000

lb/mmBtuO2 1.74E-13 1.40E-12 5.60E-13 0.000

ng/dscm 1.41E-04 1.14E-03 4.34E-04 0.001

ng/dscm@7%O2 2.02E-04 1.62E-03 6.49E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000263 0.00000000267 0.00000000226 0.000

lb/mmBtuO2 3.37E-13 3.34E-13 7.40E-13 0.000

ng/dscm 2.72E-04 2.73E-04 5.74E-04 0.000

ng/dscm@7%O2 3.90E-04 3.87E-04 8.58E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000202 0.00000000225 0.00000000255 0.000

lb/mmBtuO2 2.58E-13 2.81E-13 8.35E-13 0.000

ng/dscm 2.09E-04 2.30E-04 6.48E-04 0.000

ng/dscm@7%O2 2.99E-04 3.26E-04 9.69E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000241 0.00000000274 0.00000000275 0.000

lb/mmBtuO2 3.08E-13 3.42E-13 9.01E-13 0.000

ng/dscm 2.49E-04 2.80E-04 6.99E-04 0.000

ng/dscm@7%O2 3.57E-04 3.97E-04 1.04E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000165 0.0000000111 0.00000000144 0.000

lb/mmBtuO2 2.11E-13 1.39E-12 4.72E-13 0.000

ng/dscm 1.71E-04 1.13E-03 3.66E-04 0.001

ng/dscm@7%O2 2.45E-04 1.60E-03 5.47E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000815 0.0000000121 0.00000000827 0.000

lb/mmBtuO2 1.04E-12 1.51E-12 2.71E-12 0.000

ng/dscm 8.44E-04 1.24E-03 2.10E-03 0.001

ng/dscm@7%O2 1.21E-03 1.76E-03 3.14E-03 0.002

Tuesday, February 15, 2011 Page 14 of 48
Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 1 2 3

Mass_mg 0.000000151 0.000000182 0.0000000702 0.000

lb/mmBtuO2 1.93E-11 2.27E-11 2.30E-11 0.000

ng/dscm 1.56E-02 1.86E-02 1.78E-02 0.017

ng/dscm@7%O2 2.24E-02 2.64E-02 2.66E-02 0.025

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

Average

RunNumber 1 2 3

Mass_mg 0.000000582 0.000000688 0.000000254 0.000

lb/mmBtuO2 7.45E-11 8.60E-11 8.32E-11 0.000

ng/dscm 6.03E-02 7.03E-02 6.45E-02 0.065

ng/dscm@7%O2 8.64E-02 9.97E-02 9.64E-02 0.094

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000663 0.0000000898 0.0000000326 0.000

lb/mmBtuO2 8.48E-12 1.12E-11 1.07E-11 0.000

ng/dscm 6.86E-03 9.18E-03 8.28E-03 0.008

ng/dscm@7%O2 9.83E-03 1.30E-02 1.24E-02 0.012

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000413 0.0000000468 0.00000000999 0.000

lb/mmBtuO2 5.28E-12 5.85E-12 3.27E-12 0.000

ng/dscm 4.28E-03 4.78E-03 2.54E-03 0.004

ng/dscm@7%O2 6.13E-03 6.78E-03 3.80E-03 0.006

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

Average

RunNumber 1 2 3

Mass_mg 0.00000188 0.00000215 0.000000786 0.000

lb/mmBtuO2 2.41E-10 2.69E-10 2.57E-10 0.000

ng/dscm 1.95E-01 2.20E-01 2.00E-01 0.205

ng/dscm@7%O2 2.79E-01 3.12E-01 2.99E-01 0.297

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000476 0.0000000635 0.000000019 0.000

lb/mmBtuO2 6.09E-12 7.94E-12 6.22E-12 0.000

ng/dscm 4.93E-03 6.49E-03 4.83E-03 0.005

ng/dscm@7%O2 7.06E-03 9.21E-03 7.22E-03 0.008

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000139 0.0000000104 0.00000000175 0.000

lb/mmBtuO2 1.78E-13 1.30E-12 5.73E-13 0.000

Tuesday, February 15, 2011 Page 15 of 48
ng/dscm 1.44E-04 1.06E-03 4.45E-04 0.001

