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 47
Facility Information:

Harding Street

3700 S. Harding Street

Indianapolis IN 46217

Contact: Angelique Oliger

Phone: (317) 261-5852

Fax: Of above personasdf

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:

10 10

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 47
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 47
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 47
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 2 3 4

Test Date 3/3/2010 3/4/2010 3/4/2010

Run Start Time 12:00:00 AM 9:30:00 

AM

12:10:00 AM

Run Finish Time 11:55:00 PM 5:55:00 PM 11:50:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 353.535 335.130 328.935 339.200

Moisture Content of Stack Gas, % 6.10 6.23 6.30 6.210

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

Carbon Dioxide, % 6.7 6.51 6.52 6.577

Oxygen, % 11.9 11.91 11.94 11.917

Average Stack Gas Temperature, °F 287.65 287.47 285.65 286.923

Dry Volumetric Flow Rate, dry scfm 100,192.0 94,053.8 96,395.7 96,880.500

Actual Wet Volumetric Flue Gas Flow Rate, acfm 153,552.1 145,296.9 148,968.9 149,272.633

Percent Isokinetic of Sampling Rate, % 96.3 97.3 93.2 95.600

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 47
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 47
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 0 -1.68 -1.68 -1.120

Moisture, %

Fuel Type 0 8.64 8.64

Fw 0 0 0 0.000

Fc Zero Zero

Tuesday, February 15, 2011 Page 7 of 47
Location Stack Exit - Method 3A CO2 3

Average

Run Number Hg-1 Hg-2 M23/HCHO 

R2

Test Date 3/2/2010 3/2/2010 3/3/2010

Run Start Time 3:30:00 AM 6:15:00 

AM

9:45:00 PM

Run Finish Time 5:30:00 AM 8:15:00 

AM

6:42:00 AM

Carbon Dioxide, % 7.07 7.07 6.55 6.897

Oxygen, % 11.52 11.55 11.83 11.633

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location Stack Exit - Method 3A CO2 3 6

Average

Run Number M23/HCHO 

R3

M23/HCH

O R4

PM/Met-1

Test Date 3/4/2010 3/4/2010 3/1/2010

Run Start Time 9:30:00 AM 7:55:00 PM 1:40:00 AM

Run Finish Time 6:04:00 PM 4:00:00 

AM

7:52:00 AM

Carbon Dioxide, % 6.52 6.54 6.84 6.633

Oxygen, % 11.9 11.94 11.86 11.900

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Tuesday, February 15, 2011 Page 8 of 47
Location Stack Exit - Method 3A CO2 3 6 9

Average

Run Number PM/Met-2 PM/Met-3 VOST/SVO

L R1

Test Date 3/1/2010 3/1/2010 3/5/2010

Run Start Time 10:11:00 AM 8:00:00 PM 11:31:00 PM

Run Finish Time 5:18:00 PM 2:15:00 

AM

2:09:00 AM

Carbon Dioxide, % 6.96 7.1 6.41 6.823

Oxygen, % 11.68 11.55 12.07 11.767

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location Stack Exit - Method 3A CO2 3 6 9 12

Average

Run Number VOST/SVO

L- R2

VOST/SV

OL-R3

Test Date 3/6/2010 3/6/2010

Run Start Time 2:46:00 AM 5:15:00 

AM

Run Finish Time 4:57:00 AM 7:20:00 

AM

Carbon Dioxide, % 6.44 6.71 6.575

Oxygen, % 12.04 11.69 11.865

Dry Volumetric Flow Rate, dry scfm 0 0 0.000

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

Moisture, % 0 0 0.000

Fuel Type Oil Oil

Fw 10320 10320 10,320.000

Fc 1420 1420 1,420.000

Tuesday, February 15, 2011 Page 9 of 47
Location Stack Exit - Method 3A O2

Average

Run Number AG Run-1 AG Run-2 AG Run-3

Test Date 3/5/2010 3/6/2010 3/5/2010

Run Start Time 5:01:00 AM 10:22:00 

AM

3:11:00 PM

Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM

Carbon Dioxide, % 6.42 6.44 6.43 6.430

Oxygen, % 11.9 11.99 11.94 11.943

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location Stack Exit - Method 3A O2 3

Average

Run Number Hg-1 Hg-2 M23/HCHO 

R2

Test Date 3/2/2010 3/2/2010 3/3/2010

Run Start Time 3:30:00 AM 6:15:00 

AM

9:45:00 PM

Run Finish Time 5:30:00 AM 8:15:00 

AM

6:42:00 AM

Carbon Dioxide, % 7.07 7.07 6.55 6.897

Oxygen, % 11.52 11.55 11.83 11.633

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Tuesday, February 15, 2011 Page 10 of 47
Location Stack Exit - Method 3A O2 3 6

Average

Run Number M23/HCHO 

R3

M23/HCH

O R4

PM/MET-1

Test Date 3/4/2010 3/4/2010 3/1/2010

Run Start Time 9:30:00 AM 7:55:00 PM 1:40:00 AM

Run Finish Time 6:04:00 PM 4:00:00 

AM

7:52:00 AM

Carbon Dioxide, % 6.52 6.54 6.84 6.633

Oxygen, % 11.9 11.94 11.86 11.900

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location Stack Exit - Method 3A O2 3 6 9

Average

Run Number PM/Met-2 PM/Met-3 VOST/SVO

L-R1

Test Date 3/1/2010 3/1/2010 3/5/2010

Run Start Time 10:11:00 AM 8:00:00 PM 11:31:00 PM

Run Finish Time 5:18:00 PM 2:15:00 

AM

2:09:00 AM

Carbon Dioxide, % 6.96 7.1 6.41 6.823

Oxygen, % 11.68 11.55 12.07 11.767

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Tuesday, February 15, 2011 Page 11 of 47
Location Stack Exit - Method 3A O2 3 6 9 12

