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.

Friday, January 14, 2011 Page 1 of 47
Facility Information:

AES Deepwater

701 Light Company Rd

Pasadena TX 77506

Contact: Ken Niznik

Phone: (713)472-8687

Fax:

Email:

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:

10670

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:

Units 1 is rated at 160 MW (gross), combusts 100% pulverized petroleum coke, and consists of a wall-fired 

combustor equipped with LNB/OFA, a dry ESP, selective catalytic reduction (SCR), wet FGD, and a wet ESP to 

reduce air emissions.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 4820100405 FRS #: 110000462785

SCC / Description 10100801 External Combustion Boilers - Electric Generation - Petroleum Coke - All Boiler 

Sizes 

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 204 0 0 0 1632 408 4 12

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

Friday, January 14, 2011 Page 2 of 47
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 3 480 0

Stack Exit Other PeCDD Method 23 3 480 0

Stack Exit Other HxCDD Method 23 3 480 0

Stack Exit Other HpCDD Method 23 3 480 0

Stack Exit Other TCDF Method 23 3 480 0

Stack Exit Other PeCDF Method 23 3 480 0

Stack Exit Other HxCDF Method 23 3 480 0

Stack Exit Other HpCDF Method 23 3 480 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 Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Antimony 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

Stack Exit Manganese Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium 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 3 240 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit O2 Method 3A O2 3 480 0

Friday, January 14, 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.

None

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit Co2 Method 3A CO2 3 240 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit Filterable Particulate Method 5/OTM-28 3 240 0

Stack Exit Total Particulate Method 5/OTM-28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit Method 5/OTM-28 3 240 0

Organic Condensible 

Particulate

Stack Exit Method 5/OTM-28 3 240 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Friday, January 14, 2011 Page 4 of 47
Sampling / Stack Data Results Summary

Location Stack Exit - Method 10

Average

Run Number 1 Form 2 Form 3 Form

Test Date 7/24/2010 7/24/2010 7/24/2010

Run Start Time 7:53:00 AM 10:25:00 

AM

1:24:00 PM

Run Finish Time 10:07:00 AM 12:47:00 

PM

3:37:00 PM

Carbon Dioxide, % 12.81 13.15 13.18 13.047

Oxygen, % 6.72 6.32 6.24 6.427

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000

Moisture, % 0 0 0 0.000

Fuel Type Override Override Override

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 7/24/2010 7/25/2010 7/26/2010

Run Start Time 8:53:00 AM 8:05:00 

AM

7:03:00 AM

Run Finish Time 5:39:00 PM 5:17:00 PM 5:56:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 287.616 302.781 305.320 298.572

Moisture Content of Stack Gas, % 13.34 13.18 13.58 13.367

Moisture Saturation at Stack Gas Temperature, % 31.84 31.37 31.22 31.477

Carbon Dioxide, % 13 13 13 13.000

Oxygen, % 6.4 6.3 6.3 6.333

Average Stack Gas Temperature, °F 158.76 158.10 157.91 158.257

Dry Volumetric Flow Rate, dry scfm 451,824.6 446,296.5 440,530.8 446,217.300

Actual Wet Volumetric Flue Gas Flow Rate, acfm 622,651.5 613,663.1 608,351.8 614,888.800

Percent Isokinetic of Sampling Rate, % 95.8 96.4 98.5 96.900

F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Friday, January 14, 2011 Page 5 of 47
Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 7/24/2010 7/24/2010 7/24/2010

Run Start Time 7:53:00 AM 10:25:00 

AM

1:24:00 PM

Run Finish Time 10:07:00 AM 12:47:00 

PM

3:37:00 PM

Carbon Dioxide, % 12.81 13.15 13.18 13.047

Oxygen, % 6.72 6.32 6.24 6.427

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000

Moisture, % 0 0 0 0.000

Fuel Type Override Override Override

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 8/18/2010 8/19/2010 8/19/2010

Run Start Time 2:36:00 PM 8:55:00 

AM

12:23:00 PM

Run Finish Time 5:50:00 PM 12:08:00 

PM

3:33:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 104.282 106.823 108.390 106.498

Moisture Content of Stack Gas, % 13.02 13.23 13.56 13.270

Moisture Saturation at Stack Gas Temperature, % 30.95 30.29 30.35 30.530

Carbon Dioxide, % 12.3 11.9 11.9 12.033

Oxygen, % 6.9 6.9 6.7 6.833

Average Stack Gas Temperature, °F 158.08 157.17 157.28 157.510

Dry Volumetric Flow Rate, dry scfm 462,071.5 474,430.2 480,363.9 472,288.533

Actual Wet Volumetric Flue Gas Flow Rate, acfm 626,056.2 643,624.5 653,838.6 641,173.100

Percent Isokinetic of Sampling Rate, % 99.5 99.3 99.5 99.433

F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Friday, January 14, 2011 Page 6 of 47
Location Stack Exit - Method 29 

Average

Run Number 1 2 3

Test Date 8/3/2010 8/3/2010 8/4/2010

Run Start Time 7:40:00 AM 1:23:00 PM 7:32:00 AM

Run Finish Time 12:05:00 PM 6:11:00 PM 12:00:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 162.570 162.529 168.316 164.472

Moisture Content of Stack Gas, % 13.65 11.88 13.69 13.073

Moisture Saturation at Stack Gas Temperature, % 33.38 33.74 33.58 33.567

Carbon Dioxide, % 12.7 13 12.8 12.833

Oxygen, % 6.6 6.5 6.9 6.667

Average Stack Gas Temperature, °F 160.73 161.15 160.98 160.953

Dry Volumetric Flow Rate, dry scfm 472,730.2 478,564.5 481,343.7 477,546.133

Actual Wet Volumetric Flue Gas Flow Rate, acfm 655,881.4 651,523.4 668,410.7 658,605.167

Percent Isokinetic of Sampling Rate, % 97.7 96.5 99.4 97.867

F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 3A CO2

Average

Run Number 1 DF 1 Form 1 Hg

Test Date 7/24/2010 7/24/2010 7/25/2010

Run Start Time 8:53:00 AM 7:53:00 

AM

7:18:00 AM

Run Finish Time 5:39:00 PM 10:07:00 

AM

9:40:00 AM

Carbon Dioxide, % 13.11 12.81 12.81 12.910

Oxygen, % 6.33 6.72 6.65 6.567

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Friday, January 14, 2011 Page 7 of 47
Location Stack Exit - Method 3A CO2 3

Average

Run Number 1 ORG 1 PM 2 DF

Test Date 7/23/2010 8/3/2010 7/25/2010

Run Start Time 8:13:00 AM 7:40:00 

AM

8:05:00 AM

Run Finish Time 10:54:00 AM 12:05:00 

PM

5:17:00 PM

Carbon Dioxide, % 13.04 12.84 13.1 12.993

Oxygen, % 6.46 6.62 6.27 6.450

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 3A CO2 3 6

Average

Run Number 2 Form 2 Hg 2 ORG

Test Date 7/24/2010 7/25/2010 7/23/2010

Run Start Time 10:25:00 AM 10:53:00 

AM

11:36:00 AM

Run Finish Time 12:47:00 PM 1:07:00 PM 1:52:00 PM

Carbon Dioxide, % 13.15 13.16 13.14 13.150

Oxygen, % 6.32 6.23 6.29 6.280

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Friday, January 14, 2011 Page 8 of 47
Location Stack Exit - Method 3A CO2 3 6 9

Average

Run Number 2 PM 3 DF 3 Form

Test Date 8/3/2010 7/26/2010 7/24/2010

Run Start Time 1:23:00 PM 6:21:00 

AM

1:24:00 PM

Run Finish Time 6:11:00 PM 6:01:00 PM 3:37:00 PM

Carbon Dioxide, % 12.97 13.07 13.18 13.073

Oxygen, % 6.4 6.31 6.24 6.317

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

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

Average

Run Number 3 Hg 3 ORG 3 PM

Test Date 7/25/2010 7/23/2010 8/4/2010

Run Start Time 1:46:00 PM 2:39:00 PM 7:32:00 AM

Run Finish Time 3:52:00 PM 5:37:00 PM 12:00:00 PM

Carbon Dioxide, % 13.19 13.15 12.9 13.080

Oxygen, % 6.16 6.23 6.52 6.303

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2

Moisture, % 0 0 0 0.000

Fuel Type

Fw

Fc

Friday, January 14, 2011 Page 9 of 47
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