ng/dscm@7%O2 2.06E-04 1.50E-03 6.65E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000153 0.0000000161 0.00000000132 0.000

lb/mmBtuO2 1.96E-13 2.01E-12 4.32E-13 0.000

ng/dscm 1.58E-04 1.65E-03 3.35E-04 0.001

ng/dscm@7%O2 2.26E-04 2.34E-03 5.01E-04 0.001

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000231 0.00000000231 0.00000000225 0.000

lb/mmBtuO2 2.96E-13 2.89E-13 7.37E-13 0.000

ng/dscm 2.39E-04 2.36E-04 5.72E-04 0.000

ng/dscm@7%O2 3.42E-04 3.35E-04 8.55E-04 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000248 0.00000000913 0.00000000135 0.000

lb/mmBtuO2 3.17E-13 1.14E-12 4.42E-13 0.000

ng/dscm 2.57E-04 9.33E-04 3.43E-04 0.001

ng/dscm@7%O2 3.68E-04 1.32E-03 5.13E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000956 0.0000000133 0.00000000933 0.000

lb/mmBtuO2 1.22E-12 1.66E-12 3.06E-12 0.000

ng/dscm 9.90E-04 1.36E-03 2.37E-03 0.002

ng/dscm@7%O2 1.42E-03 1.93E-03 3.54E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.000000013 0.0000000174 0.00000000881 0.000

lb/mmBtuO2 1.66E-12 2.17E-12 2.89E-12 0.000

ng/dscm 1.35E-03 1.78E-03 2.24E-03 0.002

ng/dscm@7%O2 1.93E-03 2.52E-03 3.35E-03 0.003

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

Average

RunNumber 1 2 3

Mass_mg 0.000000222 0.000000252 0.0000000852 0.000

lb/mmBtuO2 2.84E-11 3.15E-11 2.79E-11 0.000

ng/dscm 2.30E-02 2.57E-02 2.16E-02 0.023

ng/dscm@7%O2 3.30E-02 3.65E-02 3.23E-02 0.034

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

Average

RunNumber 1 2 3

Tuesday, February 15, 2011 Page 16 of 48
Mass_mg 0.0000000124 0.000000011 0.0000000078 0.000

lb/mmBtuO2 1.59E-12 1.37E-12 2.55E-12 0.000

ng/dscm 1.28E-03 1.12E-03 1.98E-03 0.001

ng/dscm@7%O2 1.83E-03 1.59E-03 2.96E-03 0.002

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000457 0.000000041 0.0000000231 0.000

lb/mmBtuO2 5.85E-12 5.12E-12 7.57E-12 0.000

ng/dscm 4.73E-03 4.19E-03 5.87E-03 0.005

ng/dscm@7%O2 6.78E-03 5.94E-03 8.77E-03 0.007

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000376 0.00000000376 0.0000000045 0.000

lb/mmBtuO2 4.81E-13 4.70E-13 1.47E-12 0.000

ng/dscm 3.89E-04 3.84E-04 1.14E-03 0.001

ng/dscm@7%O2 5.57E-04 5.45E-04 1.70E-03 0.001

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0 0.0000000154 0 0.000

lb/mmBtuO2 0.00E+00 1.92E-12 0.00E+00 0.000

ng/dscm 0.00E+00 1.57E-03 0.00E+00 0.001

ng/dscm@7%O2 0.00E+00 2.23E-03 0.00E+00 0.001

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000111 0.00000000929 0 0.000

lb/mmBtuO2 1.42E-12 1.16E-12 0.00E+00 0.000

ng/dscm 1.15E-03 9.49E-04 0.00E+00 0.001

ng/dscm@7%O2 1.65E-03 1.35E-03 0.00E+00 0.001

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000422 0.0000000221 0.00000000212 0.000

lb/mmBtuO2 5.40E-13 2.76E-12 6.94E-13 0.000

ng/dscm 4.37E-04 2.26E-03 5.39E-04 0.001

ng/dscm@7%O2 6.26E-04 3.21E-03 8.06E-04 0.002

Tuesday, February 15, 2011 Page 17 of 48
Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0 0.0000000091 0 0.000

lb/mmBtuO2 0.00E+00 1.14E-12 0.00E+00 0.000

ng/dscm 0.00E+00 9.30E-04 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 1.32E-03 0.00E+00 0.000

