Name: Shawn Glacken

Title: Senior VP, Environmental Services

Company: Luminant

Sign Date: 9/2/2010

Name: Mike Hutcherson

Title: Project Manager

Company: METCO Environmental

Sign Date: 8/5/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Luminant Power Monticello Mt. Pleasant, TX

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.

Thursday, January 20, 2011 Page 1 of 33
Luminant Power Monticello Mt. Pleasant, TX

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Facility Information:

Monticello Steam Electric Station

1574 Monticello Plant Road

Mt. Pleasant TX 75455

Contact: Craig Birkenfeld

Phone: 214-875-8326

Fax: 214-875-8333

Email: craigbirkenfeld@luminant.com

Testing Company:

METCO Environmental

P.O. Box 598

Addison TX 75001

Contact:Mike Hutcherson-Project Manager

Phone: 972-931-7127

Fax: 972-931-8398

Email: mhutcherson@metcoenv.com

Air Permit Number:

6147

Permitted Source ID/Name:

B2 Unit Number 2 Boiler

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate: Target Process Test Rate

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

Tangential-fired boiler with low-NOx burners and overfire air burning a blend of low-sulfur subbituminous coal and 

lignite. SNCR with urea for NOx control, followed by Activated Carbon Injection for mercury control, then ESPs in 

parallel with Baghouses for PM control.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 4844900003 FRS #: 110000598835

SCC / Description 10100222 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Subbituminous 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

Unit #2 Stack 

(EPN S2)

272.25 0 0 0 1633 2615 4 3

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Carbon Monoxide Method 10 3 120 0 Apx time; the actual 

time varied from run 

to run.

Unit #2 Stack 

(EPN S2)

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

(EPN S2)

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

(EPN S2)

Thursday, January 20, 2011 Page 2 of 33
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Unit #2 Stack 1,2,3,4,7,8-HxCDD Method 23 3 480 0

(EPN S2)

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

(EPN S2)

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

(EPN S2)

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

(EPN S2)

Unit #2 Stack OCDD Method 23 3 480 0

(EPN S2)

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

(EPN S2)

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

(EPN S2)

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

(EPN S2)

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

(EPN S2)

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

(EPN S2)

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

(EPN S2)

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

(EPN S2)

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

(EPN S2)

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

(EPN S2)

Unit #2 Stack OCDF Method 23 3 480 0

(EPN S2)

Unit #2 Stack 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

(EPN S2)

Unit #2 Stack 3,4,4',5-TCB (PCB81) Method 23 3 480 0

(EPN S2)

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

(EPN S2)

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

(EPN S2)

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

(EPN S2)

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

(EPN S2)

Unit #2 Stack 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

(EPN S2)

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

HxCB (PCBs156/157)

Unit #2 Stack Method 23 3 480 0

(EPN S2)

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

(EPN S2)

Unit #2 Stack 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

(EPN S2)

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

(PCB189)

Unit #2 Stack Method 23 3 480 0

(EPN S2)

Unit #2 Stack Total PCBs Method 23 3 480 0

(EPN S2)

Thursday, January 20, 2011 Page 3 of 33
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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.

See attached report.

Total organic compounds 

(TOC) as Propane

Method 25A 3 120 0 Apx time; the actual 

time varied from run 

to run.

Unit #2 Stack 

(EPN S2)

Unit #2 Stack Hydrogen Fluoride Method 26A 3 180 0

(EPN S2)

Unit #2 Stack Hydrogen Chloride Method 26A 3 180 0

(EPN S2)

Filterable PM2.5 OTM - 27/28 3 360 0 Apx time; the actual 

time varied from run 

to run.

Unit #2 Stack 

(EPN S2)

Unit #2 Stack Total PM2.5 OTM - 27/28 3 360 0

(EPN S2)

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 360 0 Apx time; the actual 

time varied from run 

to run.

Unit #2 Stack 

(EPN S2)

Unit #2 Stack Filterable Particulate OTM - 27/28 3 360 0

(EPN S2)

Organic Condensible 

Particulate

OTM - 27/28 3 360 0 Apx time; the actual 

time varied from run 

to run.

Unit #2 Stack 

(EPN S2)

Unit #2 Stack Total Particulate OTM - 27/28 3 360 0

(EPN S2)

Unit #2 Stack Cobalt Method 29 3 240 0

(EPN S2)

Unit #2 Stack Phosphorus (yellow or white) Method 29 3 240 0

(EPN S2)

Unit #2 Stack Lead Method 29 3 240 0

(EPN S2)

Unit #2 Stack Cadmium Method 29 3 240 0

(EPN S2)

Unit #2 Stack Chromium Method 29 3 240 0

(EPN S2)

Unit #2 Stack Arsenic Method 29 3 240 0

(EPN S2)

Unit #2 Stack Antimony Method 29 3 240 0

(EPN S2)

Unit #2 Stack Manganese Method 29 3 240 0

(EPN S2)

Unit #2 Stack Nickel Method 29 3 240 0

(EPN S2)

Unit #2 Stack Selenium Method 29 3 240 0

(EPN S2)

Unit #2 Stack Beryllium Method 29 3 240 0

(EPN S2)

Filterable Particulate Method 5 3 240 0 This was from the FH 

of the M29 train.

Unit #2 Stack 

(EPN S2)

Unit #2 Stack Sulfur Dioxide Method 6C 3 240 0

(EPN S2)

Unit #2 Stack Nitrogen oxides (NOx) Method 7E 3 240 0

(EPN S2)

Thursday, January 20, 2011 Page 4 of 33
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Thursday, January 20, 2011 Page 5 of 33
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Thursday, January 20, 2011 Page 6 of 33
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Sampling / Stack Data Results Summary

Location Unit #2 Stack (EPN S2) - Method 10

Average

Run Number 1 2 3

Test Date 4/28/2010 4/29/2010 4/29/2010

Run Start Time 8:10:00 AM 12:21:00 

AM

5:10:00 PM

Run Finish Time 10:33:00 AM 2:41:00 

AM

7:26:00 PM

Carbon Dioxide, % 13.66 13.28 13.48 13.473

Oxygen, % 6.18 6.34 6.22 6.247

Dry Volumetric Flow Rate, dry scfm 1337930 1330471 1299355 1,322,585.33

3

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Moisture, % 11.36 11.76 11.8 11.640

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 1910 0 0 636.667

Location Unit #2 Stack (EPN S2) - Method 23

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 9:35:00 AM 11:50:00 

AM

2:15:00 AM

Run Finish Time 6:00:00 PM 11:20:00 

PM

10:40:00 AM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 304.776 301.915 307.620 304.770

Moisture Content of Stack Gas, % 11.34 11.74 11.77 11.617

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

Carbon Dioxide, % 13.7 13.3 13.5 13.500

Oxygen, % 6.2 6.3 6.2 6.233

Average Stack Gas Temperature, °F 372.23 376.23 375.10 374.520

Dry Volumetric Flow Rate, dry scfm 1,334,730.5 1,326,532.9 1,295,744.1 1,319,002.50

0

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,425,572.0 2,441,580.8 2,396,465.1 2,421,205.96

7

Percent Isokinetic of Sampling Rate, % 92.7 94.4 98.4 95.167

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, January 20, 2011 Page 7 of 33
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Location Unit #2 Stack (EPN S2) - Method 25A

