Name: Steve Saum

Title: General Manager

Company: Richmond Power and Light

Sign Date: 9/14/2010

Name: Carl Vineyard

Title: Utility MACT Project Manager

Company: Grace Consulting, Inc.

Sign Date: 9/14/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Richmond Power & Light, Unit 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.

Friday, January 28, 2011 Page 1 of 13
Richmond Power & Light, Unit 2

9/14/2010

Facility Information:

White Water Facility, Unit 2

2000 US 27

Richmond IN 47374

Contact: Dan Straight

Phone: 765-973-7292

Fax: 765-973-7296

Email: DanS@rp-l.com

Testing Company:

Grace Consulting, Inc.

510 Dickson Street

Wellington OH 44090

Contact:Carl Vineyard

Phone: 440-647-6672

Fax: 440-647-6673

Email: carlvineyard@gcitest.com

Air Permit Number:

15989

Permitted Source ID/Name:

RP&L White Water Valley, Unit 2

Permitted Maximum Process Rate: Max. Normal Operation Process Rate: Target Process Test Rate

61000 tons/hr

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

 process flow diagram:

Upstream Downstream drawing attached.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 1817700009 FRS #: 110000592662

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, Unit 2 147 0 0 1414.32 900 1200 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack, Unit 2 Hydrogen Chloride Method 26A 3 0

Stack, Unit 2 Hydrogen Fluoride Method 26A 3 0

Stack, Unit 2 O2 Method 3A O2 3 0

Stack, Unit 2 Co2 Method 3A CO2 3 0

Stack, Unit 2 Sulfur Dioxide Method 6C 3 0

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

Regulation Description Compound Limit Unit

Section 114 Clean Air HAPS 0

Friday, January 28, 2011 Page 2 of 13
Richmond Power & Light, Unit 2

9/14/2010

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.

The HCN was sampled using CTM 033 with 2 Normal NaOH and an additional impinger for one hour per the 

clarification given by the USEPA. Complete explanation in the Comments Section.

Friday, January 28, 2011 Page 3 of 13
Richmond Power & Light, Unit 2

9/14/2010

Sampling / Stack Data Results Summary

Location Stack, Unit 2 - Method 26A

Average

Run Number 1 2 3

Test Date 6/3/2010 6/3/2010 6/3/2010

Run Start Time 9:30:00 AM 1:30:00 PM 6:05:00 PM

Run Finish Time 12:40:00 PM 4:40:00 PM 9:15:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 107.759 108.563 111.330 109.217

Moisture Content of Stack Gas, % 13.52 15.75 15.20 14.823

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

Carbon Dioxide, % 12.4 12.5 12.3 12.400

Oxygen, % 6.2 6.2 6.3 6.233

Average Stack Gas Temperature, °F 335.58 338.17 339.08 337.610

Dry Volumetric Flow Rate, dry scfm 172,022.4 169,931.4 171,543.0 171,165.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 306,692.7 311,996.3 313,269.2 310,652.733

Percent Isokinetic of Sampling Rate, % 103.2 105.2 106.9 105.100

F-Factor, dscfm/MMBtu @ %O2 9752 9806 9776 9,778.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack, Unit 2 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 6/3/2010 6/3/2010 6/3/2010

Run Start Time 9:54:00 AM 1:31:00 PM 6:11:00 PM

Run Finish Time 12:53:00 PM 4:43:00 PM 9:16:00 PM

Carbon Dioxide, % 12.4 12.5 12.3 12.400

Oxygen, % 6.2 6.2 6.3 6.233

Dry Volumetric Flow Rate, dry scfm 198946 201869 202234 201,016.333

F-Factor, dscfm/MMBtu @ %O2 9752 9806 9776 9,778.000

Moisture, % 13.51 15.74 15.21 14.820

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, January 28, 2011 Page 4 of 13
Richmond Power & Light, Unit 2

