### Name: Mark Kehoe

Title: Director, Environmental and Safety Pr Company: GWF Power Systems Sign Date: 8/23/2010 Name: Rick Campbell Title: Senior Project Manager Company:Shaw Environmental and Infrastruct Sign Date: 8/20/2010 Permitted Facility Representative / Date Testing Company Representative / Date



## GWF Power Systems Co., Inc. fluidized-bed combustor Hanford 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, February 10, 2011 Page 1 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 Facility Information:
Hanford L.P.
10596 Idaho Ave

Hanford CA93230 Contact:Neftali Nevarez Phone:925 431-1445 Fax: Email: nnevarez@gwfpower.com Testing Company:
Shaw Environmental and Infrastructure Inc.
5050 Section Avenue

Cincinnati OH45212 Contact:Rick Campbell Phone:513-782-4515 Fax: 513-782-4807 Email:richard.campbell@shawgrp.com

Air Permit Number: C-603 Permitted Source ID/Name: Hanford L.P. Power Plant CB1302 Permitted Maximum Process Rate: 320 mmbtu/hr Max. Normal Operation Process Rate: Target Process Test Rate 90%

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: The fluidized bed combustor is fueled by petrolium coke utilizing a baghouse for particulate control. Industry/SCC/NAIS221112

Sampling Location Information:

Test Parameter Information: AFS #:06-031-C0603 FRS #:110040966078

SCC / Description10100801 External Combustion Boilers - Electric Generation - Petroleum Coke - All Boiler Sizes

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 Baghouse outlet 59.5 240 360 2 0 24 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location 2,3,7,8-TCDD Method 23 3 480 0 Baghouse outlet 1,2,3,7,8-PeCDD Method 23 3 480 0 Baghouse outlet 1,2,3,4,7,8-HxCDD Method 23 3 480 0 Baghouse outlet Regulation Description Compound Limit Unit
None 0



### Thursday, February 10, 2011 Page 2 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 1,2,3,6,7,8-HxCDD Method 23 3 480 0 Baghouse outlet 1,2,3,7,8,9-HxCDD Method 23 3 480 0 Baghouse outlet 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0 Baghouse outlet 2,3,7,8-TCDF Method 23 3 480 0 Baghouse outlet 1,2,3,7,8-PeCDF Method 23 3 480 0 Baghouse outlet 2,3,4,7,8-PeCDF Method 23 3 480 0 Baghouse outlet 1,2,3,4,7,8-HxCDF Method 23 3 480 0 Baghouse outlet 1,2,3,6,7,8-HxCDF Method 23 3 480 0 Baghouse outlet 2,3,4,6,7,8-HxCDF Method 23 3 480 0 Baghouse outlet 1,2,3,7,8,9-HxCDF Method 23 3 480 0 Baghouse outlet 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0 Baghouse outlet 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0 Baghouse outlet 3,3',4,4'-TCB (PCB77) Method 23 3 480 0 Baghouse outlet 3,4,4',5-TCB (PCB81) Method 23 3 480 0 Baghouse outlet 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0 Baghouse outlet 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0 Baghouse outlet 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0 Baghouse outlet 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0 Baghouse outlet 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0 Baghouse outlet 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) Method 23 3 480 0 Baghouse outlet 2,3',4,4',5,5'-HxCB (PCB167)Method 23 3 480 0 Baghouse outlet 3,3',4,4',5,5'-HxCB (PCB169)Method 23 3 480 0 Baghouse outlet 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 0 Baghouse outlet Total organic compounds

(TOC) as Propane Method 25A 3 120 0 Baghouse outlet Total Particulate OTM - 27/28 3 360 0 Baghouse outlet Organic Condensible

Particulate OTM - 27/28 3 360 0 Baghouse outlet Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 360 0 Baghouse outlet Total PM2.5 OTM - 27/28 3 360 0 Baghouse outlet



### Thursday, February 10, 2011 Page 3 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010

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.
None Filterable PM2.5 OTM - 27/28 3 360 0 Baghouse outlet Filterable Particulate OTM - 27/28 3 360 0 Baghouse outlet Arsenic Method 29 3 240 0 Baghouse outlet Selenium Method 29 3 240 0 Baghouse outlet Antimony Method 29 3 240 0 Baghouse outlet Beryllium Method 29 3 240 0 Baghouse outlet Cadmium Method 29 3 240 0 Baghouse outlet Chromium Method 29 3 240 0 Baghouse outlet Cobalt Method 29 3 240 0 Baghouse outlet Lead Method 29 3 240 0 Baghouse outlet Manganese Method 29 3 240 0 Baghouse outlet Nickel Method 29 3 240 0 Baghouse outlet O2 Method 3A O2 3 120 0 Baghouse outlet Co2 Method 3A CO2 3 120 0 Baghouse outlet



### Thursday, February 10, 2011 Page 4 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 Sampling / Stack Data Results Summary



### LocationBaghouse outlet - Method 23 Average Run Number 1 2 3
Test Date 5/18/2010 5/19/2010 5/20/2010 Run Start Time 9:00:00 AM 8:00:00 AM 8:00:00 AM