Average

Run Number 1 2 3

Test Date 4/28/2010 4/29/2010 4/29/2010

Run Start Time 8:10:00 AM 12:21:00 

AM

5:10:00 PM

Run Finish Time 10:33:00 AM 2:41:00 

AM

7:26:00 PM

Carbon Dioxide, % 13.66 13.28 13.48 13.473

Oxygen, % 6.18 6.34 6.22 6.247

Dry Volumetric Flow Rate, dry scfm 1337930 1330471 1299355 1,322,585.33

3

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Moisture, % 11.36 11.76 11.8 11.640

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit #2 Stack (EPN S2) - Method 26A

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 7:01:00 PM 5:09:00 PM 1:17:00 PM

Run Finish Time 10:32:00 PM 8:31:00 PM 4:47:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 113.575 113.798 109.888 112.420

Moisture Content of Stack Gas, % 14.14 11.98 14.06 13.393

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

Carbon Dioxide, % 13.7 13.3 13.5 13.500

Oxygen, % 6.2 6.3 6.2 6.233

Average Stack Gas Temperature, °F 383.42 390.53 394.42 389.457

Dry Volumetric Flow Rate, dry scfm 1,262,272.2 1,314,252.5 1,230,596.9 1,269,040.53

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,403,014.2 2,475,538.8 2,396,465.1 2,425,006.03

3

Percent Isokinetic of Sampling Rate, % 99.5 95.7 98.7 97.967

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, January 20, 2011 Page 8 of 33
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Location Unit #2 Stack (EPN S2) - Method 29

Average

Run Number 1 2 3

Test Date 4/28/2010 4/28/2010 4/29/2010

Run Start Time 1:40:00 AM 12:17:00 

AM

11:27:00 AM

Run Finish Time 6:07:00 AM 11:55:00 

PM

4:20:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 156.875 144.910 149.350 150.378

Moisture Content of Stack Gas, % 10.36 12.42 12.62 11.800

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

Carbon Dioxide, % 13.7 13.3 13.5 13.500

Oxygen, % 6.2 6.3 6.2 6.233

Average Stack Gas Temperature, °F 384.67 375.81 377.58 379.353

Dry Volumetric Flow Rate, dry scfm 1,302,571.8 1,275,903.5 1,287,597.6 1,288,690.96

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,377,060.6 2,374,392.4 2,415,869.7 2,389,107.56

7

Percent Isokinetic of Sampling Rate, % 99.9 94.2 96.2 96.767

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Fw

Fc

Thursday, January 20, 2011 Page 9 of 33
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Location Unit #2 Stack (EPN S2) - Method 5

Average

Run Number 1 2 3

Test Date 4/28/2010 4/28/2010 4/29/2010

Run Start Time 1:40:00 AM 12:17:00 

AM

11:27:00 AM

Run Finish Time 6:07:00 AM 11:55:00 

PM

4:20:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 156.875 144.910 149.350 150.378

Moisture Content of Stack Gas, % 10.36 12.42 12.62 11.800

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

Carbon Dioxide, % 13.7 13.3 13.5 13.500

Oxygen, % 6.2 6.3 6.2 6.233

Average Stack Gas Temperature, °F 384.67 375.81 377.58 379.353

Dry Volumetric Flow Rate, dry scfm 1,302,571.8 1,275,903.5 1,287,597.6 1,288,690.96

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,377,060.6 2,374,392.4 2,415,869.7 2,389,107.56

7

Percent Isokinetic of Sampling Rate, % 99.9 94.2 96.2 96.767

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit #2 Stack (EPN S2) - Method 6C

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 9:35:00 AM 10:56:00 

AM

3:17:00 AM

Run Finish Time 1:35:00 PM 2:56:00 PM 7:17:00 AM

Carbon Dioxide, % 13.66 13.28 13.48 13.473

Oxygen, % 6.18 6.34 6.22 6.247

Dry Volumetric Flow Rate, dry scfm 1337930 1330471 1299355 1,322,585.33

3

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Moisture, % 11.36 11.76 11.8 11.640

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 1910 0 0 636.667

Thursday, January 20, 2011 Page 10 of 33
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Location Unit #2 Stack (EPN S2) - Method 7E

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 9:35:00 AM 10:56:00 

AM

3:17:00 AM

Run Finish Time 1:35:00 PM 2:56:00 PM 7:17:00 AM

Carbon Dioxide, % 13.66 13.28 13.48 13.473

Oxygen, % 6.18 6.34 6.22 6.247

Dry Volumetric Flow Rate, dry scfm 1337930 1330471 1299355 1,322,585.33

3

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Moisture, % 11.36 11.76 11.8 11.640

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit #2 Stack (EPN S2) - OTM - 27/28

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 9:35:00 AM 8:39:00 

AM

5:05:00 AM

Run Finish Time 4:42:45 PM 3:37:15 PM 11:47:00 AM

Net Run Time, minutes 427.75 418.25 402

Dry Gas Meter Volume Sampled, dscf 141.541 139.933 135.114 138.863

Moisture Content of Stack Gas, % 10.21 11.53 11.57 11.103

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

Carbon Dioxide, % 13.7 13.3 13.5 13.500

Oxygen, % 6.2 6.3 6.2 6.233

Average Stack Gas Temperature, °F 391.28 391.57 389.44 390.763

Dry Volumetric Flow Rate, dry scfm 1,349,640.5 1,314,378.0 1,283,108.5 1,315,709.00

0

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,477,236.7 2,449,342.6 2,410,048.3 2,445,542.53

3

Percent Isokinetic of Sampling Rate, % 99.7 103.5 106.5 103.233

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, January 20, 2011 Page 11 of 33
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Emissions Summary

Location: Unit #2 Stack (EPN S2) - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 6.46E-01 6.67E-01 6.59E-01 0.657

ppm 6.53E+02 6.66E+02 6.64E+02 661.000

ppm@7%O2 6.17E+02 6.36E+02 6.29E+02 627.333

Location: Unit #2 Stack (EPN S2) - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000041 0.0000000026 0.0000000059 0.000

lb/mmBtuO2 4.04E-13 2.61E-13 5.77E-13 0.000

ng/dscm 4.75E-04 3.04E-04 6.77E-04 0.000

ng/dscm@7%O2 4.49E-04 2.89E-04 6.40E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000011 0.0000000024 0.000000004 0.000

lb/mmBtuO2 1.08E-12 2.41E-13 3.91E-13 0.000

ng/dscm 1.27E-03 2.81E-04 4.59E-04 0.001

ng/dscm@7%O2 1.20E-03 2.68E-04 4.34E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000043 0.0000000027 0.0000000052 0.000

lb/mmBtuO2 4.24E-13 2.71E-13 5.08E-13 0.000

ng/dscm 4.98E-04 3.16E-04 5.97E-04 0.000

ng/dscm@7%O2 4.71E-04 3.01E-04 5.65E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000037 0.0000000021 0.0000000042 0.000

lb/mmBtuO2 3.65E-13 2.11E-13 4.10E-13 0.000

ng/dscm 4.29E-04 2.46E-04 4.82E-04 0.000

ng/dscm@7%O2 4.06E-04 2.34E-04 4.56E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000089 0.0000000018 0.0000000028 0.000

lb/mmBtuO2 8.78E-13 1.80E-13 2.74E-13 0.000

ng/dscm 1.03E-03 2.11E-04 3.21E-04 0.001

ng/dscm@7%O2 9.74E-04 2.01E-04 3.04E-04 0.000

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

Average

Thursday, January 20, 2011 Page 12 of 33
Luminant Power Monticello Mt. Pleasant, TX