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000053 0.000000114 0 0.000

lb/mmBtuO2 6.78E-13 1.42E-11 0.00E+00 0.000

ng/dscm 5.49E-04 1.16E-02 0.00E+00 0.004

ng/dscm@7%O2 7.87E-04 1.65E-02 0.00E+00 0.006

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000131 0.0000000505 0.00000000267 0.000

lb/mmBtuO2 1.68E-12 6.31E-12 8.74E-13 0.000

ng/dscm 1.36E-03 5.16E-03 6.78E-04 0.002

ng/dscm@7%O2 1.95E-03 7.32E-03 1.01E-03 0.003

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000202 0.000000314 0 0.000

lb/mmBtuO2 2.58E-12 3.92E-11 0.00E+00 0.000

ng/dscm 2.09E-03 3.21E-02 0.00E+00 0.011

ng/dscm@7%O2 2.99E-03 4.55E-02 0.00E+00 0.016

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.00000009279 0.00000014695 0.00000004201 0.000

lb/mmBtuO2 1.19E-11 1.84E-11 1.38E-11 0.000

ng/dscm 9.61E-03 1.50E-02 1.07E-02 0.012

ng/dscm@7%O2 1.38E-02 2.13E-02 1.60E-02 0.017

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.0000000518 0.00000053127 0.00000002345 0.000

lb/mmBtuO2 6.63E-12 6.64E-11 7.68E-12 0.000

ng/dscm 5.36E-03 5.43E-02 5.96E-03 0.022

ng/dscm@7%O2 7.68E-03 7.70E-02 8.91E-03 0.031

Compound: Total Mono-CBs

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

Tuesday, February 15, 2011 Page 18 of 48
ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Total Nona-CBs

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Total Octa-CBs

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Total PCBs

Average

RunNumber 1 2 3

Mass_mg 0.000003033 0.000003526 0.000001291 0.000

lb/mmBtuO2 3.88E-10 4.41E-10 4.23E-10 0.000

ng/dscm 3.14E-01 3.60E-01 3.28E-01 0.334

ng/dscm@7%O2 4.50E-01 5.11E-01 4.90E-01 0.484

Compound: Total PeCDD

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Total PeCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Total Penta-CBs

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Total TCDD

Average

RunNumber 1 2 3

Tuesday, February 15, 2011 Page 19 of 48
Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Total TCDF 

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Total TEQ

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Total Tetra-CBs

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Total Tri-CBs

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 0.00E+00 3.15E-03 1.85E-03 0.002

ppm 0.00E+00 1.42E+00 7.93E-01 0.738

ppm@7%O2 0.00E+00 1.99E+00 1.17E+00 1.053

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.287 0.309 0.319 0.305

Elb/hr 2.72E-02 2.99E-02 3.08E-02 0.029

lb/mmBtuO2 8.74E-05 1.00E-04 9.99E-05 0.000

mg/dscm 7.14E-02 7.87E-02 7.83E-02 0.076

Tuesday, February 15, 2011 Page 20 of 48
mg/dscm@7%O2 1.01E-01 1.16E-01 1.16E-01 0.111