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

Friday, January 14, 2011 Page 10 of 47
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

Location Stack Exit - Method 3A O2 3 6 9

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Friday, January 14, 2011 Page 11 of 47
Location Stack Exit - Method 3A O2 3 6 9 12

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 5/OTM-28

Average

Run Number 1 2 3

Test Date 8/3/2010 8/3/2010 8/4/2010

Run Start Time 7:40:00 AM 1:23:00 PM 7:32:00 AM

Run Finish Time 12:05:00 PM 6:11:00 PM 12:00:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 154.524 147.779 151.689 151.331

Moisture Content of Stack Gas, % 13.63 13.52 13.65 13.600

Moisture Saturation at Stack Gas Temperature, % 33.64 34.32 33.64 33.867

Carbon Dioxide, % 13 13 12.8 12.933

Oxygen, % 6.4 6.3 6.6 6.433

Average Stack Gas Temperature, °F 161.06 161.90 161.06 161.340

Dry Volumetric Flow Rate, dry scfm 450,901.9 448,805.9 455,800.9 451,836.233

Actual Wet Volumetric Flue Gas Flow Rate, acfm 625,783.9 622,923.9 632,729.4 627,145.733

Percent Isokinetic of Sampling Rate, % 97.4 93.6 94.6 95.200

F-Factor, dscfm/MMBtu @ %O2 99360 9936 9936 39,744.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, January 14, 2011 Page 12 of 47
Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 Form 2 Form 3 Form

lb/mmBtuO2 5.92E-02 1.74E-01 1.81E-01 0.138

ppm 5.56E+01 1.68E+02 1.75E+02 132.867

ppm@7%O2 5.45E+01 1.60E+02 1.66E+02 126.833

Location: Stack Exit - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000277 0.00000000244 0.00000000401 0.000

lb/mmBtuO2 3.04E-13 2.53E-13 4.12E-13 0.000

ng/dscm 3.40E-04 2.85E-04 4.64E-04 0.000

ng/dscm@7%O2 3.26E-04 2.71E-04 4.42E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000175 0.00000000672 0.0000000154 0.000

lb/mmBtuO2 1.92E-12 6.96E-13 1.58E-12 0.000

ng/dscm 2.15E-03 7.84E-04 1.78E-03 0.002

ng/dscm@7%O2 2.06E-03 7.46E-04 1.69E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000112 0.00000000989 0.0000000209 0.000

lb/mmBtuO2 1.23E-12 1.02E-12 2.15E-12 0.000

ng/dscm 1.38E-03 1.15E-03 2.42E-03 0.002

ng/dscm@7%O2 1.32E-03 1.09E-03 2.30E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000215 0.00000000212 0.00000000287 0.000

lb/mmBtuO2 2.36E-13 2.20E-13 2.95E-13 0.000

ng/dscm 2.64E-04 2.47E-04 3.32E-04 0.000

ng/dscm@7%O2 2.53E-04 2.35E-04 3.16E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000297 0.00000000118 0.00000000195 0.000

lb/mmBtuO2 3.26E-13 1.22E-13 2.00E-13 0.000

ng/dscm 3.65E-04 1.38E-04 2.26E-04 0.000

ng/dscm@7%O2 3.50E-04 1.31E-04 2.15E-04 0.000

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

Average

Friday, January 14, 2011 Page 13 of 47
RunNumber 1 2 3

Mass_mg 0.00000000212 0.00000000207 0.00000000308 0.000

lb/mmBtuO2 2.33E-13 2.14E-13 3.16E-13 0.000

ng/dscm 2.60E-04 2.41E-04 3.56E-04 0.000

ng/dscm@7%O2 2.49E-04 2.29E-04 3.39E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000113 0.00000000111 0.00000000205 0.000

lb/mmBtuO2 1.24E-13 1.15E-13 2.11E-13 0.000

ng/dscm 1.39E-04 1.29E-04 2.37E-04 0.000

ng/dscm@7%O2 1.33E-04 1.23E-04 2.26E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000215 0.00000000203 0.00000000286 0.000

lb/mmBtuO2 2.36E-13 2.10E-13 2.94E-13 0.000

ng/dscm 2.64E-04 2.37E-04 3.31E-04 0.000

ng/dscm@7%O2 2.53E-04 2.26E-04 3.15E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000144 0.00000000131 0.00000000223 0.000

lb/mmBtuO2 1.58E-13 1.36E-13 2.29E-13 0.000

ng/dscm 1.77E-04 1.53E-04 2.58E-04 0.000

ng/dscm@7%O2 1.70E-04 1.46E-04 2.46E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000266 0.00000000217 0.00000000345 0.000

lb/mmBtuO2 2.92E-13 2.25E-13 3.54E-13 0.000

ng/dscm 3.27E-04 2.53E-04 3.99E-04 0.000

ng/dscm@7%O2 3.13E-04 2.41E-04 3.80E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000228 0.000000002 0.00000000299 0.000

lb/mmBtuO2 2.50E-13 2.07E-13 3.07E-13 0.000

ng/dscm 2.80E-04 2.33E-04 3.46E-04 0.000

ng/dscm@7%O2 2.68E-04 2.22E-04 3.29E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000728 0.00000000673 0.00000000751 0.000

lb/mmBtuO2 7.99E-13 6.97E-13 7.71E-13 0.000

ng/dscm 8.94E-04 7.85E-04 8.69E-04 0.001

ng/dscm@7%O2 8.57E-04 7.47E-04 8.27E-04 0.001

Friday, January 14, 2011 Page 14 of 47
Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 1 2 3

Mass_mg 0.0000000143 0.0000000148 0.0000000155 0.000

lb/mmBtuO2 1.57E-12 1.53E-12 1.59E-12 0.000

ng/dscm 1.76E-03 1.73E-03 1.79E-03 0.002

ng/dscm@7%O2 1.69E-03 1.65E-03 1.70E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.000000072 0.000000095 0.000000102 0.000

lb/mmBtuO2 7.90E-12 9.84E-12 1.05E-11 0.000

ng/dscm 8.84E-03 1.11E-02 1.18E-02 0.011

ng/dscm@7%O2 8.47E-03 1.06E-02 1.12E-02 0.010

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000396 0.0000000044 0.00000000592 0.000

lb/mmBtuO2 4.35E-13 4.56E-13 6.08E-13 0.000

ng/dscm 4.86E-04 5.13E-04 6.85E-04 0.001

ng/dscm@7%O2 4.66E-04 4.88E-04 6.52E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000399 0.00000000903 0.00000000898 0.000

lb/mmBtuO2 4.38E-13 9.35E-13 9.22E-13 0.000

ng/dscm 4.90E-04 1.05E-03 1.04E-03 0.001

ng/dscm@7%O2 4.70E-04 1.00E-03 9.90E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000164 0.000000229 0.000000258 0.000

lb/mmBtuO2 1.80E-11 2.37E-11 2.65E-11 0.000

ng/dscm 2.01E-02 2.67E-02 2.98E-02 0.026

ng/dscm@7%O2 1.93E-02 2.54E-02 2.84E-02 0.024

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000393 0.00000000724 0.0000000085 0.000

lb/mmBtuO2 4.31E-13 7.50E-13 8.73E-13 0.000

ng/dscm 4.83E-04 8.45E-04 9.83E-04 0.001

ng/dscm@7%O2 4.63E-04 8.04E-04 9.36E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000116 0.00000000116 0.00000000195 0.000

lb/mmBtuO2 1.27E-13 1.20E-13 2.00E-13 0.000

Friday, January 14, 2011 Page 15 of 47
ng/dscm 1.42E-04 1.35E-04 2.26E-04 0.000

ng/dscm@7%O2 1.36E-04 1.29E-04 2.15E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000215 0.00000000193 0.00000000296 0.000

lb/mmBtuO2 2.36E-13 2.00E-13 3.04E-13 0.000

ng/dscm 2.64E-04 2.25E-04 3.42E-04 0.000

ng/dscm@7%O2 2.53E-04 2.14E-04 3.26E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000192 0.00000000184 0.00000000308 0.000

lb/mmBtuO2 2.11E-13 1.91E-13 3.16E-13 0.000

ng/dscm 2.36E-04 2.15E-04 3.56E-04 0.000

ng/dscm@7%O2 2.26E-04 2.05E-04 3.39E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000151 0.00000000216 0.00000000279 0.000