Run Finish Time 5:30:00 PM4:20:00 PM 4:20:00 PM Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 291.904 297.951 300.790 296.882 Moisture Content of Stack Gas, % 13.12 12.95 12.59 12.887 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 15.5 16 15.7 15.733 Oxygen, % 3.8 3.7 4 3.833 Average Stack Gas Temperature, °F 343.42 339.63 343.83 342.293 Dry Volumetric Flow Rate, dry scfm 68,561.5 70,815.1 70,645.4 70,007.333 Actual Wet Volumetric Flue Gas Flow Rate, acfm 118,495.5 121,415.0 122,550.4 120,820.300 Percent Isokinetic of Sampling Rate, % 102.5 101.3 102.5 102.100 F-Factor, dscfm/MMBtu @ %O2 9827 9768 9930 9,841.667
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Location Baghouse outlet - Method 25A Average Run Number 1 2 3
Test Date 5/18/2010 5/18/2010 5/18/2010 Run Start Time 9:00:00 AM 11:15:00 AM 1:35:00 PM

Run Finish Time 11:00:00 AM1:15:00 PM 3:35:00 PM Carbon Dioxide, % 15.92 15.87 15.61 15.800 Oxygen, % 4.02 3.96 3.76 3.913 Dry Volumetric Flow Rate, dry scfm 68553 68553 68553 68,553.000 F-Factor, dscfm/MMBtu @ %O2 9866 9778 9836 9,826.667 Moisture, % 13.1 13.1 13.1 13.100 Fuel Type Override Override Override
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Thursday, February 10, 2011 Page 5 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010
Location Baghouse outlet - Method 29 Average Run Number
Test Date Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Location Baghouse outlet - Method 3A CO2 Average Run Number 1 2 3
Test Date 5/18/2010 5/18/2010 5/18/2010 Run Start Time 9:00:00 AM 11:15:00 AM 1:35:00 PM

Run Finish Time 11:00:00 AM1:15:00 PM 3:35:00 PM Carbon Dioxide, % 15.72 15.75 15.46 15.643 Oxygen, % 3.98 3.92 3.76 3.887 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9866 9778 9836 9,826.667 Moisture, % 0 0 0 0.000 Fuel Type Override Override Override
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Thursday, February 10, 2011 Page 6 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010
Location Baghouse outlet - Method 3A O2 Average Run Number 1 2 3
Test Date 5/18/2010 5/18/2010 5/18/2010 Run Start Time 9:00:00 AM 11:15:00 AM 1:35:00 PM

Run Finish Time 11:00:00 AM1:15:00 PM 3:35:00 PM Carbon Dioxide, % 15.72 15.75 15.46 15.643 Oxygen, % 3.98 3.92 3.76 3.887 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Moisture, % 0 0 0 0.000 Fuel Type
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Location Baghouse outlet - OTM - 27/28 Average Run Number Baghouse outlet Baghouse

outlet Baghouse

outlet
Test Date Run Start Time 5/20/2010 5/21/2010 5/21/2010
Run Finish Time OTM - 27/28 OTM - 27/28OTM - 27/28

Net Run Time, minutes 12:18:00 PM 8:05:00 AM 2:58:00 PM

Dry Gas Meter Volume Sampled, dscf 0.44 0.44 0.44 0.440 Moisture Content of Stack Gas, % 123.755 125.714 123.304 124.258 Moisture Saturation at Stack Gas Temperature, % 364.9 333.5 329.1 342.500 Carbon Dioxide, % 12.19 11.10 11.16 11.483 Oxygen, % 100.00 100.00 100.00 100.000 Average Stack Gas Temperature, °F 29.13 29.25 29.25 29.210 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 0 0 0 0.000 Percent Isokinetic of Sampling Rate, % 19.309 19.309 19.309 19.309 F-Factor, dscfm/MMBtu @ %O2 111,602.2 115,124.1 112,853.4 113,193.233
Fw 23.3 24.0 24.0 23.767
Fc 101.7 98.6 99.8 100.033



### Thursday, February 10, 2011 Page 7 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 Emissions Summary



### Location: Baghouse outlet - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.000000054 0.000000029 0.000000017 0.000 Elb/hr 1.68E-09 9.12E-10 5.28E-10 0.000 lb/mmBtuO2 4.90E-12 2.55E-12 1.53E-12 0.000 ng/dscm 6.53E-03 3.44E-03 2.00E-03 0.004 ng/dscm@7%O2 5.31E-03 2.78E-03 1.64E-03 0.003 pg/dscm 6.53E+00 3.44E+00 2.00E+00 3.990 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.000000035 0.000000013 0.0000000096 0.000 Elb/hr 1.09E-09 4.09E-10 2.98E-10 0.000 lb/mmBtuO2 3.17E-12 1.14E-12 8.64E-13 0.000 ng/dscm 4.23E-03 1.54E-03 1.13E-03 0.002 ng/dscm@7%O2 3.44E-03 1.24E-03 9.29E-04 0.002 pg/dscm 4.23E+00 1.54E+00 1.13E+00 2.300 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.00000002 0.0000000079 0.0000000087 0.000 Elb/hr 6.21E-10 2.48E-10 2.70E-10 0.000 lb/mmBtuO2 1.81E-12 6.94E-13 7.83E-13 0.000 ng/dscm 2.42E-03 9.36E-04 1.02E-03 0.001 ng/dscm@7%O2 1.97E-03 7.56E-04 8.39E-04 0.001 pg/dscm 2.42E+00 9.36E-01 1.02E+00 1.459 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000076 0.0000000051 0.0000000056 0.000 Elb/hr 2.36E-10 1.60E-10 1.74E-10 0.000 lb/mmBtuO2 6.89E-13 4.48E-13 5.04E-13 0.000 ng/dscm 9.20E-04 6.05E-04 6.58E-04 0.001 ng/dscm@7%O2 7.48E-04 4.89E-04 5.41E-04 0.001 pg/dscm 9.20E-01 6.05E-01 6.58E-01 0.728 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.000000016 0.0000000062 0.0000000039 0.000 Elb/hr 4.97E-10 1.95E-10 1.21E-10 0.000 lb/mmBtuO2 1.45E-12 5.45E-13 3.51E-13 0.000 ng/dscm 1.94E-03 7.35E-04 4.58E-04 0.001 ng/dscm@7%O2 1.58E-03 5.94E-04 3.77E-04 0.001 pg/dscm 1.94E+00 7.35E-01 4.58E-01 1.044