Average

Run Number VOST/SVO

L-R2

VOST/SV

OL-R3

Test Date 3/6/2010 3/6/2010

Run Start Time 2:46:00 AM 5:15:00 

AM

Run Finish Time 4:57:00 AM 7:20:00 

AM

Carbon Dioxide, % 6.44 6.71 6.575

Oxygen, % 12.04 11.69 11.865

Dry Volumetric Flow Rate, dry scfm 0 0 0.000

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

Moisture, % 0 0 0.000

Fuel Type Oil Oil

Fw 10320 10320 10,320.000

Fc 1420 1420 1,420.000

Location Stack Exit - Method 6C

Average

Run Number AG Run 1 AG Run 2 AG Run 3

Test Date 3/5/2010 3/5/2010 3/5/2010

Run Start Time 5:01:00 AM 10:22:00 

AM

3:11:00 PM

Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM

Carbon Dioxide, % 6.42 6.44 6.43 6.430

Oxygen, % 11.9 11.99 11.94 11.943

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Tuesday, February 15, 2011 Page 12 of 47
Location Stack Exit - Method 7E

Average

Run Number AG Run 1 AG Run 2 AG Run 3

Test Date 3/5/2010 3/5/2010 3/5/2010

Run Start Time 5:01:00 AM 10:22:00 

AM

3:11:00 PM

Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM

Carbon Dioxide, % 6.42 6.44 6.43 6.430

Oxygen, % 11.9 11.99 11.94 11.943

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

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 13 of 47
Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run M23/HCHO R2 M23/HCHO R3 M23/HCHO R4

lb/mmBtuO2 -3.06E-05 5.71E-04 1.37E-03 0.001

ppm -1.99E-02 3.68E-01 8.77E-01 0.408

ppm@7%O2 -3.05E-02 5.68E-01 1.36E+00 0.633

Location: Stack Exit - Method 23

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000202 0.0000000127 0.0000000178 0.000

lb/mmBtuO2 2.69E-12 1.78E-12 2.56E-12 0.000

ng/dscm 2.02E-03 1.34E-03 1.91E-03 0.002

ng/dscm@7%O2 3.12E-03 2.07E-03 2.96E-03 0.003

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000161 0.00000000372 0.000000017 0.000

lb/mmBtuO2 2.14E-12 5.23E-13 2.44E-12 0.000

ng/dscm 1.61E-03 3.92E-04 1.83E-03 0.001

ng/dscm@7%O2 2.49E-03 6.06E-04 2.84E-03 0.002

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

Average

RunNumber 2 3 4

Mass_mg 0.00000000307 0.00000000196 0.00000000351 0.000

lb/mmBtuO2 4.09E-13 2.75E-13 5.04E-13 0.000

ng/dscm 3.07E-04 2.07E-04 3.77E-04 0.000

ng/dscm@7%O2 4.74E-04 3.20E-04 5.85E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.00000000593 0.00000000199 0.00000000441 0.000

lb/mmBtuO2 7.89E-13 2.80E-13 6.34E-13 0.000

ng/dscm 5.92E-04 2.10E-04 4.74E-04 0.000

ng/dscm@7%O2 9.14E-04 3.25E-04 7.35E-04 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000149 0.00000000224 0.0000000151 0.000

lb/mmBtuO2 1.98E-12 3.15E-13 2.17E-12 0.000

ng/dscm 1.49E-03 2.36E-04 1.62E-03 0.001

ng/dscm@7%O2 2.30E-03 3.65E-04 2.51E-03 0.002

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

Average

Tuesday, February 15, 2011 Page 14 of 47
RunNumber 2 3 4

Mass_mg 0.00000000861 0.00000000209 0.00000000675 0.000

lb/mmBtuO2 1.15E-12 2.94E-13 9.70E-13 0.000

ng/dscm 8.60E-04 2.20E-04 7.25E-04 0.001

ng/dscm@7%O2 1.33E-03 3.40E-04 1.12E-03 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000259 0.00000000247 0.0000000247 0.000

lb/mmBtuO2 3.45E-12 3.47E-13 3.55E-12 0.000

ng/dscm 2.59E-03 2.60E-04 2.65E-03 0.002

ng/dscm@7%O2 4.00E-03 4.02E-04 4.11E-03 0.003

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

Average

RunNumber 2 3 4

Mass_mg 0.00000000918 0.00000000229 0.00000000754 0.000

lb/mmBtuO2 1.22E-12 3.22E-13 1.08E-12 0.000

ng/dscm 9.17E-04 2.41E-04 8.10E-04 0.001

ng/dscm@7%O2 1.42E-03 3.73E-04 1.26E-03 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.00000000294 0.00000000203 0.00000000208 0.000

lb/mmBtuO2 3.91E-13 2.85E-13 2.99E-13 0.000

ng/dscm 2.94E-04 2.14E-04 2.23E-04 0.000

ng/dscm@7%O2 4.54E-04 3.31E-04 3.46E-04 0.000

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000147 0.00000000252 0.00000000917 0.000

lb/mmBtuO2 1.96E-12 3.54E-13 1.32E-12 0.000

ng/dscm 1.47E-03 2.66E-04 9.85E-04 0.001

ng/dscm@7%O2 2.27E-03 4.11E-04 1.53E-03 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000264 0.00000000283 0.0000000219 0.000

lb/mmBtuO2 3.51E-12 3.98E-13 3.15E-12 0.000

ng/dscm 2.64E-03 2.98E-04 2.35E-03 0.002

ng/dscm@7%O2 4.08E-03 4.61E-04 3.65E-03 0.003

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

Average

RunNumber 2 3 4

Mass_mg 0.00000000454 0.0000000112 0.00000000971 0.000

lb/mmBtuO2 6.04E-13 1.57E-12 1.40E-12 0.000

ng/dscm 4.54E-04 1.18E-03 1.04E-03 0.001

ng/dscm@7%O2 7.01E-04 1.82E-03 1.61E-03 0.001

Tuesday, February 15, 2011 Page 15 of 47
Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 2 3 4