lb/mmBtuO2 1.66E-13 2.24E-13 2.87E-13 0.000

ng/dscm 1.85E-04 2.52E-04 3.23E-04 0.000

ng/dscm@7%O2 1.77E-04 2.40E-04 3.08E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000399 0.00000000409 0.00000000561 0.000

lb/mmBtuO2 4.38E-13 4.24E-13 5.76E-13 0.000

ng/dscm 4.90E-04 4.77E-04 6.49E-04 0.001

ng/dscm@7%O2 4.70E-04 4.54E-04 6.18E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000315 0.00000000653 0.00000000953 0.000

lb/mmBtuO2 3.46E-13 6.76E-13 9.79E-13 0.000

ng/dscm 3.87E-04 7.62E-04 1.10E-03 0.001

ng/dscm@7%O2 3.71E-04 7.25E-04 1.05E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000298 0.0000000455 0.000000047 0.000

lb/mmBtuO2 3.27E-12 4.71E-12 4.83E-12 0.000

ng/dscm 3.66E-03 5.31E-03 5.44E-03 0.005

ng/dscm@7%O2 3.51E-03 5.06E-03 5.18E-03 0.005

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

Average

RunNumber 1 2 3

Friday, January 14, 2011 Page 16 of 47
Mass_mg 0.00000000188 0.0000000038 0.00000000493 0.000

lb/mmBtuO2 2.06E-13 3.94E-13 5.06E-13 0.000

ng/dscm 2.31E-04 4.43E-04 5.70E-04 0.000

ng/dscm@7%O2 2.21E-04 4.22E-04 5.43E-04 0.000

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000164 0.00000000945 0.00000000988 0.000

lb/mmBtuO2 1.80E-12 9.79E-13 1.01E-12 0.000

ng/dscm 2.01E-03 1.10E-03 1.14E-03 0.001

ng/dscm@7%O2 1.93E-03 1.05E-03 1.09E-03 0.001

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000346 0.0000000109 0.0000000187 0.000

lb/mmBtuO2 3.80E-12 1.13E-12 1.92E-12 0.000

ng/dscm 4.25E-03 1.27E-03 2.16E-03 0.003

ng/dscm@7%O2 4.07E-03 1.21E-03 2.06E-03 0.002

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0 0.0000000029 0 0.000

lb/mmBtuO2 0.00E+00 3.00E-13 0.00E+00 0.000

ng/dscm 0.00E+00 3.38E-04 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 3.22E-04 0.00E+00 0.000

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

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

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

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

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

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

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000477 0.00000000183 0 0.000

lb/mmBtuO2 5.24E-13 1.90E-13 0.00E+00 0.000

ng/dscm 5.86E-04 2.13E-04 0.00E+00 0.000

ng/dscm@7%O2 5.62E-04 2.03E-04 0.00E+00 0.000

Friday, January 14, 2011 Page 17 of 47
Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

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

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

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

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

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

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000051 0.00000000973 0.0000000174 0.000

lb/mmBtuO2 5.60E-13 1.01E-12 1.79E-12 0.000

ng/dscm 6.26E-04 1.14E-03 2.01E-03 0.001

ng/dscm@7%O2 6.00E-04 1.09E-03 1.91E-03 0.001

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0 0 0 0.000

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

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

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

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.00000003527 0.00000003475 0.00000004663 0.000

lb/mmBtuO2 3.87E-12 3.60E-12 4.79E-12 0.000

ng/dscm 4.33E-03 4.05E-03 5.39E-03 0.005

ng/dscm@7%O2 4.15E-03 3.86E-03 5.13E-03 0.004

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.00000008071 0.00000004019 0.00000007192 0.000

lb/mmBtuO2 8.86E-12 4.16E-12 7.39E-12 0.000

ng/dscm 9.91E-03 4.69E-03 8.32E-03 0.008

ng/dscm@7%O2 9.50E-03 4.47E-03 7.92E-03 0.007

Compound: Total PCBs

Average

RunNumber 1 2 3

Mass_mg 0.0000003083 0.0000004261 0.0000004735 0.000

lb/mmBtuO2 3.38E-11 4.41E-11 4.86E-11 0.000

Friday, January 14, 2011 Page 18 of 47
ng/dscm 3.79E-02 4.97E-02 5.48E-02 0.047

ng/dscm@7%O2 3.63E-02 4.73E-02 5.22E-02 0.045

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 2.79E-04 3.20E-04 3.21E-04 0.000

ppm 1.66E-01 1.96E-01 1.98E-01 0.187

ppm@7%O2 1.63E-01 1.87E-01 1.88E-01 0.179

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.0598 0.064 0.0601 0.061

Elb/hr 3.50E-02 3.76E-02 3.52E-02 0.036

lb/mmBtuO2 1.88E-05 1.96E-05 1.79E-05 0.000

mg/dscm 2.03E-02 2.12E-02 1.96E-02 0.020

mg/dscm@7%O2 2.02E-02 2.10E-02 1.92E-02 0.020

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.158 0.169 0.159 0.162

Elb/hr 9.26E-02 9.93E-02 9.32E-02 0.095

lb/mmBtuO2 4.95E-05 5.17E-05 4.73E-05 0.000

mg/dscm 5.35E-02 5.59E-02 5.18E-02 0.054

mg/dscm@7%O2 5.31E-02 5.55E-02 5.07E-02 0.053

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00007 0.00015 0.00006 0.000

Elb/hr 2.69E-05 5.84E-05 2.27E-05 0.000

lb/mmBtuO2 1.38E-08 2.93E-08 1.17E-08 0.000

mg/dscm 1.52E-05 3.26E-05 1.26E-05 0.000

mg/dscm@7%O2 1.48E-05 3.15E-05 1.25E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00028 0.00016 0.0002 0.000

Elb/hr 1.08E-04 6.23E-05 7.57E-05 0.000

lb/mmBtuO2 5.51E-08 3.13E-08 3.89E-08 0.000

mg/dscm 6.08E-05 3.48E-05 4.20E-05 0.000

mg/dscm@7%O2 5.91E-05 3.36E-05 4.17E-05 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Friday, January 14, 2011 Page 19 of 47
Mass_mg 0.00003 0.00003 0.00003 0.000

Elb/hr 1.15E-05 1.17E-05 1.13E-05 0.000

lb/mmBtuO2 5.91E-09 5.87E-09 5.83E-09 0.000

mg/dscm 6.52E-06 6.52E-06 6.30E-06 0.000

mg/dscm@7%O2 6.34E-06 6.29E-06 6.26E-06 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00008 0.0001 0.00014 0.000

Elb/hr 3.08E-05 3.89E-05 5.30E-05 0.000

lb/mmBtuO2 1.58E-08 1.96E-08 2.72E-08 0.000

mg/dscm 1.74E-05 2.17E-05 2.94E-05 0.000

mg/dscm@7%O2 1.69E-05 2.09E-05 2.92E-05 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.00685 0.00799 0.00335 0.006

Elb/hr 2.63E-03 3.11E-03 1.27E-03 0.002

lb/mmBtuO2 1.35E-06 1.56E-06 6.51E-07 0.000

mg/dscm 1.49E-03 1.74E-03 7.03E-04 0.001

mg/dscm@7%O2 1.45E-03 1.68E-03 6.98E-04 0.001

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00033 0.0002 0.00032 0.000

Elb/hr 1.27E-04 7.79E-05 1.21E-04 0.000

lb/mmBtuO2 6.50E-08 3.91E-08 6.22E-08 0.000

mg/dscm 7.17E-05 4.35E-05 6.71E-05 0.000

mg/dscm@7%O2 6.97E-05 4.20E-05 6.66E-05 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 47.5 33.3 40.2 40.333

Elb/hr 1.83E+01 1.30E+01 1.52E+01 15.500

lb/mmBtuO2 9.35E-03 6.51E-03 7.81E-03 0.008

mg/dscm 1.03E+01 7.24E+00 8.44E+00 8.660

mg/dscm@7%O2 1.00E+01 6.99E+00 8.38E+00 8.457

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00266 0.00121 0.00174 0.002

Elb/hr 1.02E-03 4.71E-04 6.58E-04 0.001

lb/mmBtuO2 5.24E-07 2.37E-07 3.38E-07 0.000

mg/dscm 5.78E-04 2.63E-04 3.65E-04 0.000

mg/dscm@7%O2 5.62E-04 2.54E-04 3.62E-04 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Friday, January 14, 2011 Page 20 of 47
Mass_mg 0.01074 0.00614 0.00714 0.008

