### Name: Mary Ann Keon

Title: Environmental Director Company: Boral Industries (Boral Brick, Inc.) Sign Date: 3/15/2011 Name: Bill Kissel Title: President Company:Analytical Testing Consultants, Inc. Sign Date: 3/15/2011 Permitted Facility Representative / Date Testing Company Representative / Date 

## Salisbury Plant 6 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.

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### Salisbury Plant 6

3/15/2011 Facility Information: Boral Bricks, Inc. 700 South Long Street

East Spencer NC28039 Contact:Ms. Mary Ann Keon Phone:(770) 849-5192 Fax: (706) 722-8222 Email:maryann.keon@boral.com Testing Company: Analytical Testing Consultants, Inc.
1630 Dale Earnhardt Blvd.

Kannapolis NC28083 Contact:Mr. Bill Kissel Phone:(800) 733-3193 Fax: (704) 932-3193 Email:bkissel@atc-net.net

Air Permit Number: Tunnel Kiln 6BK Permitted Maximum Process Rate: 27.8 Max. Normal Operation Process Rate: 20 tph Target Process Test Rat 20 tph

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: Brick Tunnel Kiln and associated dryer Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information: AFS #: FRS #:

SCC / Description

The following state and federal regulations that apply to the proposed testing: Permitted Source ID/Name:

LocationRound

Duct Diam. Distance from upstream dist. Distance from

downstream dist. Number of

Traverse Ports Equiv. Diam Min.Travers Points Rect. Duct Length /Width DIFF Stack 84.5 4 6.4 2 0 24 0 0 Dryer 3 2 4 1.84 24 39 51

Target Parameter Test Method Number of

Test RunsTest Run

DurationSample

Points Comments Location2,3,7,8-TCDD Method 23 3 240 0 Diff Stack 1,2,3,7,8-PeCDD Method 23 3 240 0 Diff Stack 1,2,3,4,7,8-HxCDD Method 23 3 240 0 Diff Stack 1,2,3,6,7,8-HxCDD Method 23 3 240 0 Diff Stack Regulation Description Compound Limit Unit Title 42, Chapter 85, Subchapter I, Part A, Section 7414 0 Section 114 of the CAA 0



### Page 2 of 29

### Salisbury Plant 6

3/15/2011 1,2,3,7,8,9-HxCDD Method 23 3 240 0 Diff Stack 1,2,3,4,6,7,8-HpCDD Method 23 3 240 0 Diff Stack OCDD Method 23 3 240 0 Diff Stack 2,3,7,8-TCDF Method 23 3 240 0 Diff Stack 1,2,3,7,8-PeCDF Method 23 3 240 0 Diff Stack 2,3,4,7,8-PeCDF Method 23 3 240 0 Diff Stack 1,2,3,4,7,8-HxCDF Method 23 3 240 0DIFF Diff Stack 1,2,3,6,7,8-HxCDF Method 23 3 240 0DIFF Diff Stack 2,3,4,6,7,8-HxCDF Method 23 3 240 0DIFF Diff Stack 1,2,3,7,8,9-HxCDF Method 23 3 240 0DIFF Diff Stack 1,2,3,4,6,7,8-HpCDF Method 23 3 240 0DIFF Diff Stack 1,2,3,4,7,8,9-HpCDF Method 23 3 240 0DIFF Diff Stack OCDF Method 23 3 240 0DIFF Diff Stack Hydrogen Chloride Method 26A 3 60 0 Diff Stack Hydrogen Fluoride Method 26A 3 60 0 Diff Stack Chlorine Method 26A 3 60 0 Diff Stack Lead Method 29 3 60 0 Diff Stack Antimony Method 29 3 60 0 Diff Stack Zinc Method 29 3 60 0 Diff Stack Thallium Method 29 3 60 0 Diff Stack Silver Method 29 3 60 0 Diff Stack Cobalt Method 29 3 60 0 Diff Stack Filterable Particulate Method 29 3 60 0 Diff Stack Nickel Method 29 3 60 0 Diff Stack Magnesium Method 29 3 60 0 Diff Stack Manganese Method 29 3 60 0 Diff Stack Mercury Method 29 3 60 0 Diff Stack Selenium Method 29 3 60 0 Diff Stack Phosphorus (yellow or white)Method 29 3 60 0 Diff Stack Copper Method 29 3 60 0 Diff Stack Arsenic Method 29 3 60 0 Diff Stack Cadmium Method 29 3 60 0 Diff Stack Chromium Method 29 3 60 0 Diff Stack Barium Method 29 3 60 0 Diff Stack Beryllium Method 29 3 60 0 Diff Stack Filterable Particulate Method 5 3 60 0 DIFF Stack2,3,7,8-TCDD Method 23 3 240 0Dryer Dryer 1,2,3,7,8-PeCDD Method 23 3 240 0Dryer Dryer 1,2,3,4,7,8-HxCDD Method 23 3 240 0Dryer Dryer 1,2,3,6,7,8-HxCDD Method 23 3 240 0Dryer Dryer 1,2,3,7,8,9-HxCDD Method 23 3 240 0Dryer Dryer 1,2,3,4,6,7,8-HpCDD Method 23 3 240 0Dryer Dryer OCDD Method 23 3 240 0Dryer Dryer 2,3,7,8-TCDF Method 23 3 240 0Dryer Dryer 1,2,3,7,8-PeCDF Method 23 3 240 0Dryer Dryer 2,3,4,7,8-PeCDF Method 23 3 240 0Dryer Dryer 1,2,3,4,7,8-HxCDF Method 23 3 240 0Dryer Dryer 1,2,3,6,7,8-HxCDF Method 23 3 240 0Dryer Dryer 2,3,4,6,7,8-HxCDF Method 23 3 240 0Dryer Dryer 1,2,3,7,8,9-HxCDF Method 23 3 240 0Dryer Dryer 1,2,3,4,6,7,8-HpCDF Method 23 3 240 0Dryer Dryer 1,2,3,4,7,8,9-HpCDF Method 23 3 240 0Dryer Dryer