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.294 0.317 0.327 0.313

Elb/hr 2.79E-02 3.06E-02 3.15E-02 0.030

lb/mmBtuO2 8.95E-05 1.03E-04 1.02E-04 0.000

mg/dscm 7.32E-02 8.08E-02 8.03E-02 0.078

mg/dscm@7%O2 1.04E-01 1.19E-01 1.19E-01 0.114

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0001 0.0002 0.0001 0.000

Elb/hr 4.81E-06 9.46E-06 4.78E-06 0.000

lb/mmBtuO2 1.62E-08 3.18E-08 1.57E-08 0.000

mg/dscm 1.27E-05 2.54E-05 1.27E-05 0.000

mg/dscm@7%O2 1.88E-05 3.68E-05 1.82E-05 0.000

Compound: Arsenic

Average

RunNumber 2 3 1

Mass_mg 0.0021 0.0007 0.0013 0.001

Elb/hr 9.94E-05 3.35E-05 6.25E-05 0.000

lb/mmBtuO2 3.34E-07 1.10E-07 2.10E-07 0.000

mg/dscm 2.67E-04 8.91E-05 1.65E-04 0.000

mg/dscm@7%O2 3.87E-04 1.28E-04 2.44E-04 0.000

Compound: Beryllium

Average

RunNumber 2 3 1

Mass_mg 0.0001 0 0.0001 0.000

Elb/hr 4.73E-06 0.00E+00 4.81E-06 0.000

lb/mmBtuO2 1.59E-08 0.00E+00 1.62E-08 0.000

mg/dscm 1.27E-05 0.00E+00 1.27E-05 0.000

mg/dscm@7%O2 1.84E-05 0.00E+00 1.88E-05 0.000

Compound: Cadmium

Average

RunNumber 2 3 1

Mass_mg 0.0005 0.0003 0.0007 0.001

Elb/hr 2.37E-05 1.43E-05 3.36E-05 0.000

lb/mmBtuO2 7.94E-08 4.72E-08 1.13E-07 0.000

mg/dscm 6.36E-05 3.82E-05 8.88E-05 0.000

mg/dscm@7%O2 9.21E-05 5.47E-05 1.31E-04 0.000

Compound: Chromium

Average

RunNumber 2 3 1

Mass_mg 0.0057 0.0014 0.002 0.003

Elb/hr 2.70E-04 6.69E-05 9.61E-05 0.000

Tuesday, February 15, 2011 Page 21 of 48
lb/mmBtuO2 9.06E-07 2.20E-07 3.24E-07 0.000

mg/dscm 7.25E-04 1.78E-04 2.54E-04 0.000

mg/dscm@7%O2 1.05E-03 2.55E-04 3.76E-04 0.001

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.0009 0.0003 0.0003 0.001

Elb/hr 4.33E-05 1.42E-05 1.43E-05 0.000

lb/mmBtuO2 1.46E-07 4.77E-08 4.72E-08 0.000

mg/dscm 1.14E-04 3.82E-05 3.82E-05 0.000

mg/dscm@7%O2 1.69E-04 5.53E-05 5.47E-05 0.000

Compound: Filterable Particulate

Average

RunNumber 2 3 1

Mass_mg 7.4 4.4 7.8 6.533

Elb/hr 3.50E-01 2.10E-01 3.75E-01 0.312

lb/mmBtuO2 1.18E-03 6.92E-04 1.26E-03 0.001

mg/dscm 9.41E-01 5.60E-01 9.90E-01 0.830

mg/dscm@7%O2 1.36E+00 8.02E-01 1.46E+00 1.207

Compound: Lead

Average

RunNumber 2 3 1

Mass_mg 0.0307 0.0203 0.0293 0.027

Elb/hr 1.45E-03 9.71E-04 1.41E-03 0.001

lb/mmBtuO2 4.88E-06 3.19E-06 4.74E-06 0.000

mg/dscm 3.91E-03 2.58E-03 3.72E-03 0.003

mg/dscm@7%O2 5.66E-03 3.70E-03 5.50E-03 0.005

Compound: Magnesium

Average

RunNumber 2 3 1

Mass_mg 0 0 0 0.000

Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000

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

mg/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

mg/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Manganese

Average

RunNumber 2 3 1

Mass_mg 0.0081 0.0029 0.0048 0.005

Elb/hr 3.83E-04 1.39E-04 2.31E-04 0.000

lb/mmBtuO2 1.29E-06 4.56E-07 7.77E-07 0.000

mg/dscm 1.03E-03 3.69E-04 6.09E-04 0.001

mg/dscm@7%O2 1.49E-03 5.29E-04 9.01E-04 0.001

Compound: Mercury

Average

RunNumber 2 3 1

Mass_mg 0 0 0 0.000

Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000

Tuesday, February 15, 2011 Page 22 of 48
lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