Elb/hr 4.13E-03 2.39E-03 2.70E-03 0.003

lb/mmBtuO2 2.12E-06 1.20E-06 1.39E-06 0.000

mg/dscm 2.33E-03 1.33E-03 1.50E-03 0.002

mg/dscm@7%O2 2.26E-03 1.28E-03 1.49E-03 0.002

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0155 0.0148 0.0089 0.013

Elb/hr 5.96E-03 5.76E-03 3.37E-03 0.005

lb/mmBtuO2 3.05E-06 2.90E-06 1.73E-06 0.000

mg/dscm 3.37E-03 3.22E-03 1.87E-03 0.003

mg/dscm@7%O2 3.28E-03 3.11E-03 1.86E-03 0.003

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.00616 0.00336 0.00576 0.005

Elb/hr 2.37E-03 1.31E-03 2.18E-03 0.002

lb/mmBtuO2 1.21E-06 6.57E-07 1.12E-06 0.000

mg/dscm 1.34E-03 7.30E-04 1.21E-03 0.001

mg/dscm@7%O2 1.30E-03 7.05E-04 1.20E-03 0.001

Location: Stack Exit - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 13.2 8.5 10.2 10.633

Elb/hr 5.10E+00 3.41E+00 4.05E+00 4.187

gr/dscf 1.32E-03 8.88E-04 1.04E-03 0.001

lb/mmBtuO2 2.70E-02 1.80E-03 2.15E-03 0.010

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 124.4 113.4 38.5 92.100

Elb/hr 4.80E+01 4.56E+01 1.53E+01 36.300

gr/dscf 1.24E-02 1.18E-02 3.92E-03 0.009

lb/mmBtuO2 2.54E-01 2.41E-02 8.13E-03 0.095

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 2.3 3.1 1.5 2.300

Elb/hr 8.88E-01 1.25E+00 5.96E-01 0.911

gr/dscf 2.30E-04 3.24E-04 1.53E-04 0.000

lb/mmBtuO2 4.70E-03 6.58E-04 3.17E-04 0.002

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 139.9 125 50.2 105.033

Friday, January 14, 2011 Page 21 of 47
Process Run Data

Elb/hr 5.40E+01 5.02E+01 2.00E+01 41.400

gr/dscf 1.40E-02 1.31E-02 5.11E-03 0.011

lb/mmBtuO2 2.86E-01 2.65E-02 1.06E-02 0.108

Friday, January 14, 2011 Page 22 of 47
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 1875 Million Btus/hr 0

