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.

Saturday, January 15, 2011 Page 1 of 30
Facility Information:

AES Warrior Run

11600 Mexico Farms Road

Cumberland MD 21502

Contact: Jeff Leaf

Phone: 301-777-0055 X 167

Fax: 301-777-8772

Email: jeff.leaf@aes.com

Testing Company:

URS Corporation

1600 Perimeter Park Drive, Suite 400

Morrisville NC 27560

Contact:Brad Justus

Phone: 919-461-1326

Fax: 919-461-1415

Email: brad_justus@urscorp.com

Air Permit Number:

10678

Permitted Source ID/Name:

Unit 1

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:

AES Warrior Run Unit 1 is rated at 180 MW. The unit combusts eastern bituminous coal and consists of a circulating 

fluidized bed combustor, selective non-catalytic reduction (SNCR) to reduce NOX emissions, and a fabric filter for 

control of particulate matter.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 2400100203 FRS #: 2400100203

SCC / Description 10100218 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Atmospheric Fluidized Bed Combustion: Circulating Bed (Bitum. 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 147 0 0 0 190 50 4 24

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 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

Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 480 0

Saturday, January 15, 2011 Page 2 of 30
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

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Organic Condensible 

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

Inorganic (Aqueous) 

Condensible Part.

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Saturday, January 15, 2011 Page 3 of 30
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.

None

Total Particulate 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

Stack Exit Filterable Particulate Method 29 3 360 0

Stack Exit Antimony Method 29 3 360 0

Stack Exit Arsenic Method 29 3 360 0

Stack Exit Beryllium Method 29 3 360 0

Stack Exit Cadmium Method 29 3 360 0

Stack Exit Chromium Method 29 3 360 0

Stack Exit Lead Method 29 3 360 0

Stack Exit Manganese Method 29 3 360 0

Stack Exit Selenium Method 29 3 360 0

Stack Exit Cobalt Method 29 3 360 0

Stack Exit Nickel Method 29 3 360 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit Co2 Method 3A CO2 3 240 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Saturday, January 15, 2011 Page 4 of 30
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 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

Saturday, January 15, 2011 Page 5 of 30
Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 3/24/2010 3/25/2010 3/26/2010

Run Start Time 6:30:00 PM 5:32:00 PM 3:00:00 PM

Run Finish Time 10:00:00 PM 9:10:00 PM 6:29:30 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 120.504 121.060 123.356 121.640

Moisture Content of Stack Gas, % 6.74 6.79 5.98 6.503

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

Carbon Dioxide, % 15.7 15.2 15.1 15.333

Oxygen, % 4.2 4.5 4.1 4.267

Average Stack Gas Temperature, °F 308.29 309.92 295.75 304.653

Dry Volumetric Flow Rate, dry scfm 408,048.0 409,672.8 405,214.8 407,645.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 654,824.6 666,280.5 637,782.2 652,962.433

Percent Isokinetic of Sampling Rate, % 99.2 99.3 102.3 100.267

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

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

Saturday, January 15, 2011 Page 6 of 30
Location Stack Exit - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 3A CO2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Saturday, January 15, 2011 Page 7 of 30
Location Stack Exit - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Saturday, January 15, 2011 Page 8 of 30
Location Stack Exit - Method 3A O2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 3A O2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Saturday, January 15, 2011 Page 9 of 30
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

Saturday, January 15, 2011 Page 10 of 30
Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.90E-01 2.28E-01 2.22E-01 0.213

ppm 2.10E+02 2.57E+02 2.46E+02 237.667

ppm@7%O2 1.78E+02 2.14E+02 2.08E+02 200.000

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.02E-03 1.14E-03 1.34E-03 0.001

ppm 7.15E-01 8.18E-01 9.39E-01 0.824

ppm@7%O2 6.06E-01 6.80E-01 7.94E-01 0.693

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 72.094 72.125 66.055 70.091

Elb/hr 3.23E+01 3.23E+01 2.87E+01 31.100

lb/mmBtuO2 1.61E-02 1.64E-02 1.44E-02 0.016

mg/dscm 2.11E+01 2.10E+01 1.89E+01 20.333

mg/dscm@7%O2 1.76E+01 1.78E+01 1.56E+01 17.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.254 0.256 0.247 0.252

