Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

1241 La Cygne 2

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.

Wednesday, February 16, 2011 Page 1 of 36
1241 La Cygne 2

Facility Information:

1241 La Cygne Generating Station

25166 East 2200 Road

La Cygne KS 66040

Contact: Theresa Goin

Phone: (913)757-4451 x5436

Fax:

Email: Theresa.Goin@kcpl.com

Testing Company:

Civil & Environmental Consultants, Inc.

4848 Park 370 Blvd.

Hazelwood MO 63042

Contact: Franklin M. Stevens

Phone: (314)656-4566

Fax: (314)656-4595

Email: fstevens@cecinc.com

Air Permit Number:

1241

Permitted Source ID/Name:

2 Enter the Boiler ID of the tested boiler (left)

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:

KCPL La Cygne Generating Station Unit 2 is designed for firing pulverized coal and is a dry bottom wall-fired 

boiler. Unit 2 has a 685 megawatt average gross load that is fired with 100% sub-bituminous Powder River Basin 

(PRB) coal and uses fuel oil for startup. Unit 2 uses an electrostatic precipitator for particulate control. The 

generating station is located approximately 40 miles south of Kansas City, Kansas.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: Enter ARS ID FRS #: 1241

SCC / Description 10100202 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Bituminous Coal) 

The following state and federal regulations that apply to the proposed testing:

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

Stack Exit 288 0 0 0 4800 2148 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 Formaldehyde Method 0011 3 120 0

Stack Exit 2,3,7,8-TCDD Method 23 3 480 0

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

Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 480 0

Wednesday, February 16, 2011 Page 2 of 36
1241 La Cygne 2

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

Stack Exit 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

Stack Exit OCDD Method 23 3 480 0

Stack Exit 2,3,7,8-TCDF Method 23 3 480 0

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

Stack Exit 2,3,4,7,8-PeCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 480 0

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

Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

Stack Exit OCDF Method 23 3 480 0

Stack Exit Other TCDD Method 23 0

Stack Exit Other PeCDD Method 23 0

Stack Exit Other HxCDD Method 23 0

Stack Exit Other HpCDD Method 23 0

Stack Exit Other TCDF Method 23 0

Stack Exit Other PeCDF Method 23 0

Stack Exit Other HxCDF Method 23 0

Stack Exit Other HpCDF Method 23 0

Stack Exit Total Dioxins Method 23 3 480 0

Stack Exit Total Furans Method 23 3 480 0

Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 480 0

Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Stack Exit Method 23 3 480 0

Stack Exit 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Stack Exit Method 23 3 480 0

Stack Exit Total PCBs Method 23 3 480 0

Stack Exit Total TEQ Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26 3 180 0

Stack Exit Hydrogen Fluoride Method 26 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Organic Condensible 

Particulate

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Wednesday, February 16, 2011 Page 3 of 36
1241 La Cygne 2

The following describes any modifications and/or deviations to the applicable test 

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

of request AND approval, including dates.

None.

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit O2 Method 3A O2 3 180 0

Stack Exit Co2 Method 3A CO2 3 180 0

Stack Exit Co2 Method 3A CO2 3 240 0

Organic Condensible 

Particulate

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Filterable Particulate Method 5 3 240 0

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

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Wednesday, February 16, 2011 Page 4 of 36
1241 La Cygne 2

Sampling / Stack Data Results Summary

Location Stack Exit - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Wednesday, February 16, 2011 Page 5 of 36
1241 La Cygne 2

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 5/20/2010 5/20/2010 5/21/2010

Run Start Time 10:48:00 AM 2:43:00 PM 7:15:00 AM

Run Finish Time 2:11:00 PM 5:59:00 PM 7:15:00 AM

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf 121.642 122.333 119.032 121.002

Moisture Content of Stack Gas, % 13.08 13.22 12.82 13.040

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

Carbon Dioxide, % 14.092 14.162 13.974 14.076

Oxygen, % 5.333 5.326 5.434 5.364

Average Stack Gas Temperature, °F 297.92 299.00 290.92 295.947

Dry Volumetric Flow Rate, dry scfm 1,599,472.2 1,591,733.5 1,563,475.2 1,584,893.63

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,778,935.1 2,787,621.0 2,688,005.0 2,751,520.36

7

Percent Isokinetic of Sampling Rate, %

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Wednesday, February 16, 2011 Page 6 of 36
1241 La Cygne 2

