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 15
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:

60 60

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 !!!!UPDATE NEEDED!!!

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 1809700033 FRS #: 110000396991

SCC / Description 10100212 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Tangential) (Bituminous Coal) 

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 116 0 0 0 232 928 4 3

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 15
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 15
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 15
Sampling / Stack Data Results Summary

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 3/13/2010 3/13/2010 3/14/2010

Run Start Time 9:05:00 AM 4:10:00 PM 9:00:00 AM

Run Finish Time 3:19:00 PM 10:26:00 

PM

3:15:00 PM

Net Run Time, minutes 360 360 360

Dry Gas Meter Volume Sampled, dscf 273.193 265.504 263.965 267.554

Moisture Content of Stack Gas, % 9.07 9.28 9.20 9.183

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

Carbon Dioxide, % 11.6 11.1 11.3 11.333

Oxygen, % 6.2 6.9 6.7 6.600

Average Stack Gas Temperature, °F 342.01 341.96 340.04 341.337

Dry Volumetric Flow Rate, dry scfm 262,261.1 255,435.1 259,395.0 259,030.400

Actual Wet Volumetric Flue Gas Flow Rate, acfm 434,181.2 423,833.0 442,327.6 433,447.267

Percent Isokinetic of Sampling Rate, % 102.4 102.2 100.0 101.533

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, February 15, 2011 Page 5 of 15
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 6 of 15
Emissions Summary

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0082 0.0081 0.0089 0.008

Elb/hr 1.04E-03 1.03E-03 1.16E-03 0.001

lb/mmBtuO2 9.20E-07 9.82E-07 1.07E-06 0.000

mg/dscm 1.06E-03 1.08E-03 1.19E-03 0.001

mg/dscm@7%O2 1.00E-03 1.07E-03 1.16E-03 0.001

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0919 0.1368 0.1217 0.117

Elb/hr 1.17E-02 1.74E-02 1.58E-02 0.015

lb/mmBtuO2 1.03E-05 1.66E-05 1.46E-05 0.000

mg/dscm 1.19E-02 1.82E-02 1.63E-02 0.015

mg/dscm@7%O2 1.13E-02 1.81E-02 1.60E-02 0.015

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.0053 0.0054 0.006 0.006

Elb/hr 6.73E-04 6.87E-04 7.80E-04 0.001

lb/mmBtuO2 5.95E-07 6.55E-07 7.21E-07 0.000

mg/dscm 6.85E-04 7.18E-04 8.03E-04 0.001

mg/dscm@7%O2 6.48E-04 7.13E-04 7.86E-04 0.001

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0031 0.0028 0.0035 0.003

Elb/hr 3.94E-04 3.56E-04 4.55E-04 0.000

lb/mmBtuO2 3.48E-07 3.39E-07 4.21E-07 0.000

mg/dscm 4.01E-04 3.72E-04 4.68E-04 0.000

mg/dscm@7%O2 3.79E-04 3.69E-04 4.58E-04 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0219 0.0186 0.031 0.024

Elb/hr 2.78E-03 2.37E-03 4.03E-03 0.003

lb/mmBtuO2 2.46E-06 2.25E-06 3.73E-06 0.000

mg/dscm 2.83E-03 2.47E-03 4.15E-03 0.003

mg/dscm@7%O2 2.68E-03 2.45E-03 4.06E-03 0.003

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.01 0.0101 0.0112 0.010

Elb/hr 1.27E-03 1.29E-03 1.46E-03 0.001

Tuesday, February 15, 2011 Page 7 of 15
lb/mmBtuO2 1.12E-06 1.22E-06 1.35E-06 0.000