Elb/hr 1.14E-01 1.15E-01 1.07E-01 0.112

lb/mmBtuO2 5.69E-05 5.81E-05 5.37E-05 0.000

mg/dscm 7.44E-02 7.47E-02 7.07E-02 0.073

mg/dscm@7%O2 6.19E-02 6.33E-02 5.85E-02 0.061

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00015 0.00009 0.00011 0.000

Elb/hr 3.50E-05 2.10E-05 2.55E-05 0.000

lb/mmBtuO2 1.81E-08 1.12E-08 1.40E-08 0.000

mg/dscm 2.38E-05 1.47E-05 1.74E-05 0.000

mg/dscm@7%O2 1.97E-05 1.22E-05 1.53E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00119 0.0008 0.00087 0.001

Elb/hr 2.78E-04 1.86E-04 2.01E-04 0.000

Saturday, January 15, 2011 Page 11 of 30
lb/mmBtuO2 1.44E-07 9.91E-08 1.11E-07 0.000

mg/dscm 1.89E-04 1.31E-04 1.37E-04 0.000

mg/dscm@7%O2 1.56E-04 1.08E-04 1.21E-04 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00016 0.00009 0.00011 0.000

Elb/hr 3.74E-05 2.10E-05 2.55E-05 0.000

lb/mmBtuO2 1.93E-08 1.12E-08 1.40E-08 0.000

mg/dscm 2.54E-05 1.47E-05 1.74E-05 0.000

mg/dscm@7%O2 2.10E-05 1.22E-05 1.53E-05 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00057 0.0007 0.00152 0.001

Elb/hr 1.33E-04 1.63E-04 3.52E-04 0.000

lb/mmBtuO2 6.88E-08 8.67E-08 1.94E-07 0.000

mg/dscm 9.05E-05 1.14E-04 2.40E-04 0.000

mg/dscm@7%O2 7.49E-05 9.43E-05 2.11E-04 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0123 0.0081 0.0069 0.009

Elb/hr 2.87E-03 1.89E-03 1.60E-03 0.002

lb/mmBtuO2 1.48E-06 1.00E-06 8.79E-07 0.000

mg/dscm 1.95E-03 1.32E-03 1.09E-03 0.001

mg/dscm@7%O2 1.61E-03 1.09E-03 9.59E-04 0.001

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00173 0.001 0.00146 0.001

Elb/hr 4.04E-04 2.33E-04 3.38E-04 0.000

lb/mmBtuO2 2.09E-07 1.24E-07 1.86E-07 0.000

mg/dscm 2.75E-04 1.63E-04 2.30E-04 0.000

mg/dscm@7%O2 2.28E-04 1.35E-04 2.02E-04 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 20.8 52.8 29.7 34.433

Elb/hr 4.86E+00 1.23E+01 6.88E+00 8.013

lb/mmBtuO2 2.51E-03 6.54E-03 3.78E-03 0.004

mg/dscm 3.30E+00 8.62E+00 4.69E+00 5.537

mg/dscm@7%O2 2.73E+00 7.13E+00 4.13E+00 4.663

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00295 0.00235 0.00305 0.003

Elb/hr 6.89E-04 5.47E-04 7.06E-04 0.001

Saturday, January 15, 2011 Page 12 of 30
lb/mmBtuO2 3.56E-07 2.91E-07 3.89E-07 0.000

mg/dscm 4.69E-04 3.83E-04 4.81E-04 0.000

mg/dscm@7%O2 3.88E-04 3.17E-04 4.23E-04 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.00963 0.00374 0.00615 0.007

Elb/hr 2.25E-03 8.71E-04 1.42E-03 0.002

lb/mmBtuO2 1.16E-06 4.63E-07 7.84E-07 0.000

mg/dscm 1.53E-03 6.10E-04 9.71E-04 0.001

mg/dscm@7%O2 1.27E-03 5.05E-04 8.54E-04 0.001

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.01392 0.00792 0.00682 0.010

Elb/hr 3.25E-03 1.84E-03 1.58E-03 0.002

lb/mmBtuO2 1.68E-06 9.81E-07 8.69E-07 0.000

mg/dscm 2.21E-03 1.29E-03 1.08E-03 0.002

mg/dscm@7%O2 1.83E-03 1.07E-03 9.50E-04 0.001

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.00056 0.00052 0.00052 0.001