Location Stack Exit - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 3A CO2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Wednesday, February 16, 2011 Page 7 of 36
1241 La Cygne 2

Location Stack Exit - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Wednesday, February 16, 2011 Page 8 of 36
1241 La Cygne 2

Location Stack Exit - Method 3A O2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 3A O2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Wednesday, February 16, 2011 Page 9 of 36
1241 La Cygne 2

Location Stack Exit - Method 6C

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 7E

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

Wednesday, February 16, 2011 Page 10 of 36
1241 La Cygne 2

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Wednesday, February 16, 2011 Page 11 of 36
1241 La Cygne 2

Emissions Summary

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 4.01E-01 2.82E-01 3.78E-01 0.354

ppm 4.20E+02 2.94E+02 3.96E+02 370.000

ppm@7%O2 3.75E+02 2.64E+02 3.54E+02 331.000

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.60E-03 4.79E-04 7.24E-04 0.001

ppm 1.06E+00 3.17E-01 4.82E-01 0.620

ppm@7%O2 9.48E-01 2.84E-01 4.30E-01 0.554

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 2.794 3.461 2.899 3.051

Elb/hr 4.86E+00 5.96E+00 5.04E+00 5.287

lb/mmBtuO2 6.65E-04 8.19E-04 7.10E-04 0.001

mg/dscm 8.11E-01 9.99E-01 8.60E-01 0.890

mg/dscm@7%O2 7.24E-01 8.92E-01 7.73E-01 0.796

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 3.012 2.805 4.135 3.317

Elb/hr 5.24E+00 4.83E+00 7.18E+00 5.750

lb/mmBtuO2 7.17E-04 6.63E-04 1.01E-03 0.001

mg/dscm 8.75E-01 8.10E-01 1.23E+00 0.972

mg/dscm@7%O2 7.81E-01 7.23E-01 1.11E+00 0.871

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 3 1 2

Mass_mg 0.02893 0.00992 0.00086 0.013

Elb/hr 3.71E-02 1.29E-02 1.12E-03 0.017

lb/mmBtuO2 5.26E-06 1.77E-06 1.55E-07 0.000

mg/dscm 6.56E-03 2.17E-03 1.90E-04 0.003

mg/dscm@7%O2 5.73E-03 1.93E-03 1.69E-04 0.003

Compound: Arsenic

Average

RunNumber 3 1 2

Mass_mg 0.00413 0.00507 0.00393 0.004

Elb/hr 5.30E-03 6.60E-03 5.10E-03 0.006

Wednesday, February 16, 2011 Page 12 of 36
1241 La Cygne 2

lb/mmBtuO2 7.51E-07 9.06E-07 7.07E-07 0.000

mg/dscm 9.37E-04 1.11E-03 8.67E-04 0.001

mg/dscm@7%O2 8.19E-04 9.89E-04 7.69E-04 0.001

Compound: Beryllium

Average

RunNumber 3 1 2

Mass_mg 0.00044 0.00028 0.0003 0.000

Elb/hr 5.64E-04 3.64E-04 3.89E-04 0.000

lb/mmBtuO2 8.00E-08 5.00E-08 5.39E-08 0.000

mg/dscm 9.98E-05 6.12E-05 6.62E-05 0.000

mg/dscm@7%O2 8.72E-05 5.45E-05 5.87E-05 0.000

Compound: Cadmium

Average

RunNumber 3 1 2

Mass_mg 0.00053 0.00144 0.00079 0.001

Elb/hr 6.80E-04 1.87E-03 1.02E-03 0.001

lb/mmBtuO2 9.64E-08 2.57E-07 1.42E-07 0.000

mg/dscm 1.20E-04 3.15E-04 1.74E-04 0.000

mg/dscm@7%O2 1.05E-04 2.81E-04 1.54E-04 0.000

Compound: Chromium

Average

RunNumber 3 1 2

Mass_mg 0.01095 0.01179 0.02207 0.015

Elb/hr 1.40E-02 1.53E-02 2.86E-02 0.019

lb/mmBtuO2 1.99E-06 2.11E-06 3.97E-06 0.000

mg/dscm 2.48E-03 2.58E-03 4.87E-03 0.003

mg/dscm@7%O2 2.17E-03 2.30E-03 4.32E-03 0.003

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00343 0.005 0.00109 0.003