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RunNumber 1 2 3

Mass_mg 0.0000000036 0.000000002 0.0000000041 0.000

lb/mmBtuO2 3.55E-13 2.00E-13 4.01E-13 0.000

ng/dscm 4.17E-04 2.34E-04 4.71E-04 0.000

ng/dscm@7%O2 3.94E-04 2.23E-04 4.45E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000047 0.0000000016 0.0000000025 0.000

lb/mmBtuO2 4.64E-13 1.60E-13 2.44E-13 0.000

ng/dscm 5.45E-04 1.87E-04 2.87E-04 0.000

ng/dscm@7%O2 5.15E-04 1.78E-04 2.71E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000036 0.0000000021 0.0000000042 0.000

lb/mmBtuO2 3.55E-13 2.11E-13 4.10E-13 0.000

ng/dscm 4.17E-04 2.46E-04 4.82E-04 0.000

ng/dscm@7%O2 3.94E-04 2.34E-04 4.56E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000025 0.0000000019 0.000000003 0.000

lb/mmBtuO2 2.47E-13 1.90E-13 2.93E-13 0.000

ng/dscm 2.90E-04 2.22E-04 3.44E-04 0.000

ng/dscm@7%O2 2.74E-04 2.11E-04 3.25E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000044 0.0000000028 0.0000000053 0.000

lb/mmBtuO2 4.34E-13 2.81E-13 5.18E-13 0.000

ng/dscm 5.10E-04 3.28E-04 6.09E-04 0.000

ng/dscm@7%O2 4.82E-04 3.12E-04 5.76E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000057 0.0000000027 0.0000000044 0.000

lb/mmBtuO2 5.62E-13 2.71E-13 4.30E-13 0.000

ng/dscm 6.61E-04 3.16E-04 5.05E-04 0.000

ng/dscm@7%O2 6.25E-04 3.01E-04 4.78E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000164 0.0000000136 0.0000000124 0.000

lb/mmBtuO2 1.62E-12 1.36E-12 1.21E-12 0.000

ng/dscm 1.90E-03 1.59E-03 1.42E-03 0.002

ng/dscm@7%O2 1.80E-03 1.51E-03 1.34E-03 0.002

Thursday, January 20, 2011 Page 13 of 33
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Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 1 2 3

Mass_mg 0.0000000564 0.0000000436 0.0000000428 0.000

lb/mmBtuO2 5.56E-12 4.37E-12 4.18E-12 0.000

ng/dscm 6.54E-03 5.10E-03 4.91E-03 0.006

ng/dscm@7%O2 6.18E-03 4.86E-03 4.64E-03 0.005

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000679 0.0000000217 0.0000000137 0.000

lb/mmBtuO2 6.70E-12 2.18E-12 1.34E-12 0.000

ng/dscm 7.87E-03 2.54E-03 1.57E-03 0.004

ng/dscm@7%O2 7.44E-03 2.42E-03 1.48E-03 0.004

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000159 0.000000012 0.000000012 0.000

lb/mmBtuO2 1.57E-12 1.20E-12 1.17E-12 0.000

ng/dscm 1.84E-03 1.40E-03 1.38E-03 0.002

ng/dscm@7%O2 1.74E-03 1.33E-03 1.30E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000208 0.0000000137 0.000000013 0.000

lb/mmBtuO2 2.05E-12 1.37E-12 1.27E-12 0.000

ng/dscm 2.41E-03 1.60E-03 1.49E-03 0.002

ng/dscm@7%O2 2.28E-03 1.52E-03 1.41E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000002118 0.0000000567 0.0000000438 0.000

lb/mmBtuO2 2.09E-11 5.68E-12 4.28E-12 0.000

ng/dscm 2.45E-02 6.63E-03 5.03E-03 0.012

ng/dscm@7%O2 2.32E-02 6.31E-03 4.76E-03 0.011

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

Average

RunNumber 1 2 3

Mass_mg 0.000000023 0.0000000151 0.0000000142 0.000

lb/mmBtuO2 2.27E-12 1.51E-12 1.39E-12 0.000

ng/dscm 2.67E-03 1.77E-03 1.63E-03 0.002

ng/dscm@7%O2 2.52E-03 1.69E-03 1.54E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.000000004 0.0000000017 0.0000000026 0.000

lb/mmBtuO2 3.95E-13 1.70E-13 2.54E-13 0.000

Thursday, January 20, 2011 Page 14 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

ng/dscm 4.64E-04 1.99E-04 2.99E-04 0.000

ng/dscm@7%O2 4.39E-04 1.89E-04 2.83E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.000000013 0.0000000028 0.0000000045 0.000

lb/mmBtuO2 1.28E-12 2.81E-13 4.40E-13 0.000

ng/dscm 1.51E-03 3.28E-04 5.17E-04 0.001

ng/dscm@7%O2 1.43E-03 3.12E-04 4.89E-04 0.001

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000072 0.0000000052 0.000000009 0.000

lb/mmBtuO2 7.10E-13 5.21E-13 8.79E-13 0.000

ng/dscm 8.34E-04 6.08E-04 1.03E-03 0.001

ng/dscm@7%O2 7.89E-04 5.79E-04 9.74E-04 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.000000015 0.0000000046 0.0000000057 0.000

lb/mmBtuO2 1.48E-12 4.61E-13 5.57E-13 0.000

ng/dscm 1.74E-03 5.38E-04 6.54E-04 0.001

ng/dscm@7%O2 1.65E-03 5.12E-04 6.18E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000162 0.0000000129 0.0000000123 0.000

lb/mmBtuO2 1.60E-12 1.29E-12 1.20E-12 0.000

ng/dscm 1.88E-03 1.51E-03 1.41E-03 0.002

ng/dscm@7%O2 1.78E-03 1.44E-03 1.33E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000219 0.0000000151 0.0000000141 0.000

lb/mmBtuO2 2.16E-12 1.51E-12 1.38E-12 0.000

ng/dscm 2.54E-03 1.77E-03 1.62E-03 0.002

ng/dscm@7%O2 2.40E-03 1.69E-03 1.53E-03 0.002

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000669 0.0000000156 0.0000000145 0.000

lb/mmBtuO2 6.60E-12 1.56E-12 1.42E-12 0.000

ng/dscm 7.75E-03 1.82E-03 1.66E-03 0.004

ng/dscm@7%O2 7.33E-03 1.73E-03 1.57E-03 0.004

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

Average

RunNumber 1 2 3

Thursday, January 20, 2011 Page 15 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Mass_mg 0.0000000211 0.0000000151 0.0000000145 0.000

lb/mmBtuO2 2.08E-12 1.51E-12 1.42E-12 0.000

ng/dscm 2.45E-03 1.77E-03 1.66E-03 0.002

ng/dscm@7%O2 2.32E-03 1.69E-03 1.57E-03 0.002

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000015 0.00000001 0.000000027 0.000

