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 30
Facility Information:

AES Shady Point, LLC

P.P. Box 1740

Panama OK 74951

Contact: Sharon Shelby

Phone: 918-962-9451

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:

10671

Permitted Source ID/Name:

Combined Stack, Units 1A, 1B, 2A, and 2B

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:

Shady Point consists of four identical circulating fluid bed (CFB) boilers identified as 1A, 1B, 2A, and 2B, each rated 

at 567,000 lb/hr of steam. Boilers 1A and 1B supply steam to a single turbine. Boilers 2A and 2B supply steam to a 

second turbine. The rated electrical output of each turbine is 180 MW gross.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 4007900001 FRS #: 325120

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 211 0 0 0 2016 1608 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 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 3 120 0

Stack Exit Hydrogen Chloride Method 26A 3 120 0

Organic Condensible 

Particulate

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

Inorganic (Aqueous) 

Condensible Part.

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Friday, January 14, 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

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Selenium Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit Co2 Method 3A CO2 3 480 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit Co2 Method 3A CO2 3 240 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit O2 Method 3A O2 3 120 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 30
Sampling / Stack Data Results Summary

Location Stack Exit - Method 10

Average

Run Number Hg 1 Hg 2 Hg 3

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

Run Start Time 8:13:00 AM 12:47:00 

PM

3:50:00 PM

Run Finish Time 1:01:00 PM 3:56:00 PM 7:15:00 PM

Carbon Dioxide, % 15.28 15.21 15.18 15.223

Oxygen, % 3.86 3.89 3.96 3.903

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 25A

Average

Run Number Hg 1 Hg 2 Hg 3

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

Run Start Time 9:35:00 AM 1:32:00 PM 5:36:00 PM

Run Finish Time 12:33:00 PM 3:52:00 PM 7:12:00 PM

Carbon Dioxide, % 15.28 15.21 15.18 15.223

Oxygen, % 3.86 3.89 3.96 3.903

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 5 of 30
Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 6/6/2010 6/7/2010 6/8/2010

Run Start Time 4:10:00 PM 7:45:00 

AM

2:40:00 PM

Run Finish Time 6:51:00 PM 1:20:00 PM 5:12:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 77.460 77.307 75.229 76.665

Moisture Content of Stack Gas, % 11.47 11.92 12.80 12.063

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

Carbon Dioxide, % 15 15.2 15.4 15.200

Oxygen, % 4.1 4 3.8 3.967

Average Stack Gas Temperature, °F 335.50 328.32 336.79 333.537

Dry Volumetric Flow Rate, dry scfm 728,465.5 720,940.9 696,782.6 715,396.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,267,687.0 1,249,620.9 1,233,885.9 1,250,397.93

3

Percent Isokinetic of Sampling Rate, % 101.7 102.5 103.2 102.467

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

Friday, January 14, 2011 Page 6 of 30
Location Stack Exit - Method 29 

Average

Run Number 1 2 3

Test Date 6/6/2010 6/7/2010 6/8/2010

Run Start Time 9:01:00 AM 2:26:00 PM 8:00:00 AM

Run Finish Time 1:43:00 PM 6:58:00 PM 12:42:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 152.768 145.683 149.137 149.196

Moisture Content of Stack Gas, % 12.44 12.57 12.62 12.543

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

Carbon Dioxide, % 15.2 15.2 15.4 15.267

Oxygen, % 3.8 3.9 3.8 3.833

Average Stack Gas Temperature, °F 332.81 331.96 334.52 333.097

Dry Volumetric Flow Rate, dry scfm 721,017.5 696,432.3 684,991.3 700,813.700

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,264,336.0 1,217,568.1 1,202,124.5 1,228,009.53

3

Percent Isokinetic of Sampling Rate, % 101.3 100.0 104.1 101.800

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 3A CO2

Average

Run Number Acid 1 Acid 2 Acid 3

Test Date 6/6/2010 6/7/2010 6/8/2010

Run Start Time 4:03:00 PM 7:17:00 

AM

2:32:00 PM

Run Finish Time 7:04:00 PM 1:29:00 PM 5:24:00 PM

Carbon Dioxide, % 14.98 15.18 15.37 15.177

Oxygen, % 4.09 3.97 3.82 3.960

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 30
Location Stack Exit - Method 3A CO2 3