### Thursday, February 10, 2011 Page 8 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 Compound: 1,2,3,6,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.000000012 0.0000000053 0.0000000048 0.000 Elb/hr 3.73E-10 1.67E-10 1.49E-10 0.000 lb/mmBtuO2 1.09E-12 4.65E-13 4.32E-13 0.000 ng/dscm 1.45E-03 6.28E-04 5.64E-04 0.001 ng/dscm@7%O2 1.18E-03 5.08E-04 4.64E-04 0.001 pg/dscm 1.45E+00 6.28E-01 5.64E-01 0.881 

### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.000000012 0.0000000044 0.0000000035 0.000 Elb/hr 3.73E-10 1.38E-10 1.09E-10 0.000 lb/mmBtuO2 1.09E-12 3.86E-13 3.15E-13 0.000 ng/dscm 1.45E-03 5.22E-04 4.11E-04 0.001 ng/dscm@7%O2 1.18E-03 4.22E-04 3.38E-04 0.001 pg/dscm 1.45E+00 5.22E-01 4.11E-01 0.794 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.000000014 0.0000000045 0.0000000048 0.000 Elb/hr 4.35E-10 1.41E-10 1.49E-10 0.000 lb/mmBtuO2 1.27E-12 3.95E-13 4.32E-13 0.000 ng/dscm 1.69E-03 5.33E-04 5.64E-04 0.001 ng/dscm@7%O2 1.37E-03 4.31E-04 4.64E-04 0.001 pg/dscm 1.69E+00 5.33E-01 5.64E-01 0.929 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.000000013 0.0000000038 0.0000000045 0.000 Elb/hr 4.04E-10 1.19E-10 1.40E-10 0.000 lb/mmBtuO2 1.18E-12 3.34E-13 4.05E-13 0.000 ng/dscm 1.57E-03 4.50E-04 5.28E-04 0.001 ng/dscm@7%O2 1.28E-03 3.64E-04 4.34E-04 0.001 pg/dscm 1.57E+00 4.50E-01 5.28E-01 0.849 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.0000000077 0.0000000067 0.0000000073 0.000 Elb/hr 2.39E-10 2.11E-10 2.27E-10 0.000 lb/mmBtuO2 6.98E-13 5.88E-13 6.57E-13 0.000 ng/dscm 9.32E-04 7.94E-04 8.57E-04 0.001 ng/dscm@7%O2 7.58E-04 6.42E-04 7.05E-04 0.001 pg/dscm 9.32E-01 7.94E-01 8.57E-01 0.861 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 2 3



### Thursday, February 10, 2011 Page 9 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 Mass_mg 0.0000000085 0.0000000036 0.0000000038 0.000 Elb/hr 2.64E-10 1.13E-10 1.18E-10 0.000 lb/mmBtuO2 7.71E-13 3.16E-13 3.42E-13 0.000 ng/dscm 1.03E-03 4.27E-04 4.46E-04 0.001 ng/dscm@7%O2 8.37E-04 3.45E-04 3.67E-04 0.001 pg/dscm 1.03E+00 4.27E-01 4.46E-01 0.634 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 1 2 3 Mass_mg 0.00000012 0.000000078 0.000000052 0.000 Elb/hr 3.73E-09 2.45E-09 1.62E-09 0.000 lb/mmBtuO2 1.09E-11 6.85E-12 4.68E-12 0.000 ng/dscm 1.45E-02 9.25E-03 6.11E-03 0.010 ng/dscm@7%O2 1.18E-02 7.48E-03 5.03E-03 0.008 pg/dscm 1.45E+01 9.25E+00 6.11E+00 9.953 

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 1 2 3 Mass_mg 0.0000012 0.0000008 0.00000057 0.000 Elb/hr 3.73E-08 2.52E-08 1.77E-08 0.000 lb/mmBtuO2 1.09E-10 7.03E-11 5.13E-11 0.000 ng/dscm 1.45E-01 9.48E-02 6.69E-02 0.102 ng/dscm@7%O2 1.18E-01 7.66E-02 5.50E-02 0.083 pg/dscm 1.45E+02 9.48E+01 6.69E+01 102.233 

### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber 1 2 3 Mass_mg 0.0000022 0.0000016 0.0000012 0.000 Elb/hr 6.84E-08 5.03E-08 3.73E-08 0.000 lb/mmBtuO2 2.00E-10 1.41E-10 1.08E-10 0.000 ng/dscm 2.66E-01 1.90E-01 1.41E-01 0.199 ng/dscm@7%O2 2.16E-01 1.54E-01 1.16E-01 0.162 pg/dscm 2.66E+02 1.90E+02 1.41E+02 199.000 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 1 2 3 Mass_mg 0.00000041 0.00000028 0.0000002 0.000 Elb/hr 1.27E-08 8.80E-09 6.21E-09 0.000 lb/mmBtuO2 3.72E-11 2.46E-11 1.80E-11 0.000 ng/dscm 4.96E-02 3.32E-02 2.35E-02 0.035 ng/dscm@7%O2 4.03E-02 2.68E-02 1.93E-02 0.029 pg/dscm 4.96E+01 3.32E+01 2.35E+01 35.433 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber 1 2 3 Mass_mg 0.000000062 0.000000046 0.000000031 0.000 Elb/hr 1.93E-09 1.45E-09 9.63E-10 0.000 lb/mmBtuO2 5.62E-12 4.04E-12 2.79E-12 0.000 ng/dscm 7.50E-03 5.45E-03 3.64E-03 0.006



### Thursday, February 10, 2011 Page 10 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 ng/dscm@7%O2 6.10E-03 4.40E-03 2.99E-03 0.004 pg/dscm 7.50E+00 5.45E+00 3.64E+00 5.530 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber 1 2 3 Mass_mg 0.0000075 0.000006 0.0000043 0.000 Elb/hr 2.33E-07 1.89E-07 1.34E-07 0.000 lb/mmBtuO2 6.80E-10 5.27E-10 3.87E-10 0.000 ng/dscm 9.07E-01 7.11E-01 5.05E-01 0.708 ng/dscm@7%O2 7.37E-01 5.75E-01 4.15E-01 0.576 pg/dscm 9.07E+02 7.11E+02 5.05E+02 707.667 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber 1 2 3 Mass_mg 0.000000005 0.0000000048 0.0000000034 0.000 Elb/hr 1.55E-10 1.51E-10 1.06E-10 0.000 lb/mmBtuO2 4.54E-13 4.22E-13 3.06E-13 0.000 ng/dscm 6.05E-04 5.69E-04 3.99E-04 0.001 ng/dscm@7%O2 4.92E-04 4.60E-04 3.28E-04 0.000 pg/dscm 6.05E-01 5.69E-01 3.99E-01 0.524 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.000000013 0.0000000042 0.0000000039 0.000 Elb/hr 4.04E-10 1.32E-10 1.21E-10 0.000 lb/mmBtuO2 1.18E-12 3.69E-13 3.51E-13 0.000 ng/dscm 1.57E-03 4.98E-04 4.58E-04 0.001 ng/dscm@7%O2 1.28E-03 4.02E-04 3.77E-04 0.001 pg/dscm 1.57E+00 4.98E-01 4.58E-01 0.842 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.000000011 0.0000000038 0.000000004 0.000 Elb/hr 3.42E-10 1.19E-10 1.24E-10 0.000 lb/mmBtuO2 9.98E-13 3.34E-13 3.60E-13 0.000 ng/dscm 1.33E-03 4.50E-04 4.70E-04 0.001 ng/dscm@7%O2 1.08E-03 3.64E-04 3.87E-04 0.001 pg/dscm 1.33E+00 4.50E-01 4.70E-01 0.750 

### Compound: 2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.0000000037 0.0000000033 0.0000000034 0.000 Elb/hr 1.15E-10 1.04E-10 1.06E-10 0.000 lb/mmBtuO2 3.36E-13 2.90E-13 3.06E-13 0.000 ng/dscm 4.48E-04 3.91E-04 3.99E-04 0.000 ng/dscm@7%O2 3.64E-04 3.16E-04 3.28E-04 0.000 pg/dscm 4.48E-01 3.91E-01 3.99E-01 0.413



### Thursday, February 10, 2011 Page 11 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 Compound: 2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.000000017 0.000000012 0.000000007 0.000 Elb/hr 5.28E-10 3.77E-10 2.17E-10 0.000 lb/mmBtuO2 1.54E-12 1.05E-12 6.30E-13 0.000 ng/dscm 2.06E-03 1.42E-03 8.22E-04 0.001 ng/dscm@7%O2 1.67E-03 1.15E-03 6.76E-04 0.001 pg/dscm 2.06E+00 1.42E+00 8.22E-01 1.434 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 1 2 3 Mass_mg 0.0000000055 0.0000000055 0.0000000046 0.000 Elb/hr 1.71E-10 1.73E-10 1.43E-10 0.000 lb/mmBtuO2 4.99E-13 4.83E-13 4.14E-13 0.000 ng/dscm 6.65E-04 6.52E-04 5.40E-04 0.001 ng/dscm@7%O2 5.41E-04 5.27E-04 4.44E-04 0.001 pg/dscm 6.65E-01 6.52E-01 5.40E-01 0.619 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber 1 2 3 Mass_mg 0.0000002 0.00000016 0.00000013 0.000 Elb/hr 6.21E-09 5.03E-09 4.04E-09 0.000 lb/mmBtuO2 1.81E-11 1.41E-11 1.17E-11 0.000 ng/dscm 2.42E-02 1.90E-02 1.53E-02 0.020 ng/dscm@7%O2 1.97E-02 1.54E-02 1.26E-02 0.016 pg/dscm 2.42E+01 1.90E+01 1.53E+01 19.500 

### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber 1 2 3 Mass_mg 0.0000000043 0.0000000061 0.0000000036 0.000 Elb/hr 1.34E-10 1.92E-10 1.12E-10 0.000 lb/mmBtuO2 3.90E-13 5.36E-13 3.24E-13 0.000 ng/dscm 5.20E-04 7.23E-04 4.23E-04 0.001 ng/dscm@7%O2 4.23E-04 5.84E-04 3.48E-04 0.000 pg/dscm 5.20E-01 7.23E-01 4.23E-01 0.555 

### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber 1 2 3 Mass_mg 0.0000000038 0.0000000054 0.0000000032 0.000 Elb/hr 1.18E-10 1.70E-10 9.94E-11 0.000 lb/mmBtuO2 3.45E-13 4.74E-13 2.88E-13 0.000 ng/dscm 4.60E-04 6.40E-04 3.76E-04 0.000 ng/dscm@7%O2 3.74E-04 5.17E-04 3.09E-04 0.000 pg/dscm 4.60E-01 6.40E-01 3.76E-01 0.492



### Location: Baghouse outlet - Method 25A Compound: Total organic compounds (TOC) as Average


### Thursday, February 10, 2011 Page 12 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010
Run 1 2 3 Elb/hr 2.68E+00 1.41E+00 1.35E+00 1.813 lb/mmBtuO2 7.96E-03 4.14E-03 3.93E-03 0.005 ppm 5.70E+00 3.00E+00 2.87E+00 3.857 ppm@7%O2 4.69E+00 2.46E+00 2.33E+00 3.160



### Location: Baghouse outlet - Method 29 Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.02541 0.025235 0.02593 0.026 Elb/hr 1.62E-03 1.63E-03 1.62E-03 0.002 lb/mmBtuO2 4.69E-06 4.69E-06 4.69E-06 0.000 mg/dscm 6.24E-03 6.24E-03 6.25E-03 0.006 ug/dscm 6.24E+00 6.24E+00 6.25E+00 6.243 

### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.794 0.768 0.79114 0.784 Elb/hr 5.05E-02 4.97E-02 4.95E-02 0.050 lb/mmBtuO2 1.47E-04 1.43E-04 1.43E-04 0.000 mg/dscm 1.95E-01 1.90E-01 1.91E-01 0.192 ug/dscm 1.95E+02 1.90E+02 1.91E+02 192.000 

### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.0018 0.0018 0.0018 0.002 Elb/hr 1.14E-04 1.16E-04 1.13E-04 0.000 lb/mmBtuO2 3.32E-07 3.35E-07 3.26E-07 0.000 mg/dscm 4.42E-04 4.45E-04 4.34E-04 0.000 ug/dscm 4.42E-01 4.45E-01 4.34E-01 0.440 

### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.003354 0.00491 0.003448 0.004 Elb/hr 2.13E-04 3.18E-04 2.16E-04 0.000 lb/mmBtuO2 6.19E-07 9.13E-07 6.24E-07 0.000 mg/dscm 8.23E-04 1.21E-03 8.31E-04 0.001 ug/dscm 8.23E-01 1.21E+00 8.31E-01 0.955 

### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.01957 0.00889 0.00713 0.012 Elb/hr 1.24E-03 5.75E-04 4.46E-04 0.001 lb/mmBtuO2 3.61E-06 1.65E-06 1.29E-06 0.000 mg/dscm 4.80E-03 2.20E-03 1.72E-03 0.003 ug/dscm 4.80E+00 2.20E+00 1.72E+00 2.907



### Thursday, February 10, 2011 Page 13 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.0068 0.00604 0.00595 0.006 Elb/hr 4.32E-04 3.91E-04 3.72E-04 0.000 lb/mmBtuO2 1.26E-06 1.12E-06 1.08E-06 0.000 mg/dscm 1.67E-03 1.49E-03 1.43E-03 0.002 ug/dscm 1.67E+00 1.49E+00 1.43E+00 1.530 

### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.05737 0.05861 0.05972 0.059 Elb/hr 3.65E-03 3.79E-03 3.74E-03 0.004 lb/mmBtuO2 1.06E-05 1.09E-05 1.08E-05 0.000 mg/dscm 1.41E-02 1.45E-02 1.44E-02 0.014 ug/dscm 1.41E+01 1.45E+01 1.44E+01 14.333 

### Compound: Manganese Average RunNumber 1 2 3 Mass_mg 0.0417 0.0385 0.0398 0.040 Elb/hr 2.65E-03 2.49E-03 2.49E-03 0.003 lb/mmBtuO2 7.70E-06 7.16E-06 7.20E-06 0.000 mg/dscm 1.02E-02 9.52E-03 9.59E-03 0.010 ug/dscm 1.02E+01 9.52E+00 9.59E+00 9.770 

### Compound: Nickel Average RunNumber 1 2 3 Mass_mg 0.0826 0.04968 0.04677 0.060 Elb/hr 5.25E-03 3.21E-03 2.93E-03 0.004 lb/mmBtuO2 1.52E-05 9.24E-06 8.46E-06 0.000 mg/dscm 2.03E-02 1.23E-02 1.13E-02 0.015 ug/dscm 2.03E+01 1.23E+01 1.13E+01 14.633 

### Compound: Selenium Average RunNumber 1 2 3 Mass_mg 0.0043 0.0092 0.0407 0.018 Elb/hr 2.73E-04 5.95E-04 2.55E-03 0.001 lb/mmBtuO2 7.94E-07 1.71E-06 7.36E-06 0.000 mg/dscm 1.06E-03 2.27E-03 9.81E-03 0.004 ug/dscm 1.06E+00 2.27E+00 9.81E+00 4.380