lb/mmBtuO2 1.48E-12 1.00E-12 2.64E-12 0.000

ng/dscm 1.74E-03 1.17E-03 3.10E-03 0.002

ng/dscm@7%O2 1.65E-03 1.11E-03 2.93E-03 0.002

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000085 0.0000000048 0.0000000071 0.000

lb/mmBtuO2 8.38E-13 4.81E-13 6.94E-13 0.000

ng/dscm 9.85E-04 5.62E-04 8.15E-04 0.001

ng/dscm@7%O2 9.31E-04 5.35E-04 7.71E-04 0.001

Compound: Total PCBs

Average

RunNumber 1 2 3

Mass_mg 0.0000005383 0.0000002351 0.0000002073 0.000

lb/mmBtuO2 5.31E-11 2.36E-11 2.03E-11 0.000

ng/dscm 6.24E-02 2.75E-02 2.38E-02 0.038

ng/dscm@7%O2 5.90E-02 2.62E-02 2.25E-02 0.036

Location: Unit #2 Stack (EPN S2) - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.65E-03 7.50E-04 1.59E-03 0.001

ppm 1.06E+00 4.76E-01 1.02E+00 0.852

ppm@7%O2 1.00E+00 4.54E-01 9.66E-01 0.807

Location: Unit #2 Stack (EPN S2) - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 1.883 2.852 3.618 2.784

lb/mmBtuO2 4.98E-04 7.59E-04 9.90E-04 0.001

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 8.401 9.442 11.529 9.791

lb/mmBtuO2 2.22E-03 2.51E-03 3.15E-03 0.003

Location: Unit #2 Stack (EPN S2) - Method 29

Thursday, January 20, 2011 Page 16 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.0082 0.0074 0.00616 0.007

lb/mmBtuO2 1.57E-06 1.55E-06 1.24E-06 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00804 0.00884 0.01574 0.011

lb/mmBtuO2 1.54E-06 1.85E-06 3.17E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00129 0.00132 0.002 0.002

lb/mmBtuO2 2.47E-07 2.76E-07 4.03E-07 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.0015 0.0015 0.00109 0.001

lb/mmBtuO2 2.87E-07 3.13E-07 2.19E-07 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.03455 0.02105 0.45745 0.171

lb/mmBtuO2 6.62E-06 4.40E-06 9.21E-05 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.0076 0.0072 0.013 0.009

lb/mmBtuO2 1.46E-06 1.50E-06 2.62E-06 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.014 0.0153 0.0274 0.019

lb/mmBtuO2 2.68E-06 3.20E-06 5.51E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.1099 0.0846 0.136 0.110

lb/mmBtuO2 2.11E-05 1.77E-05 2.74E-05 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.02802 0.01114 0.17854 0.073

lb/mmBtuO2 5.37E-06 2.33E-06 3.59E-05 0.000

Thursday, January 20, 2011 Page 17 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Mass_mg 1.14101 1.24035 1.82168 1.401

lb/mmBtuO2 2.19E-04 2.59E-04 3.67E-04 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.2832 0.3986 0.4596 0.380

lb/mmBtuO2 5.43E-05 8.33E-05 9.25E-05 0.000

Location: Unit #2 Stack (EPN S2) - Method 5

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 187.6 139.1 353 226.567

gr/dscf 1.85E-02 1.48E-02 3.65E-02 0.023

gr/dscf@7%O2 1.75E-02 1.41E-02 3.45E-02 0.022

lb/mmBtuO2 3.59E-02 2.91E-02 7.10E-02 0.045

Location: Unit #2 Stack (EPN S2) - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 8.89E-01 7.65E-01 7.95E-01 0.816

ppm 3.92E+02 3.34E+02 3.50E+02 358.667

ppm@7%O2 3.70E+02 3.19E+02 3.31E+02 340.000

Location: Unit #2 Stack (EPN S2) - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 1.40E-01 1.21E-01 1.14E-01 0.125

ppm 8.60E+01 7.37E+01 6.98E+01 76.500

ppm@7%O2 8.12E+01 7.04E+01 6.61E+01 72.567

Location: Unit #2 Stack (EPN S2) - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 187.6 139.1 353 226.567

lb/mmBtuO2 3.98E-02 3.01E-02 7.85E-02 0.049

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 566.6 69.9 104.1 246.867

lb/mmBtuO2 1.20E-01 1.51E-02 2.32E-02 0.053

Thursday, January 20, 2011 Page 18 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Process Run Data

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 61 285.1 71 139.033

lb/mmBtuO2 1.30E-02 6.17E-02 1.58E-02 0.030

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 11 5.6 10.1 8.900

lb/mmBtuO2 2.34E-03 1.21E-03 2.25E-03 0.002

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 259.6 429.8 434.1 374.500

lb/mmBtuO2 5.51E-02 9.30E-02 9.66E-02 0.082

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 638.6 360.6 185.2 394.800

lb/mmBtuO2 1.36E-01 7.80E-02 4.12E-02 0.085

Thursday, January 20, 2011 Page 19 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Feed Rate 6.14 tons/min The set of tests 

began at 1035 on 

04/27/10 and was 

completed at 1115 

on 04/28/10. This 

is the average for 

that time period.

1 Heat Input 5590 MMBtu/hr The set of tests 

began at 1035 on 

04/27/10 and was 

completed at 1115 

on 04/28/10. This 

is the average for 

that time period.

1 Steam Output 81.7 KPPH The set of tests 

began at 1035 on 

04/27/10 and was 

completed at 1115 

on 04/28/10. This 

is the average for 

that time period.

2 Coal Feed Rate 6.13 tons/min The set of tests 

began at 0939 on 

04/28/10 and was 

completed at 0300 

on 04/29/10. This 

is the average for 

that time period.

2 Heat Input 5570 MMBtu/hr The set of tests 

began at 0939 on 

04/28/10 and was 

completed at 0300 

on 04/29/10. This 

is the average for 

that time period.

2 Steam Output 81.7 KPPH The set of tests 

began at 0939 on 

04/28/10 and was 

completed at 0300 

on 04/29/10. This 

is the average for 

that time period.

Thursday, January 20, 2011 Page 20 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

APCD Run Data

3 Coal Feed Rate 6.09 tons/min The set of tests 

began at 0605 on 

04/29/10 and was 

completed at 2039 

on 04/29/10. This 

is the average for 

that time period.

3 Heat Input 5555 MMBtu/hr The set of tests 

began at 0605 on 

04/29/10 and was 

completed at 2039 

on 04/29/10. This 

is the average for 

that time period.

3 Steam Output 81.9 KPPH The set of tests 

began at 0605 on 

04/29/10 and was 

completed at 2039 

on 04/29/10. This 

is the average for 

that time period.