Elb/hr 4.46E-03 6.48E-03 1.40E-03 0.004

lb/mmBtuO2 6.13E-07 8.99E-07 1.98E-07 0.000

mg/dscm 7.49E-04 1.10E-03 2.47E-04 0.001

mg/dscm@7%O2 6.67E-04 9.76E-04 2.16E-04 0.001

Compound: Filterable Particulate

Average

RunNumber 2 3 1

Mass_mg 34.1 19.2 32.5 28.600

Elb/hr 4.42E+01 2.46E+01 4.23E+01 37.033

lb/mmBtuO2 6.13E-03 3.49E-03 5.81E-03 0.005

mg/dscm 7.53E+00 4.35E+00 7.10E+00 6.327

mg/dscm@7%O2 6.68E+00 3.80E+00 6.33E+00 5.603

Compound: Lead

Average

RunNumber 3 1 2

Mass_mg 0.01659 0.03299 0.01337 0.021

Elb/hr 2.13E-02 4.29E-02 1.73E-02 0.027

Wednesday, February 16, 2011 Page 13 of 36
1241 La Cygne 2

lb/mmBtuO2 3.02E-06 5.89E-06 2.40E-06 0.000

mg/dscm 3.76E-03 7.21E-03 2.95E-03 0.005

mg/dscm@7%O2 3.29E-03 6.42E-03 2.62E-03 0.004

Compound: Manganese

Average

RunNumber 3 1 2

Mass_mg 0.00991 0.01755 0.01605 0.015

Elb/hr 1.27E-02 2.28E-02 2.08E-02 0.019

lb/mmBtuO2 1.80E-06 3.13E-06 2.89E-06 0.000

mg/dscm 2.25E-03 3.83E-03 3.54E-03 0.003

mg/dscm@7%O2 1.97E-03 3.41E-03 3.14E-03 0.003

Compound: Nickel

Average

RunNumber 3 1 2

Mass_mg 0.01006 0.00978 0.02581 0.015

Elb/hr 1.29E-02 1.27E-02 3.35E-02 0.020

lb/mmBtuO2 1.83E-06 1.75E-06 4.64E-06 0.000

mg/dscm 2.28E-03 2.14E-03 5.70E-03 0.003

mg/dscm@7%O2 1.99E-03 1.91E-03 5.06E-03 0.003

Compound: Selenium

Average

RunNumber 2 3 1

Mass_mg 0.0028 0.0148 0.02337 0.014

Elb/hr 3.63E-03 1.90E-02 3.04E-02 0.018

lb/mmBtuO2 5.03E-07 2.69E-06 4.17E-06 0.000

mg/dscm 6.18E-04 3.36E-03 5.11E-03 0.003

mg/dscm@7%O2 5.48E-04 2.94E-03 4.55E-03 0.003

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 4.97E+03 5.02E+03 4.93E+03 4,973.333

lb/mmBtuO2 6.79E-01 6.90E-01 6.94E-01 0.688

mg/dscm 8.29E+02 8.42E+02 8.41E+02 837.333

mg/dscm@7%O2 7.40E+02 7.51E+02 7.56E+02 749.000

ppm 3.11E+02 3.16E+02 3.16E+02 314.333

ppm@7%O2 2.78E+02 2.82E+02 2.84E+02 281.333

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 2.44E+03 2.46E+03 2.58E+03 2,493.333

lb/mmBtuO2 3.33E-01 3.38E-01 3.63E-01 0.345

mg/dscm 4.07E+02 4.13E+02 4.40E+02 420.000

mg/dscm@7%O2 3.63E+02 3.69E+02 3.95E+02 375.667

ppm 2.13E+02 2.16E+02 2.30E+02 219.667

ppm@7%O2 1.90E+02 1.93E+02 2.07E+02 196.667

Wednesday, February 16, 2011 Page 14 of 36
1241 La Cygne 2

Process Run Data

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 21.2 15 12.9 16.367

lb/mmBtuO2 7.30E-03 5.13E-03 4.29E-03 0.006

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 14.3 12 10 12.100

lb/mmBtuO2 4.92E-03 4.11E-03 3.33E-03 0.004

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 14.6 16 17 15.867

lb/mmBtuO2 5.03E-03 5.48E-03 5.66E-03 0.005

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 4.4 3.9 3.3 3.867

lb/mmBtuO2 1.52E-03 1.33E-03 1.10E-03 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 40.2 34.9 33.2 36.100

lb/mmBtuO2 1.38E-02 1.19E-02 1.10E-02 0.012

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 33.3 31.9 30.3 31.833

lb/mmBtuO2 1.15E-02 1.09E-02 1.01E-02 0.011

Wednesday, February 16, 2011 Page 15 of 36
1241 La Cygne 2

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Firing Rate 392.9daily avg tons/hour Organic HAP Run 