10 Heat Input 1727 Million Btus/hr 0

11 Heat Input 1899 Million Btus/hr 0

12 Heat Input 1899 Million Btus/hr 0

13 Heat Input 1899 Million Btus/hr 0

14 Heat Input 1888 Million Btus/hr 0

15 Heat Input 1898 Million Btus/hr 0

16 Heat Input 1892 Million Btus/hr 0

17 Heat Input 1899 Million Btus/hr 0

18 Heat Input 1899 Million Btus/hr 0

2 Heat Input 1899 Million Btus/hr 0

3 Heat Input 1899 Million Btus/hr 0

4 Heat Input 1869 Million Btus/hr 0

5 Heat Input 1849 Million Btus/hr 0

6 Heat Input 1829 Million Btus/hr 0

7 Heat Input 1727 Million Btus/hr 0

8 Heat Input 1899 Million Btus/hr 0

9 Heat Input 1899 Million Btus/hr 0

1 Steam Output 1366 1000 lb steam/hr 0

10 Steam Output 1346 1000 lb steam/hr 0

11 Steam Output 1411 1000 lb steam/hr 0

12 Steam Output 1413 1000 lb steam/hr 0

13 Steam Output 1418 1000 lb steam/hr 0

14 Steam Output 1296 1000 lb steam/hr 0

15 Steam Output 1417 1000 lb steam/hr 0

16 Steam Output 1346 1000 lb steam/hr 0

17 Steam Output 1411 1000 lb steam/hr 0

18 Steam Output 1413 1000 lb steam/hr 0

2 Steam Output 1412 1000 lb steam/hr 0

3 Steam Output 1361 1000 lb steam/hr 0

4 Steam Output 1360 1000 lb steam/hr 0

5 Steam Output 1342 1000 lb steam/hr 0

6 Steam Output 1395 1000 lb steam/hr 0

Friday, January 14, 2011 Page 23 of 47
7 Steam Output 1346 1000 lb steam/hr 0

8 Steam Output 1411 1000 lb steam/hr 0

9 Steam Output 1413 1000 lb steam/hr 0

1 Standard Pressure 1 atm 0

10 Standard Pressure 1 atm 0

11 Standard Pressure 1 atm 0

12 Standard Pressure 1 atm 0

13 Standard Pressure 1 atm 0

14 Standard Pressure 1 atm 0

15 Standard Pressure 1 atm 0

16 Standard Pressure 1 atm 0

17 Standard Pressure 1 atm 0

18 Standard Pressure 1 atm 0

2 Standard Pressure 1 atm 0

3 Standard Pressure 1 atm 0

4 Standard Pressure 1 atm 0

5 Standard Pressure 1 atm 0

6 Standard Pressure 1 atm 0

7 Standard Pressure 1 atm 0

8 Standard Pressure 1 atm 0

9 Standard Pressure 1 atm 0

1 Standard Temperature 68 Deg F 0

10 Standard Temperature 68 Deg F 0

11 Standard Temperature 68 Deg F 0

12 Standard Temperature 68 Deg F 0

13 Standard Temperature 68 Deg F 0

14 Standard Temperature 68 Deg F 0

15 Standard Temperature 68 Deg F 0

16 Standard Temperature 68 Deg F 0

17 Standard Temperature 68 Deg F 0

18 Standard Temperature 68 Deg F 0

2 Standard Temperature 68 Deg F 0

3 Standard Temperature 68 Deg F 0

4 Standard Temperature 68 Deg F 0

5 Standard Temperature 68 Deg F 0

6 Standard Temperature 68 Deg F 0

Friday, January 14, 2011 Page 24 of 47
APCD Run Data

Process Lab Run Data

7 Standard Temperature 68 Deg F 0

8 Standard Temperature 68 Deg F 0

9 Standard Temperature 68 Deg F 0

1 Unit Net Electric Generation 132 MWh 0

10 Unit Net Electric Generation 116 MWh 0

11 Unit Net Electric Generation 133 MWh 0

12 Unit Net Electric Generation 137 MWh 0

13 Unit Net Electric Generation 137 MWh 0

14 Unit Net Electric Generation 131 MWh 0

15 Unit Net Electric Generation 137 MWh 0

16 Unit Net Electric Generation 131 MWh 0

17 Unit Net Electric Generation 137 MWh 0

18 Unit Net Electric Generation 137 MWh 0

2 Unit Net Electric Generation 137 MWh 0

3 Unit Net Electric Generation 132 MWh 0

4 Unit Net Electric Generation 132 MWh 0

5 Unit Net Electric Generation 135 MWh 0

6 Unit Net Electric Generation 135 MWh 0

7 Unit Net Electric Generation 116 MWh 0

8 Unit Net Electric Generation 133 MWh 0

9 Unit Net Electric Generation 137 MWh 0

Run Name Value UOM Comments

Target

Value

1 OVERFIRE AIR 0 0

1 ELECTROSTATIC PRECIPITATOR 0 0

1 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

1 WET ELECTROSTATIC PRECIPITATOR 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 14811 Btu/lb

1 Fuel Moisture 4.2 %

1 Fuel Mercury Content 0.0009 ppm

1 Fuel Cadmium Content 0.15 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 314 ppm

Friday, January 14, 2011 Page 25 of 47
1 Fuel Arsenic Content 0.13 ppm 1 Fuel Chromium Content 0.2 ppm 1 Fuel Beryllium Content 0.11 ppm 1 Fuel Lead Content 0.09 ppm 1 Fuel Manganese Content 0.1 ppm 1 Fuel Chlorine Content 7.5 ppm 1 Fuel Fluorine Content 0 ppm 2 Fuel Higher Heating Value 14527 Btu/lb 2 Fuel Moisture 5.5 % 2 Fuel Mercury Content 0.019 ppm 2 Fuel Cadmium Content 0.15 ppm 2 Ultimate/Proximate Analysis 0 2 Fuel Nickel Content 313 ppm 2 Fuel Arsenic Content 0.13 ppm 2 Fuel Chromium Content 0.2 ppm 2 Fuel Beryllium Content 0.11 ppm 2 Fuel Lead Content 0.09 ppm 2 Fuel Manganese Content 0.1 ppm 2 Fuel Chlorine Content 7.5 ppm 2 Fuel Fluorine Content 0 ppm 3 Fuel Higher Heating Value 14752 Btu/lb 3 Fuel Moisture 4.5 % 3 Fuel Mercury Content 0.021 ppm 3 Fuel Cadmium Content 0.15 ppm 3 Ultimate/Proximate Analysis 0 3 Fuel Nickel Content 318 ppm 3 Fuel Arsenic Content 0.13 ppm 3 Fuel Chromium Content 0.2 ppm 3 Fuel Beryllium Content 0.11 ppm 3 Fuel Lead Content 1.4 ppm 3 Fuel Manganese Content 0.1 ppm 3 Fuel Chlorine Content 7.5 ppm 3 Fuel Fluorine Content 0 ppm 4 Fuel Higher Heating Value 14704 Btu/lb 4 Fuel Moisture 4.7 % 4 Fuel Mercury Content 0 ppm 4 Fuel Cadmium Content 0 ppm 4 Ultimate/Proximate Analysis 0 4 Fuel Nickel Content 0 ppm 4 Fuel Arsenic Content 0 ppm 4 Fuel Chromium Content 0 ppm 4 Fuel Beryllium Content 0 ppm 4 Fuel Lead Content 0 ppm

Friday, January 14, 2011 Page 26 of 47
4 Fuel Manganese Content

0 ppm

4 Fuel Chlorine Content 7.5 ppm 4 Fuel Fluorine Content 0 ppm 5 Fuel Higher Heating Value 14854 Btu/lb 5 Fuel Moisture 4 % 5 Fuel Mercury Content 0 ppm 5 Fuel Cadmium Content 0 ppm 5 Ultimate/Proximate Analysis 0 5 Fuel Nickel Content 0 ppm 5 Fuel Arsenic Content 0 ppm 5 Fuel Chromium Content 0 ppm 5 Fuel Beryllium Content 0 ppm 5 Fuel Lead Content 0 ppm 5 Fuel Manganese Content 0 ppm 5 Fuel Chlorine Content 7.5 ppm 5 Fuel Fluorine Content 0 ppm 6 Fuel Higher Heating Value 14593 Btu/lb 6 Fuel Moisture 5.4 % 6 Fuel Mercury Content 0 ppm 6 Fuel Cadmium Content 0 ppm 6 Ultimate/Proximate Analysis 0 6 Fuel Nickel Content 0 ppm 6 Fuel Arsenic Content 0 ppm 6 Fuel Chromium Content 0 ppm 6 Fuel Beryllium Content 0 ppm 6 Fuel Lead Content 0 ppm 6 Fuel Manganese Content 0 ppm 6 Fuel Chlorine Content 7.5 ppm 6 Fuel Fluorine Content 0 ppm 7 Fuel Higher Heating Value 14847 Btu/lb 7 Fuel Moisture 3 % 7 Fuel Mercury Content 0 ppm 7 Fuel Cadmium Content 0 ppm 7 Ultimate/Proximate Analysis 0 7 Fuel Nickel Content 0 ppm 7 Fuel Arsenic Content 0 ppm 7 Fuel Chromium Content 0 ppm 7 Fuel Beryllium Content 0 ppm 7 Fuel Lead Content 0 ppm 7 Fuel Manganese Content 0 ppm 7 Fuel Chlorine Content 7.5 ppm 7 Fuel Fluorine Content 3 ppm 8 Fuel Higher Heating Value 14677 Btu/lb

Friday, January 14, 2011 Page 27 of 47
8 Fuel Moisture

5%

8 Fuel Mercury Content0 ppm

8 Fuel Cadmium Content0 ppm

8 Ultimate/Proximate Analysis0

8 Fuel Nickel Content0 ppm

8 Fuel Arsenic Content0 ppm

8 Fuel Chromium Content0 ppm

8 Fuel Beryllium Content0 ppm

8 Fuel Lead Content0 ppm

8 Fuel Manganese Content0 ppm

8 Fuel Chlorine Content 7.5 ppm 8 Fuel Fluorine Content 3 ppm 9 Fuel Higher Heating Value 14430 Btu/lb 9 Fuel Moisture 6 % 9 Fuel Mercury Content 0 ppm 9 Fuel Cadmium Content 0 ppm 9 Ultimate/Proximate Analysis 0 9 Fuel Nickel Content 0 ppm 9 Fuel Arsenic Content 0 ppm 9 Fuel Chromium Content 0 ppm 9 Fuel Beryllium Content 0 ppm 9 Fuel Lead Content 0 ppm 9 Fuel Manganese Content 0 ppm 9 Fuel Chlorine Content 7.5 ppm 9 Fuel Fluorine Content 3 ppm