Run Name Value UOM Comments

Target

Value

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

40.5 PPH

2 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

45.7 PPH

3 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

53.7 PPH

1 ACTIVATED CARBON ADSORPTION 120 PPH

2 ACTIVATED CARBON ADSORPTION 101 PPH

3 ACTIVATED CARBON ADSORPTION 106 PPH

1 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-1 INLET FIELD

5.6 kVA

2 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-1 INLET FIELD

5.3 kVA

3 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-1 INLET FIELD

5.7 kVA

1 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-1 MIDDLE FIELD

30.3 kVA

2 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-1 MIDDLE FIELD

30.5 kVA

3 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-1 MIDDLE FIELD

32 kVA

1 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-1 OUTLET FIELD

37 kVA

Thursday, January 20, 2011 Page 21 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

2 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-1 OUTLET FIELD

35.6 kVA

3 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-1 OUTLET FIELD

38.9 kVA

1 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-2 INLET FIELD

21.1 kVA

2 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-2 INLET FIELD

18.7 kVA

3 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-2 INLET FIELD

18.4 kVA

1 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-2 MIDDLE FIELD

40.9 kVA

2 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-2 MIDDLE FIELD

34.9 kVA

3 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-2 MIDDLE FIELD

34.3 kVA

1 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-2 OUTLET FIELD

59.4 kVA

2 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-2 OUTLET FIELD

57.7 kVA

3 ELECTROSTATIC PRECIPITATOR SOUTH 

SIDE A BOX A-2 OUTLET FIELD

58.2 kVA

1 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-3 INLET FIELD

32.4 kVA

2 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-3 INLET FIELD

26.7 kVA

3 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-3 INLET FIELD

25.8 kVA

1 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-3 MIDDLE FIELD

61.2 kVA

2 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-3 MIDDLE FIELD

54.8 kVA

3 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-3 MIDDLE FIELD

54.1 kVA

1 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-3 OUTLET FIELD

58.7 kVA

2 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-3 OUTLET FIELD

58.4 kVA

3 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-3 OUTLET FIELD

58.4 kVA

1 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-4 INLET FIELD

15.1 kVA

2 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-4 INLET FIELD

12.9 kVA

3 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-4 INLET FIELD

13.1 kVA

Thursday, January 20, 2011 Page 22 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Process Lab Run Data

1 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-4 MIDDLE FIELD

54.6 kVA

2 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-4 MIDDLE FIELD

50.6 kVA

3 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-4 MIDDLE FIELD

53.8 kVA

1 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-4 OUTLET FIELD

40.6 kVA

2 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-4 OUTLET FIELD

38.5 kVA

3 ELECTROSTATIC PRECIPITATOR NORTH 

SIDE B BOX B-4 OUTLET FIELD

43.9 kVA

1 BAGHOUSE A PRESSURE DROP 9 "H2O

2 BAGHOUSE A PRESSURE DROP 9 "H2O

3 BAGHOUSE A PRESSURE DROP 8.8 "H2O

1 BAGHOUSE B PRESSURE DROP 9 "H2O

2 BAGHOUSE B PRESSURE DROP 9 "H2O

3 BAGHOUSE B PRESSURE DROP 8.8 "H2O

Run Name Value UOM Comments

1 Fuel (Coal) Heating Value 7875 Btu/lb (wet)

1 Fuel Moisture 31.24 %

1 Fuel Ash Content 7.44 % wet

1 Volatile Matter 29.64 % wet

1 Fixed Carbon 31.68 % wet

1 Carbon 45.17 % wet

1 Sulfur 0.32 %wet

1 Hydrogen 3.16 %wet

1 Nitrogen 0.64 %wet

1 Oxygen 12.03 %wet

1 Antimony 2 dry ug/g

1 Arsenic 2 dry ug/g

1 Beryllium 0.4 dry ug/g

1 Cadmium 0.4 dry ug/g

1 Chromium 9 dry ug/g

1 Cobalt 2 dry ug/g

1 Lead 4 dry ug/g

1 Manganese 27 dry ug/g

1 Nickel 6 dry ug/g

1 Mercury 0.11 dry ug/g

1 Selenium 2 dry ug/g

Thursday, January 20, 2011 Page 23 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

1 Total Chlorine 14 dry ug/g

1 Total Fluorine 59 dry ug/g

2 Fuel (Coal) Heating Value 7622 Btu/lb (wet)

2 Fuel Moisture 31.33 %

2 Fuel Ash Content 9.53 % wet

2 Volatile Matter 29.16 % wet

2 Fixed Carbon 29.98 % wet

2 Carbon 43.55 % wet

2 Sulfur 0.39 %wet

2 Hydrogen 3.15 %wet

2 Nitrogen 0.67 %wet

2 Oxygen 11.39 %wet

2 Antimony 2 dry ug/g

2 Arsenic 2 dry ug/g

2 Beryllium 0.6 dry ug/g

2 Cadmium 0.4 dry ug/g

2 Chromium 11 dry ug/g

2 Cobalt 2 dry ug/g

2 Lead 5 dry ug/g

2 Manganese 47 dry ug/g

2 Nickel 7 dry ug/g

2 Mercury 0.16 dry ug/g

2 Selenium 3 dry ug/g

2 Total Chlorine 14 dry ug/g

2 Total Fluorine 75 dry ug/g

3 Fuel (Coal) Heating Value 7727 Btu/lb (wet)

3 Fuel Moisture 31.21 %

3 Fuel Ash Content 8.82 % wet

3 Volatile Matter 29.51 % wet

3 Fixed Carbon 30.47 % wet

3 Carbon 44.22 % wet

3 Sulfur 0.42 %wet

3 Hydrogen 3.15 %wet

3 Nitrogen 0.67 %wet

3 Oxygen 11.51 %wet

3 Antimony 2 dry ug/g

3 Arsenic 2 dry ug/g

3 Beryllium 0.5 dry ug/g

3 Cadmium 0.4 dry ug/g

3 Chromium 11 dry ug/g

3 Cobalt 2 dry ug/g

3 Lead 5 dry ug/g

3 Manganese 37 dry ug/g

Thursday, January 20, 2011 Page 24 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

3 Nickel 7 dry ug/g

3 Mercury 0.18 dry ug/g

3 Selenium 3 dry ug/g

3 Total Chlorine 12 dry ug/g

3 Total Fluorine 77 dry ug/g

Thursday, January 20, 2011 Page 25 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Sampling / Stack Data Results Detail

Location Unit #2 Stack (EPN S2) - Method 10

Average

Run Number 1 2 3

Test Date 4/28/2010 4/29/2010 4/29/2010

Run Start Time 8:10:00 AM 12:21:00 AM 5:10:00 PM

Run Finish Time 10:33:00 AM 2:41:00 AM 7:26:00 PM

Carbon Dioxide, % 13.66 13.28 13.48 13.473

Oxygen, % 6.18 6.34 6.22 6.247

Fuel Factor 1.08 1.1 1.09

Dry Volumetric Flow Rate, dry scfm 1337930 1330471 1299355 1,322,585.3

33

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Moisture, % 11.36 11.76 11.8 11.640

Analyzer Make Thermo Thermo Thermo

Analyzer Model 48l 48l 48l

Analyzer Serial Number 77401385 77401385 77401385 77,401,385.

