Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Wednesday, February 02, 2011 Page 1 of 13
Facility Information:

IN_Marshall Generating Station Unit 4

8320 East NC Highway 150

Terrell NC 28682

Contact: Jon Hays

Phone: 317-838-4445

Fax: 317-8382490

Email: jon.hays@duke.energy.com

Testing Company:

AECOM

2 Technology Park Drive

Westford MA 01886

Contact: Patrick Ford

Phone: 978-589-3427

Fax: 978-589-3100

Email: pat.ford@aecom.com

Air Permit Number:

03676T45

Permitted Source ID/Name:

Unit 4 No. 2 Fuel Oil/Coal-Fired Electric Utility Boilers

Permitted Maximum Process Rate:

7,110 MMBtu/hr

Max. Normal Operation Process Rate:

7,110 MMBtu/hr

Target Process Test Rate

7,110 MMBtu/hr

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

 process flow diagram:

This description should describe the process and associated controls to differentiate this facility from, or document 

similarity with others of same SCC.

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.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

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 354 0 0 0 8 2 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 60 0

Stack Exit Hydrogen Fluoride Method 26A 3 60 0

Stack Exit Hydrogen Chloride Method 26A 3 60 0

Stack Exit O2 Method 3A O2 3 60 0

Stack Exit Co2 Method 3A CO2 3 60 0

Stack Exit Sulfur Dioxide Method 6C 3 60 0

Stack Exit Nitrogen oxides (NOx) Method 7E 3 60 0

Wednesday, February 02, 2011 Page 2 of 13
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.

Wednesday, February 02, 2011 Page 3 of 13
Sampling / Stack Data Results Summary

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 8/24/2010 8/4/2010 8/4/2010

Run Start Time 8:08:00 AM 9:39:00 

AM

11:08:00 AM

Run Finish Time 9:19:00 AM 10:51:00 

AM

12:20:00 PM

Net Run Time, minutes 60 60 60

Dry Gas Meter Volume Sampled, dscf 42.101 42.945 43.023 42.690

Moisture Content of Stack Gas, % 13.69 13.74 14.34 13.923

Moisture Saturation at Stack Gas Temperature, % 13.02 13.13 13.31 13.153

Carbon Dioxide, % 11.58 11.64 11.64 11.620

Oxygen, % 8.03 7.99 7.94 7.987

Average Stack Gas Temperature, °F 123.33 123.63 124.13 123.697

Dry Volumetric Flow Rate, dry scfm 1,886,325.1 1,933,212.

9

1,932,534.1 1,917,357.36

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,474,518.1 2,540,543.

5

2,547,105.0 2,520,722.20

0

Percent Isokinetic of Sampling Rate, % 103.7 103.2 103.5 103.467

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 3A CO2

Average

Run Number 1 2 3

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

Run Start Time 8:08:00 AM 9:39:00 

AM

11:08:00 AM

Run Finish Time 9:19:00 AM 10:51:00 

AM

12:20:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 0 0 0 0.000

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, February 02, 2011 Page 4 of 13
Location Stack Exit - Method 3A O2

Average

Run Number 1 2 3

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

Run Start Time 8:08:00 AM 9:39:00 

AM

11:08:00 AM

Run Finish Time 9:19:00 AM 10:51:00 

AM

12:20:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 0 0 0 0.000

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 6C

Average

Run Number 1 2 3

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

Run Start Time 8:08:00 AM 9:39:00 

AM

11:08:00 AM

Run Finish Time 9:19:00 AM 10:51:00 

AM

12:20:00 PM

Carbon Dioxide, % 11.58 11.64 11.64 11.620

Oxygen, % 8.03 7.99 7.94 7.987

Dry Volumetric Flow Rate, dry scfm 1913265 1939124 1939327 1,930,572.00

0

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

Moisture, % 12.92 12.92 13.45 13.097

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, February 02, 2011 Page 5 of 13
Location Stack Exit - Method 7E

Average

Run Number 1 2 3

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

Run Start Time 8:08:00 AM 9:39:00 

AM

11:08:00 AM

Run Finish Time 9:19:00 AM 10:51:00 

AM

12:20:00 PM

Carbon Dioxide, % 11.58 11.64 11.64 11.620

Oxygen, % 8.03 7.99 7.94 7.987

Dry Volumetric Flow Rate, dry scfm 1913265 1939124 1939327 1,930,572.00

0

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

Moisture, % 12.92 1.92 13.45 9.430

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, February 02, 2011 Page 6 of 13
Emissions Summary