9/14/2010

Location Stack, Unit 2 - Method 3A O2

Average

Run Number 1 2 3

Test Date 6/3/2010 6/3/2010 6/3/2010

Run Start Time 9:54:00 AM 1:31:00 PM 6:11:00 PM

Run Finish Time 12:53:00 PM 4:43:00 PM 9:16:00 PM

Carbon Dioxide, % 12.4 12.5 12.3 12.400

Oxygen, % 6.2 6.2 6.3 6.233

Dry Volumetric Flow Rate, dry scfm 198946 201869 202234 201,016.333

F-Factor, dscfm/MMBtu @ %O2 9752 9806 9776 9,778.000

Moisture, % 13.51 15.74 15.21 14.820

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack, Unit 2 - Method 6C

Average

Run Number 1 2 3

Test Date 6/3/2010 6/3/2010 6/3/2010

Run Start Time 9:54:00 AM 1:31:00 PM 6:11:00 PM

Run Finish Time 12:53:00 PM 4:43:00 PM 9:16:00 PM

Carbon Dioxide, % 12.4 12.5 12.3 12.400

Oxygen, % 6.2 6.2 6.3 6.233

Dry Volumetric Flow Rate, dry scfm 198946 201869 202234 201,016.333

F-Factor, dscfm/MMBtu @ %O2 9752 9806 9776 9,778.000

Moisture, % 13.51 15.74 15.21 14.820

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, January 28, 2011 Page 5 of 13
Richmond Power & Light, Unit 2

9/14/2010

Location Stack, Unit 2 - Method 7E

Average

Run Number 1 2 3

Test Date 6/3/2010 6/3/2010 6/3/2010

Run Start Time 9:54:00 AM 1:31:00 PM 6:11:00 PM

Run Finish Time 12:53:00 PM 4:43:00 PM 9:16:00 PM

Carbon Dioxide, % 12.4 12.5 12.3 12.400

Oxygen, % 6.2 6.2 6.3 6.233

Dry Volumetric Flow Rate, dry scfm 198946 201869 202234 201,016.333

F-Factor, dscfm/MMBtu @ %O2 9752 9806 9776 9,778.000

Moisture, % 13.51 15.74 15.21 14.820

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, January 28, 2011 Page 6 of 13
Richmond Power & Light, Unit 2

9/14/2010

Emissions Summary

Process Run Data

Location: Stack, Unit 2 - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 18.7 31.2 27.6 25.833

lb/mmBtuO2 5.30E-03 8.83E-03 7.65E-03 0.007

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 12.8 20 17.3 16.700

lb/mmBtuO2 3.63E-03 5.66E-03 4.79E-03 0.005

Location: Stack, Unit 2 - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 3.40E+00 3.55E+00 3.69E+00 3.547

ppm 1.48E+03 1.53E+03 1.59E+03 1,533.333

ppm@7%O2 1.40E+03 1.45E+03 1.51E+03 1,453.333

Location: Stack, Unit 2 - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 2.81E-01 2.41E-01 2.43E-01 0.255

ppm 1.70E+02 1.45E+02 1.45E+02 153.333

ppm@7%O2 1.61E+02 1.37E+02 1.38E+02 145.333

Friday, January 28, 2011 Page 7 of 13
Richmond Power & Light, Unit 2

9/14/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Steam Flow 494769 lb/hr Run 1 - Methods 