000

Operating Range 1000 1000 1000 1,000.000

Operating Units ppm ppm ppm

No. Readings/Avg. 1052 1040 1024 1,038.667

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID ALM004870-

Zero

ALM004870

-Zero

ALM004870-

Zero

Calibration Pre Zero Cylinder Instrument Response 0.09 0.12 0.18 0.130

Calibration Pre Zero Cylinder Bias 0 0 0.01 0.003

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID BLM005148-

CO

BLM005148

-CO

BLM005148-

CO

Calibration Pre High Cylinder Instrument Response 463.64 457.58 460.63 460.617

Calibration Pre High Cylinder Bias -0.06 -0.72 -0.39 -0.390

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID ALM004870-

Zero

ALM004870

-Zero

ALM004870-

Zero

Calibration Post Zero Cylinder Instrument Response 0.11 0.16 0.52 0.263

Calibration Post Zero Cylinder Bias 0 0.01 0.05 0.020

Calibration Post Zero Cylinder Drift 0 0.01 0.04 0.017

Calibration Post High Cylinder ID BLM005148-

CO

BLM005148

-CO

BLM005148-

CO

Calibration Post High Cylinder Instrument Response 458.12 453.54 458.32 456.660

Calibration Post High Cylinder Bias -0.66 -1.15 -0.64 -0.817

Calibration Post High Cylinder Drift 0.6 0.43 0.25 0.427

Cavg 649.79 655.54 658.56 654.630

Cavg Units ppmvd ppmvd ppmvd

Cgas 652.8202 666.3085 663.7653 660.965

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 1910 0 0 636.667

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, January 20, 2011 Page 26 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Location Unit #2 Stack (EPN S2) - Method 23

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 9:35:00 AM 11:50:00 AM 2:15:00 AM

Run Finish Time 6:00:00 PM 11:20:00 PM 10:40:00 AM

Net Traversing Points 48 48 48

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.195 0.193 0.193 0.194

Pitot Tube Coefficient 0.81 0.816 0.81 0.812

Dry Gas Meter Calibration Factor 0.985 0.985 0.985 0.985

Barometric Pressure, inches of Mercury 29.42 29.32 29.15 29.297

Average Orifice Meter Differential, inches H2O 1.39 1.45 1.41 1.417

Dry Gas Meter Volume Sampled, cubic feet 310.302 320.695 318.057 316.351

Average Dry Gas Meter Temperature, °F 62.47 83.32 65.75 70.513

Dry Gas Meter Volume Sampled, dscf 304.776 301.915 307.620 304.770

Total Moisture Liquid collected, g 828.6 853 871.8 851.133

Volume of Water Vapor, standard cubic feet 39.00 40.15 41.04 40.063

Moisture Content of Stack Gas, % 11.34 11.74 11.77 11.617

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

Dry Mole Fraction 0.8866 0.8826 0.8823 0.884

Carbon Dioxide, % 13.7 13.3 13.5 13.500

Oxygen, % 6.2 6.3 6.2 6.233

Carbon Monoxide & Nitrogen, % 80.1 80.4 80.3 80.267

Fuel Factor 1.07 1.10 1.09

Dry Molecular Weight, lb/lb-Mole 30.44 30.38 30.41 30.410

Wet Molecular weight, lb/lb-Mole 29.03 28.93 28.95 28.970

Flue Gas Static Pressure, inches of H2O -2.1 -2.1 -2.1 -2.100

Absolute Flue Gas Pressure, inches of Mercury 29.27 29.17 29.00 29.147

Average Stack Gas Temperature, °F 372.23 376.23 375.10 374.520

Average Velocity Head, inches of H2O 2.1291679809

4331

2.101348315

79752

2.046513226

72972

2.092

Average Stack Gas Velocity, feet/second 100.00 100.66 98.80 99.820

Stack Cross-Sectional Area, square feet 404.262 404.262 404.262 404.262

Dry Volumetric Flow Rate, dry scfm 1,334,730.5 1,326,532.9 1,295,744.1 1,319,002.5

00

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,425,572.0 2,441,580.8 2,396,465.1 2,421,205.9

67

Percent Isokinetic of Sampling Rate, % 92.7 94.4 98.4 95.167

Percent Excess Air, % 41.5 42.2 41.3 41.667

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Round Duct Diameter, inches 272.25 272.25 272.25

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

Thursday, January 20, 2011 Page 27 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Location Unit #2 Stack (EPN S2) - Method 25A

Average

Run Number 1 2 3

Test Date 4/28/2010 4/29/2010 4/29/2010

Run Start Time 8:10:00 AM 12:21:00 AM 5:10:00 PM

Run Finish Time 10:33:00 AM 2:41:00 AM 7:26:00 PM

Carbon Dioxide, % 13.66 13.28 13.48 13.473

Oxygen, % 6.18 6.34 6.22 6.247

Fuel Factor 1.08 1.1 1.09

Dry Volumetric Flow Rate, dry scfm 1337930 1330471 1299355 1,322,585.3

33

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Moisture, % 11.36 11.76 11.8 11.640

Analyzer Make VIG VIG VIG

Analyzer Model 210 210 210 210.000

Analyzer Serial Number 1141002 1141002 1141002 1,141,002.0

00

Operating Range 100 100 100 100.000

Operating Units ppm ppm ppm

No. Readings/Avg. 15 15 15 15.000

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID ALM004870-

Zero

ALM004870

-Zero

ALM004870-

Zero

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC16756-CH4 CC16756-

CH4

CC16756-

CH4

Calibration Pre High Cylinder Instrument Response 66.7 66.7 66.7 66.700

Calibration Pre High Cylinder Bias -0.13 -0.13 -0.13 -0.130

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID ALM004870-

Zero

ALM004870

-Zero

ALM004870-

Zero

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID CC16756-CH4 CC16756-

CH4

CC16756-

CH4

Calibration Post High Cylinder Instrument Response 66.7 66.7 66.7 66.700

Calibration Post High Cylinder Bias -0.13 -0.13 -0.13 -0.130

Calibration Post High Cylinder Drift 0 0 0 0.000

Cavg 0.94 0.42 0.9 0.753

Cavg Units ppmvw ppmvw ppmvw

Cgas 1.0605 0.476 1.0204 0.852

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0.94 0.42 0.9 0.753

Cgasw Units ppmvw ppmvw ppmvw

Thursday, January 20, 2011 Page 28 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Location Unit #2 Stack (EPN S2) - Method 26A

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 7:01:00 PM 5:09:00 PM 1:17:00 PM

Run Finish Time 10:32:00 PM 8:31:00 PM 4:47:00 PM

Net Traversing Points 36 36 36

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.193 0.193 0.193 0.193

Pitot Tube Coefficient 0.81 0.816 0.816 0.814

Dry Gas Meter Calibration Factor 0.985 0.989 0.989 0.988

Barometric Pressure, inches of Mercury 29.36 29.22 29.08 29.220

Average Orifice Meter Differential, inches H2O 1.28 1.37 1.29 1.313

Dry Gas Meter Volume Sampled, cubic feet 115.910 120.578 117.530 118.006

Average Dry Gas Meter Temperature, °F 62.51 82.22 84.60 76.443

Dry Gas Meter Volume Sampled, dscf 113.575 113.798 109.888 112.420

Total Moisture Liquid collected, g 397.4 329 382 369.467

Volume of Water Vapor, standard cubic feet 18.71 15.49 17.98 17.393

Moisture Content of Stack Gas, % 14.14 11.98 14.06 13.393

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

Dry Mole Fraction 0.8586 0.8802 0.8594 0.866

Carbon Dioxide, % 13.7 13.3 13.5 13.500

Oxygen, % 6.2 6.3 6.2 6.233

Carbon Monoxide & Nitrogen, % 80.1 80.4 80.3 80.267

Fuel Factor 1.07 1.10 1.09

Dry Molecular Weight, lb/lb-Mole 30.44 30.38 30.41 30.410

Wet Molecular weight, lb/lb-Mole 28.68 28.90 28.67 28.750

Flue Gas Static Pressure, inches of H2O -1.6 -2.1 -2.1 -1.933

Absolute Flue Gas Pressure, inches of Mercury 29.24 29.07 28.93 29.080

Average Stack Gas Temperature, °F 383.42 390.53 394.42 389.457

Average Velocity Head, inches of H2O 2.0353319197

9757

2.114314694

85871

1.947130996

47251

2.032

Average Stack Gas Velocity, feet/second 99.07 102.06 98.80 99.977

Stack Cross-Sectional Area, square feet 404.262 404.262 404.262 404.262

Dry Volumetric Flow Rate, dry scfm 1,262,272.2 1,314,252.5 1,230,596.9 1,269,040.5