Process Run Data

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.35 0.34 0.35 0.347

Elb/hr 2.07E+00 2.02E+00 2.08E+00 2.057

lb/mmBtuO2 2.91E-04 2.76E-04 2.83E-04 0.000

mg/dscm 2.94E-01 2.80E-01 2.87E-01 0.287

ppm 1.94E-01 1.84E-01 1.90E-01 0.189

ppm@7%O2 2.10E-01 1.98E-01 2.04E-01 0.204

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.21 0.21 0.21 0.210

Elb/hr 1.24E+00 1.25E+00 1.25E+00 1.247

lb/mmBtuO2 1.75E-04 1.71E-04 1.70E-04 0.000

mg/dscm 1.76E-01 1.73E-01 1.72E-01 0.174

ppm 2.12E-01 2.08E-01 2.07E-01 0.209

ppm@7%O2 2.29E-01 2.24E-01 2.22E-01 0.225

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 7.16E+02 6.91E+02 6.67E+02 691.333

lb/mmBtuO2 9.90E-02 9.41E-02 9.04E-02 0.095

ppm 3.75E+01 3.57E+01 3.45E+01 35.900

ppm@7%O2 4.05E+01 3.84E+01 3.70E+01 38.633

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 1.81E+03 1.61E+03 1.56E+03 1,660.000

lb/mmBtuO2 2.50E-01 2.19E-01 2.11E-01 0.227

ppm 1.32E+02 1.16E+02 1.12E+02 120.000

ppm@7%O2 1.43E+02 1.25E+02 1.20E+02 129.333

Wednesday, February 02, 2011 Page 7 of 13
Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Unit Gross Electrical Output 0 MW 660 Run 1 PM/Metals

4 Unit Gross Electrical Output 0 MW 660

5 Unit Gross Electrical Output 0 MW 660 Run 2 PM/Metals

6 Unit Gross Electrical Output 0 MW 660 Run 3 PM/Metals

1 Heat Input 0 MillionBTU/Hr 7110 Run 1 PM/Metals

5 Heat Input 0 MillionBTU/Hr 7110 Run 2 PM/Metals

6 Heat Input 0 MillionBTU/Hr 7110 Run 3 PM/Metals

Run Name Value UOM Comments

Target

Value

1 List all emissions control devices in order of 

process flow. Choose from

0 0

1 drop down lists. If not on list add description and 

provide detailed

0 0

1 desription in section 5a. 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %

1 Ultimate/Proximate Analysis 0

1 Fuel Chlorine Content 0 mg/kg

1 Fuel Fluorine Content 0 mg/kg

1 Metals Content 0 mg/kg

Wednesday, February 02, 2011 Page 8 of 13
Sampling / Stack Data Results Detail

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 8/24/2010 8/4/2010 8/4/2010

Run Start Time 8:08:00 AM 9:39:00 AM 11:08:00 AM

Run Finish Time 9:19:00 AM 10:51:00 AM 12:20:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 60 60 60