Average

Run Number Hg 1 Hg 2 Hg 3

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

Run Start Time 8:13:00 AM 12:47:00 

PM

3:50:00 PM

Run Finish Time 12:59:00 PM 3:54:00 PM 7:17:00 PM

Carbon Dioxide, % 15.28 15.21 15.18 15.223

Oxygen, % 3.86 3.89 3.96 3.903

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

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 8 of 30
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 9 of 30
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 - OTM - 27/28

Average

Run Number 1 2 3

Test Date 6/6/2010 6/7/2010 6/8/2010

Run Start Time 9:00:00 AM 1:40:00 PM 8:00:00 AM

Run Finish Time 3:53:15 PM 8:12:45 PM 2:30:00 PM

Net Run Time, minutes 413.25 392.75 390

Dry Gas Meter Volume Sampled, dscf 137.270 130.400 128.866 132.179

Moisture Content of Stack Gas, % 12.37 14.28 14.51 13.720

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

Carbon Dioxide, % 15.2 15.2 15.4 15.267

Oxygen, % 3.8 3.9 3.8 3.833

Average Stack Gas Temperature, °F 335.92 330.67 335.25 333.947

Dry Volumetric Flow Rate, dry scfm 769,547.4 750,921.5 745,054.5 755,174.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,353,646.7 1,341,408.3 1,343,156.7 1,346,070.56

7

Percent Isokinetic of Sampling Rate, % 88.9 91.1 91.4 90.467

F-Factor, dscfm/MMBtu @ %O2 10100 9780 9780 9,886.667

Fw 10540 10640 10640 10,606.667

Fc 1970 1800 1800 1,856.667

Friday, January 14, 2011 Page 10 of 30
Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run Hg 1 Hg 2 Hg 3

lb/mmBtuO2 4.60E-02 4.93E-02 4.95E-02 0.048

ppm 5.28E+01 5.65E+01 5.65E+01 55.267

ppm@7%O2 4.31E+01 4.62E+01 4.64E+01 45.233

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run Hg 1 Hg 2 Hg 3

lb/mmBtuO2 4.27E-04 4.46E-04 4.01E-04 0.000

ppm 3.11E-01 3.24E-01 2.90E-01 0.308

ppm@7%O2 2.54E-01 2.65E-01 2.38E-01 0.252

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 8.862 10.196 9.162 9.407

Elb/hr 1.10E+01 1.26E+01 1.12E+01 11.600

lb/mmBtuO2 3.07E-03 3.52E-03 3.21E-03 0.003

mg/dscm 4.04E+00 4.66E+00 4.30E+00 4.333

mg/dscm@7%O2 3.34E+00 3.83E+00 3.50E+00 3.557

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.877 0.551 0.333 0.587

Elb/hr 1.09E+00 6.80E-01 4.08E-01 0.726

lb/mmBtuO2 3.04E-04 1.90E-04 1.17E-04 0.000

mg/dscm 4.00E-01 2.52E-01 1.56E-01 0.269

mg/dscm@7%O2 3.31E-01 2.07E-01 1.27E-01 0.222

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00012 0.00013 0.00016 0.000

Elb/hr 7.49E-05 8.22E-05 9.72E-05 0.000

lb/mmBtuO2 2.07E-08 2.37E-08 2.83E-08 0.000

mg/dscm 2.77E-05 3.15E-05 3.79E-05 0.000

mg/dscm@7%O2 2.25E-05 2.58E-05 3.08E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.000595 0.000555 0.000665 0.001

Elb/hr 3.71E-04 3.51E-04 4.04E-04 0.000

Friday, January 14, 2011 Page 11 of 30
lb/mmBtuO2 1.03E-07 1.01E-07 1.18E-07 0.000

mg/dscm 1.38E-04 1.35E-04 1.57E-04 0.000

mg/dscm@7%O2 1.12E-04 1.10E-04 1.28E-04 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000052 0.000052 0.000072 0.000

Elb/hr 3.25E-05 3.29E-05 4.37E-05 0.000

lb/mmBtuO2 8.97E-09 9.46E-09 1.27E-08 0.000

mg/dscm 1.20E-05 1.26E-05 1.71E-05 0.000

mg/dscm@7%O2 9.75E-06 1.03E-05 1.39E-05 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00009 0.00103 0.00049 0.001

Elb/hr 5.62E-05 6.51E-04 2.98E-04 0.000

lb/mmBtuO2 1.55E-08 1.87E-07 8.66E-08 0.000

mg/dscm 2.08E-05 2.50E-04 1.16E-04 0.000

mg/dscm@7%O2 1.69E-05 2.04E-04 9.43E-05 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0033 0.005 0.00414 0.004