mg/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

mg/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Nickel

Average

RunNumber 2 3 1

Mass_mg 0.0069 0.003 0.0048 0.005

Elb/hr 3.26E-04 1.43E-04 2.31E-04 0.000

lb/mmBtuO2 1.10E-06 4.72E-07 7.77E-07 0.000

mg/dscm 8.78E-04 3.82E-04 6.09E-04 0.001

mg/dscm@7%O2 1.27E-03 5.47E-04 9.01E-04 0.001

Compound: Selenium

Average

RunNumber 2 3 1

Mass_mg 0.0012 0.0012 0.001 0.001

Elb/hr 5.68E-05 5.74E-05 4.81E-05 0.000

lb/mmBtuO2 1.91E-07 1.89E-07 1.62E-07 0.000

mg/dscm 1.53E-04 1.53E-04 1.27E-04 0.000

mg/dscm@7%O2 2.22E-04 2.19E-04 1.88E-04 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000

lb/mmBtuO2 1.85E-02 2.35E-02 2.21E-02 0.021

mg/dscm 1.54E+01 1.88E+01 1.77E+01 17.300

mg/dscm@7%O2 2.14E+01 2.73E+01 2.56E+01 24.767

ppm 5.78E+00 7.06E+00 6.64E+00 6.493

ppm@7%O2 8.03E+00 1.03E+01 9.60E+00 9.310

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000

lb/mmBtuO2 1.84E-01 1.87E-01 1.88E-01 0.186

mg/dscm 1.53E+02 1.50E+02 1.51E+02 151.333

mg/dscm@7%O2 2.13E+02 2.18E+02 2.18E+02 216.333

ppm 8.02E+01 7.82E+01 7.88E+01 79.067

ppm@7%O2 1.11E+02 1.14E+02 1.14E+02 113.000

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 8.8 7.2 12.3 9.433

lb/mmBtuO2 2.81E-03 2.67E-03 3.98E-03 0.003

Tuesday, February 15, 2011 Page 23 of 48
Process Run Data

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 4.6 4.9 1 3.500

lb/mmBtuO2 1.47E-03 1.82E-03 3.24E-04 0.001

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 7.2 3.9 5.2 5.433

lb/mmBtuO2 2.30E-03 1.44E-03 1.68E-03 0.002

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 4.1 3.3 3.6 3.667

lb/mmBtuO2 1.31E-03 1.22E-03 1.17E-03 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 20.1 14.4 21.1 18.533

lb/mmBtuO2 6.43E-03 5.34E-03 6.83E-03 0.006

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 15.9 12.1 9.8 12.600

lb/mmBtuO2 5.09E-03 4.48E-03 3.17E-03 0.004

Tuesday, February 15, 2011 Page 24 of 48
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Distillate Oil (No. 1 & 2) Burned 1.614 1000 Gallons/hr 0

10 Distillate Oil (No. 1 & 2) Burned 1.674 1000 Gallons/hr 0

11 Distillate Oil (No. 1 & 2) Burned 1.668 1000 Gallons/hr 0

12 Distillate Oil (No. 1 & 2) Burned 1.668 1000 Gallons/hr 0

2 Distillate Oil (No. 1 & 2) Burned 1.656 1000 Gallons/hr 0

3 Distillate Oil (No. 1 & 2) Burned 1.656 1000 Gallons/hr 0

4 Distillate Oil (No. 1 & 2) Burned 1.6548 1000 Gallons/hr 0

5 Distillate Oil (No. 1 & 2) Burned 1.6507 1000 Gallons/hr 0

6 Distillate Oil (No. 1 & 2) Burned 1.368 1000 Gallons/hr 0

7 Distillate Oil (No. 1 & 2) Burned 1.7385 1000 Gallons/hr 0

8 Distillate Oil (No. 1 & 2) Burned 1.674 1000 Gallons/hr 0

9 Distillate Oil (No. 1 & 2) Burned 1.674 1000 Gallons/hr 0

1 Average Heat Input 222.97 MMBtu/hr 0

10 Average Heat Input 231.26 MMBtu/hr 0

11 Average Heat Input 230.43 MMBtu/hr 0

12 Average Heat Input 230.43 MMBtu/hr 0

2 Average Heat Input 228.78 MMBtu/hr 0

3 Average Heat Input 228.78 MMBtu/hr 0

4 Average Heat Input 228.61 MMBtu/hr 0

5 Average Heat Input 228.04 MMBtu/hr 0

6 Average Heat Input 188.99 MMBtu/hr 0

7 Average Heat Input 240.17 MMBtu/hr 0

8 Average Heat Input 231.26 MMBtu/hr 0

9 Average Heat Input 231.26 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

12 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

Tuesday, February 15, 2011 Page 25 of 48
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 Synfuel Firing Rate 0 0