1

0

1 Average Heat Input 6759.8 MMBtu/hr Organic HAP Run 

1

0

1 Steam Output 4288 1000 lb steam/hr Organic HAP Run 

1

0

1 Synfuel Firing Rate 0 0

1 Petroleum Coke Firing Rate 0 0

1 Coal Gas Firing Rate 0 0

1 Fuel Oil Firing Rate 0 0

1 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg 

Moisture 12.8%. 

Organic HAP Run 

1

0

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

1 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

1 Unit Gross Electrical Output 683.5 MW Organic HAP Run 

1

0

1 Unit Net Electric Generation 653.3 MWh Organic HAP Run 

1

0

2 Coal Firing Rate 392.9daily avg tons/hour Organic HAP Run 

2

0

2 Average Heat Input 6759.8 MMBtu/hr Organic HAP Run 

2

0

2 Steam Output 4288 1000 lb steam/hr Organic HAP Run 

2

0

2 Synfuel Firing Rate 0 0

2 Petroleum Coke Firing Rate 0 0

Wednesday, February 16, 2011 Page 16 of 36
1241 La Cygne 2

2 Coal Gas Firing Rate 0 0

2 Fuel Oil Firing Rate 0 0

2 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg 

Moisture 12.8%. 

Organic HAP Run 

2

0

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

2 FGD Scrubber Liquor pH 0 pH 0

2 FGD Scrubber Liquor Flow Rate 0 gal/min 0

2 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

2 Flue Gas Oxygen Content 0 % 0

2 Flue Gas Carbon Dioxide Content 0 % 0

2 Flue Gas Moisture Content 0 % 0

2 Flue Gas Sampling Point Temperature 0 Deg F 0

2 Flue Gas Pressure 0 atm 0

2 Standard Pressure 0 atm 0

2 Standard Temperature 0 Deg F 0

2 Unit Gross Electrical Output 683.5 MW Organic HAP Run 

2

0

2 Unit Net Electric Generation 653.3 MWh Organic HAP Run 

2

0

3 Coal Firing Rate 392.9daily avg tons/hour Organic HAP Run 

3

0

3 Average Heat Input 6759.8 MMBtu/hr Organic HAP Run 

3

0

3 Steam Output 4288 1000 lb steam/hr Organic HAP Run 

3

0

3 Synfuel Firing Rate 0 0

3 Petroleum Coke Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

3 Fuel Oil Firing Rate 0 0

3 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg 

Moisture 12.8%. 

Organic HAP Run 

3

0

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

3 FGD Scrubber Liquor pH 0 pH 0

3 FGD Scrubber Liquor Flow Rate 0 gal/min 0

3 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

Wednesday, February 16, 2011 Page 17 of 36
1241 La Cygne 2

3 Flue Gas Oxygen Content 0 % 0

3 Flue Gas Carbon Dioxide Content 0 % 0

3 Flue Gas Moisture Content 0 % 0

3 Flue Gas Sampling Point Temperature 0 Deg F 0

3 Flue Gas Pressure 0 atm 0

3 Standard Pressure 0 atm 0

3 Standard Temperature 0 Deg F 0

3 Unit Gross Electrical Output 683.5 MW Organic HAP Run 

3

0

3 Unit Net Electric Generation 653.3 MWh Organic HAP Run 

3

0

4 Coal Firing Rate 409.2daily avg tons/hour Acid Gas HAP 

Run 1

0

4 Average Heat Input 6827.9 MMBtu/hr Acid Gas HAP 

Run 1

0

4 Steam Output 4271 1000 lb steam/hr Acid Gas HAP 

Run 1

0

4 Synfuel Firing Rate 0 0

4 Petroleum Coke Firing Rate 0 0

4 Coal Gas Firing Rate 0 0

4 Fuel Oil Firing Rate 0 0

4 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg 

Moisture 12.8%. 