Elb/hr 2.06E-03 3.16E-03 2.52E-03 0.003

lb/mmBtuO2 5.69E-07 9.10E-07 7.32E-07 0.000

mg/dscm 7.63E-04 1.21E-03 9.80E-04 0.001

mg/dscm@7%O2 6.20E-04 9.89E-04 7.97E-04 0.001

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 26.5 25.2 29.5 27.067

Elb/hr 1.65E+01 1.59E+01 1.79E+01 16.767

lb/mmBtuO2 4.57E-03 4.59E-03 5.21E-03 0.005

mg/dscm 6.13E+00 6.11E+00 6.99E+00 6.410

mg/dscm@7%O2 4.98E+00 5.00E+00 5.68E+00 5.220

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00118 0.00115 0.00071 0.001

Elb/hr 7.37E-04 7.27E-04 4.31E-04 0.001

lb/mmBtuO2 2.04E-07 2.09E-07 1.25E-07 0.000

mg/dscm 2.73E-04 2.79E-04 1.68E-04 0.000

mg/dscm@7%O2 2.22E-04 2.28E-04 1.37E-04 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.00275 0.00068 0.00107 0.002

Elb/hr 1.72E-03 4.30E-04 6.50E-04 0.001

Friday, January 14, 2011 Page 12 of 30
lb/mmBtuO2 4.74E-07 1.24E-07 1.89E-07 0.000

mg/dscm 6.36E-04 1.65E-04 2.53E-04 0.000

mg/dscm@7%O2 5.17E-04 1.35E-04 2.06E-04 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.00275 0.00426 0.00295 0.003

Elb/hr 1.72E-03 2.69E-03 1.79E-03 0.002

lb/mmBtuO2 4.74E-07 7.75E-07 5.21E-07 0.000

mg/dscm 6.36E-04 1.03E-03 6.99E-04 0.001

mg/dscm@7%O2 5.17E-04 8.42E-04 5.68E-04 0.001

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.00052 0.00052 0.00052 0.001

Elb/hr 3.25E-04 3.29E-04 3.16E-04 0.000

lb/mmBtuO2 8.97E-08 9.46E-08 9.19E-08 0.000

mg/dscm 1.20E-04 1.26E-04 1.23E-04 0.000

mg/dscm@7%O2 9.75E-05 1.03E-04 1.00E-04 0.000

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 400.1 300.7 44.7 248.500

lb/mmBtuO2 7.93E-02 6.11E-02 9.14E-03 0.050

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 362.6 296.6 38.3 232.500

lb/mmBtuO2 7.19E-02 6.03E-02 7.83E-03 0.047

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 21.2 23.9 21.2 22.100

lb/mmBtuO2 4.20E-03 4.86E-03 4.34E-03 0.004

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 7.5 3.8 2.8 4.700

lb/mmBtuO2 1.49E-03 7.72E-04 5.73E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 428.8 328.4 68.7 275.300

lb/mmBtuO2 8.50E-02 6.68E-02 1.40E-02 0.055

Friday, January 14, 2011 Page 13 of 30
Process Run Data

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 66.2 31.8 30.4 42.800

lb/mmBtuO2 1.31E-02 6.46E-03 6.22E-03 0.009

Friday, January 14, 2011 Page 14 of 30
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 211.4 Tons 0