mg/dscm 1.29E-03 1.34E-03 1.50E-03 0.001

mg/dscm@7%O2 1.22E-03 1.33E-03 1.47E-03 0.001

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 93.8 93.2 156.8 114.600

Elb/hr 1.19E+01 1.19E+01 2.04E+01 14.733

lb/mmBtuO2 1.05E-02 1.13E-02 1.89E-02 0.014

mg/dscm 1.21E+01 1.24E+01 2.10E+01 15.167

mg/dscm@7%O2 1.14E+01 1.23E+01 2.06E+01 14.767

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.0543 0.0597 0.0614 0.058

Elb/hr 6.90E-03 7.60E-03 7.98E-03 0.007

lb/mmBtuO2 6.09E-06 7.24E-06 7.38E-06 0.000

mg/dscm 7.02E-03 7.94E-03 8.22E-03 0.008

mg/dscm@7%O2 6.64E-03 7.88E-03 8.05E-03 0.008

Compound: Magnesium

Average

RunNumber 1 2 3

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 1 2 3

Mass_mg 0.0193 0.0203 0.0228 0.021

Elb/hr 2.45E-03 2.58E-03 2.96E-03 0.003

lb/mmBtuO2 2.17E-06 2.46E-06 2.74E-06 0.000

mg/dscm 2.50E-03 2.70E-03 3.05E-03 0.003

mg/dscm@7%O2 2.36E-03 2.68E-03 2.99E-03 0.003

Compound: Mercury

Average

RunNumber 1 2 3

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: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.053 0.05 0.0585 0.054

Elb/hr 6.73E-03 6.36E-03 7.60E-03 0.007

Tuesday, February 15, 2011 Page 8 of 15
Process Run Data

lb/mmBtuO2 5.95E-06 6.06E-06 7.03E-06 0.000

mg/dscm 6.85E-03 6.65E-03 7.83E-03 0.007

mg/dscm@7%O2 6.48E-03 6.60E-03 7.66E-03 0.007

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 1.1764 0.8553 0.9822 1.005

Elb/hr 1.49E-01 1.09E-01 1.28E-01 0.129

lb/mmBtuO2 1.32E-04 1.04E-04 1.18E-04 0.000

mg/dscm 1.52E-01 1.14E-01 1.31E-01 0.132

mg/dscm@7%O2 1.44E-01 1.13E-01 1.28E-01 0.128

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 85.8 100.5 75.3 87.200

lb/mmBtuO2 1.95E-02 2.32E-02 1.73E-02 0.020

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 37.3 47.1 42.8 42.400

lb/mmBtuO2 8.46E-03 1.09E-02 9.83E-03 0.010

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 43.1 161 125 109.700

lb/mmBtuO2 9.78E-03 3.71E-02 2.87E-02 0.025

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 101 72.4 38.7 70.700

lb/mmBtuO2 2.29E-02 1.67E-02 8.89E-03 0.016

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 229.9 333.9 239 267.600

lb/mmBtuO2 5.22E-02 7.70E-02 5.49E-02 0.061

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 181.4 280.5 206.5 222.800

lb/mmBtuO2 4.12E-02 6.46E-02 4.74E-02 0.051

Tuesday, February 15, 2011 Page 9 of 15
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 0 Tons/hr 0