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### Salisbury Plant 6

3/15/2011

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. Methods 1-4, 26a (in combination w/ M5 - PM), 29, 23 - DIFF Methods 1-4, 23 - Dryer

OCDF Method 23 3 240 0Dryer Dryer



### Page 4 of 29

### Salisbury Plant 6

3/15/2011 Sampling / Stack Data Results Summary

LocationDiff Stack - Method 23 Average Run Number 1 2 2
Test Date 9/22/20109/23/2010 9/22/2010 Run Start Time
Run Finish Time Net Run Time, minutes 240 240 Dry Gas Meter Volume Sampled, dscf 173.777 175.433 174.605 Moisture Content of Stack Gas, % 4.76 5.61 5.185 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.000 Carbon Dioxide, % 1.73 1.63 1.680 Oxygen, % 18.86 19.05 18.955 Average Stack Gas Temperature, °F 381.00 386.00 Dry Volumetric Flow Rate, dry scfm 63,933.8 64,800.564,367.150 Actual Wet Volumetric Flue Gas Flow Rate, acfm 109,074.4 112,135.4110,604.900 Percent Isokinetic of Sampling Rate, % 96.8 96.4 96.600 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Page 5 of 29

### Salisbury Plant 6

3/15/2011

LocationDiff Stack - Method 23 3 Average Run Number 3
Test Date 9/22/2010 Run Start Time
Run Finish Time Net Run Time, minutes 240 Dry Gas Meter Volume Sampled, dscf 182.233 182.233 Moisture Content of Stack Gas, % 5.25 5.250 Moisture Saturation at Stack Gas Temperature, % 100.00 100.000 Carbon Dioxide, % 1.65 1.650 Oxygen, % 19.05 19.050 Average Stack Gas Temperature, °F 382.00 382.000 Dry Volumetric Flow Rate, dry scfm 64,364.8 64,364.800 Actual Wet Volumetric Flue Gas Flow Rate, acfm 110,546.4 110,546.400 Percent Isokinetic of Sampling Rate, % 100.9 100.900 F-Factor, dscfm/MMBtu @ %O2 0 0.000
Fw 0 0.000
Fc 0 0.000



### LocationDiff Stack - Method 26A Average Run Number 1 2 3
Test Date 9/21/20109/21/2010 9/21/2010 Run Start Time
Run Finish Time Net Run Time, minutes 60 60 60 Dry Gas Meter Volume Sampled, dscf 44.207 41.752 42.027 42.662 Moisture Content of Stack Gas, % 3.39 6.24 5.21 4.947 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 2.08 2.13 2.03 2.080 Oxygen, % 18.36 18.36 18.39 18.370 Average Stack Gas Temperature, °F 365.00 371.00 376.04 370.680 Dry Volumetric Flow Rate, dry scfm 65,261.5 61,961.0 62,403.863,208.767 Actual Wet Volumetric Flue Gas Flow Rate, acfm 107,672.4105,919.9 106,013.4106,535.233 Percent Isokinetic of Sampling Rate, % 96.5 96.0 96.0 96.167 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Page 6 of 29

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LocationDiff Stack - Method 29 Average Run Number 1 2 3
Test Date 9/21/20109/21/2010 9/21/2010 Run Start Time
Run Finish Time Net Run Time, minutes 60 60 60 Dry Gas Meter Volume Sampled, dscf 43.943 42.258 42.325 42.842 Moisture Content of Stack Gas, % 5.18 5.27 6.25 5.567 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 2.08 2.13 2.03 2.080 Oxygen, % 18.45 18.45 18.48 18.460 Average Stack Gas Temperature, °F 389.00 388.00 389.00 388.667 Dry Volumetric Flow Rate, dry scfm 62,697.8 62,611.4 62,041.262,450.133 Actual Wet Volumetric Flue Gas Flow Rate, acfm 108,093.0108,139.7 108,513.6108,248.767 Percent Isokinetic of Sampling Rate, % 99.9 96.2 97.2 97.767 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### LocationDIFF Stack - Method 5 Average Run Number 1 2 3
Test Date 9/21/20109/21/2010 9/21/2010 Run Start Time
Run Finish Time Net Run Time, minutes 60 60 60 Dry Gas Meter Volume Sampled, dscf 44.207 41.675 42.028 42.637 Moisture Content of Stack Gas, % 3.39 6.25 5.21 4.950 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 2.08 2.13 2.03 2.080 Oxygen, % 18.36 18.36 18.39 18.370 Average Stack Gas Temperature, °F 365.00 372.00 376.00 371.000 Dry Volumetric Flow Rate, dry scfm 65,261.5 61,920.9 62,406.863,196.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 107,672.4105,990.0 106,013.4106,558.600 Percent Isokinetic of Sampling Rate, % 96.5 95.9 96.0 96.133 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Page 7 of 29

