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 CA 93230

Contact: Neftali Nevarez

Phone: 925 431-1445

Fax:

Email: nnevarez@gwfpower.com

Testing Company:

Shaw Environmental and Infrastructure Inc.

5050 Section Avenue

Cincinnati OH 45212

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:

CB1302 Hanford L.P. Power Plant

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/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 06-031-C0603 FRS #: 110040966078

SCC / Description 10100801 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 0 0 0 240 360 2 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Baghouse 2,3,7,8-TCDD Method 23 3 480 0

outlet

Baghouse 1,2,3,7,8-PeCDD Method 23 3 480 0

outlet

Baghouse 1,2,3,4,7,8-HxCDD Method 23 3 480 0

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

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Baghouse 1,2,3,6,7,8-HxCDD Method 23 3 480 0

outlet

Baghouse 1,2,3,7,8,9-HxCDD Method 23 3 480 0

outlet

Baghouse 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

outlet

Baghouse 2,3,7,8-TCDF Method 23 3 480 0

outlet

Baghouse 1,2,3,7,8-PeCDF Method 23 3 480 0

outlet

Baghouse 2,3,4,7,8-PeCDF Method 23 3 480 0

outlet

Baghouse 1,2,3,4,7,8-HxCDF Method 23 3 480 0

outlet

Baghouse 1,2,3,6,7,8-HxCDF Method 23 3 480 0

outlet

Baghouse 2,3,4,6,7,8-HxCDF Method 23 3 480 0

outlet

Baghouse 1,2,3,7,8,9-HxCDF Method 23 3 480 0

outlet

Baghouse 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

outlet

Baghouse 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

outlet

Baghouse 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

outlet

Baghouse 3,4,4',5-TCB (PCB81) Method 23 3 480 0

outlet

Baghouse 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

outlet

Baghouse 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

outlet

Baghouse 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

outlet

Baghouse 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

outlet

Baghouse 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

outlet

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

HxCB (PCBs156/157)

Baghouse Method 23 3 480 0

outlet

Baghouse 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

outlet

Baghouse 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

outlet

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

(PCB189)

Baghouse Method 23 3 480 0

outlet

Total organic compounds 

(TOC) as Propane

Baghouse Method 25A 3 120 0

outlet

Baghouse Total Particulate OTM - 27/28 3 360 0

outlet

Organic Condensible 

Particulate

Baghouse OTM - 27/28 3 360 0

outlet

Inorganic (Aqueous) 

Condensible Part.

Baghouse OTM - 27/28 3 360 0

outlet

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

outlet

Thursday, February 10, 2011 Page 3 of 22
GWF Power Systems Co., Inc. fluidized-bed combustor Hanford

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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.

None

Baghouse Filterable PM2.5 OTM - 27/28 3 360 0

outlet

Baghouse Filterable Particulate OTM - 27/28 3 360 0

outlet

Baghouse Arsenic Method 29 3 240 0

outlet

Baghouse Selenium Method 29 3 240 0

outlet

Baghouse Antimony Method 29 3 240 0

outlet

Baghouse Beryllium Method 29 3 240 0

outlet

Baghouse Cadmium Method 29 3 240 0

outlet

Baghouse Chromium Method 29 3 240 0

outlet

Baghouse Cobalt Method 29 3 240 0

outlet

Baghouse Lead Method 29 3 240 0

outlet

Baghouse Manganese Method 29 3 240 0

outlet

Baghouse Nickel Method 29 3 240 0

outlet

Baghouse O2 Method 3A O2 3 120 0

outlet

Baghouse Co2 Method 3A CO2 3 120 0

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

Location Baghouse 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 PM 4:20:00 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 AM 1:15:00 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

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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 AM 1:15:00 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 AM 1:15:00 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 - 

27/28

OTM - 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

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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

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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

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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

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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 0 5/18/10

5 Gross Unit Heat Rate 279.1 BTU/KWh 0 5/19/10

6 Gross Unit Heat Rate 275 BTU/KWh 0 5/20/10

7 Gross Unit Heat Rate 273.6 BTU/KWh 0 5/21/10

8 Gross Unit Heat Rate 274.6 BTU/KWh 0 5/21/10

1 Steam Flow Rate 218.82 1000 lb/h 0 5/18/10

5 Steam Flow Rate 223.54 1000 lb/h 0 5/19/10

6 Steam Flow Rate 221.24 1000 lb/h 0 5/20/10

7 Steam Flow Rate 220.29 1000 lb/h 0 5/21/10

8 Steam Flow Rate 221.05 1000 lb/h 0 5/21/10

1 Total Coke Feed Rate 20.05 Klb/hr 0 5/18/10

5 Total Coke Feed Rate 20.2 Klb/hr 0 5/19/10

6 Total Coke Feed Rate 19.91 Klb/hr 0 5/20/10

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

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

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

Location Baghouse 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 PM 4:20:00 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

0189

2.349724042

33072

2.357404995

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 70,645.4 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

Percent Excess Air, % 21.7 21.1 23.3 22.033

F-Factor, dscfm/MMBtu @ %O2 9827 9768 9930 9,841.667

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 AM 11:15:00 AM 1:35:00 PM

Run Finish Time 11:00:00 AM 1:15:00 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 68553 68,553.000

F-Factor, dscfm/MMBtu @ %O2 9866 9778 9836 9,826.667

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 07122024-50 07122024-50 07122024-50

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

AL

SG9135100B

AL

SG9135100B

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 

M

XCO025416

B M

XCO025416

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

AL

SG9135100B

AL

SG9135100B

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 

M

XCO025416

B M

XCO025416

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 AM 11:15:00 AM 1:35:00 PM

Run Finish Time 11:00:00 AM 1:15:00 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 9836 9,826.667

Moisture, % 0 0 0 0.000

Analyzer Make Servomex Servomex Servomex

Analyzer Model 1440 1440 1440 1,440.000

Analyzer Serial Number 01550D1/4111 01440D1/41

11

01440D1/411

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

AL

SG9135100B

AL

SG9135100B

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 

CO2

SG9152394 

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

AL

SG9135100B

AL

SG9135100B

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 

CO2

SG9152394 

CO2

SG9152394 

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

5821

15.87475247

52475

15.60933333

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 AM 11:15:00 AM 1:35:00 PM

Run Finish Time 11:00:00 AM 1:15:00 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 01440D1/4111 01440D1/41

11

01440D1/411

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

AL

SG9135100B

AL

SG9135100B

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 

O2

SG9152394 

O2

SG9152394 

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

AL

SG9135100B

AL

SG9135100B

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 

O2

SG9152394 

O2

SG9152394 

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

7119

3.958187208

80983

3.766319327

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 - 27/28 OTM - 27/28 OTM - 27/28

Net Traversing Points 1 2 3

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

Nozzle Diameter, inches 6:26:00 PM 2:16:00 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 65,673.7 66,053.000

F-Factor, dscfm/MMBtu @ %O2 111,602.2 115,124.1 112,853.4 113,193.233

Round Duct Diameter, inches 347.63 340.54 349.29

Rectangular Duct Width, inches 1.9601318238

9546

2.102943401

00694

1.997616671

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