Mass_mg 0.0000001 0.00000014 0.000000139 0.000

lb/mmBtuO2 1.33E-11 1.97E-11 2.00E-11 0.000

ng/dscm 9.99E-03 1.48E-02 1.49E-02 0.013

ng/dscm@7%O2 1.54E-02 2.29E-02 2.31E-02 0.020

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

Average

RunNumber 2 3 4

Mass_mg 0.000000591 0.000000717 0.000000694 0.000

lb/mmBtuO2 7.87E-11 1.01E-10 9.97E-11 0.000

ng/dscm 5.90E-02 7.56E-02 7.45E-02 0.070

ng/dscm@7%O2 9.11E-02 1.17E-01 1.16E-01 0.108

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000422 0.0000000566 0.0000000591 0.000

lb/mmBtuO2 5.62E-12 7.95E-12 8.49E-12 0.000

ng/dscm 4.22E-03 5.97E-03 6.35E-03 0.006

ng/dscm@7%O2 6.52E-03 9.23E-03 9.85E-03 0.009

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000483 0.0000000588 0.0000000625 0.000

lb/mmBtuO2 6.43E-12 8.26E-12 8.98E-12 0.000

ng/dscm 4.83E-03 6.20E-03 6.71E-03 0.006

ng/dscm@7%O2 7.46E-03 9.59E-03 1.04E-02 0.009

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

Average

RunNumber 2 3 4

Mass_mg 0.00000193 0.00000213 0.00000227 0.000

lb/mmBtuO2 2.57E-10 2.99E-10 3.26E-10 0.000

ng/dscm 1.93E-01 2.24E-01 2.44E-01 0.220

ng/dscm@7%O2 2.98E-01 3.46E-01 3.79E-01 0.341

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

Average

RunNumber 2 3 4

Mass_mg 0.000000052 0.0000000525 0.000000178 0.000

lb/mmBtuO2 6.92E-12 7.38E-12 2.56E-11 0.000

ng/dscm 5.20E-03 5.53E-03 1.91E-02 0.010

ng/dscm@7%O2 8.03E-03 8.55E-03 2.96E-02 0.015

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000238 0.00000000266 0.0000000254 0.000

lb/mmBtuO2 3.17E-12 3.74E-13 3.65E-12 0.000

Tuesday, February 15, 2011 Page 16 of 47
ng/dscm 2.38E-03 2.80E-04 2.73E-03 0.002

ng/dscm@7%O2 3.68E-03 4.33E-04 4.24E-03 0.003

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000452 0.00000000271 0.0000000366 0.000

lb/mmBtuO2 6.02E-12 3.81E-13 5.26E-12 0.000

ng/dscm 4.52E-03 2.86E-04 3.93E-03 0.003

ng/dscm@7%O2 6.98E-03 4.42E-04 6.10E-03 0.005

Compound: 2,3,7,8-TCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000151 0.00000000167 0.00000000975 0.000

lb/mmBtuO2 2.01E-12 2.35E-13 1.40E-12 0.000

ng/dscm 1.51E-03 1.76E-04 1.05E-03 0.001

ng/dscm@7%O2 2.33E-03 2.72E-04 1.63E-03 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 2 3 4

Mass_mg 0.0000000186 0.00000000326 0.0000000126 0.000

lb/mmBtuO2 2.48E-12 4.58E-13 1.81E-12 0.000

ng/dscm 1.86E-03 3.44E-04 1.35E-03 0.001

ng/dscm@7%O2 2.87E-03 5.32E-04 2.09E-03 0.002

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

Average

RunNumber 2 3 4

Mass_mg 0.00000000592 0.0000000104 0.00000000998 0.000

lb/mmBtuO2 7.88E-13 1.46E-12 1.43E-12 0.000

ng/dscm 5.91E-04 1.10E-03 1.07E-03 0.001

ng/dscm@7%O2 9.13E-04 1.70E-03 1.66E-03 0.001

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

Average

RunNumber 2 3 4

Mass_mg 0.0000000144 0.0000000164 0.0000000152 0.000

lb/mmBtuO2 1.92E-12 2.30E-12 2.18E-12 0.000

ng/dscm 1.44E-03 1.73E-03 1.63E-03 0.002

ng/dscm@7%O2 2.22E-03 2.67E-03 2.53E-03 0.002

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

Average

RunNumber 2 3 4

Mass_mg 0.000000206 0.000000275 0.000000285 0.000

lb/mmBtuO2 2.74E-11 3.87E-11 4.09E-11 0.000

ng/dscm 2.06E-02 2.90E-02 3.06E-02 0.027

ng/dscm@7%O2 3.18E-02 4.48E-02 4.75E-02 0.041

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

Average

RunNumber 2 3 4

Tuesday, February 15, 2011 Page 17 of 47
Mass_mg 0.0000000171 0.0000000151 0.0000000198 0.000

lb/mmBtuO2 2.28E-12 2.12E-12 2.84E-12 0.000

ng/dscm 1.71E-03 1.59E-03 2.13E-03 0.002

ng/dscm@7%O2 2.64E-03 2.46E-03 3.30E-03 0.003

Compound: OCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000636 0.0000000534 0.0000000434 0.000

lb/mmBtuO2 8.46E-12 7.51E-12 6.24E-12 0.000

ng/dscm 6.35E-03 5.63E-03 4.66E-03 0.006

ng/dscm@7%O2 9.81E-03 8.70E-03 7.23E-03 0.009

Compound: OCDF

Average

RunNumber 2 3 4

Mass_mg 0.00000000356 0.00000000327 0.0000000034 0.000

lb/mmBtuO2 4.74E-13 4.60E-13 4.88E-13 0.000

ng/dscm 3.56E-04 3.45E-04 3.65E-04 0.000

ng/dscm@7%O2 5.50E-04 5.33E-04 5.66E-04 0.001

Compound: Other HpCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000257 0 0.0000000206 0.000

lb/mmBtuO2 3.42E-12 0.00E+00 2.96E-12 0.000

ng/dscm 2.57E-03 0.00E+00 2.21E-03 0.002

ng/dscm@7%O2 3.97E-03 0.00E+00 3.43E-03 0.002

Compound: Other HpCDF

Average

RunNumber 2 3 4

Mass_mg 0 0 0.00000000352 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 5.06E-13 0.000

ng/dscm 0.00E+00 0.00E+00 3.78E-04 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 5.86E-04 0.000