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LocationDryer - Method 23 Average Run Number 1 2 3
Test Date 9/23/20109/23/2010 9/23/2010 Run Start Time
Run Finish Time Net Run Time, minutes 240 240 240 Dry Gas Meter Volume Sampled, dscf 161.568 158.915 158.652 159.712 Moisture Content of Stack Gas, % 3.60 3.74 3.88 3.740 Moisture Saturation at Stack Gas Temperature, % 12.75 12.73 13.06 12.847 Carbon Dioxide, % 0 0 0 0.000 Oxygen, % 20.9 20.9 20.9 20.900 Average Stack Gas Temperature, °F 123.00 123.00 124.00 123.333 Dry Volumetric Flow Rate, dry scfm 30,102.8 30,390.9 30,350.230,281.300 Actual Wet Volumetric Flue Gas Flow Rate, acfm 35,173.4 35,513.2 35,529.835,405.467 Percent Isokinetic of Sampling Rate, % 100.8 98.2 98.2 99.067 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Page 8 of 29

### Salisbury Plant 6

3/15/2011 Emissions Summary

Location:Diff Stack - Method 23 Compound:1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 2 Mass_mg 0.00000000763 0.00000000764 0.00000000764 7.64E-09 Eg/hr 1.68E-07 1.69E-07 1.69E-07 Elb/hr 3.71E-10 3.73E-10 3.72E-10 mg/dscm 1.55E-09 1.54E-09 1.55E-09 mg/dscm@7%O2 1.06E-08 1.16E-08 1.11E-08 

### Compound:1,2,3,4,6,7,8-HpCDF Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,7,8,9-HpCDF Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,7,8-HxCDD Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,7,8-HxCDF Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,6,7,8-HxCDD Average RunNumber Mass_mg #Error Eg/hr #Error



### Page 9 of 29

### Salisbury Plant 6

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Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,6,7,8-HxCDF Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,7,8,9-HxCDD Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm Diff Stack Diff Stack Diff Stack 0.00E+00 mg/dscm@7%O2 Method 23 Method 23 Method 23 0.00E+00 

### Compound:1,2,3,7,8,9-HxCDF Average RunNumber 1 2 2 Mass_mg 0.000000000957 0.000000000892 0.000000000892 9.14E-10 Eg/hr 2.11E-08 1.98E-08 2.05E-08 Elb/hr 4.66E-11 4.36E-11 4.51E-11 mg/dscm 1.95E-10 1.80E-10 1.88E-10 mg/dscm@7%O2 1.33E-09 1.35E-09 1.34E-09 

### Compound:1,2,3,7,8-PeCDD Average RunNumber 1 2 2 Mass_mg 0.00000000143 0.00000000132 0.00000000132 1.36E-09 Eg/hr 3.16E-08 2.93E-08 3.05E-08 Elb/hr 6.96E-11 6.45E-11 6.71E-11 mg/dscm 2.91E-10 2.66E-10 2.79E-10 mg/dscm@7%O2 1.98E-09 2.00E-09 1.99E-09 

### Compound:1,2,3,7,8-PeCDF Average RunNumber 1 2 2 Mass_mg 0.00000000385 0.00000000268 0.00000000268 3.07E-09 Eg/hr 8.50E-08 5.94E-08 7.22E-08 Elb/hr 1.87E-10 1.31E-10 1.59E-10 mg/dscm 7.83E-10 5.40E-10 6.62E-10 mg/dscm@7%O2 5.34E-09 4.06E-09 4.70E-09 

### Compound:2,3,4,6,7,8-HxCDF Average RunNumber 1 2 2 Mass_mg 0.00000000142 0.000000000934 0.000000000934 1.10E-09 Eg/hr 3.13E-08 2.07E-08 2.60E-08



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### Salisbury Plant 6

3/15/2011
Elb/hr 6.91E-11 4.56E-11 5.74E-11 mg/dscm 2.89E-10 1.88E-10 2.39E-10 mg/dscm@7%O2 1.97E-09 1.41E-09 1.69E-09 

### Compound:2,3,4,7,8-PeCDF Average RunNumber 1 2 2 Mass_mg 0.00000000342 0.00000000258 0.00000000258 2.86E-09 Eg/hr 7.55E-08 5.72E-08 6.64E-08 Elb/hr 1.66E-10 1.26E-10 1.46E-10 mg/dscm 6.95E-10 5.19E-10 6.07E-10 mg/dscm@7%O2 4.74E-09 3.90E-09 4.32E-09 