### Location: Baghouse outlet - OTM - 27/28 Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 19.8 23.7 21.2 21.567 Elb/hr 1.37E+00 1.69E+00 1.49E+00 1.517 gr/dscf 2.47E-03 2.91E-03 2.65E-03 0.003 lb/mmBtuO2 4.33E-03 5.09E-03 4.65E-03 0.005


### Thursday, February 10, 2011 Page 14 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010

Process Run Data Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 1.1 1.7 0.8 1.200 Elb/hr 7.60E-02 1.21E-01 5.64E-02 0.084 gr/dscf 1.37E-04 2.09E-04 1.00E-04 0.000 lb/mmBtuO2 2.41E-04 3.65E-04 1.75E-04 0.000 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 239.4 191.2 256.5 229.033 Elb/hr 1.65E+01 1.36E+01 1.81E+01 16.067 gr/dscf 2.99E-02 2.35E-02 3.21E-02 0.029 lb/mmBtuO2 5.24E-02 4.11E-02 5.62E-02 0.050 

### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 7 12.9 32.1 17.333 Elb/hr 4.84E-01 9.21E-01 2.26E+00 1.222 gr/dscf 8.73E-04 1.58E-03 4.02E-03 0.002 lb/mmBtuO2 1.53E-03 2.77E-03 7.03E-03 0.004 

### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 266.2 227.8 309.8 267.933 Elb/hr 1.84E+01 1.63E+01 2.18E+01 18.833 gr/dscf 3.32E-02 2.80E-02 3.88E-02 0.033 lb/mmBtuO2 5.82E-02 4.90E-02 6.79E-02 0.058 

### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 6.2 3.2 1.9 3.767 Elb/hr 4.29E-01 2.28E-01 1.34E-01 0.264 gr/dscf 7.73E-04 3.93E-04 2.38E-04 0.000 lb/mmBtuO2 1.36E-03 6.88E-04 4.16E-04 0.001



### Thursday, February 10, 2011 Page 15 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 Process Run Data

APCD Run Data

Process Lab Run Data 

### Run Name Value UOM Comments Target Value 1 Gross Unit Heat Rate 277 BTU/KWh 5/18/10 0


### 5 Gross Unit Heat Rate 279.1 BTU/KWh 5/19/10 0
6 Gross Unit Heat Rate 275 BTU/KWh 5/20/10 0
7 Gross Unit Heat Rate 273.6 BTU/KWh 5/21/10 0


### 8 Gross Unit Heat Rate 274.6 BTU/KWh 5/21/10 0
1 Steam Flow Rate 218.82 1000 lb/h 5/18/10 0
5 Steam Flow Rate 223.54 1000 lb/h 5/19/10 0


### 6 Steam Flow Rate 221.24 1000 lb/h 5/20/10 0
7 Steam Flow Rate 220.29 1000 lb/h 5/21/10 0
8 Steam Flow Rate 221.05 1000 lb/h 5/21/10 0


### 1 Total Coke Feed Rate 20.05 Klb/hr 5/18/10 0
5 Total Coke Feed Rate 20.2 Klb/hr 5/19/10 0
6 Total Coke Feed Rate 19.91 Klb/hr 5/20/10 0


### 7 Total Coke Feed Rate 19.81 Klb/hr 5/21/10 0
8 Total Coke Feed Rate 19.88 Klb/hr 5/21/10 0

Run Name Value UOM Comments Target Value 

### 1 BAGHOUSE 0 0

Thursday, February 10, 2011 Page 16 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010 Sampling / Stack Data Results Detail



### LocationBaghouse outlet - Method 23 Average Run Number 1 2 3 Test Date 5/18/2010 5/19/2010 5/20/2010 Run Start Time 9:00:00 AM8:00:00 AM 8:00:00 AM Run Finish Time 5:30:00 PM4:20:00 PM 4:20:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.175 0.175 0.175 0.175 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.967 0.967 0.967 0.967 Barometric Pressure, inches of Mercury 30.18 30.22 29.9 30.100 Average Orifice Meter Differential, inches H2O 1.25 1.32 1.28 1.283 Dry Gas Meter Volume Sampled, cubic feet 316.512 317.595 315.328 316.478 Average Dry Gas Meter Temperature, °F 100.13 91.46 76.58 89.390 Dry Gas Meter Volume Sampled, dscf 291.904 297.951 300.790 296.882 Total Moisture Liquid collected, g 936.7 941.3 920.8 932.933 Volume of Water Vapor, standard cubic feet 44.09 44.31 43.34 43.913 Moisture Content of Stack Gas, % 13.12 12.95 12.59 12.887 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8688 0.8705 0.8741 0.871 Carbon Dioxide, % 15.5 16 15.7 15.733 Oxygen, % 3.8 3.7 4 3.833 Carbon Monoxide & Nitrogen, % 80.7 80.3 80.3 80.433 Fuel Factor 1.10 1.08 1.08 Dry Molecular Weight, lb/lb-Mole 30.63 30.71 30.67 30.670 Wet Molecular weight, lb/lb-Mole 28.97 29.06 29.07 29.033 Flue Gas Static Pressure, inches of H2O 1.9 1.9 1.9 1.900 Absolute Flue Gas Pressure, inches of Mercury 30.32 30.36 30.04 30.240 Average Stack Gas Temperature, °F 343.42 339.63 343.83 342.293 Average Velocity Head, inches of H2O 2.2180182802 01892.349724042