10 Fuel Higher Heating Value 14793 Btu/lb

10 Fuel Moisture 3.8%

10 Fuel Mercury Content0 ppm

10 Fuel Cadmium Content0 ppm

10 Ultimate/Proximate Analysis0

10 Fuel Nickel Content0 ppm

10 Fuel Arsenic Content0 ppm

10 Fuel Chromium Content0 ppm

10 Fuel Beryllium Content0 ppm

10 Fuel Lead Content0 ppm

10 Fuel Manganese Content0 ppm

10 Fuel Chlorine Content 7.5 ppm

10 Fuel Fluorine Content0 ppm

11 Fuel Higher Heating Value 14840 Btu/lb

11 Fuel Moisture 3.9%

11 Fuel Mercury Content0 ppm

11 Fuel Cadmium Content0 ppm

11 Ultimate/Proximate Analysis0

Friday, January 14, 2011 Page 28 of 47
11 Fuel Nickel Content

0 ppm

11 Fuel Arsenic Content0 ppm

11 Fuel Chromium Content0 ppm

11 Fuel Beryllium Content0 ppm

11 Fuel Lead Content0 ppm

11 Fuel Manganese Content0 ppm

11 Fuel Chlorine Content 7.5 ppm

11 Fuel Fluorine Content0 ppm

12 Fuel Higher Heating Value 14744 Btu/lb

12 Fuel Moisture 4.3%

12 Fuel Mercury Content0 ppm

12 Fuel Cadmium Content0 ppm

12 Ultimate/Proximate Analysis0

12 Fuel Nickel Content0 ppm

12 Fuel Arsenic Content0 ppm

12 Fuel Chromium Content0 ppm

12 Fuel Beryllium Content0 ppm

12 Fuel Lead Content0 ppm

12 Fuel Manganese Content0 ppm

12 Fuel Chlorine Content 7.5 ppm

12 Fuel Fluorine Content0 ppm

13 Fuel Higher Heating Value 14854 Btu/lb

13 Fuel Moisture 3.8%

13 Fuel Mercury Content0 ppm

13 Fuel Cadmium Content0 ppm

13 Ultimate/Proximate Analysis0

13 Fuel Nickel Content0 ppm

13 Fuel Arsenic Content0 ppm

13 Fuel Chromium Content0 ppm

13 Fuel Beryllium Content0 ppm

13 Fuel Lead Content0 ppm

13 Fuel Manganese Content0 ppm

13 Fuel Chlorine Content 52 ppm

13 Fuel Fluorine Content0 ppm

14 Fuel Higher Heating Value 14716 Btu/lb

14 Fuel Moisture 4.7%

14 Fuel Mercury Content0 ppm

14 Fuel Cadmium Content0 ppm

14 Ultimate/Proximate Analysis0

14 Fuel Nickel Content0 ppm

14 Fuel Arsenic Content0 ppm

14 Fuel Chromium Content0 ppm

14 Fuel Beryllium Content0 ppm

Friday, January 14, 2011 Page 29 of 47
14 Fuel Lead Content

0 ppm

14 Fuel Manganese Content0 ppm

14 Fuel Chlorine Content 7.5 ppm

14 Fuel Fluorine Content0 ppm

15 Fuel Higher Heating Value 14734 Btu/lb

15 Fuel Moisture 4.1%

15 Fuel Mercury Content0 ppm

15 Fuel Cadmium Content0 ppm

15 Ultimate/Proximate Analysis0

15 Fuel Nickel Content0 ppm

15 Fuel Arsenic Content0 ppm

15 Fuel Chromium Content0 ppm

15 Fuel Beryllium Content0 ppm

15 Fuel Lead Content0 ppm

15 Fuel Manganese Content0 ppm

15 Fuel Chlorine Content 7.5 ppm

15 Fuel Fluorine Content0 ppm

16 Fuel Higher Heating Value 14768 Btu/lb

16 Fuel Moisture 4.2%

16 Fuel Mercury Content0 ppm

16 Fuel Cadmium Content0 ppm

16 Ultimate/Proximate Analysis0

16 Fuel Nickel Content0 ppm

16 Fuel Arsenic Content0 ppm

16 Fuel Chromium Content0 ppm

16 Fuel Beryllium Content0 ppm

16 Fuel Lead Content0 ppm

16 Fuel Manganese Content0 ppm

16 Fuel Chlorine Content 52 ppm

16 Fuel Fluorine Content0 ppm

17 Fuel Higher Heating Value 14717 Btu/lb

17 Fuel Moisture 4.7%

17 Fuel Mercury Content0 ppm

17 Fuel Cadmium Content0 ppm

17 Ultimate/Proximate Analysis0

17 Fuel Nickel Content0 ppm

17 Fuel Arsenic Content0 ppm

17 Fuel Chromium Content0 ppm

17 Fuel Beryllium Content0 ppm

17 Fuel Lead Content0 ppm

17 Fuel Manganese Content0 ppm

17 Fuel Chlorine Content 7.5 ppm

17 Fuel Fluorine Content0 ppm

Friday, January 14, 2011 Page 30 of 47
18 Fuel Higher Heating Value 14876 Btu/lb

18 Fuel Moisture 3.8 %

18 Fuel Mercury Content 0 ppm

18 Fuel Cadmium Content 0 ppm

18 Ultimate/Proximate Analysis 0

18 Fuel Nickel Content 0 ppm

18 Fuel Arsenic Content 0 ppm

18 Fuel Chromium Content 0 ppm

18 Fuel Beryllium Content 0 ppm

18 Fuel Lead Content 0 ppm

18 Fuel Manganese Content 0 ppm

18 Fuel Chlorine Content 7.5 ppm

18 Fuel Fluorine Content 0 ppm

Friday, January 14, 2011 Page 31 of 47
Sampling / Stack Data Results Detail

Location Stack Exit - Method 10

Average

Run Number 1 Form 2 Form 3 Form

Test Date 7/24/2010 7/24/2010 7/24/2010

Run Start Time 7:53:00 AM 10:25:00 AM 1:24:00 PM

Run Finish Time 10:07:00 AM 12:47:00 PM 3:37:00 PM

Carbon Dioxide, % 12.81 13.15 13.18 13.047

Oxygen, % 6.72 6.32 6.24 6.427

Fuel Factor 1.11 1.11 1.11

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000

Moisture, % 0 0 0 0.000

Analyzer Make TECO TECO TECO

Analyzer Model 48i 48i 48i

Analyzer Serial Number Mick Mick Mick

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Pre Zero Cylinder Instrument Response 0.33 0.37 0.5 0.400

Calibration Pre Zero Cylinder Bias 0.03 0.04 0.07 0.047

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM46599 ALM46599 ALM46599

Calibration Pre High Cylinder Instrument Response 244.93 245.35 244.99 245.090

Calibration Pre High Cylinder Bias -0.23 -0.15 -0.22 -0.200

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Post Zero Cylinder Instrument Response 0.37 0.5 0.47 0.447

Calibration Post Zero Cylinder Bias 0.04 0.07 0.06 0.057

Calibration Post Zero Cylinder Drift 0.01 0.03 0.01 0.017

Calibration Post High Cylinder ID ALM46599 ALM46599 ALM46599

Calibration Post High Cylinder Instrument Response 245.35 244.99 245.39 245.243

Calibration Post High Cylinder Bias -0.15 -0.22 -0.14 -0.170

Calibration Post High Cylinder Drift 0.08 0.07 0.08 0.077

Cavg 55.6 167.2 174.77 132.523

Cavg Units ppmvd ppmvd ppmvd

Cgas 55.5908 167.8314 175.421 132.948

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Friday, January 14, 2011 Page 32 of 47
Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 7/24/2010 7/25/2010 7/26/2010

Run Start Time 8:53:00 AM 8:05:00 AM 7:03:00 AM

Run Finish Time 5:39:00 PM 5:17:00 PM 5:56:00 PM

Net Traversing Points 0 0 0

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.24 0.247 0.247 0.245

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.001 1.001 1.001 1.001

Barometric Pressure, inches of Mercury 29.39 29.37 29.37 29.377

Average Orifice Meter Differential, inches H2O 1.43 1.56 1.61 1.533

Dry Gas Meter Volume Sampled, cubic feet 312.152 327.279 327.867 322.433

Average Dry Gas Meter Temperature, °F 105.47 102.98 99.37 102.607

Dry Gas Meter Volume Sampled, dscf 287.616 302.781 305.320 298.572

Total Moisture Liquid collected, g 940.2 976.2 1019.2 978.533

Volume of Water Vapor, standard cubic feet 44.26 45.95 47.97 46.060

Moisture Content of Stack Gas, % 13.34 13.18 13.58 13.367

Moisture Saturation at Stack Gas Temperature, % 31.84 31.37 31.22 31.477

Dry Mole Fraction 0.8666 0.8682 0.8642 0.866

Carbon Dioxide, % 13 13 13 13.000

Oxygen, % 6.4 6.3 6.3 6.333

Carbon Monoxide & Nitrogen, % 80.6 80.7 80.7 80.667

Fuel Factor 1.12 1.12 1.12

Dry Molecular Weight, lb/lb-Mole 30.34 30.33 30.33 30.333

Wet Molecular weight, lb/lb-Mole 28.69 28.70 28.66 28.683

Flue Gas Static Pressure, inches of H2O -0.35 -0.35 -0.4 -0.367

Absolute Flue Gas Pressure, inches of Mercury 29.36 29.34 29.34 29.347

Average Stack Gas Temperature, °F 158.76 158.10 157.91 158.257

Average Velocity Head, inches of H2O 0.5517523451

48963

0.536280816

54093

0.526480138

804762

0.538

Average Stack Gas Velocity, feet/second 45.72 45.06 44.67 45.150

Stack Cross-Sectional Area, square feet 226.980 226.980 226.980 226.980

Dry Volumetric Flow Rate, dry scfm 451,824.6 446,296.5 440,530.8 446,217.300

Actual Wet Volumetric Flue Gas Flow Rate, acfm 622,651.5 613,663.1 608,351.8 614,888.800

Percent Isokinetic of Sampling Rate, % 95.8 96.4 98.5 96.900

Percent Excess Air, % 43.0 42.0 42.0 42.333

F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000

Round Duct Diameter, inches 204 204 204

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

Friday, January 14, 2011 Page 33 of 47
Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 7/24/2010 7/24/2010 7/24/2010

Run Start Time 7:53:00 AM 10:25:00 AM 1:24:00 PM

Run Finish Time 10:07:00 AM 12:47:00 PM 3:37:00 PM

Carbon Dioxide, % 12.81 13.15 13.18 13.047

Oxygen, % 6.72 6.32 6.24 6.427

Fuel Factor 1.11 1.11 1.11

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000

Moisture, % 0 0 0 0.000

Analyzer Make TECO TECO TECO

Analyzer Model 51CHT 51CHT 51CHT

Analyzer Serial Number Buddy Buddy Buddy

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Pre Zero Cylinder Instrument Response 0 0 0.04 0.013

Calibration Pre Zero Cylinder Bias 0 0 0.19 0.063

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC155319 CC155319 CC155319

Calibration Pre High Cylinder Instrument Response 12.7 12.67 12.62 12.663

Calibration Pre High Cylinder Bias 0.38 0.24 0 0.207

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Post Zero Cylinder Instrument Response 0 0.04 0.02 0.020

Calibration Post Zero Cylinder Bias 0 0.19 0.09 0.093

Calibration Post Zero Cylinder Drift 0 0.14 0.1 0.080

Calibration Post High Cylinder ID CC155319 CC155319 CC155319

Calibration Post High Cylinder Instrument Response 12.67 12.62 12.53 12.607

Calibration Post High Cylinder Bias 0.24 0 -0.42 -0.060

Calibration Post High Cylinder Drift 0.14 0.14 0.66 0.313

Cavg 0.2 0.22 0.23 0.217

Cavg Units ppmvd ppmvd ppmvd

Cgas 0.1662 0.1964 0.1977 0.187

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Friday, January 14, 2011 Page 34 of 47
Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 8/18/2010 8/19/2010 8/19/2010