### Compound:2,3,7,8-TCDD Average RunNumber 1 2 2 Mass_mg 0.00000000154 0.00000000111 0.00000000111 1.25E-09 Eg/hr 3.40E-08 2.46E-08 2.93E-08 Elb/hr 7.49E-11 5.42E-11 6.46E-11 mg/dscm 3.13E-10 2.23E-10 2.68E-10 mg/dscm@7%O2 2.13E-09 1.68E-09 1.91E-09 

### Compound:2,3,7,8-TCDF Average RunNumber 1 2 2 Mass_mg 0.0000000141 0.00000000928 0.00000000928 1.09E-08 Eg/hr 3.11E-07 2.06E-07 2.59E-07 Elb/hr 6.86E-10 4.53E-10 5.70E-10 mg/dscm 2.87E-09 1.87E-09 2.37E-09 mg/dscm@7%O2 1.96E-08 1.41E-08 1.69E-08 

### Compound:OCDD Average RunNumber 1 2 2 Mass_mg 0.0000000823 0.0000000631 0.0000000631 6.95E-08 Eg/hr 1.82E-06 1.40E-06 1.61E-06 Elb/hr 4.01E-09 3.08E-09 3.55E-09 mg/dscm 1.67E-08 1.27E-08 1.47E-08 mg/dscm@7%O2 1.14E-07 9.54E-08 1.05E-07 

### Compound:OCDF Average RunNumber 1 2 2 Mass_mg 0.00000000454 0.00000000368 0.00000000368 3.97E-09 Eg/hr 1.00E-07 8.16E-08 9.08E-08 Elb/hr 2.21E-10 1.80E-10 2.01E-10 mg/dscm 9.23E-10 7.41E-10 8.32E-10 mg/dscm@7%O2 6.29E-09 5.57E-09 5.93E-09



### Location:Diff Stack - Method 23 3 Compound:1,2,3,4,6,7,8-HpCDD Average RunNumber



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### Salisbury Plant 6

3/15/2011 Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,6,7,8-HpCDF Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,7,8,9-HpCDF Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,7,8-HxCDD Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,7,8-HxCDF Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,6,7,8-HxCDD Average RunNumber Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,6,7,8-HxCDF Average RunNumber



### Page 12 of 29

### Salisbury Plant 6

3/15/2011 Mass_mg #Error Eg/hr #Error Elb/hr #Error mg/dscm #Error mg/dscm@7%O2 #Error 

### Compound:1,2,3,7,8,9-HxCDD Average RunNumber 2 2 3 Mass_mg 0 0 0.00000000276 9.20E-10 Eg/hr 0.00E+00 5.85E-08 2.93E-08 Elb/hr 0.00E+00 1.29E-10 6.45E-11 mg/dscm 0.00E+00 5.35E-10 2.68E-10 mg/dscm@7%O2 0.00E+00 4.02E-09 2.01E-09 

### Compound:1,2,3,7,8,9-HxCDF Average RunNumber 2 2 3 Mass_mg 0 0 0.00000000105 3.50E-10 Eg/hr 0.00E+00 2.23E-08 1.12E-08 Elb/hr 0.00E+00 4.91E-11 2.46E-11 mg/dscm 0.00E+00 2.04E-10 1.02E-10 mg/dscm@7%O2 0.00E+00 1.53E-09 7.65E-10 

### Compound:1,2,3,7,8-PeCDD Average RunNumber 2 2 3 Mass_mg 0 0 0.00000000131 4.37E-10 Eg/hr 0.00E+00 2.78E-08 1.39E-08 Elb/hr 0.00E+00 6.12E-11 3.06E-11 mg/dscm 0.00E+00 2.54E-10 1.27E-10 mg/dscm@7%O2 0.00E+00 1.91E-09 9.55E-10 

### Compound:1,2,3,7,8-PeCDF Average RunNumber 2 2 3 Mass_mg 0 0 0.00000000312 1.04E-09 Eg/hr 0.00E+00 6.61E-08 3.31E-08 Elb/hr 0.00E+00 1.46E-10 7.30E-11 mg/dscm 0.00E+00 6.05E-10 3.03E-10 mg/dscm@7%O2 0.00E+00 4.55E-09 2.28E-09 

### Compound:2,3,4,6,7,8-HxCDF Average RunNumber 2 2 3 Mass_mg 0 0 0.00000000189 6.30E-10 Eg/hr 0.00E+00 4.01E-08 2.01E-08 Elb/hr 0.00E+00 8.83E-11 4.42E-11 mg/dscm 0.00E+00 3.66E-10 1.83E-10 mg/dscm@7%O2 0.00E+00 2.75E-09 1.38E-09 

### Compound:2,3,4,7,8-PeCDF Average RunNumber 2 2 3



### Page 13 of 29

### Salisbury Plant 6

3/15/2011 Mass_mg 0 0 0.00000000401 1.34E-09 Eg/hr 0.00E+00 8.50E-08 4.25E-08 Elb/hr 0.00E+00 1.87E-10 9.35E-11 mg/dscm 0.00E+00 7.77E-10 3.89E-10 mg/dscm@7%O2 0.00E+00 5.84E-09 2.92E-09 