330722.357404995

93743 2.308
Average Stack Gas Velocity, feet/second 102.28 104.80 105.78 104.287 Stack Cross-Sectional Area, square feet 19.309 19.309 19.309 19.309 Dry Volumetric Flow Rate, dry scfm 68,561.5 70,815.1 70,645.470,007.333 Actual Wet Volumetric Flue Gas Flow Rate, acfm 118,495.5 121,415.0 122,550.4120,820.300 Percent Isokinetic of Sampling Rate, % 102.5 101.3 102.5 102.100 Percent Excess Air, % 21.7 21.1 23.3 22.033 F-Factor, dscfm/MMBtu @ %O2 9827 9768 99309,841.667 Round Duct Diameter, inches 59.5 59.5 59.5 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, February 10, 2011 Page 17 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010
Location Baghouse outlet - Method 25A Average Run Number 1 2 3 Test Date 5/18/2010 5/18/2010 5/18/2010 Run Start Time 9:00:00 AM11:15:00 AM 1:35:00 PM Run Finish Time 11:00:00 AM1:15:00 PM 3:35:00 PM Carbon Dioxide, % 15.92 15.87 15.61 15.800 Oxygen, % 4.02 3.96 3.76 3.913 Fuel Factor 1.06 1.07 1.1 Dry Volumetric Flow Rate, dry scfm 68553 68553 6855368,553.000 F-Factor, dscfm/MMBtu @ %O2 9866 9778 98369,826.667 Moisture, % 13.1 13.1 13.1 13.100 Analyzer Make J.U.M. J.U.M. J.U.M. Analyzer Model VE5 VE5 VE5 Analyzer Serial Number 07122024-5007122024-5007122024-50 Operating Range 100 100 100 100.000 Operating Units PPM % % No. Readings/Avg. 120 120 120 120.000 Calibration Set 3 3 3 3.000 Calibration Pre Zero Cylinder ID SG9135100B ALSG9135100B

ALSG9135100B

AL 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 XCO025416B MXCO025416

B MXCO025416

B M Calibration Pre High Cylinder Instrument Response 50 50 50 50.000 Calibration Pre High Cylinder Bias 0 0 0 0.000 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID SG9135100B ALSG9135100B

ALSG9135100B

AL Calibration Post Zero Cylinder Instrument Response 0.1 0.8 1.4 0.767 Calibration Post Zero Cylinder Bias 0.1 0.8 1.4 0.767 Calibration Post Zero Cylinder Drift 0.1 0.8 1.4 0.767 Calibration Post High Cylinder ID XCO025416B MXCO025416

B MXCO025416

B M Calibration Post High Cylinder Instrument Response 49.3 50.8 49.1 49.733 Calibration Post High Cylinder Bias -0.7 0.8 -0.9 -0.267 Calibration Post High Cylinder Drift 0.7 0.8 0.9 0.800 Cavg 5.7 3.4 3.5 4.200 Cavg Units ppmvd ppmvd ppmvd Cgas 5.6956 3 2.8659 3.854 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, February 10, 2011 Page 18 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010
Location Baghouse outlet - Method 29 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Thursday, February 10, 2011 Page 19 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010
Location Baghouse outlet - Method 3A CO2 Average Run Number 1 2 3 Test Date 5/18/2010 5/18/2010 5/18/2010 Run Start Time 9:00:00 AM11:15:00 AM 1:35:00 PM Run Finish Time 11:00:00 AM1:15:00 PM 3:35:00 PM Carbon Dioxide, % 15.72 15.75 15.46 15.643 Oxygen, % 3.98 3.92 3.76 3.887 Fuel Factor 1.08 1.08 1.11 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9866 9778 98369,826.667 Moisture, % 0 0 0 0.000 Analyzer Make Servomex Servomex Servomex Analyzer Model 1440 1440 1440 1,440.000 Analyzer Serial Number 01550D1/411101440D1/41 1101440D1/411

1 Operating Range 20 20 20 20.000 Operating Units % % % No. Readings/Avg. 120 120 120 120.000 Calibration Set 1 1 1 1.000 Calibration Pre Zero Cylinder ID SG9135100B ALSG9135100B

ALSG9135100B

AL 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 SG9152394 CO2SG9152394

CO2 SG9152394

CO2 Calibration Pre High Cylinder Instrument Response 10 10.1 10.1 10.067 Calibration Pre High Cylinder Bias -0.5 0 0 -0.167 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID SG9135100B ALSG9135100B

ALSG9135100B

AL Calibration Post Zero Cylinder Instrument Response 0 0 0.1 0.033 Calibration Post Zero Cylinder Bias 0 0 0.5 0.167 Calibration Post Zero Cylinder Drift 0 0 0.5 0.167 Calibration Post High Cylinder ID SG9152394 CO2SG9152394

CO2SG9152394

CO2 Calibration Post High Cylinder Instrument Response 10.1 10.1 10.1 10.100 Calibration Post High Cylinder Bias 0 0 0 0.000 Calibration Post High Cylinder Drift 0.5 0 0 0.167 Cavg 15.72 15.75 15.46 15.643 Cavg Units ppmvw ppmvw ppmvw Cgas 15.9233 15.8748 15.6093 15.802 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 15.923343283 582115.87475247