Run Start Time 2:36:00 PM 8:55:00 AM 12:23:00 PM

Run Finish Time 5:50:00 PM 12:08:00 PM 3:33:00 PM

Net Traversing Points 0 22 0

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.229 0.229 0.229 0.229

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.999 0.999 0.999 0.999

Barometric Pressure, inches of Mercury 29.75 29.73 29.75 29.743

Average Orifice Meter Differential, inches H2O 1.28 1.35 1.39 1.340

Dry Gas Meter Volume Sampled, cubic feet 112.374 114.211 116.114 114.233

Average Dry Gas Meter Temperature, °F 106.96 102.24 103.78 104.327

Dry Gas Meter Volume Sampled, dscf 104.282 106.823 108.390 106.498

Total Moisture Liquid collected, g 331.6 346.1 361.4 346.367

Volume of Water Vapor, standard cubic feet 15.61 16.29 17.01 16.303

Moisture Content of Stack Gas, % 13.02 13.23 13.56 13.270

Moisture Saturation at Stack Gas Temperature, % 30.95 30.29 30.35 30.530

Dry Mole Fraction 0.8698 0.8677 0.8644 0.867

Carbon Dioxide, % 12.3 11.9 11.9 12.033

Oxygen, % 6.9 6.9 6.7 6.833

Carbon Monoxide & Nitrogen, % 80.8 81.2 81.4 81.133

Fuel Factor 1.14 1.18 1.19

Dry Molecular Weight, lb/lb-Mole 30.24 30.18 30.17 30.197

Wet Molecular weight, lb/lb-Mole 28.65 28.57 28.52 28.580

Flue Gas Static Pressure, inches of H2O -0.42 -0.33 -0.33 -0.360

Absolute Flue Gas Pressure, inches of Mercury 29.72 29.71 29.73 29.720

Average Stack Gas Temperature, °F 158.08 157.17 157.28 157.510

Average Velocity Head, inches of H2O 0.5645799915

06418

0.595699487

66388

0.613847494

842037

0.591

Average Stack Gas Velocity, feet/second 45.97 47.26 48.01 47.080

Stack Cross-Sectional Area, square feet 226.980 226.980 226.980 226.980

Dry Volumetric Flow Rate, dry scfm 462,071.5 474,430.2 480,363.9 472,288.533

Actual Wet Volumetric Flue Gas Flow Rate, acfm 626,056.2 643,624.5 653,838.6 641,173.100

Percent Isokinetic of Sampling Rate, % 99.5 99.3 99.5 99.433

Percent Excess Air, % 47.8 47.5 45.3 46.867

F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000

Round Duct Diameter, inches 204 204 204

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

Friday, January 14, 2011 Page 35 of 47
Location Stack Exit - Method 29 

Average

Run Number 1 2 3

Test Date 8/3/2010 8/3/2010 8/4/2010

Run Start Time 7:40:00 AM 1:23:00 PM 7:32:00 AM

Run Finish Time 12:05:00 PM 6:11:00 PM 12:00:00 PM

Net Traversing Points 0 0 0

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.247 0.247 0.247 0.247

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.989 0.989 0.989 0.989

Barometric Pressure, inches of Mercury 29.39 29.37 29.39 29.383

Average Orifice Meter Differential, inches H2O 1.67 1.67 1.79 1.710

Dry Gas Meter Volume Sampled, cubic feet 178.043 179.038 184.209 180.430

Average Dry Gas Meter Temperature, °F 104.11 107.02 103.89 105.007

Dry Gas Meter Volume Sampled, dscf 162.570 162.529 168.316 164.472

Total Moisture Liquid collected, g 546.1 465.4 567.2 526.233

Volume of Water Vapor, standard cubic feet 25.70 21.91 26.70 24.770

Moisture Content of Stack Gas, % 13.65 11.88 13.69 13.073

Moisture Saturation at Stack Gas Temperature, % 33.38 33.74 33.58 33.567

Dry Mole Fraction 0.8635 0.8812 0.8631 0.869

Carbon Dioxide, % 12.7 13 12.8 12.833

Oxygen, % 6.6 6.5 6.9 6.667

Carbon Monoxide & Nitrogen, % 80.7 80.5 80.3 80.500

Fuel Factor 1.13 1.11 1.09

Dry Molecular Weight, lb/lb-Mole 30.30 30.34 30.32 30.320

Wet Molecular weight, lb/lb-Mole 28.62 28.87 28.63 28.707

Flue Gas Static Pressure, inches of H2O -0.42 -0.35 -0.4 -0.390

Absolute Flue Gas Pressure, inches of Mercury 29.36 29.34 29.36 29.353

Average Stack Gas Temperature, °F 160.73 161.15 160.98 160.953

Average Velocity Head, inches of H2O 0.6089638607

10644

0.605229324

309334

0.632231528

467615

0.615

Average Stack Gas Velocity, feet/second 48.16 47.84 49.08 48.360

Stack Cross-Sectional Area, square feet 226.980 226.980 226.980 226.980

Dry Volumetric Flow Rate, dry scfm 472,730.2 478,564.5 481,343.7 477,546.133

Actual Wet Volumetric Flue Gas Flow Rate, acfm 655,881.4 651,523.4 668,410.7 658,605.167

Percent Isokinetic of Sampling Rate, % 97.7 96.5 99.4 97.867

Percent Excess Air, % 44.9 44.1 48.3 45.767

F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000

Round Duct Diameter, inches 204 204 204

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

Friday, January 14, 2011 Page 36 of 47
Location Stack Exit - Method 3A CO2

Average

Run Number 1 DF 1 Form 1 Hg

Test Date 7/24/2010 7/24/2010 7/25/2010

Run Start Time 8:53:00 AM 7:53:00 AM 7:18:00 AM

Run Finish Time 5:39:00 PM 10:07:00 AM 9:40:00 AM

Carbon Dioxide, % 13.11 12.81 12.81 12.910

Oxygen, % 6.33 6.72 6.65 6.567

Fuel Factor 1.11 1.11 1.11

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1440 1440 1440 1,440.000

Analyzer Serial Number Waits Waits Waits

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 11 11 111 44.333

Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Pre Zero Cylinder Instrument Response 0.08 0.08 0.15 0.103

Calibration Pre Zero Cylinder Bias 0 0 0.1 0.033

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM015275 ALM015275 ALM015275

Calibration Pre High Cylinder Instrument Response 9.61 9.61 9.61 9.610

Calibration Pre High Cylinder Bias -0.51 -0.51 -0.56 -0.527

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Post Zero Cylinder Instrument Response 0.16 0.14 0.16 0.153

Calibration Post Zero Cylinder Bias 0.41 0.31 0.15 0.290

Calibration Post Zero Cylinder Drift 0.41 0.31 0.05 0.257

Calibration Post High Cylinder ID ALM015275 ALM015275 ALM015275

Calibration Post High Cylinder Instrument Response 9.61 9.63 9.62 9.620

Calibration Post High Cylinder Bias -0.51 -0.41 0 -0.307

Calibration Post High Cylinder Drift 0 0.1 0 0.033

Cavg 13.11 12.81 12.81 12.910

Cavg Units ppmvd ppmvd ppmvd

Cgas 12.9763 12.6599 25.7999 17.145

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Friday, January 14, 2011 Page 37 of 47
Location Stack Exit - Method 3A CO2 3

Average

Run Number 1 ORG 1 PM 2 DF

Test Date 7/23/2010 8/3/2010 7/25/2010

Run Start Time 8:13:00 AM 7:40:00 AM 8:05:00 AM

Run Finish Time 10:54:00 AM 12:05:00 PM 5:17:00 PM

Carbon Dioxide, % 13.04 12.84 13.1 12.993

Oxygen, % 6.46 6.62 6.27 6.450

Fuel Factor 1.11 1.11 1.12

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1440 1440 1440 1,440.000

Analyzer Serial Number Waits Waits Waits

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 1 10 111 40.667

Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Pre Zero Cylinder Instrument Response 0.08 0.14 0.15 0.123

Calibration Pre Zero Cylinder Bias 0.1 0.15 0.1 0.117

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM015275 ALM015275 ALM015275

Calibration Pre High Cylinder Instrument Response 9.59 9.59 9.61 9.597

Calibration Pre High Cylinder Bias -0.51 -0.51 -0.56 -0.527

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Post Zero Cylinder Instrument Response 0.14 0.18 0.21 0.177