10 Bituminous Coal Burned 202.75 Tons 0

11 Bituminous Coal Burned 203.05 Tons 0

12 Bituminous Coal Burned 209.55 Tons 0

2 Bituminous Coal Burned 209.4 Tons 0

3 Bituminous Coal Burned 209.1 Tons 0

4 Bituminous Coal Burned 206.75 Tons 0

5 Bituminous Coal Burned 205.6 Tons 0

6 Bituminous Coal Burned 210.3 Tons 0

7 Bituminous Coal Burned 205.2 Tons 0

8 Bituminous Coal Burned 207.15 Tons 0

9 Bituminous Coal Burned 210.8 Tons 0

1 Average Heat Input 4542 MMBtu/hr 0

10 Average Heat Input 4245.9 MMBtu/hr 0

11 Average Heat Input 4358.1 MMBtu/hr 0

12 Average Heat Input 4627.2 MMBtu/hr 0

2 Average Heat Input 4716.9 MMBtu/hr 0

3 Average Heat Input 4710.6 MMBtu/hr 0

4 Average Heat Input 4485.5 MMBtu/hr 0

5 Average Heat Input 4644.3 MMBtu/hr 0

6 Average Heat Input 4754 MMBtu/hr 0

7 Average Heat Input 4367 MMBtu/hr 0

8 Average Heat Input 4543.5 MMBtu/hr 0

9 Average Heat Input 4774.1 MMBtu/hr 0

1 Steam Output 2E+06 1000 lb steam/hr 0

10 Steam Output 2E+06 1000 lb steam/hr 0

11 Steam Output 2E+06 1000 lb steam/hr 0

12 Steam Output 2E+06 1000 lb steam/hr 0

2 Steam Output 2E+06 1000 lb steam/hr 0

3 Steam Output 2E+06 1000 lb steam/hr 0

4 Steam Output 2E+06 1000 lb steam/hr 0

5 Steam Output 2E+06 1000 lb steam/hr 0

6 Steam Output 2E+06 1000 lb steam/hr 0

Friday, January 14, 2011 Page 15 of 30
7 Steam Output 2E+06 1000 lb steam/hr 0

8 Steam Output 2E+06 1000 lb steam/hr 0

9 Steam Output 2E+06 1000 lb steam/hr 0

1 Fuel Oil Firing Rate 0 0

10 Fuel Oil Firing Rate 0 0

11 Fuel Oil Firing Rate 0 0

12 Fuel Oil Firing Rate 0 0

2 Fuel Oil Firing Rate 0 0

3 Fuel Oil Firing Rate 0 0

4 Fuel Oil Firing Rate 0 0

5 Fuel Oil Firing Rate 0 0

6 Fuel Oil Firing Rate 0 0

7 Fuel Oil Firing Rate 0 0

8 Fuel Oil Firing Rate 0 0

9 Fuel Oil Firing Rate 0 0

1 Standard Pressure 0 atm 0

10 Standard Pressure 0 atm 0

11 Standard Pressure 0 atm 0

12 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

10 Standard Temperature 0 Deg F 0

11 Standard Temperature 0 Deg F 0

12 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

Friday, January 14, 2011 Page 16 of 30
APCD Run Data

Process Lab Run Data

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 0 MW 0

10 Unit Gross Electrical Output 0 MW 0

11 Unit Gross Electrical Output 0 MW 0

12 Unit Gross Electrical Output 0 MW 0

2 Unit Gross Electrical Output 0 MW 0

3 Unit Gross Electrical Output 0 MW 0

4 Unit Gross Electrical Output 0 MW 0

5 Unit Gross Electrical Output 0 MW 0

6 Unit Gross Electrical Output 0 MW 0

7 Unit Gross Electrical Output 0 MW 0

8 Unit Gross Electrical Output 0 MW 0

9 Unit Gross Electrical Output 0 MW 0

1 Unit Net Electric Generation 0 MWh 0

10 Unit Net Electric Generation 0 MWh 0

11 Unit Net Electric Generation 0 MWh 0

12 Unit Net Electric Generation 0 MWh 0

2 Unit Net Electric Generation 0 MWh 0

3 Unit Net Electric Generation 0 MWh 0

4 Unit Net Electric Generation 0 MWh 0

5 Unit Net Electric Generation 0 MWh 0

6 Unit Net Electric Generation 0 MWh 0

7 Unit Net Electric Generation 0 MWh 0

8 Unit Net Electric Generation 0 MWh 0

9 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 9169 Btu/lb

2 Fuel Higher Heating Value 9041 Btu/lb

3 Fuel Higher Heating Value 8797 Btu/lb

4 Fuel Higher Heating Value 8814 Btu/lb

Friday, January 14, 2011 Page 17 of 30