Elb/hr 1.31E-04 1.21E-04 1.20E-04 0.000

lb/mmBtuO2 6.75E-08 6.44E-08 6.63E-08 0.000

mg/dscm 8.89E-05 8.49E-05 8.21E-05 0.000

mg/dscm@7%O2 7.36E-05 7.02E-05 7.22E-05 0.000

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 61.6 43.3 133.4 79.433

lb/mmBtuO2 1.28E-02 8.98E-03 2.96E-02 0.017

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 47.2 34.7 107.2 63.033

lb/mmBtuO2 9.78E-03 7.20E-03 2.38E-02 0.014

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 10.8 49.8 9.3 23.300

lb/mmBtuO2 2.24E-03 1.03E-02 2.06E-03 0.005

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Saturday, January 15, 2011 Page 13 of 30
Process Run Data

Mass_mg 9.3 7.5 104 40.267

lb/mmBtuO2 1.93E-03 1.56E-03 2.31E-02 0.009

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 81.7 100.6 246.7 143.000

lb/mmBtuO2 1.69E-02 2.09E-02 5.47E-02 0.031

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 34.5 65.9 139.5 79.967

lb/mmBtuO2 7.15E-03 1.37E-02 3.09E-02 0.017

Saturday, January 15, 2011 Page 14 of 30
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 0 Tons 0