10 Synfuel Firing Rate 0 0

11 Synfuel Firing Rate 0 0

12 Synfuel Firing Rate 0 0

2 Synfuel Firing Rate 0 0

3 Synfuel Firing Rate 0 0

4 Synfuel Firing Rate 0 0

5 Synfuel Firing Rate 0 0

6 Synfuel Firing Rate 0 0

7 Synfuel Firing Rate 0 0

8 Synfuel Firing Rate 0 0

9 Synfuel Firing Rate 0 0

1 Petroleum Coke Firing Rate 0 0

10 Petroleum Coke Firing Rate 0 0

11 Petroleum Coke Firing Rate 0 0

12 Petroleum Coke Firing Rate 0 0

2 Petroleum Coke Firing Rate 0 0

3 Petroleum Coke Firing Rate 0 0

4 Petroleum Coke Firing Rate 0 0

5 Petroleum Coke Firing Rate 0 0

6 Petroleum Coke Firing Rate 0 0

7 Petroleum Coke Firing Rate 0 0

8 Petroleum Coke Firing Rate 0 0

9 Petroleum Coke Firing Rate 0 0

1 Coal Gas Firing Rate 0 0

10 Coal Gas Firing Rate 0 0

11 Coal Gas Firing Rate 0 0

12 Coal Gas Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

4 Coal Gas Firing Rate 0 0

5 Coal Gas Firing Rate 0 0

6 Coal Gas Firing Rate 0 0

Tuesday, February 15, 2011 Page 26 of 48
7 Coal Gas Firing Rate 0 0

8 Coal Gas Firing Rate 0 0

9 Coal Gas Firing Rate 0 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

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 Flue Gas Flow Rate 0 dscfm 0