5 Fuel Higher Heating Value 9189 Btu/lb 6 Fuel Higher Heating Value 9191 Btu/lb 1 Fuel Moisture 21.9 % 2 Fuel Moisture 23.3 % 3 Fuel Moisture 25.8 % 4 Fuel Moisture 23.2 % 5 Fuel Moisture 20.7 % 6 Fuel Moisture 19.8 % 1 Fuel Mercury Content 0.308 ppm 2 Fuel Mercury Content 0.256 ppm 3 Fuel Mercury Content 0.22 ppm 4 Fuel Mercury Content 0.301 ppm 5 Fuel Mercury Content 0.213 ppm 6 Fuel Mercury Content 0.452 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 1 Ultimate/Proximate Analysis 0 2 Ultimate/Proximate Analysis 0 3 Ultimate/Proximate Analysis 0 4 Ultimate/Proximate Analysis 0 5 Ultimate/Proximate Analysis 0 6 Ultimate/Proximate Analysis 0 1 Fuel Nickel Content 16 ppm 2 Fuel Nickel Content 14 ppm 3 Fuel Nickel Content 8.5 ppm 4 Fuel Nickel Content 8.9 ppm 5 Fuel Nickel Content 12 ppm 6 Fuel Nickel Content 17 ppm 1 Fuel Arsenic Content 5.8 ppm 2 Fuel Arsenic Content 5.3 ppm 3 Fuel Arsenic Content 7.8 ppm 4 Fuel Arsenic Content 2.5 ppm 5 Fuel Arsenic Content 3.9 ppm 6 Fuel Arsenic Content 5.4 ppm 1 Fuel Chromium Content 7.9 ppm 2 Fuel Chromium Content 8.2 ppm 3 Fuel Chromium Content 7.8 ppm 4 Fuel Chromium Content 7.4 ppm 5 Fuel Chromium Content 9.5 ppm

Friday, January 14, 2011 Page 18 of 30
6 Fuel Chromium Content 9.2 ppm

1 Fuel Beryllium Content 0.52 ppm

2 Fuel Beryllium Content 0 ppm

3 Fuel Beryllium Content 0 ppm

4 Fuel Beryllium Content 0.61 ppm

5 Fuel Beryllium Content 0.6 ppm

6 Fuel Beryllium Content 0 ppm

1 Fuel Lead Content 6.1 ppm

2 Fuel Lead Content 8 ppm

3 Fuel Lead Content 2.9 ppm

4 Fuel Lead Content 3.3 ppm

5 Fuel Lead Content 4.6 ppm

6 Fuel Lead Content 6.3 ppm

1 Fuel Manganese Content 59 ppm

2 Fuel Manganese Content 78 ppm

3 Fuel Manganese Content 37 ppm

4 Fuel Manganese Content 59 ppm

5 Fuel Manganese Content 102 ppm

6 Fuel Manganese Content 126 ppm

1 Fuel Chlorine Content 0 ppm

2 Fuel Chlorine Content 0 ppm

3 Fuel Chlorine Content 0 ppm

4 Fuel Chlorine Content 105 ppm

5 Fuel Chlorine Content 101 ppm

6 Fuel Chlorine Content 105 ppm

1 Fuel Fluorine Content 0 ppm

2 Fuel Fluorine Content 0 ppm

3 Fuel Fluorine Content 0 ppm

4 Fuel Fluorine Content 0 ppm

5 Fuel Fluorine Content 0 ppm

6 Fuel Fluorine Content 0 ppm

Friday, January 14, 2011 Page 19 of 30
Sampling / Stack Data Results Detail

Location Stack Exit - Method 10

Average

Run Number Hg 1 Hg 2 Hg 3

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

Run Start Time 8:13:00 AM 12:47:00 PM 3:50:00 PM

Run Finish Time 1:01:00 PM 3:56:00 PM 7:15:00 PM

Carbon Dioxide, % 15.28 15.21 15.18 15.223

Oxygen, % 3.86 3.89 3.96 3.903

Fuel Factor 1.12 1.12 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 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 Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 1.1 0.9 0.77 0.923

Calibration Pre Zero Cylinder Bias 0.9 0.7 0.57 0.723

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC69247 CC69247 CC69247

Calibration Pre High Cylinder Instrument Response 51.6 51.2 51.13 51.310

Calibration Pre High Cylinder Bias 0.5 0.1 0.03 0.210

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.9 0.77 0.9 0.857

Calibration Post Zero Cylinder Bias 0.7 0.57 0.7 0.657

Calibration Post Zero Cylinder Drift 0.2 0.13 0.13 0.153

Calibration Post High Cylinder ID CC69247 CC69247 CC69247

Calibration Post High Cylinder Instrument Response 51.2 51.13 51.2 51.177

Calibration Post High Cylinder Bias 0.1 0 0.1 0.067

Calibration Post High Cylinder Drift 0.4 0 0.07 0.157

Cavg 53.99 57.45 57.46 56.300

Cavg Units ppmvd ppmvd ppmvd

Cgas 52.7797 56.4688 56.4787 55.242

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 20 of 30
Location Stack Exit - Method 25A