2 Bituminous Coal Burned 0 Tons 0

3 Bituminous Coal Burned 0 Tons 0

4 Bituminous Coal Burned 0 Tons 0

5 Bituminous Coal Burned 0 Tons 0

6 Bituminous Coal Burned 0 Tons 0

7 Bituminous Coal Burned 0 Tons 0

8 Bituminous Coal Burned 0 Tons 0

9 Bituminous Coal Burned 0 Tons 0

1 Average Heat Input 2026.7 MMBtu/hr 0

2 Average Heat Input 2027.6 MMBtu/hr 0

3 Average Heat Input 2061.9 MMBtu/hr 0

4 Average Heat Input 2066.8 MMBtu/hr 0

5 Average Heat Input 2020.9 MMBtu/hr 0

6 Average Heat Input 2050.6 MMBtu/hr 0

7 Average Heat Input 1956.1 MMBtu/hr 0

8 Average Heat Input 2109.5 MMBtu/hr 0

9 Average Heat Input 2048.4 MMBtu/hr 0

1 Steam Output 1264.3 1000 lb steam/hr 0

2 Steam Output 1267.1 1000 lb steam/hr 0

3 Steam Output 1262.4 1000 lb steam/hr 0

4 Steam Output 1270.3 1000 lb steam/hr 0

5 Steam Output 1270.6 1000 lb steam/hr 0

6 Steam Output 1267.4 1000 lb steam/hr 0

7 Steam Output 1267.4 1000 lb steam/hr 0

8 Steam Output 1268.5 1000 lb steam/hr 0

9 Steam Output 1263.2 1000 lb steam/hr 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

Saturday, January 15, 2011 Page 15 of 30
7 Fuel Oil Firing Rate 0 0

8 Fuel Oil Firing Rate 0 0

9 Fuel Oil Firing Rate 0 0

1 Standard Pressure 0 atm 0

2 Standard Pressure 0 atm 0

3 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

2 Standard Temperature 0 Deg F 0

3 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 202.01 MW 0

2 Unit Gross Electrical Output 202.52 MW 0

3 Unit Gross Electrical Output 202.07 MW 0

4 Unit Gross Electrical Output 202.63 MW 0

5 Unit Gross Electrical Output 202.78 MW 0

6 Unit Gross Electrical Output 203.19 MW 0

7 Unit Gross Electrical Output 203.83 MW 0

8 Unit Gross Electrical Output 203.65 MW 0

9 Unit Gross Electrical Output 202.34 MW 0

1 Unit Net Electric Generation 181.42 MWh 0

2 Unit Net Electric Generation 181.42 MWh 0

3 Unit Net Electric Generation 181.42 MWh 0

4 Unit Net Electric Generation 181.42 MWh 0

5 Unit Net Electric Generation 181.42 MWh 0

6 Unit Net Electric Generation 181.42 MWh 0

Saturday, January 15, 2011 Page 16 of 30
APCD Run Data

Process Lab Run Data

7 Unit Net Electric Generation 181.42 MWh 0

8 Unit Net Electric Generation 181.42 MWh 0

9 Unit Net Electric Generation 181.42 MWh 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 12336 Btu/lb

2 Fuel Higher Heating Value 11601 Btu/lb

3 Fuel Higher Heating Value 11808 Btu/lb

4 Fuel Higher Heating Value 11488 Btu/lb

5 Fuel Higher Heating Value 11330 Btu/lb

6 Fuel Higher Heating Value 11355 Btu/lb

7 Fuel Higher Heating Value 11677 Btu/lb

8 Fuel Higher Heating Value 11788 Btu/lb

9 Fuel Higher Heating Value 11740 Btu/lb

1 Fuel Moisture 4.1 %

2 Fuel Moisture 5.8 %

3 Fuel Moisture 6.4 %

4 Fuel Moisture 5.6 %

5 Fuel Moisture 7.9 %

6 Fuel Moisture 6.5 %

7 Fuel Moisture 6.2 %

8 Fuel Moisture 5 %

9 Fuel Moisture 7.3 %

1 Fuel Mercury Content 0 ppm

2 Fuel Mercury Content 0 ppm

3 Fuel Mercury Content 0 ppm

4 Fuel Mercury Content 0 ppm

5 Fuel Mercury Content 0 ppm

6 Fuel Mercury Content 0 ppm

7 Fuel Mercury Content 0.291 ppm

8 Fuel Mercury Content 0.249 ppm

9 Fuel Mercury Content 0.254 ppm

1 Fuel Cadmium Content 0 ppm

2 Fuel Cadmium Content 0 ppm

3 Fuel Cadmium Content 0 ppm

4 Fuel Cadmium Content 0 ppm

5 Fuel Cadmium Content 0 ppm

6 Fuel Cadmium Content 0 ppm

Saturday, January 15, 2011 Page 17 of 30
7 Fuel Cadmium Content

0 ppm

8 Fuel Cadmium Content0 ppm

9 Fuel Cadmium Content0 ppm

1 Ultimate/Proximate Analysis0

2 Ultimate/Proximate Analysis0

3 Ultimate/Proximate Analysis0

4 Ultimate/Proximate Analysis0

5 Ultimate/Proximate Analysis0

6 Ultimate/Proximate Analysis0

7 Ultimate/Proximate Analysis0

8 Ultimate/Proximate Analysis0

9 Ultimate/Proximate Analysis0

1 Fuel Nickel Content0 ppm

2 Fuel Nickel Content0 ppm

3 Fuel Nickel Content0 ppm

4 Fuel Nickel Content0 ppm

5 Fuel Nickel Content0 ppm

6 Fuel Nickel Content0 ppm

7 Fuel Nickel Content0 ppm

8 Fuel Nickel Content0 ppm

9 Fuel Nickel Content0 ppm

1 Fuel Arsenic Content0 ppm

2 Fuel Arsenic Content0 ppm

3 Fuel Arsenic Content0 ppm

4 Fuel Arsenic Content0 ppm

5 Fuel Arsenic Content0 ppm

6 Fuel Arsenic Content0 ppm

7 Fuel Arsenic Content 9.9 ppm 8 Fuel Arsenic Content 15 ppm 9 Fuel Arsenic Content 9.4 ppm 1 Fuel Chromium Content 0 ppm 2 Fuel Chromium Content 0 ppm 3 Fuel Chromium Content 0 ppm 4 Fuel Chromium Content 0 ppm 5 Fuel Chromium Content 0 ppm 6 Fuel Chromium Content 0 ppm 7 Fuel Chromium Content 8.2 ppm 8 Fuel Chromium Content 9.4 ppm 9 Fuel Chromium Content 7.7 ppm 1 Fuel Beryllium Content 0 ppm 2 Fuel Beryllium Content 0 ppm 3 Fuel Beryllium Content 0 ppm 4 Fuel Beryllium Content 0 ppm