Acid Gas HAP 

Run 1

0

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

4 FGD Scrubber Liquor pH 0 pH 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

4 Flue Gas Oxygen Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

4 Flue Gas Sampling Point Temperature 0 Deg F 0

4 Flue Gas Pressure 0 atm 0

4 Standard Pressure 0 atm 0

4 Standard Temperature 0 Deg F 0

4 Unit Gross Electrical Output 683.5 MW Acid Gas HAP 

Run 1

0

4 Unit Net Electric Generation 653.3 MWh Acid Gas HAP 

Run 1

0

Wednesday, February 16, 2011 Page 18 of 36
1241 La Cygne 2

5 Coal Firing Rate 409.2daily avg tons/hour Acid Gas HAP 

Run 2

0

5 Average Heat Input 6827.9 MMBtu/hr Acid Gas HAP 

Run 2

0

5 Steam Output 4271 1000 lb steam/hr Acid Gas HAP 

Run 2

0

5 Synfuel Firing Rate 0 0

5 Petroleum Coke Firing Rate 0 0

5 Coal Gas Firing Rate 0 0

5 Fuel Oil Firing Rate 0 0

5 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg 

Moisture 12.8%. 

Acid Gas HAP 

Run 2

0

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

5 FGD Scrubber Liquor pH 0 pH 0

5 FGD Scrubber Liquor Flow Rate 0 gal/min 0

5 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

5 Flue Gas Oxygen Content 0 % 0

5 Flue Gas Carbon Dioxide Content 0 % 0

5 Flue Gas Moisture Content 0 % 0

5 Flue Gas Sampling Point Temperature 0 Deg F 0

5 Flue Gas Pressure 0 atm 0

5 Standard Pressure 0 atm 0

5 Standard Temperature 0 Deg F 0

5 Unit Gross Electrical Output 683.5 MW Acid Gas HAP 

Run 2

0

5 Unit Net Electric Generation 653.3 MWh Acid Gas HAP 

Run 2

0

6 Coal Firing Rate 391.4daily avg tons/hour Acid Gas HAP 

Run 3

0

6 Average Heat Input 6772.3 MMBtu/hr Acid Gas HAP 

Run 3

0

6 Steam Output 4329 1000 lb steam/hr Acid Gas HAP 

Run 3

0

6 Synfuel Firing Rate 0 0

6 Petroleum Coke Firing Rate 0 0

6 Coal Gas Firing Rate 0 0

6 Fuel Oil Firing Rate 0 0

Wednesday, February 16, 2011 Page 19 of 36
1241 La Cygne 2

6 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg 

Moisture 12.8%. 

Acid Gas HAP 

Run 3

0

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

6 FGD Scrubber Liquor pH 0 pH 0

6 FGD Scrubber Liquor Flow Rate 0 gal/min 0

6 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

6 Flue Gas Oxygen Content 0 % 0

6 Flue Gas Carbon Dioxide Content 0 % 0

6 Flue Gas Moisture Content 0 % 0

6 Flue Gas Sampling Point Temperature 0 Deg F 0

6 Flue Gas Pressure 0 atm 0

6 Standard Pressure 0 atm 0

6 Standard Temperature 0 Deg F 0

6 Unit Gross Electrical Output 691.1 MW Acid Gas HAP 

Run 3

0

6 Unit Net Electric Generation 661.7 MWh Acid Gas HAP 

Run 3

0

7 Coal Firing Rate 391.4daily avg tons/hour 0 Metals/PM Run 1

7 Average Heat Input 6772.3 MMBtu/hr 0 Metals/PM Run 1

7 Steam Output 4329 1000 lb steam/hr 0 Metals/PM Run 1

7 Synfuel Firing Rate 0 0

7 Petroleum Coke Firing Rate 0 0

7 Coal Gas Firing Rate 0 0

7 Fuel Oil Firing Rate 0 0

7 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg 

Moisture 12.8%. 