10 Flue Gas Flow Rate 0 dscfm 0

11 Flue Gas Flow Rate 0 dscfm 0

12 Flue Gas Flow Rate 0 dscfm 0

4 Flue Gas Flow Rate 0 dscfm 0

5 Flue Gas Flow Rate 0 dscfm 0

6 Flue Gas Flow Rate 0 dscfm 0

7 Flue Gas Flow Rate 0 dscfm 0

8 Flue Gas Flow Rate 0 dscfm 0

9 Flue Gas Flow Rate 0 dscfm 0

1 Pressure Drop Across FGD (if applicable) 0 in H20 0

10 Pressure Drop Across FGD (if applicable) 0 in H20 0

11 Pressure Drop Across FGD (if applicable) 0 in H20 0

12 Pressure Drop Across FGD (if applicable) 0 in H20 0

4 Pressure Drop Across FGD (if applicable) 0 in H20 0

5 Pressure Drop Across FGD (if applicable) 0 in H20 0

6 Pressure Drop Across FGD (if applicable) 0 in H20 0

7 Pressure Drop Across FGD (if applicable) 0 in H20 0

8 Pressure Drop Across FGD (if applicable) 0 in H20 0

9 Pressure Drop Across FGD (if applicable) 0 in H20 0

1 FGD Scrubber Liquor pH 0 pH 0

Tuesday, February 15, 2011 Page 27 of 48
10 FGD Scrubber Liquor pH 0 pH 0

11 FGD Scrubber Liquor pH 0 pH 0

12 FGD Scrubber Liquor pH 0 pH 0

4 FGD Scrubber Liquor pH 0 pH 0

5 FGD Scrubber Liquor pH 0 pH 0

6 FGD Scrubber Liquor pH 0 pH 0

7 FGD Scrubber Liquor pH 0 pH 0

8 FGD Scrubber Liquor pH 0 pH 0

9 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

10 FGD Scrubber Liquor Flow Rate 0 gal/min 0

11 FGD Scrubber Liquor Flow Rate 0 gal/min 0

12 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

5 FGD Scrubber Liquor Flow Rate 0 gal/min 0

6 FGD Scrubber Liquor Flow Rate 0 gal/min 0

7 FGD Scrubber Liquor Flow Rate 0 gal/min 0

8 FGD Scrubber Liquor Flow Rate 0 gal/min 0

9 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

10 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

11 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

12 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

5 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

6 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

7 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

8 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

9 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

Tuesday, February 15, 2011 Page 28 of 48
10 Flue Gas Oxygen Content 0 % 0

11 Flue Gas Oxygen Content 0 % 0

12 Flue Gas Oxygen Content 0 % 0

4 Flue Gas Oxygen Content 0 % 0

5 Flue Gas Oxygen Content 0 % 0

6 Flue Gas Oxygen Content 0 % 0

7 Flue Gas Oxygen Content 0 % 0

8 Flue Gas Oxygen Content 0 % 0

9 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

10 Flue Gas Carbon Dioxide Content 0 % 0

11 Flue Gas Carbon Dioxide Content 0 % 0

12 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0

5 Flue Gas Carbon Dioxide Content 0 % 0

6 Flue Gas Carbon Dioxide Content 0 % 0

7 Flue Gas Carbon Dioxide Content 0 % 0

8 Flue Gas Carbon Dioxide Content 0 % 0

9 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

10 Flue Gas Moisture Content 0 % 0

11 Flue Gas Moisture Content 0 % 0

12 Flue Gas Moisture Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

5 Flue Gas Moisture Content 0 % 0

6 Flue Gas Moisture Content 0 % 0

7 Flue Gas Moisture Content 0 % 0

8 Flue Gas Moisture Content 0 % 0

9 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

10 Flue Gas Sampling Point Temperature 0 Deg F 0

11 Flue Gas Sampling Point Temperature 0 Deg F 0

12 Flue Gas Sampling Point Temperature 0 Deg F 0

4 Flue Gas Sampling Point Temperature 0 Deg F 0

5 Flue Gas Sampling Point Temperature 0 Deg F 0

6 Flue Gas Sampling Point Temperature 0 Deg F 0

Tuesday, February 15, 2011 Page 29 of 48
7 Flue Gas Sampling Point Temperature 0 Deg F 0