Saturday, January 15, 2011 Page 18 of 30
5 Fuel Beryllium Content

0 ppm

6 Fuel Beryllium Content0 ppm

7 Fuel Beryllium Content 0.7 ppm 8 Fuel Beryllium Content 0.71 ppm 9 Fuel Beryllium Content 0.69 ppm 1 Fuel Lead Content 0 ppm 2 Fuel Lead Content 0 ppm 3 Fuel Lead Content 0 ppm 4 Fuel Lead Content 0 ppm 5 Fuel Lead Content 0 ppm 6 Fuel Lead Content 0 ppm 7 Fuel Lead Content 8.5 ppm 8 Fuel Lead Content 11 ppm 9 Fuel Lead Content 7.9 ppm 1 Fuel Manganese Content 0 ppm 2 Fuel Manganese Content 0 ppm 3 Fuel Manganese Content 0 ppm 4 Fuel Manganese Content 0 ppm 5 Fuel Manganese Content 0 ppm 6 Fuel Manganese Content 0 ppm 7 Fuel Manganese Content 33 ppm 8 Fuel Manganese Content 43 ppm 9 Fuel Manganese Content 45 ppm 1 Fuel Chlorine Content 280 ppm 2 Fuel Chlorine Content 280 ppm 3 Fuel Chlorine Content 240 ppm 4 Fuel Chlorine Content 0 ppm 5 Fuel Chlorine Content 0 ppm 6 Fuel Chlorine Content 0 ppm 7 Fuel Chlorine Content 240 ppm 8 Fuel Chlorine Content 230 ppm 9 Fuel Chlorine Content 270 ppm 1 Fuel Fluorine Content 69 ppm 2 Fuel Fluorine Content 92 ppm 3 Fuel Fluorine Content 87 ppm 4 Fuel Fluorine Content 0 ppm 5 Fuel Fluorine Content 0 ppm 6 Fuel Fluorine Content 0 ppm 7 Fuel Fluorine Content 0 ppm 8 Fuel Fluorine Content 0 ppm 9 Fuel Fluorine Content 0 ppm

Saturday, January 15, 2011 Page 19 of 30
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

Saturday, January 15, 2011 Page 20 of 30
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

Saturday, January 15, 2011 Page 21 of 30
Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 3/24/2010 3/25/2010 3/26/2010

Run Start Time 6:30:00 PM 5:32:00 PM 3:00:00 PM

Run Finish Time 10:00:00 PM 9:10:00 PM 6:29:30 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.189 0.189 0.189 0.189

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 29.19 28.88 29.04 29.037

Average Orifice Meter Differential, inches H2O 1.37 1.36 1.40 1.377

Dry Gas Meter Volume Sampled, cubic feet 120.685 124.235 121.545 122.155

Average Dry Gas Meter Temperature, °F 64.92 72.17 53.83 63.640

Dry Gas Meter Volume Sampled, dscf 120.504 121.060 123.356 121.640

Total Moisture Liquid collected, g 185.1 187.3 166.5 179.633

Volume of Water Vapor, standard cubic feet 8.71 8.82 7.84 8.457

Moisture Content of Stack Gas, % 6.74 6.79 5.98 6.503

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

Dry Mole Fraction 0.9326 0.9321 0.9402 0.935

Carbon Dioxide, % 15.7 15.2 15.1 15.333

Oxygen, % 4.2 4.5 4.1 4.267

Carbon Monoxide & Nitrogen, % 80.1 80.3 80.8 80.400

Fuel Factor 1.06 1.08 1.11

Dry Molecular Weight, lb/lb-Mole 30.68 30.61 30.58 30.623

Wet Molecular weight, lb/lb-Mole 29.83 29.75 29.83 29.803

Flue Gas Static Pressure, inches of H2O -1.4 -1.4 -1.4 -1.400

Absolute Flue Gas Pressure, inches of Mercury 29.09 28.78 28.94 28.937

Average Stack Gas Temperature, °F 308.29 309.92 295.75 304.653

Average Velocity Head, inches of H2O 1.8781521952

7651

1.914492366

47505

1.801592919

42618

1.865

Average Stack Gas Velocity, feet/second 92.60 94.22 90.19 92.337

Stack Cross-Sectional Area, square feet 117.859 117.859 117.859 117.859

Dry Volumetric Flow Rate, dry scfm 408,048.0 409,672.8 405,214.8 407,645.200

Actual Wet Volumetric Flue Gas Flow Rate, acfm 654,824.6 666,280.5 637,782.2 652,962.433

Percent Isokinetic of Sampling Rate, % 99.2 99.3 102.3 100.267

Percent Excess Air, % 24.8 26.9 23.8 25.167

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

Round Duct Diameter, inches 147 147 147

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

Saturday, January 15, 2011 Page 22 of 30
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

Saturday, January 15, 2011 Page 23 of 30
Location Stack Exit - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, January 15, 2011 Page 24 of 30
Location Stack Exit - Method 3A CO2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, January 15, 2011 Page 25 of 30
Location Stack Exit - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, January 15, 2011 Page 26 of 30
Location Stack Exit - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, January 15, 2011 Page 27 of 30
Location Stack Exit - Method 3A O2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, January 15, 2011 Page 28 of 30
Location Stack Exit - Method 3A O2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, January 15, 2011 Page 29 of 30
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

Saturday, January 15, 2011 Page 30 of 30