Compound: Other HxCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000839 0.00000000826 0.0000000487 0.000

lb/mmBtuO2 1.12E-11 1.16E-12 7.00E-12 0.000

ng/dscm 8.38E-03 8.71E-04 5.23E-03 0.005

ng/dscm@7%O2 1.29E-02 1.35E-03 8.11E-03 0.007

Compound: Other HxCDF

Average

RunNumber 2 3 4

Mass_mg 0.0000000684 0.00000000656 0.0000000565 0.000

lb/mmBtuO2 9.10E-12 9.22E-13 8.12E-12 0.000

ng/dscm 6.83E-03 6.91E-04 6.07E-03 0.005

ng/dscm@7%O2 1.05E-02 1.07E-03 9.42E-03 0.007

Tuesday, February 15, 2011 Page 18 of 47
Compound: Other PeCDD

Average

RunNumber 2 3 4

Mass_mg 0.000000156 0.00000000756 0.000000101 0.000

lb/mmBtuO2 2.08E-11 1.06E-12 1.45E-11 0.000

ng/dscm 1.56E-02 7.97E-04 1.08E-02 0.009

ng/dscm@7%O2 2.41E-02 1.23E-03 1.68E-02 0.014

Compound: Other PeCDF

Average

RunNumber 2 3 4

Mass_mg 0.000000301 0.00000000602 0.00000032 0.000

lb/mmBtuO2 4.01E-11 8.46E-13 4.60E-11 0.000

ng/dscm 3.01E-02 6.34E-04 3.44E-02 0.022

ng/dscm@7%O2 4.65E-02 9.80E-04 5.34E-02 0.034

Compound: Other TCDD

Average

RunNumber 2 3 4

Mass_mg 0.000000321 0.0000000221 0.000000222 0.000

lb/mmBtuO2 4.27E-11 3.11E-12 3.19E-11 0.000

ng/dscm 3.21E-02 2.33E-03 2.38E-02 0.019

ng/dscm@7%O2 4.96E-02 3.60E-03 3.69E-02 0.030

Compound: Other TCDF

Average

RunNumber 2 3 4

Mass_mg 0.000000811 0.000000032 0.000000823 0.000

lb/mmBtuO2 1.08E-10 4.50E-12 1.18E-10 0.000

ng/dscm 8.10E-02 3.37E-03 8.84E-02 0.058

ng/dscm@7%O2 1.25E-01 5.21E-03 1.37E-01 0.089

Compound: Total Dioxins

Average

RunNumber 2 3 4

Mass_mg 0.0000007236 0.00000011458 0.00000049112 0.000

lb/mmBtuO2 9.63E-11 1.61E-11 7.06E-11 0.000

ng/dscm 7.23E-02 1.21E-02 5.27E-02 0.046

ng/dscm@7%O2 1.12E-01 1.87E-02 8.18E-02 0.071

Compound: Total Furans

Average

RunNumber 2 3 4

Mass_mg 0.0000013609 0.00000007173 0.00000136531 0.000

lb/mmBtuO2 1.81E-10 1.01E-11 1.96E-10 0.000

ng/dscm 1.36E-01 7.56E-03 1.47E-01 0.097

ng/dscm@7%O2 2.10E-01 1.17E-02 2.28E-01 0.150

Compound: Total Mono-CBs

Average

RunNumber 2 3 4

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 19 of 47
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 2 3 4

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 2 3 4

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 2 3 4

Mass_mg 0.000003011 0.000003483 0.000003742 0.000

lb/mmBtuO2 4.01E-10 4.90E-10 5.38E-10 0.000

ng/dscm 3.01E-01 3.67E-01 4.02E-01 0.357

ng/dscm@7%O2 4.65E-01 5.67E-01 6.24E-01 0.552

Compound: Total PeCDD

Average

RunNumber 2 3 4

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 2 3 4

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 2 3 4

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 2 3 4

Tuesday, February 15, 2011 Page 20 of 47
Process Run Data

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 2 3 4

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 2 3 4

Mass_mg 0 0.000

lb/mmBtuO2 0.00E+00 0.000

ng/dscm #Num!

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

Tuesday, February 15, 2011 Page 21 of 47
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Distillate Oil (No. 1 & 2) Burned 1.5737 1000 Gallons 0

10 Distillate Oil (No. 1 & 2) Burned 1.6193 1000 Gallons 0

11 Distillate Oil (No. 1 & 2) Burned 1.6406 1000 Gallons 0

12 Distillate Oil (No. 1 & 2) Burned 1.5618 1000 Gallons 0

2 Distillate Oil (No. 1 & 2) Burned 1.5551 1000 Gallons 0

3 Distillate Oil (No. 1 & 2) Burned 1.5493 1000 Gallons 0

4 Distillate Oil (No. 1 & 2) Burned 1.5456 1000 Gallons 0

5 Distillate Oil (No. 1 & 2) Burned 1.5396 1000 Gallons 0

6 Distillate Oil (No. 1 & 2) Burned 1.5504 1000 Gallons 0

7 Distillate Oil (No. 1 & 2) Burned 1.552 1000 Gallons 0

8 Distillate Oil (No. 1 & 2) Burned 1.564 1000 Gallons 0

9 Distillate Oil (No. 1 & 2) Burned 1.604 1000 Gallons 0

1 Average Heat Input 217.41 MMBtu/hr 0

10 Average Heat Input 223.7 MMBtu/hr 0

11 Average Heat Input 226.65 MMBtu/hr 0

12 Average Heat Input 215.76 MMBtu/hr 0

2 Average Heat Input 214.84 MMBtu/hr 0

3 Average Heat Input 214.04 MMBtu/hr 0

4 Average Heat Input 213.52 MMBtu/hr 0

5 Average Heat Input 212.7 MMBtu/hr 0

6 Average Heat Input 214.19 MMBtu/hr 0

7 Average Heat Input 214.41 MMBtu/hr 0

8 Average Heat Input 216.07 MMBtu/hr 0

9 Average Heat Input 221.59 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 22 of 47
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 23 of 47
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 24 of 47
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 25 of 47
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 26 of 47
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 0 atm 0