### Compound:2,3,7,8-TCDD Average RunNumber 2 2 3 Mass_mg 0 0 0.00000000141 4.70E-10 Eg/hr 0.00E+00 2.99E-08 1.50E-08 Elb/hr 0.00E+00 6.59E-11 3.30E-11 mg/dscm 0.00E+00 2.73E-10 1.37E-10 mg/dscm@7%O2 0.00E+00 2.05E-09 1.03E-09 

### Compound:2,3,7,8-TCDF Average RunNumber 2 2 3 Mass_mg 0 0 0.00000000741 2.47E-09 Eg/hr 0.00E+00 1.57E-07 7.85E-08 Elb/hr 0.00E+00 3.46E-10 1.73E-10 mg/dscm 0.00E+00 1.44E-09 7.20E-10 mg/dscm@7%O2 0.00E+00 1.08E-08 5.40E-09 

### Compound:OCDD Average RunNumber 2 2 3 Mass_mg 0 0 0.0000000443 1.48E-08 Eg/hr 0.00E+00 9.39E-07 4.70E-07 Elb/hr 0.00E+00 2.07E-09 1.04E-09 mg/dscm 0.00E+00 8.59E-09 4.30E-09 mg/dscm@7%O2 0.00E+00 6.45E-08 3.23E-08 

### Compound:OCDF Average RunNumber 2 2 3 Mass_mg 0 0 0.00000000611 2.04E-09 Eg/hr 0.00E+00 1.29E-07 6.45E-08 Elb/hr 0.00E+00 2.85E-10 1.43E-10 mg/dscm 0.00E+00 1.18E-09 5.90E-10 mg/dscm@7%O2 0.00E+00 8.87E-09 4.44E-09



### Location:Diff Stack - Method 26A Compound:Chlorine Average RunNumber 1 2 3 Mass_mg 134.8 0 6.4 4.71E+01 Eg/hr 1.19E+04 0.00E+00 5.70E+02 4.16E+03 Elb/hr 2.63E+01 0.00E+00 1.26E+00 9.19E+00 ppm 3.65E+01 0.00E+00 1.82E+00 1.28E+01 ppm@7%O2 2.00E+02 0.00E+00 1.01E+01 7.00E+01



### Page 14 of 29

### Salisbury Plant 6

3/15/2011 Compound:Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 0.3 0.3 0.2 2.67E-01 Eg/hr 2.66E+01 2.67E+01 1.78E+01 2.37E+01 Elb/hr 5.86E-02 5.89E-02 3.93E-02 5.23E-02 ppm 1.58E-01 1.67E-01 1.11E-01 1.45E-01 ppm@7%O2 8.65E-01 9.14E-01 6.15E-01 7.98E-01 

### Compound:Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 28700 0 0 9.57E+03 Eg/hr 2.54E+06 0.00E+00 0.00E+00 8.47E+05 Elb/hr 5.60E+03 0.00E+00 0.00E+00 1.87E+03 ppm 2.76E+04 0.00E+00 0.00E+00 9.20E+03 ppm@7%O2 1.51E+05 0.00E+00 0.00E+00 5.03E+04



### Location:Diff Stack - Method 29 Compound:Antimony Average RunNumber 1 2 3 Mass_mg 0.0024 0.0025 0.0024 2.43E-03 Eg/hr 2.05E-01 2.22E-01 2.11E-01 2.13E-01 Elb/hr 4.53E-04 4.90E-04 4.65E-04 4.69E-04 mg/dscm 1.93E-03 2.09E-03 2.00E-03 2.01E-03 mg/dscm@7%O2 1.09E-02 1.19E-02 1.15E-02 1.14E-02 

### Compound:Arsenic Average RunNumber 1 2 3 Mass_mg 0.0001 0.0013 0.0012 8.67E-04 Eg/hr 8.56E-03 1.16E-01 1.06E-01 7.69E-02 Elb/hr 1.89E-05 2.55E-04 2.33E-04 1.69E-04 mg/dscm 8.04E-05 1.09E-03 1.00E-03 7.23E-04 mg/dscm@7%O2 4.56E-04 6.18E-03 5.74E-03 4.13E-03 

### Compound:Barium Average RunNumber 1 2 3 Mass_mg 0.0159 0.0064 0.0089 1.04E-02 Eg/hr 1.36E+00 5.69E-01 7.83E-01 9.04E-01 Elb/hr 3.00E-03 1.25E-03 1.73E-03 1.99E-03 mg/dscm 1.28E-02 5.35E-03 7.43E-03 8.53E-03 mg/dscm@7%O2 7.26E-02 3.04E-02 4.27E-02 4.86E-02 

### Compound:Beryllium Average RunNumber 1 2 3 Mass_mg 0.00012 0.00013 0.00012 1.23E-04 Eg/hr 1.03E-02 1.16E-02 1.06E-02 1.08E-02 Elb/hr 2.26E-05 2.55E-05 2.33E-05 2.38E-05 mg/dscm 9.65E-05 1.09E-04 1.00E-04 1.02E-04



