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 12
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:

70 70

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 312 0 0 0 624 2496 4 3

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Tuesday, February 15, 2011 Page 2 of 12
The following describes any modifications and/or deviations to the applicable test 

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

of request AND approval, including dates.

Stack Exit Antimony Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

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

Tuesday, February 15, 2011 Page 3 of 12
Sampling / Stack Data Results Summary

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 8:20:00 AM 2:40:00 PM 8:20:00 AM

Run Finish Time 1:15:00 PM 7:10:00 PM 12:50:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 136.587 133.297 135.375 135.086

Moisture Content of Stack Gas, % 13.12 13.55 11.59 12.753

Moisture Saturation at Stack Gas Temperature, % 12.24 12.66 12.14 12.347

Carbon Dioxide, % 11.1 10.8 11.6 11.167

Oxygen, % 8 7.8 8 7.933

Average Stack Gas Temperature, °F 121.13 122.33 120.98 121.480

Dry Volumetric Flow Rate, dry scfm 1,224,579.9 1,214,985.4 1,230,951.3 1,223,505.53

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,584,504.5 1,582,911.7 1,573,036.4 1,580,150.86

7

Percent Isokinetic of Sampling Rate, % 102.6 100.9 101.1 101.533

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 4 of 12
Location Stack Exit - Method 5/OTM-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 5 of 12
Emissions Summary

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0019 0.0016 0.001 0.002

Elb/hr 2.25E-03 1.93E-03 1.20E-03 0.002

lb/mmBtuO2 4.86E-07 4.13E-07 2.58E-07 0.000

mg/dscm 4.91E-04 4.24E-04 2.61E-04 0.000

mg/dscm@7%O2 5.29E-04 4.50E-04 2.81E-04 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0174 0.0147 0.009 0.014

Elb/hr 2.06E-02 1.77E-02 1.08E-02 0.016

lb/mmBtuO2 4.45E-06 3.79E-06 2.32E-06 0.000

mg/dscm 4.50E-03 3.90E-03 2.35E-03 0.004

mg/dscm@7%O2 4.85E-03 4.14E-03 2.53E-03 0.004

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.001 0.0009 0.0005 0.001

Elb/hr 1.19E-03 1.09E-03 6.01E-04 0.001

lb/mmBtuO2 2.56E-07 2.32E-07 1.29E-07 0.000

mg/dscm 2.59E-04 2.38E-04 1.30E-04 0.000

mg/dscm@7%O2 2.79E-04 2.53E-04 1.40E-04 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0017 0.0013 0.0009 0.001

Elb/hr 2.02E-03 1.57E-03 1.08E-03 0.002

lb/mmBtuO2 4.35E-07 3.35E-07 2.32E-07 0.000

mg/dscm 4.40E-04 3.44E-04 2.35E-04 0.000

mg/dscm@7%O2 4.74E-04 3.65E-04 2.53E-04 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0285 0.0153 0.018 0.021

Elb/hr 3.38E-02 1.84E-02 2.17E-02 0.025

lb/mmBtuO2 7.29E-06 3.95E-06 4.64E-06 0.000

mg/dscm 7.37E-03 4.05E-03 4.70E-03 0.005

mg/dscm@7%O2 7.94E-03 4.30E-03 5.06E-03 0.006

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.0016 0.0012 0.0011 0.001

Elb/hr 1.90E-03 1.45E-03 1.32E-03 0.002

Tuesday, February 15, 2011 Page 6 of 12
lb/mmBtuO2 4.09E-07 3.10E-07 2.84E-07 0.000

mg/dscm 4.14E-04 3.18E-04 2.87E-04 0.000

mg/dscm@7%O2 4.46E-04 3.37E-04 3.09E-04 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 116.6 117 108.2 113.933

Elb/hr 1.38E+02 1.41E+02 1.30E+02 136.333

lb/mmBtuO2 2.98E-02 3.02E-02 2.79E-02 0.029

mg/dscm 3.02E+01 3.10E+01 2.82E+01 29.800

mg/dscm@7%O2 3.25E+01 3.29E+01 3.04E+01 31.933

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.0192 0.0559 0.0248 0.033

Elb/hr 2.28E-02 6.74E-02 2.98E-02 0.040

lb/mmBtuO2 4.91E-06 1.44E-05 6.40E-06 0.000

mg/dscm 4.96E-03 1.48E-02 6.47E-03 0.009

mg/dscm@7%O2 5.34E-03 1.57E-02 6.97E-03 0.009

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0266 0.0122 0.0143 0.018

Elb/hr 3.15E-02 1.47E-02 1.72E-02 0.021

lb/mmBtuO2 6.80E-06 3.15E-06 3.69E-06 0.000

mg/dscm 6.88E-03 3.23E-03 3.73E-03 0.005

mg/dscm@7%O2 7.41E-03 3.43E-03 4.02E-03 0.005

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0382 0.0182 0.0133 0.023

Elb/hr 4.53E-02 2.19E-02 1.60E-02 0.028

lb/mmBtuO2 9.77E-06 4.70E-06 3.43E-06 0.000

mg/dscm 9.88E-03 4.82E-03 3.47E-03 0.006

mg/dscm@7%O2 1.06E-02 5.11E-03 3.74E-03 0.006

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0901 0.0792 0.0748 0.081

Elb/hr 1.07E-01 9.55E-02 9.00E-02 0.098

lb/mmBtuO2 2.30E-05 2.04E-05 1.93E-05 0.000

mg/dscm 2.33E-02 2.10E-02 1.95E-02 0.021

mg/dscm@7%O2 2.51E-02 2.23E-02 2.10E-02 0.023

Location: Stack Exit - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Tuesday, February 15, 2011 Page 7 of 12
Process Run Data