10 Standard Pressure 0 atm 0

11 Standard Pressure 0 atm 0

12 Standard Pressure 0 atm 0

4 Standard Pressure 0 atm 0

5 Standard Pressure 0 atm 0

6 Standard Pressure 0 atm 0

7 Standard Pressure 0 atm 0

8 Standard Pressure 0 atm 0

9 Standard Pressure 0 atm 0

1 Standard Temperature 0 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 0 Deg F 0

5 Standard Temperature 0 Deg F 0

6 Standard Temperature 0 Deg F 0

7 Standard Temperature 0 Deg F 0

8 Standard Temperature 0 Deg F 0

9 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 13.59 MW 0

10 Unit Gross Electrical Output 14.41 MW 0

11 Unit Gross Electrical Output 15.08 MW 0

Tuesday, February 15, 2011 Page 27 of 47
APCD Run Data

Process Lab Run Data

12 Unit Gross Electrical Output 13.96 MW 0

4 Unit Gross Electrical Output 13.13 MW 0

5 Unit Gross Electrical Output 13.4 MW 0

6 Unit Gross Electrical Output 13.38 MW 0

7 Unit Gross Electrical Output 12.98 MW 0

8 Unit Gross Electrical Output 13.31 MW 0

9 Unit Gross Electrical Output 13.98 MW 0

1 Unit Net Electric Generation 12.78 MWh 0

10 Unit Net Electric Generation 13.33 MWh 0

11 Unit Net Electric Generation 14.14 MWh 0

12 Unit Net Electric Generation 13.16 MWh 0

4 Unit Net Electric Generation 12.25 MWh 0

5 Unit Net Electric Generation 12.21 MWh 0

6 Unit Net Electric Generation 12.45 MWh 0

7 Unit Net Electric Generation 12.46 MWh 0

8 Unit Net Electric Generation 12.61 MWh 0

9 Unit Net Electric Generation 12.95 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 28 of 47
1 Fuel Manganese Content 0 ppm

1 Fuel Chlorine Content 0 ppm

1 Fuel Fluorine Content 0 ppm

Tuesday, February 15, 2011 Page 29 of 47
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 30 of 47
Location Stack Exit - Method 23

Average

Run Number 2 3 4

Test Date 3/3/2010 3/4/2010 3/4/2010

Run Start Time 12:00:00 AM 9:30:00 AM 12:10:00 AM

Run Finish Time 11:55:00 PM 5:55:00 PM 11:50:00 PM

Net Traversing Points 96 96 96

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.25 0.25 0.25 0.250

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 29.46 29.26 29.2 29.307

Average Orifice Meter Differential, inches H2O 1.59 1.48 1.45 1.507

Dry Gas Meter Volume Sampled, cubic feet 336.760 329.736 316.230 327.575

Average Dry Gas Meter Temperature, °F 44.14 57.07 44.16 48.457

Dry Gas Meter Volume Sampled, dscf 353.535 335.130 328.935 339.200

Total Moisture Liquid collected, g 488.1 473.4 469.8 477.100

Volume of Water Vapor, standard cubic feet 22.97 22.28 22.11 22.453

Moisture Content of Stack Gas, % 6.10 6.23 6.30 6.210

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

Dry Mole Fraction 0.939 0.9377 0.937 0.938

Carbon Dioxide, % 6.7 6.51 6.52 6.577

Oxygen, % 11.9 11.91 11.94 11.917

Carbon Monoxide & Nitrogen, % 81.4 81.58 81.54 81.507

Fuel Factor 1.34 1.38 1.37

Dry Molecular Weight, lb/lb-Mole 29.55 29.52 29.52 29.530

Wet Molecular weight, lb/lb-Mole 28.85 28.80 28.79 28.813

Flue Gas Static Pressure, inches of H2O -0.22 -0.22 -0.22 -0.220

Absolute Flue Gas Pressure, inches of Mercury 29.44 29.24 29.18 29.287

Average Stack Gas Temperature, °F 287.65 287.47 285.65 286.923

Average Velocity Head, inches of H2O 0.7229526987

4778

0.642005349

640043

0.674988302

136405

0.680

Average Stack Gas Velocity, feet/second 57.29 54.21 55.58 55.693

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

Dry Volumetric Flow Rate, dry scfm 100,192.0 94,053.8 96,395.7 96,880.500

Actual Wet Volumetric Flue Gas Flow Rate, acfm 153,552.1 145,296.9 148,968.9 149,272.633

Percent Isokinetic of Sampling Rate, % 96.3 97.3 93.2 95.600

Percent Excess Air, % 124.1 123.7 124.5 124.100

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 31 of 47
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 32 of 47
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 33 of 47
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 34 of 47
Location Stack Exit - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor 0 -0.02 -0.06

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2 0 -1.68 -1.68 -1.120

Moisture, %

Analyzer Make

Analyzer Model Stack Exit Stack Exit Stack Exit

Analyzer Serial Number Method 3A 

CO2

Method 3A 

CO2

Method 3A 

CO2

Operating Range AG Run 1 AG Run 2 AG Run 3

Operating Units 3/5/2010 3/5/2010 3/5/2010

No. Readings/Avg. 10:22:00 AM 3:11:00 PM

Calibration Set 0 0 0 0.000

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift 0 0 6.43 2.143

Calibration Pre High Cylinder ID 6.44

Calibration Pre High Cylinder Instrument Response 0 0 11.94 3.980

Calibration Pre High Cylinder Bias 11.99 11.990

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID 0 0 0

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias 0 2 2 1.333

Calibration Post High Cylinder Drift Zero Zero

Cavg 0 -0.04 -0.04 -0.027

Cavg Units 0 -0.2 -0.2

Cgas 0 0 0 0.000

Cgas Units CC179326 CC179326

Fuel Type 0 8.64 8.64

Fw 0 0 0 0.000

Fc Zero Zero

Cgasw 0 -0.1 -0.3 -0.133

Cgasw Units 0 0.1 0.1

Tuesday, February 15, 2011 Page 35 of 47
Location Stack Exit - Method 3A CO2 3

Average

Run Number Hg-1 Hg-2 M23/HCHO 

R2

Test Date 3/2/2010 3/2/2010 3/3/2010

Run Start Time 3:30:00 AM 6:15:00 AM 9:45:00 PM

Run Finish Time 5:30:00 AM 8:15:00 AM 6:42:00 AM

Carbon Dioxide, % 7.07 7.07 6.55 6.897

Oxygen, % 11.52 11.55 11.83 11.633

Fuel Factor 1.33 1.32 1.38

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 2 2 21 8.333

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response -0.02 -0.02 -0.01 -0.017

Calibration Pre Zero Cylinder Bias -0.1 -0.1 0.2 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC179326 CC179326 CC179326