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### Salisbury Plant 6

3/15/2011 mg/dscm@7%O2 5.47E-04 6.18E-04 5.74E-04 5.80E-04 

### Compound:Cadmium Average RunNumber 1 2 3 Mass_mg 0.00073 0.00075 0.00071 7.30E-04 Eg/hr 6.25E-02 6.67E-02 6.24E-02 6.39E-02 Elb/hr 1.38E-04 1.47E-04 1.38E-04 1.41E-04 mg/dscm 5.87E-04 6.27E-04 5.92E-04 6.02E-04 mg/dscm@7%O2 3.33E-03 3.56E-03 3.40E-03 3.43E-03 

### Compound:Chromium Average RunNumber 1 2 3 Mass_mg 0.0047 0.0021 0.0021 2.97E-03 Eg/hr 4.02E-01 1.87E-01 1.85E-01 2.58E-01 Elb/hr 8.87E-04 4.12E-04 4.07E-04 5.69E-04 mg/dscm 3.78E-03 1.76E-03 1.75E-03 2.43E-03 mg/dscm@7%O2 2.14E-02 9.99E-03 1.01E-02 1.38E-02 

### Compound:Cobalt Average RunNumber 1 2 3 Mass_mg 0.0007 0.0008 0.0007 7.33E-04 Eg/hr 5.99E-02 7.11E-02 6.16E-02 6.42E-02 Elb/hr 1.32E-04 1.57E-04 1.36E-04 1.42E-04 mg/dscm 5.63E-04 6.69E-04 5.84E-04 6.05E-04 mg/dscm@7%O2 3.19E-03 3.80E-03 3.35E-03 3.45E-03 

### Compound:Copper Average RunNumber 1 2 3 Mass_mg 0.0014 0.0018 0.002 1.73E-03 Eg/hr 1.20E-01 1.60E-01 1.76E-01 1.52E-01 Elb/hr 2.64E-04 3.53E-04 3.88E-04 3.35E-04 mg/dscm 1.13E-03 1.50E-03 1.67E-03 1.43E-03 mg/dscm@7%O2 6.41E-03 8.51E-03 9.59E-03 8.17E-03 

### Compound:Filterable Particulate Average RunNumber 1 2 3 Mass_mg 0 0.00E+00 Eg/hr 0.00E+00 0.00E+00 Elb/hr 0.00E+00 0.00E+00 mg/dscm 0.00E+00 0.00E+00 mg/dscm@7%O2 0.00E+00 0.00E+00 

### Compound:Lead Average RunNumber 1 2 3 Mass_mg 0.0012 0.0013 0.0012 1.23E-03 Eg/hr 1.03E-01 1.16E-01 1.06E-01 1.08E-01 Elb/hr 2.26E-04 2.55E-04 2.33E-04 2.38E-04 mg/dscm 9.65E-04 1.09E-03 1.00E-03 1.02E-03



### Page 16 of 29

### Salisbury Plant 6

3/15/2011 mg/dscm@7%O2 5.47E-03 6.18E-03 5.74E-03 5.80E-03 

### Compound:Magnesium Average RunNumber 1 2 3 Mass_mg 0.0161 0.0188 0.0181 1.77E-02 Eg/hr 1.38E+00 1.67E+00 1.59E+00 1.55E+00 Elb/hr 3.04E-03 3.68E-03 3.51E-03 3.41E-03 mg/dscm 1.29E-02 1.57E-02 1.51E-02 1.46E-02 mg/dscm@7%O2 7.32E-02 8.91E-02 8.67E-02 8.30E-02 

### Compound:Manganese Average RunNumber 1 2 3 Mass_mg 0.003 0.0035 0.0129 6.47E-03 Eg/hr 2.57E-01 3.11E-01 1.13E+00 5.66E-01 Elb/hr 5.66E-04 6.86E-04 2.50E-03 1.25E-03 mg/dscm 2.41E-03 2.93E-03 1.08E-02 5.38E-03 mg/dscm@7%O2 1.37E-02 1.66E-02 6.20E-02 3.08E-02 

### Compound:Mercury Average RunNumber 1 2 3 Mass_mg 0.0034 0.0033 0.0036 3.43E-03 Eg/hr 2.91E-01 2.93E-01 3.17E-01 3.00E-01 Elb/hr 6.42E-04 6.47E-04 6.98E-04 6.62E-04 mg/dscm 2.73E-03 2.76E-03 3.00E-03 2.83E-03 mg/dscm@7%O2 1.55E-02 1.57E-02 1.72E-02 1.61E-02 

### Compound:Nickel Average RunNumber 1 2 3 Mass_mg 0.017 0.0027 0.0022 7.30E-03 Eg/hr 1.46E+00 2.40E-01 1.93E-01 6.31E-01 Elb/hr 3.21E-03 5.29E-04 4.27E-04 1.39E-03 mg/dscm 1.37E-02 2.26E-03 1.84E-03 5.93E-03 mg/dscm@7%O2 7.77E-02 1.28E-02 1.06E-02 3.37E-02 