2 Bituminous Coal Burned 0 Tons/hr 0

3 Bituminous Coal Burned 0 Tons/hr 0

4 Bituminous Coal Burned 0 Tons/hr 0

5 Bituminous Coal Burned 0 Tons/hr 0

6 Bituminous Coal Burned 0 Tons/hr 0

1 Average Heat Input 936.76 MMBtu/hr 0

2 Average Heat Input 947.33 MMBtu/hr 0

3 Average Heat Input 970.11 MMBtu/hr 0

4 Average Heat Input 1063.4 MMBtu/hr 0

5 Average Heat Input 783.04 MMBtu/hr 0

6 Average Heat Input 1072.6 MMBtu/hr 0

1 Steam Output 755.85 1000 lb steam/hr 0

2 Steam Output 753.2 1000 lb steam/hr 0

3 Steam Output 762.43 1000 lb steam/hr 0

4 Steam Output 804.2 1000 lb steam/hr 0

5 Steam Output 578.51 1000 lb steam/hr 0

6 Steam Output 751.82 1000 lb steam/hr 0

1 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

1 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

1 Coal Gas Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

Tuesday, February 15, 2011 Page 10 of 15
4 Coal Gas Firing Rate 0 0

5 Coal Gas Firing Rate 0 0

6 Coal Gas Firing Rate 0 0

1 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

1 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

1 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

1 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

1 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

1 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

1 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

1 Flue Gas Carbon Dioxide Content 0 % 0

Tuesday, February 15, 2011 Page 11 of 15
APCD Run Data

4 Flue Gas Carbon Dioxide Content 0 % 0

5 Flue Gas Carbon Dioxide Content 0 % 0

6 Flue Gas Carbon Dioxide Content 0 % 0

1 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

1 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

1 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

1 Standard Pressure 0 atm 0

4 Standard Pressure 0 atm 0

5 Standard Pressure 0 atm 0

6 Standard Pressure 0 atm 0

1 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

1 Unit Gross Electrical Output 103.63 MW 0

4 Unit Gross Electrical Output 109.89 MW 0

5 Unit Gross Electrical Output 79.97 MW 0

6 Unit Gross Electrical Output 103.4 MW 0

1 Unit Net Electric Generation 98.61 MWh 0

4 Unit Net Electric Generation 104.68 MWh 0

5 Unit Net Electric Generation 75.41 MWh 0

6 Unit Net Electric Generation 98.35 MWh 0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 OVERFIRE AIR 0 0

Tuesday, February 15, 2011 Page 12 of 15
Process Lab Run Data

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 0

1 ELECTROSTATIC PRECIPITATOR 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

1 Fuel Manganese Content 0 ppm

1 Fuel Chlorine Content 0 ppm

1 Fuel Fluorine Content 0 ppm

Tuesday, February 15, 2011 Page 13 of 15
Sampling / Stack Data Results Detail

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 3/13/2010 3/13/2010 3/14/2010

Run Start Time 9:05:00 AM 4:10:00 PM 9:00:00 AM

Run Finish Time 3:19:00 PM 10:26:00 PM 3:15:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 360 360 360

Nozzle Diameter, inches 0.195 0.195 0.195 0.195

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9925 0.9925 0.9925 0.993

Barometric Pressure, inches of Mercury 29.67 29.67 28.77 29.370

Average Orifice Meter Differential, inches H2O 1.98 1.87 1.99 1.947

Dry Gas Meter Volume Sampled, cubic feet 272.481 265.255 269.510 269.082

Average Dry Gas Meter Temperature, °F 60.85 61.58 57.10 59.843

Dry Gas Meter Volume Sampled, dscf 273.193 265.504 263.965 267.554

Total Moisture Liquid collected, g 578.8 576.9 567.9 574.533

Volume of Water Vapor, standard cubic feet 27.24 27.15 26.73 27.040

Moisture Content of Stack Gas, % 9.07 9.28 9.20 9.183

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

Dry Mole Fraction 0.9093 0.9072 0.908 0.908

Carbon Dioxide, % 11.6 11.1 11.3 11.333

Oxygen, % 6.2 6.9 6.7 6.600

Carbon Monoxide & Nitrogen, % 82.2 82 82 82.067

Fuel Factor 1.27 1.26 1.26

Dry Molecular Weight, lb/lb-Mole 30.10 30.05 30.08 30.077

Wet Molecular weight, lb/lb-Mole 29.00 28.93 28.97 28.967

Flue Gas Static Pressure, inches of H2O 7.1 7.1 7 7.067

Absolute Flue Gas Pressure, inches of Mercury 30.19 30.19 29.28 29.887

Average Stack Gas Temperature, °F 342.01 341.96 340.04 341.337

Average Velocity Head, inches of H2O 2.0580368800

2385

1.956386724

39042

2.074705522

24057

2.030

Average Stack Gas Velocity, feet/second 98.60 96.25 100.45 98.433

Stack Cross-Sectional Area, square feet 73.391 73.391 73.391 73.391

Dry Volumetric Flow Rate, dry scfm 262,261.1 255,435.1 259,395.0 259,030.400

Actual Wet Volumetric Flue Gas Flow Rate, acfm 434,181.2 423,833.0 442,327.6 433,447.267

Percent Isokinetic of Sampling Rate, % 102.4 102.2 100.0 101.533

Percent Excess Air, % 40.0 46.8 44.8 43.867

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 116 116 116

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, February 15, 2011 Page 14 of 15
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 15 of 15