Average

Run Number Hg 1 Hg 2 Hg 3

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

Run Start Time 9:35:00 AM 1:32:00 PM 5:36:00 PM

Run Finish Time 12:33:00 PM 3:52:00 PM 7:12:00 PM

Carbon Dioxide, % 15.28 15.21 15.18 15.223

Oxygen, % 3.86 3.89 3.96 3.903

Fuel Factor 1.12 1.12 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 TECO TECO TECO

Analyzer Model 51i 51i 51i

Analyzer Serial Number Cash Cash Cash

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 Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response -0.01 -0.02 0.01 -0.007

Calibration Pre Zero Cylinder Bias -0.04 -0.08 0.04 -0.027

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC52469 CC52469 CC52469

Calibration Pre High Cylinder Instrument Response 7.41 7.48 7.45 7.447

Calibration Pre High Cylinder Bias -0.44 -0.16 -0.28 -0.293

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.02 -0.04 -0.02 -0.013

Calibration Post Zero Cylinder Bias 0.08 -0.16 -0.08 -0.053

Calibration Post Zero Cylinder Drift 0.12 0.08 0.12 0.107

Calibration Post High Cylinder ID CC52469 CC52469 CC52469

Calibration Post High Cylinder Instrument Response 7.49 7.45 7.44 7.460

Calibration Post High Cylinder Bias -0.12 -0.28 -0.32 -0.240

Calibration Post High Cylinder Drift 0.32 0.12 0.04 0.160

Cavg 0.31 0.29 0.28 0.293

Cavg Units ppmvd ppmvd ppmvd

Cgas 0.3109 0.3241 0.2904 0.308

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 21 of 30
Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 6/6/2010 6/7/2010 6/8/2010

Run Start Time 4:10:00 PM 7:45:00 AM 2:40:00 PM

Run Finish Time 6:51:00 PM 1:20:00 PM 5:12:00 PM

Net Traversing Points 24 25 24

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.197 0.197 0.197 0.197

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.998 0.998 1.005 1.000

Barometric Pressure, inches of Mercury 29.33 29.33 29.31 29.323

Average Orifice Meter Differential, inches H2O 1.48 1.40 1.33 1.403

Dry Gas Meter Volume Sampled, cubic feet 82.980 80.340 80.555 81.292

Average Dry Gas Meter Temperature, °F 95.42 78.70 98.48 90.867

Dry Gas Meter Volume Sampled, dscf 77.460 77.307 75.229 76.665

Total Moisture Liquid collected, g 213.4 222.3 234.5 223.400

Volume of Water Vapor, standard cubic feet 10.04 10.46 11.04 10.513

Moisture Content of Stack Gas, % 11.47 11.92 12.80 12.063

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

Dry Mole Fraction 0.8853 0.8808 0.872 0.879

Carbon Dioxide, % 15 15.2 15.4 15.200

Oxygen, % 4.1 4 3.8 3.967

Carbon Monoxide & Nitrogen, % 80.9 80.8 80.8 80.833

Fuel Factor 1.12 1.11 1.11

Dry Molecular Weight, lb/lb-Mole 30.56 30.59 30.62 30.590

Wet Molecular weight, lb/lb-Mole 29.12 29.09 29.00 29.070

Flue Gas Static Pressure, inches of H2O -1 -1 -1 -1.000

Absolute Flue Gas Pressure, inches of Mercury 29.26 29.26 29.24 29.253

Average Stack Gas Temperature, °F 335.50 328.32 336.79 333.537

Average Velocity Head, inches of H2O 1.5722650896

0144

1.540271602

72287

1.480208393

62868

1.531

Average Stack Gas Velocity, feet/second 87.01 85.77 84.69 85.823

Stack Cross-Sectional Area, square feet 242.824 242.824 242.824 242.824

Dry Volumetric Flow Rate, dry scfm 728,465.5 720,940.9 696,782.6 715,396.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,267,687.0 1,249,620.9 1,233,885.9 1,250,397.9

33

Percent Isokinetic of Sampling Rate, % 101.7 102.5 103.2 102.467

Percent Excess Air, % 23.8 23.1 21.7 22.867

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

Round Duct Diameter, inches 211 211 211

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 22 of 30
Location Stack Exit - Method 29 

Average

Run Number 1 2 3

Test Date 6/6/2010 6/7/2010 6/8/2010

Run Start Time 9:01:00 AM 2:26:00 PM 8:00:00 AM

Run Finish Time 1:43:00 PM 6:58:00 PM 12:42:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.197 0.197 0.197 0.197