Nozzle Diameter, inches 0.212 0.212 0.212 0.212

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.025 1.025 1.025 1.025

Barometric Pressure, inches of Mercury 29.02 29.02 29.02 29.020

Average Orifice Meter Differential, inches H2O 1.73 1.80 1.83 1.787

Dry Gas Meter Volume Sampled, cubic feet 44.675 45.872 46.108 45.552

Average Dry Gas Meter Temperature, °F 99.46 103.25 105.17 102.627

Dry Gas Meter Volume Sampled, dscf 42.101 42.945 43.023 42.690

Total Moisture Liquid collected, g 142 145.4 152.9 146.767

Volume of Water Vapor, standard cubic feet 6.68 6.84 7.20 6.907

Moisture Content of Stack Gas, % 13.69 13.74 14.34 13.923

Moisture Saturation at Stack Gas Temperature, % 13.02 13.13 13.31 13.153

Dry Mole Fraction 0.8698 0.8687 0.8669 0.868

Carbon Dioxide, % 11.58 11.64 11.64 11.620

Oxygen, % 8.03 7.99 7.94 7.987

Carbon Monoxide & Nitrogen, % 80.39 80.37 80.42 80.393

Fuel Factor 1.11 1.11 1.11

Dry Molecular Weight, lb/lb-Mole 30.17 30.18 30.18 30.177

Wet Molecular weight, lb/lb-Mole 28.71 28.69 28.74 28.713

Flue Gas Static Pressure, inches of H2O -0.65 -0.65 -0.65 -0.650

Absolute Flue Gas Pressure, inches of Mercury 28.97 28.97 28.97 28.970

Average Stack Gas Temperature, °F 123.33 123.63 124.13 123.697

Average Velocity Head, inches of H2O 1.0067063765

3585

1.059678262

23997

1.066250179

15542

1.044

Average Stack Gas Velocity, feet/second 60.34 61.95 62.11 61.467

Stack Cross-Sectional Area, square feet 683.493 683.493 683.493 683.493

Dry Volumetric Flow Rate, dry scfm 1,886,325.1 1,933,212.9 1,932,534.1 1,917,357.3

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,474,518.1 2,540,543.5 2,547,105.0 2,520,722.2

00

Percent Isokinetic of Sampling Rate, % 103.7 103.2 103.5 103.467

Percent Excess Air, % 60.9 60.4 59.7 60.333

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

Round Duct Diameter, inches 354 354 354

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 02, 2011 Page 9 of 13
Location Stack Exit - Method 3A CO2

Average

Run Number 1 2 3

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

Run Start Time 8:08:00 AM 9:39:00 AM 11:08:00 AM

Run Finish Time 9:19:00 AM 10:51:00 AM 12:20:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 0 0 0 0.000

Fuel Factor 0 0 0

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 20 20 20 20.000

Operating Units % % %

No. Readings/Avg. 0 0 0 0.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID 1 1 1

Calibration Pre Zero Cylinder Instrument Response 0 -0.01 -0.01 -0.007

Calibration Pre Zero Cylinder Bias 0 -0.06 -0.06 -0.040

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID 4 4 4

Calibration Pre High Cylinder Instrument Response 9.01 8.98 9 8.997

Calibration Pre High Cylinder Bias 0 -0.17 -0.06 -0.077

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 1 1 1

Calibration Post Zero Cylinder Instrument Response -0.01 -0.01 0.01 -0.003

Calibration Post Zero Cylinder Bias -0.06 -0.06 0.06 -0.020

Calibration Post Zero Cylinder Drift 0.06 0 0.12 0.060

Calibration Post High Cylinder ID 4 4 4

Calibration Post High Cylinder Instrument Response 8.98 9 9.02 9.000

Calibration Post High Cylinder Bias -0.17 -0.06 0.06 -0.057

Calibration Post High Cylinder Drift 0.17 0.11 0.12 0.133

Cavg 11.52 11.58 11.6 11.567

Cavg Units %vd %vd %vd

Cgas 11.5762 11.6415 11.6386 11.619

Cgas Units %vd %vd %vd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, February 02, 2011 Page 10 of 13
Location Stack Exit - Method 3A O2

Average

Run Number 1 2 3

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

Run Start Time 8:08:00 AM 9:39:00 AM 11:08:00 AM

Run Finish Time 9:19:00 AM 10:51:00 AM 12:20:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 0 0 0 0.000

Fuel Factor 0 0 0

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 0 0 0 0.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID 1 1 1

Calibration Pre Zero Cylinder Instrument Response -0.01 -0.02 -0.01 -0.013

Calibration Pre Zero Cylinder Bias 0 -0.05 0 -0.017

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID 2 2 2

Calibration Pre High Cylinder Instrument Response 10.96 10.94 10.98 10.960

Calibration Pre High Cylinder Bias 0.05 -0.05 0.15 0.050

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 1 1 1

Calibration Post Zero Cylinder Instrument Response -0.02 -0.01 0 -0.010

Calibration Post Zero Cylinder Bias -0.05 0 0.05 0.000

Calibration Post Zero Cylinder Drift 0.05 0.05 0.05 0.050

Calibration Post High Cylinder ID 2 2 2

Calibration Post High Cylinder Instrument Response 10.94 10.98 11 10.973

Calibration Post High Cylinder Bias -0.05 0.15 0.24 0.113

Calibration Post High Cylinder Drift 0.1 0.2 0.09 0.130

Cavg 8.01 7.98 7.95 7.980

Cavg Units %vd %vd %vd

Cgas 8.0287 7.9914 7.9369 7.986

Cgas Units %vd %vd %vd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, February 02, 2011 Page 11 of 13
Location Stack Exit - Method 6C