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,403,014.2 2,475,538.8 2,396,465.1 2,425,006.0

33

Percent Isokinetic of Sampling Rate, % 99.5 95.7 98.7 97.967

Percent Excess Air, % 41.5 42.2 41.3 41.667

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Round Duct Diameter, inches 272.25 272.25 272.25

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

Thursday, January 20, 2011 Page 29 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Location Unit #2 Stack (EPN S2) - Method 29

Average

Run Number 1 2 3

Test Date 4/28/2010 4/28/2010 4/29/2010

Run Start Time 1:40:00 AM 12:17:00 AM 11:27:00 AM

Run Finish Time 6:07:00 AM 11:55:00 PM 4:20:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.193 0.193 0.193 0.193

Pitot Tube Coefficient 0.816 0.81 0.81 0.812

Dry Gas Meter Calibration Factor 0.989 0.985 0.985 0.986

Barometric Pressure, inches of Mercury 29.38 29.2 29.1 29.227

Average Orifice Meter Differential, inches H2O 1.38 1.28 1.43 1.363

Dry Gas Meter Volume Sampled, cubic feet 159.010 150.710 159.051 156.257

Average Dry Gas Meter Temperature, °F 61.54 69.58 80.63 70.583

Dry Gas Meter Volume Sampled, dscf 156.875 144.910 149.350 150.378

Total Moisture Liquid collected, g 385.1 436.5 458.2 426.600

Volume of Water Vapor, standard cubic feet 18.13 20.55 21.57 20.083

Moisture Content of Stack Gas, % 10.36 12.42 12.62 11.800

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

Dry Mole Fraction 0.8964 0.8758 0.8738 0.882

Carbon Dioxide, % 13.7 13.3 13.5 13.500

Oxygen, % 6.2 6.3 6.2 6.233

Carbon Monoxide & Nitrogen, % 80.1 80.4 80.3 80.267

Fuel Factor 1.07 1.10 1.09

Dry Molecular Weight, lb/lb-Mole 30.44 30.38 30.41 30.410

Wet Molecular weight, lb/lb-Mole 29.15 28.84 28.84 28.943

Flue Gas Static Pressure, inches of H2O -1.6 -1.9 -2.1 -1.867

Absolute Flue Gas Pressure, inches of Mercury 29.26 29.06 28.95 29.090

Average Stack Gas Temperature, °F 384.67 375.81 377.58 379.353

Average Velocity Head, inches of H2O 1.9927659345

382

2.003748726

11986

2.062055417

001

2.020

Average Stack Gas Velocity, feet/second 98.00 97.89 99.60 98.497

Stack Cross-Sectional Area, square feet 404.262 404.262 404.262 404.262

Dry Volumetric Flow Rate, dry scfm 1,302,571.8 1,275,903.5 1,287,597.6 1,288,690.9

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,377,060.6 2,374,392.4 2,415,869.7 2,389,107.5

67

Percent Isokinetic of Sampling Rate, % 99.9 94.2 96.2 96.767

Percent Excess Air, % 41.5 42.2 41.3 41.667

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Round Duct Diameter, inches 272.25 272.25 272.25

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw

Fc

Thursday, January 20, 2011 Page 30 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Location Unit #2 Stack (EPN S2) - Method 5

Average

Run Number 1 2 3

Test Date 4/28/2010 4/28/2010 4/29/2010

Run Start Time 1:40:00 AM 12:17:00 AM 11:27:00 AM

Run Finish Time 6:07:00 AM 11:55:00 PM 4:20:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.193 0.193 0.193 0.193

Pitot Tube Coefficient 0.816 0.81 0.81 0.812

Dry Gas Meter Calibration Factor 0.989 0.985 0.985 0.986

Barometric Pressure, inches of Mercury 29.38 29.2 29.1 29.227

Average Orifice Meter Differential, inches H2O 1.38 1.28 1.43 1.363

Dry Gas Meter Volume Sampled, cubic feet 159.010 150.710 159.051 156.257

Average Dry Gas Meter Temperature, °F 61.54 69.58 80.63 70.583

Dry Gas Meter Volume Sampled, dscf 156.875 144.910 149.350 150.378

Total Moisture Liquid collected, g 385.1 436.5 458.2 426.600

Volume of Water Vapor, standard cubic feet 18.13 20.55 21.57 20.083

Moisture Content of Stack Gas, % 10.36 12.42 12.62 11.800

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

Dry Mole Fraction 0.8964 0.8758 0.8738 0.882

Carbon Dioxide, % 13.7 13.3 13.5 13.500

Oxygen, % 6.2 6.3 6.2 6.233

Carbon Monoxide & Nitrogen, % 80.1 80.4 80.3 80.267

Fuel Factor 1.07 1.10 1.09

Dry Molecular Weight, lb/lb-Mole 30.44 30.38 30.41 30.410

Wet Molecular weight, lb/lb-Mole 29.15 28.84 28.84 28.943

Flue Gas Static Pressure, inches of H2O -1.6 -1.9 -2.1 -1.867

Absolute Flue Gas Pressure, inches of Mercury 29.26 29.06 28.95 29.090

Average Stack Gas Temperature, °F 384.67 375.81 377.58 379.353

Average Velocity Head, inches of H2O 1.9927659345

382

2.003748726

11986

2.062055417

001

2.020

Average Stack Gas Velocity, feet/second 98.00 97.89 99.60 98.497

Stack Cross-Sectional Area, square feet 404.262 404.262 404.262 404.262

Dry Volumetric Flow Rate, dry scfm 1,302,571.8 1,275,903.5 1,287,597.6 1,288,690.9

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,377,060.6 2,374,392.4 2,415,869.7 2,389,107.5

67

Percent Isokinetic of Sampling Rate, % 99.9 94.2 96.2 96.767

Percent Excess Air, % 41.5 42.2 41.3 41.667

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Round Duct Diameter, inches 272.25 272.25 272.25

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

Thursday, January 20, 2011 Page 31 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Location Unit #2 Stack (EPN S2) - Method 6C

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 9:35:00 AM 10:56:00 AM 3:17:00 AM

Run Finish Time 1:35:00 PM 2:56:00 PM 7:17:00 AM

Carbon Dioxide, % 13.66 13.28 13.48 13.473

Oxygen, % 6.18 6.34 6.22 6.247

Fuel Factor 1.08 1.1 1.09

Dry Volumetric Flow Rate, dry scfm 1337930 1330471 1299355 1,322,585.3

33

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Moisture, % 11.36 11.76 11.8 11.640

