### 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 OH44090 Contact:Carl Vineyard Phone:440-647-6672 Fax: 440-647-6673 Email: carlvineyard@gcitest.com

Air Permit Number: 15989 Permitted Source ID/Name: White Water Valley, Unit 2 RP&L 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 / Description10100202 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 2 147 900 1200 4 1414.32 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location 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 Stack, Unit 2 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 AM1:30:00 PM 6:05:00 PM Run Finish Time 12:40:00 PM4:40:00 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 AM1:31:00 PM 6:11:00 PM Run Finish Time 12:53:00 PM4:43:00 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 AM1:31:00 PM 6:11:00 PM Run Finish Time 12:53:00 PM4:43:00 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 AM1:31:00 PM 6:11:00 PM Run Finish Time 12:53:00 PM4:43:00 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 AM1:31:00 PM 6:11:00 PM Run Finish Time 12:53:00 PM4:43:00 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 038910.391572584

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 172,022.4 169,931.4 171,543.0171,165.600 Actual Wet Volumetric Flue Gas Flow Rate, acfm 306,692.7 311,996.3 313,269.2310,652.733 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 202234201,016.333 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 101415C/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_

CO2CC275954_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_

CO2CC275954_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 202234201,016.333 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 101415C/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 202234201,016.333 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-721M8997-1 AA-721M8997-1 AA-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 202234201,016.333 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 08366345120836634512 0836634512836,634,512 .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