3A, 6C, 7E, 26A, 

033

492000

1 MW 63 MWh Run 1 - Methods 

3A, 6C, 7E, 26A, 

033

60

1 Bituminous Coal Burned 61662 Tons/hr Run 1 - Methods 

3A, 6C, 7E, 26A, 

033

61000

2 Steam Flow 520615 lb/hr Run 2 - Methods 

3A, 6C, 7E, 26A, 

033

492000

2 MW 65 MWh Run 2 - Methods 

3A, 6C, 7E, 26A, 

033

60

2 Bituminous Coal Burned 62123 Tons/hr Run 2 - Methods 

3A, 6C, 7E, 26A, 

033

61000

3 Steam Flow 533333 lb/hr Run 3 - Methods 

3A, 6C, 7E, 26A, 

033

492000

3 MW 68 MWh Run 3 - Methods 

3A, 6C, 7E, 26A, 

033

60

3 Bituminous Coal Burned 62910 Tons/hr Run 3 - Methods 

3A, 6C, 7E, 26A, 

M033

61000

Run Name Value UOM Comments

Target

Value

1 Coal Fired Precipitators 0 0

Run Name Value UOM Comments

1 N/A 0

Friday, January 28, 2011 Page 8 of 13
Richmond Power & Light, Unit 2

9/14/2010

Sampling / Stack Data Results Detail

Location Stack, Unit 2 - Method 26A

Average

Run Number 1 2 3

Test Date 6/3/2010 6/3/2010 6/3/2010

Run Start Time 9:30:00 AM 1:30:00 PM 6:05:00 PM

Run Finish Time 12:40:00 PM 4:40:00 PM 9:15:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.27 0.27 0.27 0.270

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.981 0.981 0.981 0.981

Barometric Pressure, inches of Mercury 29.25 29.25 29.25 29.250

Average Orifice Meter Differential, inches H2O 1.34 1.38 1.39 1.370

Dry Gas Meter Volume Sampled, cubic feet 115.820 117.386 117.800 117.002

Average Dry Gas Meter Temperature, °F 86.08 89.42 77.67 84.390

Dry Gas Meter Volume Sampled, dscf 107.759 108.563 111.330 109.217

Total Moisture Liquid collected, g 357.7 431.2 424 404.300

Volume of Water Vapor, standard cubic feet 16.84 20.30 19.96 19.033

Moisture Content of Stack Gas, % 13.52 15.75 15.20 14.823

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

Dry Mole Fraction 0.8648 0.8425 0.848 0.852

Carbon Dioxide, % 12.4 12.5 12.3 12.400

Oxygen, % 6.2 6.2 6.3 6.233

Carbon Monoxide & Nitrogen, % 81.4 81.3 81.4 81.367

Fuel Factor 1.19 1.18 1.19

Dry Molecular Weight, lb/lb-Mole 30.23 30.25 30.22 30.233

Wet Molecular weight, lb/lb-Mole 28.58 28.32 28.36 28.420

Flue Gas Static Pressure, inches of H2O -0.12 -0.09 -0.11 -0.107

Absolute Flue Gas Pressure, inches of Mercury 29.24 29.24 29.24 29.240

Average Stack Gas Temperature, °F 335.58 338.17 339.08 337.610

Average Velocity Head, inches of H2O 0.3830584375

03891

0.391572584

077056

0.394920857

532772

0.390

Average Stack Gas Velocity, feet/second 43.37 44.12 44.30 43.930

Stack Cross-Sectional Area, square feet 117.859 117.859 117.859 117.859

Dry Volumetric Flow Rate, dry scfm 172,022.4 169,931.4 171,543.0 171,165.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 306,692.7 311,996.3 313,269.2 310,652.733

Percent Isokinetic of Sampling Rate, % 103.2 105.2 106.9 105.100

Percent Excess Air, % 40.6 40.6 41.5 40.900

F-Factor, dscfm/MMBtu @ %O2 9752 9806 9776 9,778.000

Round Duct Diameter, inches 147 147 147

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, January 28, 2011 Page 9 of 13
Richmond Power & Light, Unit 2

9/14/2010

Location Stack, Unit 2 - Method 3A CO2

Average

Run Number 1 2 3

Test Date 6/3/2010 6/3/2010 6/3/2010

Run Start Time 9:54:00 AM 1:31:00 PM 6:11:00 PM

Run Finish Time 12:53:00 PM 4:43:00 PM 9:16:00 PM

Carbon Dioxide, % 12.4 12.5 12.3 12.400

Oxygen, % 6.2 6.2 6.3 6.233

Fuel Factor 1.19 1.18 1.19

Dry Volumetric Flow Rate, dry scfm 198946 201869 202234 201,016.333

F-Factor, dscfm/MMBtu @ %O2 9752 9806 9776 9,778.000

Moisture, % 13.51 15.74 15.21 14.820

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1400 1400 1400 1,400.000

Analyzer Serial Number 01415C/1191 01415C/119

1

01415C/1191

Operating Range 18 18 18 18.000

Operating Units % % %

No. Readings/Avg. 180 180 180 180.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Pre Zero Cylinder Instrument Response 0.22 0 0.22 0.147