### Compound:Phosphorus (yellow or white) Average RunNumber 1 2 3 Mass_mg 0.0369 0.0348 0.0388 3.68E-02 Eg/hr 3.16E+00 3.09E+00 3.41E+00 3.22E+00 Elb/hr 6.96E-03 6.82E-03 7.52E-03 7.10E-03 mg/dscm 2.97E-02 2.91E-02 3.24E-02 3.04E-02 mg/dscm@7%O2 1.69E-01 1.65E-01 1.86E-01 1.73E-01 

### Compound:Selenium Average RunNumber 1 2 3 Mass_mg 0.0029 0.0025 0.0024 2.60E-03 Eg/hr 2.48E-01 2.22E-01 2.11E-01 2.27E-01 Elb/hr 5.47E-04 4.90E-04 4.65E-04 5.01E-04 mg/dscm 2.33E-03 2.09E-03 2.00E-03 2.14E-03



### Page 17 of 29

### Salisbury Plant 6

3/15/2011 mg/dscm@7%O2 1.32E-02 1.19E-02 1.15E-02 1.22E-02 

### Compound:Silver Average RunNumber 1 2 3 Mass_mg 0.0012 0.0013 0.0012 1.23E-03 Eg/hr 1.03E-01 1.16E-01 1.06E-01 1.08E-01 Elb/hr 2.26E-04 2.55E-04 2.33E-04 2.38E-04 mg/dscm 9.65E-04 1.09E-03 1.00E-03 1.02E-03 mg/dscm@7%O2 5.47E-03 6.18E-03 5.74E-03 5.80E-03 

### Compound:Thallium Average RunNumber 1 2 3 Mass_mg 0.0012 0.0013 0.0012 1.23E-03 Eg/hr 1.03E-01 1.16E-01 1.06E-01 1.08E-01 Elb/hr 2.26E-04 2.55E-04 2.33E-04 2.38E-04 mg/dscm 9.65E-04 1.09E-03 1.00E-03 1.02E-03 mg/dscm@7%O2 5.47E-03 6.18E-03 5.74E-03 5.80E-03 

### Compound:Zinc Average RunNumber 1 2 3 Mass_mg 0.005 0.0064 0.0068 6.07E-03 Eg/hr 4.28E-01 5.69E-01 5.98E-01 5.32E-01 Elb/hr 9.44E-04 1.25E-03 1.32E-03 1.17E-03 mg/dscm 4.02E-03 5.35E-03 5.67E-03 5.01E-03 mg/dscm@7%O2 2.28E-02 3.04E-02 3.26E-02 2.86E-02



### Location:DIFF Stack - Method 5 

### Compound:Filterable Particulate Average RunNumber 1 2 3 Mass_mg 1.6 0 1 8.67E-01 Eg/hr 1.42E+02 0.00E+00 8.91E+01 7.70E+01 Elb/hr 3.12E-01 0.00E+00 1.96E-01 1.69E-01 mg/dscm 1.28E+00 0.00E+00 8.40E-01 7.07E-01 mg/dscm@7%O2 7.00E+00 0.00E+00 4.65E+00 3.88E+00



### Location:Dryer - Method 23 Compound:1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.00000000553 0.00000000968 0.00000000945 8.22E-09 Eg/hr 6.18E-08 1.11E-07 1.08E-07 9.36E-08 Elb/hr 1.36E-10 2.45E-10 2.39E-10 2.07E-10 mg/dscm 1.21E-09 2.15E-09 2.10E-09 1.82E-09 mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.00000000145 0.00000000439 0.00000000353 3.12E-09



### Page 18 of 29

### Salisbury Plant 6

3/15/2011 Eg/hr 1.62E-08 5.04E-08 4.05E-08 3.57E-08 Elb/hr 3.57E-11 1.11E-10 8.93E-11 7.87E-11 mg/dscm 3.17E-10 9.76E-10 7.86E-10 6.93E-10 mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.00000000214 0.00000000166 0.00000000218 1.99E-09 Eg/hr 2.39E-08 1.90E-08 2.50E-08 2.26E-08 Elb/hr 5.27E-11 4.20E-11 5.52E-11 5.00E-11 mg/dscm 4.68E-10 3.69E-10 4.85E-10 4.41E-10 mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.00000000212 0.00000000178 0.00000000218 2.03E-09 Eg/hr 2.37E-08 2.04E-08 2.50E-08 2.30E-08 Elb/hr 5.22E-11 4.50E-11 5.52E-11 5.08E-11 mg/dscm 4.63E-10 3.96E-10 4.85E-10 4.48E-10 mg/dscm@7%O2 #Error 

### Compound:1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000136 0.00000000163 0.00000000136 1.45E-09 Eg/hr 1.52E-08 1.87E-08 1.56E-08 1.65E-08 Elb/hr 3.35E-11 4.12E-11 3.44E-11 3.64E-11 mg/dscm 2.97E-10 3.62E-10 3.03E-10 3.21E-10 mg/dscm@7%O2 #Error 