Average

Run Number 1 2 3

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

Run Start Time 8:08:00 AM 9:39:00 AM 11:08:00 AM

Run Finish Time 9:19:00 AM 10:51:00 AM 12:20:00 PM

Carbon Dioxide, % 11.58 11.64 11.64 11.620

Oxygen, % 8.03 7.99 7.94 7.987

Fuel Factor 1.11 1.11 1.11

Dry Volumetric Flow Rate, dry scfm 1913265 1939124 1939327 1,930,572.0

00

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

Moisture, % 12.92 12.92 13.45 13.097

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 100 100 100 100.000

Operating Units ppm ppm ppm

No. Readings/Avg. 0 0 0 0.000

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID 1 1 1

Calibration Pre Zero Cylinder Instrument Response 0.1 0.24 -0.04 0.100

Calibration Pre Zero Cylinder Bias 0 0.14 -0.14 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID 8 8 8

Calibration Pre High Cylinder Instrument Response 50.42 50.78 50.28 50.493

Calibration Pre High Cylinder Bias -0.06 0.3 -0.2 0.013

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 1 1 1

Calibration Post Zero Cylinder Instrument Response 0.24 -0.04 -0.08 0.040

Calibration Post Zero Cylinder Bias 0.14 -0.14 -0.18 -0.060

Calibration Post Zero Cylinder Drift 0.14 0.28 0.04 0.153

Calibration Post High Cylinder ID 8 8 8

Calibration Post High Cylinder Instrument Response 50.78 50.28 50.16 50.407

Calibration Post High Cylinder Bias 0.3 -0.2 -0.32 -0.073

Calibration Post High Cylinder Drift 0.36 0.5 0.12 0.327

Cavg 37.54 35.72 34.19 35.817

Cavg Units ppmvd ppmvd ppmvd

Cgas 37.496 35.7401 34.468 35.901

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, February 02, 2011 Page 12 of 13
Location Stack Exit - Method 7E

Average

Run Number 1 2 3

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

Run Start Time 8:08:00 AM 9:39:00 AM 11:08:00 AM

Run Finish Time 9:19:00 AM 10:51:00 AM 12:20:00 PM

Carbon Dioxide, % 11.58 11.64 11.64 11.620

Oxygen, % 8.03 7.99 7.94 7.987

Fuel Factor 1.11 1.11 1.11

Dry Volumetric Flow Rate, dry scfm 1913265 1939124 1939327 1,930,572.0

00

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

Moisture, % 12.92 1.92 13.45 9.430

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 200 200 200 200.000

Operating Units ppm ppm ppm

No. Readings/Avg. 0 0 0 0.000

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID 1 1 1

Calibration Pre Zero Cylinder Instrument Response 0.1 0.04 0.18 0.107

Calibration Pre Zero Cylinder Bias 0.02 -0.01 0.06 0.023

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID 6 6 6

Calibration Pre High Cylinder Instrument Response 108.3 108.2 108.11 108.203

Calibration Pre High Cylinder Bias -0.05 -0.1 -0.15 -0.100

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID 1 1 1

Calibration Post Zero Cylinder Instrument Response 0.04 0.18 0.22 0.147

Calibration Post Zero Cylinder Bias -0.01 0.06 0.08 0.043

Calibration Post Zero Cylinder Drift 0.03 0.07 0.02 0.040

Calibration Post High Cylinder ID 6 6 6

Calibration Post High Cylinder Instrument Response 108.2 108.11 108.16 108.157

Calibration Post High Cylinder Bias -0.1 -0.15 -0.12 -0.123

Calibration Post High Cylinder Drift 0.05 0.05 0.03 0.043

Cavg 131.62 115.65 111.6 119.623

Cavg Units ppmvd ppmvd ppmvd

Cgas 131.9391 116.0266 111.9831 119.983

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, February 02, 2011 Page 13 of 13