Calibration Pre Zero Cylinder Bias 0.61 -0.61 0.61 0.203

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC275954_C

O2

CC275954_

CO2

CC275954_C

O2

Calibration Pre High Cylinder Instrument Response 10.91 11.01 10.94 10.953

Calibration Pre High Cylinder Bias 1.56 2.11 1.72 1.797

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Post Zero Cylinder Instrument Response 0 0.22 0.21 0.143

Calibration Post Zero Cylinder Bias -0.61 0.61 0.56 0.187

Calibration Post Zero Cylinder Drift 1.22 1.22 4.999999999

99999E-02

0.830

Calibration Post High Cylinder ID CC275954_C

O2

CC275954_

CO2

CC275954_C

O2

Calibration Post High Cylinder Instrument Response 11.01 10.94 11.09 11.013

Calibration Post High Cylinder Bias 2.11 1.72 2.56 2.130

Calibration Post High Cylinder Drift 0.55 0.39 0.84 0.593

Cavg 12.9 13.09 12.82 12.937

Cavg Units %vd %vd %vd

Cgas 12.3774 12.5439 12.2549 12.392

Cgas Units %vd %vd %vd

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 ppmvw

Friday, January 28, 2011 Page 10 of 13
Richmond Power & Light, Unit 2

9/14/2010

Location Stack, Unit 2 - Method 3A O2

Average

Run Number 1 2 3

Test Date 6/3/2010 6/3/2010 6/3/2010

Run Start Time 9:54:00 AM 1:31:00 PM 6:11:00 PM

Run Finish Time 12:53:00 PM 4:43:00 PM 9:16:00 PM

Carbon Dioxide, % 12.4 12.5 12.3 12.400

Oxygen, % 6.2 6.2 6.3 6.233

Fuel Factor 1.19 1.18 1.19

Dry Volumetric Flow Rate, dry scfm 198946 201869 202234 201,016.333

F-Factor, dscfm/MMBtu @ %O2 9752 9806 9776 9,778.000

Moisture, % 13.51 15.74 15.21 14.820

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1400 1400 1400 1,400.000

Analyzer Serial Number 01415C/1191 01415C/119

1

01415C/1191

Operating Range 22.3 22.3 22.3 22.300

Operating Units % % %

No. Readings/Avg. 180 180 180 180.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Pre Zero Cylinder Instrument Response 0.31 0.21 0.18 0.233

Calibration Pre Zero Cylinder Bias -0.04 -0.49 -0.63 -0.387

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC275954 CC275954 CC275954

Calibration Pre High Cylinder Instrument Response 10.92 10.93 11.13 10.993

Calibration Pre High Cylinder Bias -1.08 -1.03 -0.13 -0.747

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Post Zero Cylinder Instrument Response 0.21 0.18 0.12 0.170

Calibration Post Zero Cylinder Bias -0.49 -0.63 -0.9 -0.673

Calibration Post Zero Cylinder Drift 0.45 0.14 0.27 0.287

Calibration Post High Cylinder ID CC275954 CC275954 CC275954

Calibration Post High Cylinder Instrument Response 10.93 11.13 11.3 11.120

Calibration Post High Cylinder Bias -1.03 -0.13 0.63 -0.177

Calibration Post High Cylinder Drift 0.05 0.9 0.76 0.570

Cavg 6.29 6.31 6.48 6.360

Cavg Units %vd %vd %vd

Cgas 6.2194 6.2081 6.2928 6.240

Cgas Units %vd %vd %vd

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

Friday, January 28, 2011 Page 11 of 13
Richmond Power & Light, Unit 2

9/14/2010

Location Stack, Unit 2 - Method 6C

Average

Run Number 1 2 3

Test Date 6/3/2010 6/3/2010 6/3/2010

Run Start Time 9:54:00 AM 1:31:00 PM 6:11:00 PM

Run Finish Time 12:53:00 PM 4:43:00 PM 9:16:00 PM

Carbon Dioxide, % 12.4 12.5 12.3 12.400

Oxygen, % 6.2 6.2 6.3 6.233

Fuel Factor 1.19 1.18 1.19

Dry Volumetric Flow Rate, dry scfm 198946 201869 202234 201,016.333

F-Factor, dscfm/MMBtu @ %O2 9752 9806 9776 9,778.000

Moisture, % 13.51 15.74 15.21 14.820

Analyzer Make Ametek Ametek Ametek

Analyzer Model 721-M 721-M 721-M

Analyzer Serial Number AA-721M8997-1AA-721M8997-1AA-721M8997-1

Operating Range 1018 1812 1812 1,547.333

Operating Units ppm ppm ppm

No. Readings/Avg. 180 180 180 180.000

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Pre Zero Cylinder Instrument Response 12.76 21.43 23.76 19.317