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.988 1.005 1.005 0.999

Barometric Pressure, inches of Mercury 29.33 29.43 29.43 29.397

Average Orifice Meter Differential, inches H2O 1.50 1.27 1.27 1.347

Dry Gas Meter Volume Sampled, cubic feet 167.179 152.479 159.620 159.759

Average Dry Gas Meter Temperature, °F 101.72 88.03 100.41 96.720

Dry Gas Meter Volume Sampled, dscf 152.768 145.683 149.137 149.196

Total Moisture Liquid collected, g 461.3 445.1 457.6 454.667

Volume of Water Vapor, standard cubic feet 21.71 20.95 21.54 21.400

Moisture Content of Stack Gas, % 12.44 12.57 12.62 12.543

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

Dry Mole Fraction 0.8756 0.8743 0.8738 0.875

Carbon Dioxide, % 15.2 15.2 15.4 15.267

Oxygen, % 3.8 3.9 3.8 3.833

Carbon Monoxide & Nitrogen, % 81 80.9 80.8 80.900

Fuel Factor 1.13 1.12 1.11

Dry Molecular Weight, lb/lb-Mole 30.58 30.59 30.62 30.597

Wet Molecular weight, lb/lb-Mole 29.02 29.01 29.03 29.020

Flue Gas Static Pressure, inches of H2O -1 -1 -1 -1.000

Absolute Flue Gas Pressure, inches of Mercury 29.26 29.36 29.36 29.327

Average Stack Gas Temperature, °F 332.81 331.96 334.52 333.097

Average Velocity Head, inches of H2O 1.5641400148

9129

1.456590502

132

1.416357040

20261

1.479

Average Stack Gas Velocity, feet/second 86.78 83.57 82.51 84.287

Stack Cross-Sectional Area, square feet 242.824 242.824 242.824 242.824

Dry Volumetric Flow Rate, dry scfm 721,017.5 696,432.3 684,991.3 700,813.700

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,264,336.0 1,217,568.1 1,202,124.5 1,228,009.5

33

Percent Isokinetic of Sampling Rate, % 101.3 100.0 104.1 101.800

Percent Excess Air, % 21.6 22.3 21.7 21.867

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

Round Duct Diameter, inches 211 211 211

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 23 of 30
Location Stack Exit - Method 3A CO2

Average

Run Number Acid 1 Acid 2 Acid 3

Test Date 6/6/2010 6/7/2010 6/8/2010

Run Start Time 4:03:00 PM 7:17:00 AM 2:32:00 PM

Run Finish Time 7:04:00 PM 1:29:00 PM 5:24:00 PM

Carbon Dioxide, % 14.98 15.18 15.37 15.177

Oxygen, % 4.09 3.97 3.82 3.960

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 Sevomex Sevomex Sevomex

Analyzer Model 1440 1440 1440 1,440.000

Analyzer Serial Number Dylan Dylan Dylan

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 22 222 2222 822.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.13 0.13 0.13 0.130

Calibration Pre Zero Cylinder Bias 0.46 0.41 0.51 0.460

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC250478CO

2

CC250478C

O2

CC250478CO

2

Calibration Pre High Cylinder Instrument Response 9.66 9.64 9.62 9.640

Calibration Pre High Cylinder Bias 0 -0.62 -0.46 -0.360

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.12 0.13 0.12 0.123

Calibration Post Zero Cylinder Bias 0.41 0.41 0.46 0.427

Calibration Post Zero Cylinder Drift 0.05 0 0.05 0.033

Calibration Post High Cylinder ID CC250478CO

2

CC250478C

O2

CC250478CO

2

Calibration Post High Cylinder Instrument Response 9.67 9.68 9.6 9.650

Calibration Post High Cylinder Bias 0.05 -0.41 -0.56 -0.307

Calibration Post High Cylinder Drift 0.05 0.21 0.1 0.120

Cavg 15.27 15.46 15.56 15.430

Cavg Units %vd %vd ppmvd

Cgas 14.9862 15.1852 15.3618 15.178

Cgas Units %vd %vd 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 24 of 30
Location Stack Exit - Method 3A CO2 3