Calibration Pre High Cylinder Instrument Response 8.88 8.88 8.67 8.810

Calibration Pre High Cylinder Bias -0.5 -0.5 -0.45 -0.483

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.04 0.03 -0.03 0.013

Calibration Post Zero Cylinder Bias 0.2 0.15 0.1 0.150

Calibration Post Zero Cylinder Drift 0.3 0.25 0.1 0.217

Calibration Post High Cylinder ID CC179326 CC179326 CC179326

Calibration Post High Cylinder Instrument Response 8.86 8.85 8.74 8.817

Calibration Post High Cylinder Bias -0.59 -0.64 -0.1 -0.443

Calibration Post High Cylinder Drift 0.09 0.14 0.35 0.193

Cavg 7.07 7.07 6.55 6.897

Cavg Units %vd %vd %vd

Cgas 7.1716 7.1766 6.7771 7.042

Cgas Units %vd %vd %vd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, February 15, 2011 Page 36 of 47
Location Stack Exit - Method 3A CO2 3 6

Average

Run Number M23/HCHO 

R3

M23/HCHO 

R4

PM/Met-1

Test Date 3/4/2010 3/4/2010 3/1/2010

Run Start Time 9:30:00 AM 7:55:00 PM 1:40:00 AM

Run Finish Time 6:04:00 PM 4:00:00 AM 7:52:00 AM

Carbon Dioxide, % 6.52 6.54 6.84 6.633

Oxygen, % 11.9 11.94 11.86 11.900

Fuel Factor 1.38 1.37 1.32

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make Servomex

Analyzer Model 1440 1,440.000

Analyzer Serial Number 3893 3,893.000

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 21 21 2 14.667

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response -0.01 -0.01 -0.02 -0.013

Calibration Pre Zero Cylinder Bias 0.2 0.2 -0.1 0.100

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC179326 CC179326 CC179326

Calibration Pre High Cylinder Instrument Response 8.67 8.67 8.88 8.740

Calibration Pre High Cylinder Bias -0.45 -0.45 -0.5 -0.467

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response -0.08 -0.06 -0.05 -0.063

Calibration Post Zero Cylinder Bias -0.15 -0.05 -0.25 -0.150

Calibration Post Zero Cylinder Drift 0.35 0.25 0.15 0.250

Calibration Post High Cylinder ID CC179326 CC179326 CC179326

Calibration Post High Cylinder Instrument Response 8.72 8.74 8.86 8.773

Calibration Post High Cylinder Bias -0.2 -0.1 -0.59 -0.297

Calibration Post High Cylinder Drift 0.25 0.35 0.09 0.230

Cavg 6.52 6.54 6.84 6.633

Cavg Units %vd %vd %vd

Cgas 6.7603 6.7706 6.9483 6.826

Cgas Units %vd %vd %vd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, February 15, 2011 Page 37 of 47
Location Stack Exit - Method 3A CO2 3 6 9

Average

Run Number PM/Met-2 PM/Met-3 VOST/SVOL 

R1

Test Date 3/1/2010 3/1/2010 3/5/2010

Run Start Time 10:11:00 AM 8:00:00 PM 11:31:00 PM

Run Finish Time 5:18:00 PM 2:15:00 AM 2:09:00 AM

Carbon Dioxide, % 6.96 7.1 6.41 6.823

Oxygen, % 11.68 11.55 12.07 11.767

Fuel Factor 1.32 1.32 1.38

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response -0.02 -0.02 -0.04 -0.027

Calibration Pre Zero Cylinder Bias -0.1 -0.1 -0.2 -0.133

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC179326 CC179326 CC179326

Calibration Pre High Cylinder Instrument Response 8.88 8.88 8.64 8.800

Calibration Pre High Cylinder Bias -0.5 -0.5 -1.68 -0.893

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response -0.01 0.02 -0.03 -0.007

Calibration Post Zero Cylinder Bias -0.05 0.1 -0.15 -0.033

Calibration Post Zero Cylinder Drift 0.05 0.2 0.15 0.133

Calibration Post High Cylinder ID CC179326 CC179326 CC179326

Calibration Post High Cylinder Instrument Response 8.86 8.87 8.7 8.810

Calibration Post High Cylinder Bias -0.59 -0.54 -1.39 -0.840

Calibration Post High Cylinder Drift 0.09 0.04 1.39 0.507

Cavg 6.96 7.1 6.41 6.823

Cavg Units %vd %vd %vd

Cgas 7.0653 7.2 6.6634 6.976

Cgas Units %vd %vd %vd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, February 15, 2011 Page 38 of 47
Location Stack Exit - Method 3A CO2 3 6 9 12

Average

Run Number VOST/SVOLR2VOST/SVO

L-R3

Test Date 3/6/2010 3/6/2010

Run Start Time 2:46:00 AM 5:15:00 AM

Run Finish Time 4:57:00 AM 7:20:00 AM

Carbon Dioxide, % 6.44 6.71 6.575

Oxygen, % 12.04 11.69 11.865

Fuel Factor 1.38 1.37

Dry Volumetric Flow Rate, dry scfm 0 0 0.000

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

Moisture, % 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0.000

Calibration Set 2 2 2.000

Calibration Pre Zero Cylinder ID Zero Zero

Calibration Pre Zero Cylinder Instrument Response -0.04 -0.04 -0.040

Calibration Pre Zero Cylinder Bias -0.21 -0.2 -0.205

Calibration Pre Zero Cylinder Drift 0 0 0.000

Calibration Pre High Cylinder ID CC179326 CC179326

Calibration Pre High Cylinder Instrument Response 8.64 8.64 8.640

Calibration Pre High Cylinder Bias -1.68 -1.68 -1.680

Calibration Pre High Cylinder Drift 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero

Calibration Post Zero Cylinder Instrument Response -0.03 -0.02 -0.025

Calibration Post Zero Cylinder Bias -0.15 -0.1 -0.125

Calibration Post Zero Cylinder Drift 0.15 0.1 0.125

Calibration Post High Cylinder ID CC179326 CC179326

Calibration Post High Cylinder Instrument Response 8.7 8.7 8.700

Calibration Post High Cylinder Bias 44.66 -1.39 21.635

Calibration Post High Cylinder Drift 44.66 1.39 23.025

Cavg 6.44 6.71 6.575

Cavg Units %vd %vd

Cgas 6.6944 6.9724 6.833

Cgas Units %vd %vd

Fuel Type Oil Oil

Fw 10320 10320 10,320.000

Fc 1420 1420 1,420.000

Cgasw 0 0 0.000

Cgasw Units

Tuesday, February 15, 2011 Page 39 of 47
Location Stack Exit - Method 3A O2

Average

Run Number AG Run-1 AG Run-2 AG Run-3

Test Date 3/5/2010 3/6/2010 3/5/2010

Run Start Time 5:01:00 AM 10:22:00 AM 3:11:00 PM

Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM

Carbon Dioxide, % 6.42 6.44 6.43 6.430

Oxygen, % 11.9 11.99 11.94 11.943

Fuel Factor 1.4 1.38 1.39

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make Servomex

Analyzer Model 1440 1,440.000

Analyzer Serial Number 3839 3,839.000

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.03 0.03 0.03 0.030

Calibration Pre Zero Cylinder Bias 0.15 0.15 0.15 0.150

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC179326 CC179326 CC179326

Calibration Pre High Cylinder Instrument Response 8.93 8.93 8.93 8.930

Calibration Pre High Cylinder Bias 45.84 45.84 45.84 45.840

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.05 0.07 0.05 0.057

Calibration Post Zero Cylinder Bias 0.26 0.36 0.26 0.293

Calibration Post Zero Cylinder Drift 0.11 0.21 0.11 0.143

Calibration Post High Cylinder ID CC179326 CC179326 CC179326

Calibration Post High Cylinder Instrument Response 8.99 9.03 8.97 8.997

Calibration Post High Cylinder Bias 46.15 46.36 46.05 46.187

Calibration Post High Cylinder Drift 0.3099999999

99995

0.519999999

999996

0.209999999

999994

0.347

Cavg 11.9 11.99 11.94 11.943

Cavg Units %vd %vd %vd

Cgas 11.9664 12.0336 12.0202 12.007

Cgas Units %vd %vd %vd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, February 15, 2011 Page 40 of 47
Location Stack Exit - Method 3A O2 3

Average

Run Number Hg-1 Hg-2 M23/HCHO 

R2

Test Date 3/2/2010 3/2/2010 3/3/2010

Run Start Time 3:30:00 AM 6:15:00 AM 9:45:00 PM

Run Finish Time 5:30:00 AM 8:15:00 AM 6:42:00 AM

Carbon Dioxide, % 7.07 7.07 6.55 6.897

Oxygen, % 11.52 11.55 11.83 11.633

Fuel Factor 1.33 1.32 1.38

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 1 1 11 4.333

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response -0.01 -0.01 0.04 0.007

Calibration Pre Zero Cylinder Bias -0.05 -0.05 0.36 0.087

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC179326 CC179326 CC179326

Calibration Pre High Cylinder Instrument Response 9.17 9.17 8.97 9.103

Calibration Pre High Cylinder Bias 47.07 47.07 -0.36 31.260

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.06 0.05 0.04 0.050

Calibration Post Zero Cylinder Bias 0.31 0.26 0.36 0.310

Calibration Post Zero Cylinder Drift 0.36 0.31 0 0.223

Calibration Post High Cylinder ID CC179326 CC179326 CC179326

Calibration Post High Cylinder Instrument Response 9.15 9.15 9.01 9.103

Calibration Post High Cylinder Bias 46.97 46.97 -0.15 31.263

Calibration Post High Cylinder Drift 0.1000000000

00001

0.100000000

000001

0.21 0.137

Cavg 11.52 11.55 11.83 11.633

Cavg Units %vd %vd %vd

Cgas 11.3251 11.3534 11.8559 11.511

Cgas Units %vd %vd %vd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, February 15, 2011 Page 41 of 47
Location Stack Exit - Method 3A O2 3 6

Average

Run Number M23/HCHO 

R3

M23/HCHO 

R4

PM/MET-1

Test Date 3/4/2010 3/4/2010 3/1/2010

Run Start Time 9:30:00 AM 7:55:00 PM 1:40:00 AM

Run Finish Time 6:04:00 PM 4:00:00 AM 7:52:00 AM

Carbon Dioxide, % 6.52 6.54 6.84 6.633

Oxygen, % 11.9 11.94 11.86 11.900

Fuel Factor 1.38 1.37 1.32

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make Servomex

Analyzer Model 1440 1,440.000

Analyzer Serial Number 3893 3,893.000

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 11 11 1 7.667

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.04 0.04 -0.01 0.023

Calibration Pre Zero Cylinder Bias 0.36 0.36 -0.05 0.223

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC179326 CC179326 CC179326

Calibration Pre High Cylinder Instrument Response 8.97 8.97 9.17 9.037

Calibration Pre High Cylinder Bias -0.36 -0.36 47.07 15.450

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.01 0.04 0.08 0.043

Calibration Post Zero Cylinder Bias 0.21 0.36 0.41 0.327

Calibration Post Zero Cylinder Drift 0.21 0 0.46 0.223

Calibration Post High Cylinder ID CC179326 CC179326 CC179326

Calibration Post High Cylinder Instrument Response 8.99 9.02 9.2 9.070

Calibration Post High Cylinder Bias -0.26 -0.1 47.23 15.623

Calibration Post High Cylinder Drift 0.26 0.26 0.159999999

999997

0.227

Cavg 11.9 11.94 11.86 11.900

Cavg Units %vd %vd %vd

Cgas 11.9347 11.9598 11.6311 11.842

Cgas Units %vd %vd %vd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, February 15, 2011 Page 42 of 47
Location Stack Exit - Method 3A O2 3 6 9

Average

Run Number PM/Met-2 PM/Met-3 VOST/SVOL

-R1

Test Date 3/1/2010 3/1/2010 3/5/2010

Run Start Time 10:11:00 AM 8:00:00 PM 11:31:00 PM

Run Finish Time 5:18:00 PM 2:15:00 AM 2:09:00 AM

Carbon Dioxide, % 6.96 7.1 6.41 6.823

Oxygen, % 11.68 11.55 12.07 11.767

Fuel Factor 1.32 1.32 1.38

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response -0.01 -0.01 0.03 0.003