Mass_mg 56.7 34.7 55.9 49.100

Elb/hr 6.68E+01 4.23E+01 6.77E+01 58.933

gr/dscf 6.46E-03 4.12E-03 6.61E-03 0.006

lb/mmBtuO2 1.46E-02 9.19E-03 1.50E-02 0.013

mg/dscm 1.48E+01 9.44E+00 1.51E+01 13.113

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 87.6 122.4 60 90.000

Elb/hr 1.03E+02 1.49E+02 7.26E+01 108.200

gr/dscf 9.98E-03 1.45E-02 7.10E-03 0.011

lb/mmBtuO2 2.26E-02 3.24E-02 1.61E-02 0.024

mg/dscm 2.28E+01 3.33E+01 1.62E+01 24.100

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 2.8 2.7 1.7 2.400

Elb/hr 3.30E+00 3.29E+00 2.06E+00 2.883

gr/dscf 3.19E-04 3.21E-04 2.01E-04 0.000

lb/mmBtuO2 7.22E-04 7.15E-04 4.55E-04 0.001

mg/dscm 7.30E-01 7.34E-01 4.60E-01 0.641

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 147.1 159.8 117.6 141.500

Elb/hr 1.73E+02 1.95E+02 1.42E+02 170.000

gr/dscf 1.68E-02 1.90E-02 1.39E-02 0.017

lb/mmBtuO2 3.79E-02 4.23E-02 3.15E-02 0.037

mg/dscm 3.83E+01 4.35E+01 3.18E+01 37.867

Tuesday, February 15, 2011 Page 8 of 12
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

1 Average Heat Input 3981.5 MMBtu/hr 0

2 Average Heat Input 4077.8 MMBtu/hr 0

3 Average Heat Input 3955.4 MMBtu/hr 0

1 Steam Output 2915.6 1000 lb steam/hr 0

2 Steam Output 2968.1 1000 lb steam/hr 0

3 Steam Output 2926.3 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 0

2 Synfuel Firing Rate 0 0

3 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

1 Coal Gas Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

3 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

1 Flue Gas Flow Rate 0 dscfm 0

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

1 FGD Scrubber Liquor pH 0.92 pH 0

1 FGD Scrubber Liquor Flow Rate 247.12 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

Tuesday, February 15, 2011 Page 9 of 12
APCD Run Data

Process Lab Run Data

1 Unit Gross Electrical Output 445.22 MW 0

1 Unit Net Electric Generation 417.38 MWh 0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 OVERFIRE AIR 0 0

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 0

1 DRY SORBENT INJECTION 0 0

1 ELECTROSTATIC PRECIPITATOR 0 0

1 CAUSTIC SCRUBBER 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 10 of 12
Sampling / Stack Data Results Detail

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 8:20:00 AM 2:40:00 PM 8:20:00 AM

Run Finish Time 1:15:00 PM 7:10:00 PM 12:50:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.21 0.21 0.21 0.210

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.017 1.017 1.017 1.017

Barometric Pressure, inches of Mercury 29.05 29.05 29.19 29.097

Average Orifice Meter Differential, inches H2O 0.95 0.95 0.94 0.947

Dry Gas Meter Volume Sampled, cubic feet 142.552 141.271 140.329 141.384

Average Dry Gas Meter Temperature, °F 85.44 93.88 84.33 87.883

Dry Gas Meter Volume Sampled, dscf 136.587 133.297 135.375 135.086

Total Moisture Liquid collected, g 438.2 443.9 377 419.700

Volume of Water Vapor, standard cubic feet 20.63 20.89 17.75 19.757

Moisture Content of Stack Gas, % 13.12 13.55 11.59 12.753

Moisture Saturation at Stack Gas Temperature, % 12.24 12.66 12.14 12.347

Dry Mole Fraction 0.8776 0.8734 0.8841 0.878

Carbon Dioxide, % 11.1 10.8 11.6 11.167

Oxygen, % 8 7.8 8 7.933

Carbon Monoxide & Nitrogen, % 80.9 81.4 80.4 80.900

Fuel Factor 1.16 1.21 1.11

Dry Molecular Weight, lb/lb-Mole 30.10 30.04 30.18 30.107

Wet Molecular weight, lb/lb-Mole 28.78 28.68 28.77 28.743

Flue Gas Static Pressure, inches of H2O -0.72 -0.72 -0.72 -0.720

Absolute Flue Gas Pressure, inches of Mercury 29.00 29.00 29.14 29.047

Average Stack Gas Temperature, °F 121.13 122.33 120.98 121.480

Average Velocity Head, inches of H2O 0.6889862053

62234

0.683835888

151936

0.682322674

348332

0.685

Average Stack Gas Velocity, feet/second 49.74 49.69 49.38 49.603

Stack Cross-Sectional Area, square feet 530.929 530.929 530.929 530.929

Dry Volumetric Flow Rate, dry scfm 1,224,579.9 1,214,985.4 1,230,951.3 1,223,505.5

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,584,504.5 1,582,911.7 1,573,036.4 1,580,150.8

67

Percent Isokinetic of Sampling Rate, % 102.6 100.9 101.1 101.533

Percent Excess Air, % 59.9 57.0 60.5 59.133

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

Round Duct Diameter, inches 312 312 312

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 11 of 12
Location Stack Exit - Method 5/OTM-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 12 of 12