5247515.60933333

33333 15.802
Cgasw Units ppmvw ppmvw ppmvw



### Thursday, February 10, 2011 Page 20 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010
Location Baghouse outlet - Method 3A O2 Average Run Number 1 2 3 Test Date 5/18/2010 5/18/2010 5/18/2010 Run Start Time 9:00:00 AM11:15:00 AM 1:35:00 PM Run Finish Time 11:00:00 AM1:15:00 PM 3:35:00 PM Carbon Dioxide, % 15.72 15.75 15.46 15.643 Oxygen, % 3.98 3.92 3.76 3.887 Fuel Factor 1.08 1.08 1.11 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Moisture, % 0 0 0 0.000 Analyzer Make Servomex Servomex Servomex Analyzer Model 1440 1440 1440 1,440.000 Analyzer Serial Number 01440D1/411101440D1/41 1101440D1/411

1 Operating Range 25 25 25 25.000 Operating Units % % % No. Readings/Avg. 120 120 120 120.000 Calibration Set 2 2 2 2.000 Calibration Pre Zero Cylinder ID SG9135100B ALSG9135100B

ALSG9135100B

AL 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 SG9152394 O2SG9152394

O2SG9152394

O2 Calibration Pre High Cylinder Instrument Response 11.89 11.71 11.9 11.833 Calibration Pre High Cylinder Bias -0.2 -0.92 -0.16 -0.427 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID SG9135100B ALSG9135100B

ALSG9135100B

AL 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 SG9152394 O2SG9152394

O2SG9152394

O2 Calibration Post High Cylinder Instrument Response 11.71 11.9 11.9 11.837 Calibration Post High Cylinder Bias -0.92 -0.16 -0.16 -0.413 Calibration Post High Cylinder Drift 0.72 0.76 0 0.493 Cavg 3.98 3.92 3.76 3.887 Cavg Units ppmvw ppmvw ppmvw Cgas 4.0205 3.9582 3.7663 3.915 Cgas Units ppmvd ppmvd ppmvd Fuel Type Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 4.0204745762 71193.958187208

809833.766319327

73109 3.915
Cgasw Units ppmvw ppmvw ppmvw



### Thursday, February 10, 2011 Page 21 of 22

### GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

8/23/2010
Location Baghouse outlet - OTM - 27/28 Average Run Number Baghouse outlet Baghouse

outlet Baghouse

outlet Test Date Run Start Time 5/20/2010 5/21/2010 5/21/2010 Run Finish Time OTM - 27/28OTM - 27/28OTM - 27/28 Net Traversing Points 1 2 3 Net Run Time, minutes 12:18:00 PM8:05:00 AM 2:58:00 PM Nozzle Diameter, inches 6:26:00 PM2:16:00 PM 9:04:00 PM Pitot Tube Coefficient 24 24 24 24.000 Dry Gas Meter Calibration Factor 360 360 360 360.000 Barometric Pressure, inches of Mercury 0.136 0.136 0.136 0.136 Average Orifice Meter Differential, inches H2O 0.84 0.84 0.84 0.840 Dry Gas Meter Volume Sampled, cubic feet 0.977 0.977 0.977 0.977 Average Dry Gas Meter Temperature, °F 30.06 29.92 29.9 29.960 Dry Gas Meter Volume Sampled, dscf 0.44 0.44 0.44 0.440 Total Moisture Liquid collected, g 130.663 130.594 128.921 130.059 Volume of Water Vapor, standard cubic feet 87.79 76.46 79.58 81.277 Moisture Content of Stack Gas, % 123.755 125.714 123.304 124.258 Moisture Saturation at Stack Gas Temperature, % 364.9 333.5 329.1 342.500 Dry Mole Fraction 17.18 15.70 15.49 16.123 Carbon Dioxide, % 12.19 11.10 11.16 11.483 Oxygen, % 100.00 100.00 100.00 100.000 Carbon Monoxide & Nitrogen, % 0.8781 0.889 0.8884 0.885 Fuel Factor 15.7 15.6 15.6 Dry Molecular Weight, lb/lb-Mole 4 4.1 4.1 4.067 Wet Molecular weight, lb/lb-Mole 80.3 80.3 80.3 80.300 Flue Gas Static Pressure, inches of H2O 1.08 1.08 1.08 1.080 Absolute Flue Gas Pressure, inches of Mercury 30.67 30.66 30.66 30.663 Average Stack Gas Temperature, °F 29.13 29.25 29.25 29.210 Average Velocity Head, inches of H2O 1.9 1.9 1.9 1.900 Average Stack Gas Velocity, feet/second 30.20 30.06 30.04 30.100 Stack Cross-Sectional Area, square feet 59.5 59.5 59.5 59.500 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 0 0 0 0.000 Percent Isokinetic of Sampling Rate, % 19.309 19.309 19.309 19.309 Percent Excess Air, % 64,667.1 67,818.2 65,673.766,053.000 F-Factor, dscfm/MMBtu @ %O2 111,602.2 115,124.1 112,853.4113,193.233 Round Duct Diameter, inches 347.63 340.54 349.29 Rectangular Duct Width, inches 1.9601318238 95462.102943401

006941.997616671

15614 Rectangular Duct Length, inches 96.33 99.37 97.41 Fw 23.3 24.0 24.0 23.767 Fc 101.7 98.6 99.8 100.033



### Thursday, February 10, 2011 Page 22 of 22