8 Flue Gas Sampling Point Temperature 0 Deg F 0

9 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

10 Flue Gas Pressure 0 atm 0

11 Flue Gas Pressure 0 atm 0

12 Flue Gas Pressure 0 atm 0

4 Flue Gas Pressure 0 atm 0

5 Flue Gas Pressure 0 atm 0

6 Flue Gas Pressure 0 atm 0

7 Flue Gas Pressure 0 atm 0

8 Flue Gas Pressure 0 atm 0

9 Flue Gas Pressure 0 atm 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

4 Standard Pressure 1 atm 0

5 Standard Pressure 1 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

4 Standard Temperature 68 Deg F 0

5 Standard Temperature 68 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 15.51 MW 0

10 Unit Gross Electrical Output 15.56 MW 0

11 Unit Gross Electrical Output 15.49 MW 0

Tuesday, February 15, 2011 Page 30 of 48
APCD Run Data

Process Lab Run Data

12 Unit Gross Electrical Output 15.35 MW 0

4 Unit Gross Electrical Output 16.11 MW 0

5 Unit Gross Electrical Output 16.11 MW 0

6 Unit Gross Electrical Output 15.79 MW 0

7 Unit Gross Electrical Output 14.64 MW 0

8 Unit Gross Electrical Output 14.43 MW 0

9 Unit Gross Electrical Output 15.51 MW 0

1 Unit Net Electric Generation 14.51 MWh 0

10 Unit Net Electric Generation 14.25 MWh 0

11 Unit Net Electric Generation 14.26 MWh 0

12 Unit Net Electric Generation 14.23 MWh 0

4 Unit Net Electric Generation 15.18 MWh 0

5 Unit Net Electric Generation 15.03 MWh 0

6 Unit Net Electric Generation 14.31 MWh 0

7 Unit Net Electric Generation 13.8 MWh 0

8 Unit Net Electric Generation 15.42 MWh 0

9 Unit Net Electric Generation 14.01 MWh 0

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 Fuel Mercury Content 0 ppm

1 Fuel Cadmium Content 0 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 0 ppm

1 Fuel Arsenic Content 0 ppm

1 Fuel Chromium Content 0 ppm

1 Fuel Beryllium Content 0 ppm

1 Fuel Lead Content 0 ppm

Tuesday, February 15, 2011 Page 31 of 48
1 Fuel Manganese Content 0 ppm

1 Fuel Chlorine Content 0 ppm

1 Fuel Fluorine Content 0 ppm

Tuesday, February 15, 2011 Page 32 of 48
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 15, 2011 Page 33 of 48
Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 3/9/2010 3/9/2010 3/10/2010

Run Start Time 4:05:00 AM 3:10:00 PM 12:00:00 AM

Run Finish Time 1:10:00 PM 11:30:00 PM 3:15:00 AM

Net Traversing Points 12 12 5

Net Run Time, minutes 485 480 195

Nozzle Diameter, inches 0.253 0.253 0.25 0.252

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 29.12 29.32 29.16 29.200

Average Orifice Meter Differential, inches H2O 1.58 1.58 1.56 1.573

Dry Gas Meter Volume Sampled, cubic feet 345.050 351.470 142.505 279.675

Average Dry Gas Meter Temperature, °F 69.10 75.55 76.97 73.873

Dry Gas Meter Volume Sampled, dscf 341.173 345.685 139.022 275.293

Total Moisture Liquid collected, g 534.6 577.5 245.9 452.667

Volume of Water Vapor, standard cubic feet 25.16 27.18 11.57 21.303

Moisture Content of Stack Gas, % 6.87 7.29 7.68 7.280

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

Dry Mole Fraction 0.9313 0.9271 0.9232 0.927

Carbon Dioxide, % 7.3 7.3 6.8 7.133

Oxygen, % 11.2 11.1 11.6 11.300

Carbon Monoxide & Nitrogen, % 81.5 81.6 81.6 81.567

Fuel Factor 1.33 1.34 1.37

Dry Molecular Weight, lb/lb-Mole 29.62 29.61 29.55 29.593

Wet Molecular weight, lb/lb-Mole 28.82 28.76 28.66 28.747

Flue Gas Static Pressure, inches of H2O -0.53 -0.35 -0.35 -0.410

Absolute Flue Gas Pressure, inches of Mercury 29.08 29.29 29.13 29.167

Average Stack Gas Temperature, °F 283.08 287.28 288.95 286.437

Average Velocity Head, inches of H2O 0.6668082556

16071

0.672690250

318953

0.668595552

63099

0.669

Average Stack Gas Velocity, feet/second 55.22 55.47 55.62 55.437

Stack Cross-Sectional Area, square feet 44.671 44.671 44.671 44.671

Dry Volumetric Flow Rate, dry scfm 95,190.6 95,338.9 94,463.4 94,997.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 148,004.0 148,674.0 149,076.1 148,584.700

Percent Isokinetic of Sampling Rate, % 94.6 96.7 98.9 96.733

Percent Excess Air, % 108.6 106.3 116.7 110.533

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

Round Duct Diameter, inches 90.5 90.5 90.5

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

Tuesday, February 15, 2011 Page 34 of 48
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 15, 2011 Page 35 of 48
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 15, 2011 Page 36 of 48
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 15, 2011 Page 37 of 48
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 15, 2011 Page 38 of 48
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

Tuesday, February 15, 2011 Page 39 of 48
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

Tuesday, February 15, 2011 Page 40 of 48
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

Tuesday, February 15, 2011 Page 41 of 48
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 15, 2011 Page 42 of 48
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

Tuesday, February 15, 2011 Page 43 of 48
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

Tuesday, February 15, 2011 Page 44 of 48
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

Tuesday, February 15, 2011 Page 45 of 48
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 15, 2011 Page 46 of 48
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 15, 2011 Page 47 of 48
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 15, 2011 Page 48 of 48