Average

Run Number Hg 1 Hg 2 Hg 3

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

Run Start Time 8:13:00 AM 12:47:00 PM 3:50:00 PM

Run Finish Time 12:59:00 PM 3:54:00 PM 7:17:00 PM

Carbon Dioxide, % 15.28 15.21 15.18 15.223

Oxygen, % 3.86 3.89 3.96 3.903

Fuel Factor 1.12 1.12 0

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 Sevomex Sevomex Sevomex

Analyzer Model 1440 1440 1440 1,440.000

Analyzer Serial Number Dylan Dylan Dylan

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID Zero Zero Zero

Calibration Pre Zero Cylinder Instrument Response 0.03 0.07 0.07 0.057

Calibration Pre Zero Cylinder Bias 0.05 0.26 0.26 0.190

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC250478CO

2

CC250478C

O2

CC250478CO

2

Calibration Pre High Cylinder Instrument Response 9.58 9.68 9.64 9.633

Calibration Pre High Cylinder Bias -0.67 -0.15 -0.36 -0.393

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Zero Zero Zero

Calibration Post Zero Cylinder Instrument Response 0.07 0.07 0.08 0.073

Calibration Post Zero Cylinder Bias 0.26 0.26 0.31 0.277

Calibration Post Zero Cylinder Drift 0.21 0 0.05 0.087

Calibration Post High Cylinder ID CC250478CO

2

CC250478C

O2

CC250478CO

2

Calibration Post High Cylinder Instrument Response 9.68 9.64 9.61 9.643

Calibration Post High Cylinder Bias -0.15 -0.36 -0.51 -0.340

Calibration Post High Cylinder Drift 0.52 0.21 0.15 0.293

Cavg 15.56 15.52 15.43 15.503

Cavg Units %vd %vd %vd

Cgas 15.2833 15.2083 15.1781 15.223

Cgas Units %vd %vd %vd

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 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

Friday, January 14, 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

Friday, January 14, 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

Friday, January 14, 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

Friday, January 14, 2011 Page 29 of 30
Location Stack Exit - OTM - 27/28

Average

Run Number 1 2 3

Test Date 6/6/2010 6/7/2010 6/8/2010

Run Start Time 9:00:00 AM 1:40:00 PM 8:00:00 AM

Run Finish Time 3:53:15 PM 8:12:45 PM 2:30:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 413.25 392.75 390

Nozzle Diameter, inches 0.147 0.147 0.147 0.147

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.005 1.005 1.005 1.005

Barometric Pressure, inches of Mercury 29.33 29.33 29.31 29.323

Average Orifice Meter Differential, inches H2O 0.44 0.39 0.39 0.407

Dry Gas Meter Volume Sampled, cubic feet 148.716 136.595 138.938 141.416

Average Dry Gas Meter Temperature, °F 104.17 85.42 101.00 96.863

Dry Gas Meter Volume Sampled, dscf 137.270 130.400 128.866 132.179

Total Moisture Liquid collected, g 411.7 461.7 464.9 446.100

Volume of Water Vapor, standard cubic feet 19.38 21.73 21.88 20.997

Moisture Content of Stack Gas, % 12.37 14.28 14.51 13.720

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

Dry Mole Fraction 0.8763 0.8572 0.8549 0.863

Carbon Dioxide, % 15.2 15.2 15.4 15.267

Oxygen, % 3.8 3.9 3.8 3.833

Carbon Monoxide & Nitrogen, % 81 80.9 80.8 80.900

Fuel Factor 1.13 1.12 1.11

Dry Molecular Weight, lb/lb-Mole 30.58 30.59 30.62 30.597

Wet Molecular weight, lb/lb-Mole 29.02 28.79 28.79 28.867

Flue Gas Static Pressure, inches of H2O -1 -1 -1 -1.000

Absolute Flue Gas Pressure, inches of Mercury 29.26 29.26 29.24 29.253

Average Stack Gas Temperature, °F 335.92 330.67 335.25 333.947

Average Velocity Head, inches of H2O 1.7857822488

1737

1.751187519

33057

1.744430689

80926

1.760

Average Stack Gas Velocity, feet/second 92.91 92.07 92.19 92.390

Stack Cross-Sectional Area, square feet 242.824 242.824 242.824 242.824

Dry Volumetric Flow Rate, dry scfm 769,547.4 750,921.5 745,054.5 755,174.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,353,646.7 1,341,408.3 1,343,156.7 1,346,070.5

67

Percent Isokinetic of Sampling Rate, % 88.9 91.1 91.4 90.467

Percent Excess Air, % 21.6 22.3 21.7 21.867

F-Factor, dscfm/MMBtu @ %O2 10100 9780 9780 9,886.667

Round Duct Diameter, inches 211 211 211

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10540 10640 10640 10,606.667

Fc 1970 1800 1800 1,856.667

Friday, January 14, 2011 Page 30 of 30