Calibration Pre Zero Cylinder Bias 0.14 0.62 0.75 0.503

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC68408 CC68408 CC68408

Calibration Pre High Cylinder Instrument Response 1004.5 986.76 980.54 990.600

Calibration Pre High Cylinder Bias 0.23 -0.75 -1.1 -0.540

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Post Zero Cylinder Instrument Response 21.43 23.76 25.77 23.653

Calibration Post Zero Cylinder Bias 0.62 0.75 0.86 0.743

Calibration Post Zero Cylinder Drift 0.48 0.13 0.11 0.240

Calibration Post High Cylinder ID CC68408 CC68408 CC68408

Calibration Post High Cylinder Instrument Response 986.76 980.54 981.26 982.853

Calibration Post High Cylinder Bias -0.75 -1.1 -1.06 -0.970

Calibration Post High Cylinder Drift 0.98 0.35 0.04 0.457

Cavg 1436.1 1468.64 1514.54 1,473.093

Cavg Units ppmvd ppmvd ppmvd

Cgas 1476.2345 1531.7269 1586.1682 1,531.377

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

Friday, January 28, 2011 Page 12 of 13
Richmond Power & Light, Unit 2

9/14/2010

Location Stack, Unit 2 - Method 7E

Average

Run Number 1 2 3

Test Date 6/3/2010 6/3/2010 6/3/2010

Run Start Time 9:54:00 AM 1:31:00 PM 6:11:00 PM

Run Finish Time 12:53:00 PM 4:43:00 PM 9:16:00 PM

Carbon Dioxide, % 12.4 12.5 12.3 12.400

Oxygen, % 6.2 6.2 6.3 6.233

Fuel Factor 1.19 1.18 1.19

Dry Volumetric Flow Rate, dry scfm 198946 201869 202234 201,016.333

F-Factor, dscfm/MMBtu @ %O2 9752 9806 9776 9,778.000

Moisture, % 13.51 15.74 15.21 14.820

Analyzer Make Thermo 

Scientific

Thermo 

Scientific

Thermo 

Scientific

Analyzer Model 42I-HL 42I-HL 42I-HL

Analyzer Serial Number 0836634512 0836634512 0836634512 836,634,512

.000

Operating Range 496 496 496 496.000

Operating Units ppm ppm ppm

No. Readings/Avg. 180 180 180 180.000

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Pre Zero Cylinder Instrument Response 1.43 1.3 1.44 1.390

Calibration Pre Zero Cylinder Bias 0.11 0.09 0.11 0.103

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0017230 EB0017230 EB0017230

Calibration Pre High Cylinder Instrument Response 250.45 249.67 247.76 249.293

Calibration Pre High Cylinder Bias 0.06 -0.09 -0.48 -0.170

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Post Zero Cylinder Instrument Response 1.3 1.44 1.67 1.470

Calibration Post Zero Cylinder Bias 0.09 0.11 0.16 0.120

Calibration Post Zero Cylinder Drift 0.02 0.02 0.05 0.030

Calibration Post High Cylinder ID EB0017230 EB0017230 EB0017230

Calibration Post High Cylinder Instrument Response 249.67 247.76 246.75 248.060

Calibration Post High Cylinder Bias -0.09 -0.48 -0.68 -0.417

Calibration Post High Cylinder Drift 0.15 0.39 0.2 0.247

Cavg 168.12 143 142.52 151.213

Cavg Units ppmvd ppmvd ppmvd

Cgas 169.6416 144.8681 145.1532 153.221

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

Friday, January 28, 2011 Page 13 of 13