Calibration Pre Zero Cylinder Bias -0.05 -0.05 0.15 0.017

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC179326 CC179326 CC179326

Calibration Pre High Cylinder Instrument Response 9.17 9.17 8.93 9.090

Calibration Pre High Cylinder Bias 47.07 47.07 45.84 46.660

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.05 0.06 0.08 0.063

Calibration Post Zero Cylinder Bias 0.26 0.31 0.41 0.327

Calibration Post Zero Cylinder Drift 0.31 0.36 0.41 0.360

Calibration Post High Cylinder ID CC179326 CC179326 CC179326

Calibration Post High Cylinder Instrument Response 9.15 9.15 9.01 9.103

Calibration Post High Cylinder Bias 46.97 46.97 46.25 46.730

Calibration Post High Cylinder Drift 0.1000000000

00001

0.100000000

000001

46.25 15.483

Cavg 11.68 11.55 12.07 11.767

Cavg Units %vd %vd %vd

Cgas 11.4814 11.3547 12.1296 11.655

Cgas Units %vd %vd %vd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, February 15, 2011 Page 43 of 47
Location Stack Exit - Method 3A O2 3 6 9 12

Average

Run Number VOST/SVOLR2VOST/SVO

L-R3

Test Date 3/6/2010 3/6/2010

Run Start Time 2:46:00 AM 5:15:00 AM

Run Finish Time 4:57:00 AM 7:20:00 AM

Carbon Dioxide, % 6.44 6.71 6.575

Oxygen, % 12.04 11.69 11.865

Fuel Factor 1.38 1.37

Dry Volumetric Flow Rate, dry scfm 0 0 0.000

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

Moisture, % 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0.000

Calibration Set 1 1 1.000

Calibration Pre Zero Cylinder ID Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.03 0.03 0.030

Calibration Pre Zero Cylinder Bias 0.15 0.15 0.150

Calibration Pre Zero Cylinder Drift 0 0 0.000

Calibration Pre High Cylinder ID CC179326 CC179326

Calibration Pre High Cylinder Instrument Response 8.93 8.93 8.930

Calibration Pre High Cylinder Bias 45.84 45.84 45.840

Calibration Pre High Cylinder Drift 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.09 0.09 0.090

Calibration Post Zero Cylinder Bias 0.46 0.46 0.460

Calibration Post Zero Cylinder Drift 0.31 0.46 0.385

Calibration Post High Cylinder ID CC179326 CC179326

Calibration Post High Cylinder Instrument Response 9.01 9 9.005

Calibration Post High Cylinder Bias 46.25 46.2 46.225

Calibration Post High Cylinder Drift 0.4099999999

99997

46.2 23.305

Cavg 12.04 11.69 11.865

Cavg Units %vd %vd

Cgas 12.101 11.7541 11.928

Cgas Units %vd %vd

Fuel Type Oil Oil

Fw 10320 10320 10,320.000

Fc 1420 1420 1,420.000

Cgasw 0 0 0.000

Cgasw Units

Tuesday, February 15, 2011 Page 44 of 47
Location Stack Exit - Method 6C

Average

Run Number AG Run 1 AG Run 2 AG Run 3

Test Date 3/5/2010 3/5/2010 3/5/2010

Run Start Time 5:01:00 AM 10:22:00 AM 3:11:00 PM

Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM

Carbon Dioxide, % 6.42 6.44 6.43 6.430

Oxygen, % 11.9 11.99 11.94 11.943

Fuel Factor 1.4 1.38 1.39

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make Bovar Bovar Bovar

Analyzer Model 721-M 721-M 721-M

Analyzer Serial Number 1W-721M8560-61W-721M8560-61W-721M8560-6

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 41 41 41 41.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.55 1.97 -0.28 0.747

Calibration Pre Zero Cylinder Bias -0.16 1.38 -1.07 0.050

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID SA 7995 SA 7995 SA 7995

Calibration Pre High Cylinder Instrument Response 47.5 49.02 46.65 47.723

Calibration Pre High Cylinder Bias -1.96 -1.96 -2.88 -2.267

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 1.97 -0.3 -1.4 0.090

Calibration Post Zero Cylinder Bias 1.38 -1.09 -2.28 -0.663

Calibration Post Zero Cylinder Drift 1.54 0.98 2.28 1.600

Calibration Post High Cylinder ID SA 7995 SA 7995 SA 7995

Calibration Post High Cylinder Instrument Response 49.02 46.7 45.1 46.940

Calibration Post High Cylinder Bias -0.3 -2.83 -4.57 -2.567

Calibration Post High Cylinder Drift 1.66 0.87 4.57 2.367

Cavg 8.05 8.19 5.78 7.340

Cavg Units ppmvd ppmvd ppmvd

Cgas 6.9634 7.5388 6.8304 7.111

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, February 15, 2011 Page 45 of 47
Location Stack Exit - Method 7E

Average

Run Number AG Run 1 AG Run 2 AG Run 3

Test Date 3/5/2010 3/5/2010 3/5/2010

Run Start Time 5:01:00 AM 10:22:00 AM 3:11:00 PM

Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM

Carbon Dioxide, % 6.42 6.44 6.43 6.430

Oxygen, % 11.9 11.99 11.94 11.943

Fuel Factor 1.4 1.38 1.39

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make Teledyne Teledyne Teledyne

Analyzer Model 200 EH 200 EH 200 EH

Analyzer Serial Number 172 172 172 172.000

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 31 31 31 31.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.87 0.83 0.07 0.590

Calibration Pre Zero Cylinder Bias 0.36 -0.03 -0.34 -0.003

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC116930 CC116930 CC116930

Calibration Pre High Cylinder Instrument Response 124.2 123.8 123.72 123.907

Calibration Pre High Cylinder Bias 0.49 -0.93 -0.96 -0.467

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.83 0.07 0.05 0.317

Calibration Post Zero Cylinder Bias 0.34 0.14 -0.35 0.043

Calibration Post Zero Cylinder Drift 0.02 0.22 9.999999999

99995E-03

0.083

Calibration Post High Cylinder ID CC116930 CC116930 CC116930

Calibration Post High Cylinder Instrument Response 123.8 123.72 124.17 123.897

Calibration Post High Cylinder Bias 0.33 0.3 0.48 0.370

Calibration Post High Cylinder Drift 0.16 0.19 0.48 0.277

Cavg 73.3 72.7 73.3 73.100

Cavg Units ppmvd ppmvd ppmvd

Cgas 72.3618 72.0684 72.7168 72.382

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0 0 0 0.000

Cgasw Units

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