Calibration Post Zero Cylinder Bias 0.41 0.36 0.41 0.393

Calibration Post Zero Cylinder Drift 0.31 0.21 0.31 0.277

Calibration Post High Cylinder ID ALM015275 ALM015275 ALM015275

Calibration Post High Cylinder Instrument Response 9.69 9.62 9.62 9.643

Calibration Post High Cylinder Bias 0 -0.36 -0.51 -0.290

Calibration Post High Cylinder Drift 0.51 0.15 0.05 0.237

Cavg 13.04 12.84 13.1 12.993

Cavg Units ppmvd ppmvd ppmvd

Cgas 12.8622 12.727 12.9816 12.857

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Friday, January 14, 2011 Page 38 of 47
Location Stack Exit - Method 3A CO2 3 6

Average

Run Number 2 Form 2 Hg 2 ORG

Test Date 7/24/2010 7/25/2010 7/23/2010

Run Start Time 10:25:00 AM 10:53:00 AM 11:36:00 AM

Run Finish Time 12:47:00 PM 1:07:00 PM 1:52:00 PM

Carbon Dioxide, % 13.15 13.16 13.14 13.150

Oxygen, % 6.32 6.23 6.29 6.280

Fuel Factor 1.11 1.11 1.11

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1440 1440 1440 1,440.000

Analyzer Serial Number Waits Waits Waits

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 11 111 1 41.000

Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Pre Zero Cylinder Instrument Response 0.14 0.16 0.14 0.147

Calibration Pre Zero Cylinder Bias 0.31 0.15 0.41 0.290

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM015275 ALM015275 ALM015275

Calibration Pre High Cylinder Instrument Response 9.63 9.62 9.69 9.647

Calibration Pre High Cylinder Bias -0.41 -0.51 0 -0.307

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Post Zero Cylinder Instrument Response 0.14 0.17 0.17 0.160

Calibration Post Zero Cylinder Bias 0.31 0.21 0.56 0.360

Calibration Post Zero Cylinder Drift 0 0.06 0.15 0.070

Calibration Post High Cylinder ID ALM015275 ALM015275 ALM015275

Calibration Post High Cylinder Instrument Response 9.61 9.66 9.64 9.637

Calibration Post High Cylinder Bias -0.51 -0.31 -0.26 -0.360

Calibration Post High Cylinder Drift 0.1 0.2 0.26 0.187

Cavg 13.15 13.16 13.14 13.150

Cavg Units ppmvd ppmvd ppmvd

Cgas 13.01 13.0019 12.944 12.985

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Friday, January 14, 2011 Page 39 of 47
Location Stack Exit - Method 3A CO2 3 6 9

Average

Run Number 2 PM 3 DF 3 Form

Test Date 8/3/2010 7/26/2010 7/24/2010

Run Start Time 1:23:00 PM 6:21:00 AM 1:24:00 PM

Run Finish Time 6:11:00 PM 6:01:00 PM 3:37:00 PM

Carbon Dioxide, % 12.97 13.07 13.18 13.073

Oxygen, % 6.4 6.31 6.24 6.317

Fuel Factor 1.12 1.12 1.11

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1440 1440 1440 1,440.000

Analyzer Serial Number Waits Waits Waits

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 10 1111 11 377.333

Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Pre Zero Cylinder Instrument Response 0.18 0.12 0.14 0.147

Calibration Pre Zero Cylinder Bias 0.36 0.15 0.31 0.273

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM015275 ALM015275 ALM015275

Calibration Pre High Cylinder Instrument Response 9.62 9.58 9.61 9.603

Calibration Pre High Cylinder Bias -0.36 -0.41 -0.51 -0.427

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718

Calibration Post Zero Cylinder Instrument Response 0.19 0.17 0.15 0.170

Calibration Post Zero Cylinder Bias 0.41 0.41 0.36 0.393

Calibration Post Zero Cylinder Drift 0.05 0.26 0.05 0.120

Calibration Post High Cylinder ID ALM015275 ALM015275 ALM015275

Calibration Post High Cylinder Instrument Response 9.6 9.59 9.61 9.600

Calibration Post High Cylinder Bias -0.46 -0.36 -0.51 -0.443

Calibration Post High Cylinder Drift 0.1 0.05 0 0.050

Cavg 12.97 13.07 13.18 13.073

Cavg Units ppmvd ppmvd ppmvd

Cgas 12.8596 12.9798 13.0557 12.965

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Friday, January 14, 2011 Page 40 of 47
Location Stack Exit - Method 3A CO2 3 6 9 12

Average

Run Number 3 Hg 3 ORG 3 PM

Test Date 7/25/2010 7/23/2010 8/4/2010

Run Start Time 1:46:00 PM 2:39:00 PM 7:32:00 AM

Run Finish Time 3:52:00 PM 5:37:00 PM 12:00:00 PM

Carbon Dioxide, % 13.19 13.15 12.9 13.080

Oxygen, % 6.16 6.23 6.52 6.303

Fuel Factor

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2

Moisture, % 0 0 0 0.000

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

Friday, January 14, 2011 Page 41 of 47
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

Friday, January 14, 2011 Page 42 of 47
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

Friday, January 14, 2011 Page 43 of 47
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

Friday, January 14, 2011 Page 44 of 47
Location Stack Exit - Method 3A O2 3 6 9

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Friday, January 14, 2011 Page 45 of 47
Location Stack Exit - Method 3A O2 3 6 9 12

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

Friday, January 14, 2011 Page 46 of 47
Location Stack Exit - Method 5/OTM-28

Average

Run Number 1 2 3

Test Date 8/3/2010 8/3/2010 8/4/2010

Run Start Time 7:40:00 AM 1:23:00 PM 7:32:00 AM

Run Finish Time 12:05:00 PM 6:11:00 PM 12:00:00 PM

Net Traversing Points 0 0 0

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.247 0.247 0.247 0.247

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.001 1.001 1.001 1.001

Barometric Pressure, inches of Mercury 29.39 29.39 29.39 29.390

Average Orifice Meter Differential, inches H2O 1.64 1.56 1.63 1.610

Dry Gas Meter Volume Sampled, cubic feet 166.676 160.938 163.415 163.676

Average Dry Gas Meter Temperature, °F 102.29 107.60 101.58 103.823

Dry Gas Meter Volume Sampled, dscf 154.524 147.779 151.689 151.331

Total Moisture Liquid collected, g 517.9 490.9 509.4 506.067

Volume of Water Vapor, standard cubic feet 24.38 23.11 23.98 23.823

Moisture Content of Stack Gas, % 13.63 13.52 13.65 13.600

Moisture Saturation at Stack Gas Temperature, % 33.64 34.32 33.64 33.867

Dry Mole Fraction 0.8637 0.8648 0.8635 0.864

Carbon Dioxide, % 13 13 12.8 12.933

Oxygen, % 6.4 6.3 6.6 6.433

Carbon Monoxide & Nitrogen, % 80.6 80.7 80.6 80.633

Fuel Factor 1.12 1.12 1.12

Dry Molecular Weight, lb/lb-Mole 30.34 30.33 30.31 30.327

Wet Molecular weight, lb/lb-Mole 28.66 28.66 28.63 28.650

Flue Gas Static Pressure, inches of H2O -0.42 -0.45 -0.35 -0.407

Absolute Flue Gas Pressure, inches of Mercury 29.36 29.36 29.36 29.360

Average Stack Gas Temperature, °F 161.06 161.90 161.06 161.340

Average Velocity Head, inches of H2O 0.5546700024

2251

0.548849500

622287

0.566405009

682954

0.557

Average Stack Gas Velocity, feet/second 45.95 45.74 46.46 46.050

Stack Cross-Sectional Area, square feet 226.980 226.980 226.980 226.980

Dry Volumetric Flow Rate, dry scfm 450,901.9 448,805.9 455,800.9 451,836.233

Actual Wet Volumetric Flue Gas Flow Rate, acfm 625,783.9 622,923.9 632,729.4 627,145.733

Percent Isokinetic of Sampling Rate, % 97.4 93.6 94.6 95.200

Percent Excess Air, % 43.0 42.0 45.0 43.333

F-Factor, dscfm/MMBtu @ %O2 99360 9936 9936 39,744.000

Round Duct Diameter, inches 204 204 204

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, January 14, 2011 Page 47 of 47