Metals/PM Run 1

0

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

7 FGD Scrubber Liquor pH 0 pH 0

7 FGD Scrubber Liquor Flow Rate 0 gal/min 0

7 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

7 Flue Gas Oxygen Content 0 % 0

7 Flue Gas Carbon Dioxide Content 0 % 0

7 Flue Gas Moisture Content 0 % 0

7 Flue Gas Sampling Point Temperature 0 Deg F 0

7 Flue Gas Pressure 0 atm 0

Wednesday, February 16, 2011 Page 20 of 36
1241 La Cygne 2

7 Standard Pressure 0 atm 0

7 Standard Temperature 0 Deg F 0

7 Unit Gross Electrical Output 691.1 MW 0 Metals/PM Run 1

7 Unit Net Electric Generation 661.7 MWh 0 Metals/PM Run 1

8 Coal Firing Rate 391.4daily avg tons/hour 0 Metals/PM Run 2

8 Average Heat Input 6772.3 MMBtu/hr 0 Metals/PM Run 2

8 Steam Output 4329 1000 lb steam/hr 0 Metals/PM Run 2

8 Synfuel Firing Rate 0 0

8 Petroleum Coke Firing Rate 0 0

8 Coal Gas Firing Rate 0 0

8 Fuel Oil Firing Rate 0 0

8 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg 

Moisture 12.8%. 

Metals/PM Run 2

0

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

8 FGD Scrubber Liquor pH 0 pH 0

8 FGD Scrubber Liquor Flow Rate 0 gal/min 0

8 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

8 Flue Gas Oxygen Content 0 % 0

8 Flue Gas Carbon Dioxide Content 0 % 0

8 Flue Gas Moisture Content 0 % 0

8 Flue Gas Sampling Point Temperature 0 Deg F 0

8 Flue Gas Pressure 0 atm 0

8 Standard Pressure 0 atm 0

8 Standard Temperature 0 Deg F 0

8 Unit Gross Electrical Output 691.1 MW 0 Metals/PM Run 2

8 Unit Net Electric Generation 661.7 MWh 0 Metals/PM Run 2

9 Coal Firing Rate 355.9daily avg tons/hour 0 Metals/PM Run 3

9 Average Heat Input 6368.5 MMBtu/hr 0 Metals/PM Run 3

9 Steam Output 4018 1000 lb steam/hr 0 Metals/PM Run 3

9 Synfuel Firing Rate 0 0

9 Petroleum Coke Firing Rate 0 0

9 Coal Gas Firing Rate 0 0

9 Fuel Oil Firing Rate 0 0

9 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg 

Moisture 12.8%. 

Metals/PM Run 3

0

Wednesday, February 16, 2011 Page 21 of 36
1241 La Cygne 2

APCD Run Data

Process Lab Run Data

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

9 FGD Scrubber Liquor pH 0 pH 0

9 FGD Scrubber Liquor Flow Rate 0 gal/min 0

9 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

9 Flue Gas Oxygen Content 0 % 0

9 Flue Gas Carbon Dioxide Content 0 % 0

9 Flue Gas Moisture Content 0 % 0

9 Flue Gas Sampling Point Temperature 0 Deg F 0

9 Flue Gas Pressure 0 atm 0

9 Standard Pressure 0 atm 0

9 Standard Temperature 0 Deg F 0

9 Unit Gross Electrical Output 644.4 MW 0 Metals/PM Run 3

9 Unit Net Electric Generation 613.5 MWh 0 Metals/PM Run 3

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 317.78 Primary Voltage 0

2 ELECTROSTATIC PRECIPITATOR 317.78 Primary Voltage 0

3 ELECTROSTATIC PRECIPITATOR 317.78 Primary Voltage 0

4 ELECTROSTATIC PRECIPITATOR 316.69 Primary Voltage 0

5 ELECTROSTATIC PRECIPITATOR 316.69 Primary Voltage 0

6 ELECTROSTATIC PRECIPITATOR 319.88 Primary Voltage 0

7 ELECTROSTATIC PRECIPITATOR 319.88 Primary Voltage 0

8 ELECTROSTATIC PRECIPITATOR 319.88 Primary Voltage 0

9 ELECTROSTATIC PRECIPITATOR 334.91 Primary Voltage 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value (as received) Btu/lb