Analyzer Make WR WR WR

Analyzer Model 721AT 721AT 721AT

Analyzer Serial Number 94721M82161 94721M8216

1

94721M8216

1

Operating Range 500 500 500 500.000

Operating Units ppm ppm ppm

No. Readings/Avg. 1920 1920 1920 1,920.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID ALM004870-

Zero

ALM004870

-Zero

ALM004870-

Zero

Calibration Pre Zero Cylinder Instrument Response -0.3 3.76 1.93 1.797

Calibration Pre Zero Cylinder Bias 0.03 0.96 0.54 0.510

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM063610-

SO2

ALM063610

-SO2

ALM063610-

SO2

Calibration Pre High Cylinder Instrument Response 242.7 248.6 245.58 245.627

Calibration Pre High Cylinder Bias -1.72 -0.37 -1.06 -1.050

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID ALM004870-

Zero

ALM004870

-Zero

ALM004870-

Zero

Calibration Post Zero Cylinder Instrument Response 3.94 5.86 2.04 3.947

Calibration Post Zero Cylinder Bias 1 1.44 0.57 1.003

Calibration Post Zero Cylinder Drift 0.97 0.48 2.999999999

99999E-02

0.493

Calibration Post High Cylinder ID ALM063610-

SO2

ALM063610

-SO2

ALM063610-

SO2

Calibration Post High Cylinder Instrument Response 247.47 246.17 243.98 245.873

Calibration Post High Cylinder Bias -0.63 -0.93 -1.43 -0.997

Calibration Post High Cylinder Drift 1.09 0.56 0.37 0.673

Cavg 380.7 326.46 339.43 348.863

Cavg Units ppmvd ppmvd ppmvd

Cgas 392.4846 334.1474 350.2384 358.957

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 1910 0 0 636.667

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, January 20, 2011 Page 32 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Location Unit #2 Stack (EPN S2) - Method 7E

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 9:35:00 AM 10:56:00 AM 3:17:00 AM

Run Finish Time 1:35:00 PM 2:56:00 PM 7:17:00 AM

Carbon Dioxide, % 13.66 13.28 13.48 13.473

Oxygen, % 6.18 6.34 6.22 6.247

Fuel Factor 1.08 1.1 1.09

Dry Volumetric Flow Rate, dry scfm 1337930 1330471 1299355 1,322,585.3

33

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Moisture, % 11.36 11.76 11.8 11.640

Analyzer Make Thermo Thermo Thermo

Analyzer Model 42l 42l 42l

Analyzer Serial Number 503010323 503010323 503010323 503,010,323

.000

Operating Range 100 100 100 100.000

Operating Units ppm ppm ppm

No. Readings/Avg. 1920 1920 1920 1,920.000

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID ALM004870-

Zero

ALM004870

-Zero

ALM004870-

Zero

Calibration Pre Zero Cylinder Instrument Response 0.21 0.07 -0.02 0.087

Calibration Pre Zero Cylinder Bias 0.23 0.09 0 0.107

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM026327-

Nox

ALM026327

-Nox

ALM026327-

Nox

Calibration Pre High Cylinder Instrument Response 44.14 44.2 46.31 44.883

Calibration Pre High Cylinder Bias -0.19 -0.13 1.98 0.553

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID ALM004870-

Zero

ALM004870

-Zero

ALM004870-

Zero

Calibration Post Zero Cylinder Instrument Response -0.02 -0.02 0.17 0.043

Calibration Post Zero Cylinder Bias 0 0 0.19 0.063

Calibration Post Zero Cylinder Drift 0.23 0.09 0.19 0.170

Calibration Post High Cylinder ID ALM026327-

Nox

ALM026327

-Nox

ALM026327-

Nox

Calibration Post High Cylinder Instrument Response 45.22 46.2 46.51 45.977

Calibration Post High Cylinder Bias 0.89 1.87 2.18 1.647

Calibration Post High Cylinder Drift 1.08 2 0.2 1.093

Cavg 84.94 73.71 71.62 76.757

Cavg Units ppmvd ppmvd ppmvd

Cgas 86.0153 73.7258 69.7925 76.511

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, January 20, 2011 Page 33 of 33
Luminant Power Monticello Mt. Pleasant, TX

9/2/2010

Location Unit #2 Stack (EPN S2) - OTM - 27/28

Average

Run Number 1 2 3

Test Date 4/27/2010 4/28/2010 4/29/2010

Run Start Time 9:35:00 AM 8:39:00 AM 5:05:00 AM

Run Finish Time 4:42:45 PM 3:37:15 PM 11:47:00 AM

Net Traversing Points 47 44 36

Net Run Time, minutes 427.75 418.25 402

Nozzle Diameter, inches 0.135 0.135 0.135 0.135

Pitot Tube Coefficient 0.816 0.816 0.816 0.816

Dry Gas Meter Calibration Factor 0.989 0.989 0.989 0.989

Barometric Pressure, inches of Mercury 29.42 29.42 29.13 29.323

Average Orifice Meter Differential, inches H2O 0.35 0.35 0.35 0.350

Dry Gas Meter Volume Sampled, cubic feet 144.319 145.633 139.951 143.301

Average Dry Gas Meter Temperature, °F 64.00 74.85 67.07 68.640

Dry Gas Meter Volume Sampled, dscf 141.541 139.933 135.114 138.863

Total Moisture Liquid collected, g 342.1 387.5 375.7 368.433

Volume of Water Vapor, standard cubic feet 16.10 18.24 17.68 17.340

Moisture Content of Stack Gas, % 10.21 11.53 11.57 11.103

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

Dry Mole Fraction 0.8979 0.8847 0.8843 0.889

Carbon Dioxide, % 13.7 13.3 13.5 13.500

Oxygen, % 6.2 6.3 6.2 6.233

Carbon Monoxide & Nitrogen, % 80.1 80.4 80.3 80.267

Fuel Factor 1.07 1.10 1.09

Dry Molecular Weight, lb/lb-Mole 30.44 30.38 30.41 30.410

Wet Molecular weight, lb/lb-Mole 29.17 28.95 28.97 29.030

Flue Gas Static Pressure, inches of H2O -2.1 -2.1 -2.1 -2.100

Absolute Flue Gas Pressure, inches of Mercury 29.27 29.27 28.98 29.173

Average Stack Gas Temperature, °F 391.28 391.57 389.44 390.763

Average Velocity Head, inches of H2O 2.1497839348

6681

2.085100815

94375

2.004977963

92866

2.080

Average Stack Gas Velocity, feet/second 102.13 100.98 99.36 100.823

Stack Cross-Sectional Area, square feet 404.262 404.262 404.262 404.262

Dry Volumetric Flow Rate, dry scfm 1,349,640.5 1,314,378.0 1,283,108.5 1,315,709.0

00

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,477,236.7 2,449,342.6 2,410,048.3 2,445,542.5

33

Percent Isokinetic of Sampling Rate, % 99.7 103.5 106.5 103.233

Percent Excess Air, % 41.5 42.2 41.3 41.667

F-Factor, dscfm/MMBtu @ %O2 9590 9590 9590 9,590.000

Round Duct Diameter, inches 272.25 272.25 272.25

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

Thursday, January 20, 2011 Page 34 of 33