1 Fuel Moisture (as received) %

1 Fuel Mercury Content ppm

1 Fuel Cadmium Content ppm

1 Ultimate/Proximate Analysis

1 Fuel Nickel Content ppm

1 Fuel Arsenic Content ppm

1 Fuel Chromium Content ppm

Wednesday, February 16, 2011 Page 22 of 36
1241 La Cygne 2

1 Fuel Beryllium Content ppm

1 Fuel Lead Content ppm

1 Fuel Manganese Content ppm

1 Fuel Chlorine Content ppm

1 Fuel Fluorine Content ppm

1 Proximate - Ash % weight

1 Proximate - Volatile % weight

1 Proximate - Fixed Carbon % weight

1 Ultimate - Carbon % weight

1 Ultimate - Nitrogen % weight

1 Ultimate - Sulfur % weight

1 Ultimate - Oxygen % weight

Wednesday, February 16, 2011 Page 23 of 36
1241 La Cygne 2

Sampling / Stack Data Results Detail

Location Stack Exit - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Wednesday, February 16, 2011 Page 24 of 36
1241 La Cygne 2

Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Wednesday, February 16, 2011 Page 25 of 36
1241 La Cygne 2

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 5/20/2010 5/20/2010 5/21/2010

Run Start Time 10:48:00 AM 2:43:00 PM 7:15:00 AM

Run Finish Time 2:11:00 PM 5:59:00 PM 7:15:00 AM

Net Traversing Points 12 12 12

Net Run Time, minutes

Nozzle Diameter, inches 0.187 0.187 0.187 0.187

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9779 0.9779 0.9779 0.978

Barometric Pressure, inches of Mercury 28.64 28.5 28.59 28.577

Average Orifice Meter Differential, inches H2O 1.78 1.77 1.68 1.743

Dry Gas Meter Volume Sampled, cubic feet 133.740 136.471 130.500 133.570

Average Dry Gas Meter Temperature, °F 85.88 91.17 83.25 86.767

Dry Gas Meter Volume Sampled, dscf 121.642 122.333 119.032 121.002

Total Moisture Liquid collected, g 388.9 396 371.8 385.567

Volume of Water Vapor, standard cubic feet 18.31 18.64 17.50 18.150

Moisture Content of Stack Gas, % 13.08 13.22 12.82 13.040

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

Dry Mole Fraction 0.8692 0.8678 0.8718 0.870

Carbon Dioxide, % 14.092 14.162 13.974 14.076

Oxygen, % 5.333 5.326 5.434 5.364

Carbon Monoxide & Nitrogen, % 80.575 80.512 80.592 80.560

Fuel Factor 1.10 1.10 1.11

Dry Molecular Weight, lb/lb-Mole 30.47 30.48 30.45 30.467

Wet Molecular weight, lb/lb-Mole 28.84 28.83 28.85 28.840

Flue Gas Static Pressure, inches of H2O -2.7 -2.7 -2.7 -2.700

Absolute Flue Gas Pressure, inches of Mercury 28.44 28.30 28.39 28.377

Average Stack Gas Temperature, °F 297.92 299.00 290.92 295.947

Average Velocity Head, inches of H2O 2.1994314876

6317

2.198468950

6087

2.074179278

13561

2.157

Average Stack Gas Velocity, feet/second 102.38 102.70 99.03 101.370

Stack Cross-Sectional Area, square feet 452.389 452.389 452.389 452.389

Dry Volumetric Flow Rate, dry scfm 1,599,472.2 1,591,733.5 1,563,475.2 1,584,893.6

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,778,935.1 2,787,621.0 2,688,005.0 2,751,520.3

67

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, % 33.5 33.4 34.3 33.733

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

Round Duct Diameter, inches 288 288 288

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

Wednesday, February 16, 2011 Page 26 of 36
1241 La Cygne 2

Location Stack Exit - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Wednesday, February 16, 2011 Page 27 of 36
1241 La Cygne 2

Location Stack Exit - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Wednesday, February 16, 2011 Page 28 of 36
1241 La Cygne 2

Location Stack Exit - Method 3A CO2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Wednesday, February 16, 2011 Page 29 of 36
1241 La Cygne 2

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

Wednesday, February 16, 2011 Page 30 of 36
1241 La Cygne 2

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

Wednesday, February 16, 2011 Page 31 of 36
1241 La Cygne 2

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

Wednesday, February 16, 2011 Page 32 of 36
1241 La Cygne 2

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

Wednesday, February 16, 2011 Page 33 of 36
1241 La Cygne 2

Location Stack Exit - Method 6C

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

Wednesday, February 16, 2011 Page 34 of 36
1241 La Cygne 2

Location Stack Exit - Method 7E

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

Wednesday, February 16, 2011 Page 35 of 36
1241 La Cygne 2

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Wednesday, February 16, 2011 Page 36 of 36