### Compound:1,2,3,6,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.00000000213 0.00000000181 0.00000000207 2.00E-09 Eg/hr 2.38E-08 2.08E-08 2.38E-08 2.28E-08 Elb/hr 5.25E-11 4.58E-11 5.24E-11 5.02E-11 mg/dscm 4.66E-10 4.02E-10 4.61E-10 4.43E-10 mg/dscm@7%O2 #Error 

### Compound:1,2,3,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000128 0.00000000165 0.00000000132 1.42E-09 Eg/hr 1.43E-08 1.89E-08 1.52E-08 1.61E-08 Elb/hr 3.15E-11 4.17E-11 3.34E-11 3.55E-11 mg/dscm 2.80E-10 3.67E-10 2.94E-10 3.14E-10 mg/dscm@7%O2 #Error 

### Compound:1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.00000000221 0.00000000195 0.00000000227 2.14E-09



### Page 19 of 29

### Salisbury Plant 6

3/15/2011 Eg/hr 2.47E-08 2.24E-08 2.61E-08 2.44E-08 Elb/hr 5.45E-11 4.93E-11 5.74E-11 5.37E-11 mg/dscm 4.83E-10 4.33E-10 5.05E-10 4.74E-10 mg/dscm@7%O2 #Error 

### Compound:1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000184 0.00000000123 0.00000000184 1.64E-09 Eg/hr 2.06E-08 1.41E-08 2.11E-08 1.86E-08 Elb/hr 4.53E-11 3.11E-11 4.66E-11 4.10E-11 mg/dscm 4.02E-10 2.73E-10 4.10E-10 3.62E-10 mg/dscm@7%O2 #Error 

### Compound:1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.00000000195 0.0000000024 0.00000000278 2.38E-09 Eg/hr 2.18E-08 2.75E-08 3.19E-08 2.71E-08 Elb/hr 4.81E-11 6.07E-11 7.03E-11 5.97E-11 mg/dscm 4.26E-10 5.33E-10 6.19E-10 5.26E-10 mg/dscm@7%O2 #Error 

### Compound:1,2,3,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.00000000153 0.00000000142 0.00000000146 1.47E-09 Eg/hr 1.71E-08 1.63E-08 1.68E-08 1.67E-08 Elb/hr 3.77E-11 3.59E-11 3.69E-11 3.68E-11 mg/dscm 3.34E-10 3.16E-10 3.25E-10 3.25E-10 mg/dscm@7%O2 #Error 

### Compound:2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000012 0.000000000933 0.00000000137 1.17E-09 Eg/hr 1.34E-08 1.07E-08 1.57E-08 1.33E-08 Elb/hr 2.96E-11 2.36E-11 3.47E-11 2.93E-11 mg/dscm 2.62E-10 2.07E-10 3.05E-10 2.58E-10 mg/dscm@7%O2 #Error 

### Compound:2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.00000000141 0.00000000131 0.00000000131 1.34E-09 Eg/hr 1.58E-08 1.50E-08 1.50E-08 1.53E-08 Elb/hr 3.48E-11 3.31E-11 3.31E-11 3.37E-11 mg/dscm 3.08E-10 2.91E-10 2.92E-10 2.97E-10 mg/dscm@7%O2 #Error 

### Compound:2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.00000000204 0.00000000186 0.00000000246 2.12E-09



### Page 20 of 29

### Salisbury Plant 6

3/15/2011 Eg/hr 2.28E-08 2.13E-08 2.82E-08 2.41E-08 Elb/hr 5.03E-11 4.71E-11 6.22E-11 5.32E-11 mg/dscm 4.46E-10 4.13E-10 5.48E-10 4.69E-10 mg/dscm@7%O2 #Error 

### Compound:2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.00000000136 0.00000000147 0.00000000148 1.44E-09 Eg/hr 1.52E-08 1.69E-08 1.70E-08 1.64E-08 Elb/hr 3.35E-11 3.72E-11 3.75E-11 3.61E-11 mg/dscm 2.97E-10 3.27E-10 3.29E-10 3.18E-10 mg/dscm@7%O2 #Error 

### Compound:OCDD Average RunNumber 1 2 3 Mass_mg 0.0000000346 0.0000000492 0.0000000449 4.29E-08 Eg/hr 3.87E-07 5.65E-07 5.15E-07 4.89E-07 Elb/hr 8.53E-10 1.24E-09 1.14E-09 1.08E-09 mg/dscm 7.56E-09 1.09E-08 1.00E-08 9.49E-09 mg/dscm@7%O2 #Error 

### Compound:OCDF Average RunNumber 1 2 3 Mass_mg 0.0000000039 0.00000000257 0.00000000254 3.00E-09 Eg/hr 4.36E-08 2.95E-08 2.92E-08 3.41E-08 Elb/hr 9.61E-11 6.50E-11 6.43E-11 7.51E-11 mg/dscm 8.53E-10 5.71E-10 5.65E-10 6.63E-10 mg/dscm@7%O2 #Error



### Page 21 of 29

### Salisbury Plant 6

3/15/2011 Process Run Data

APCD Run Data

Process Lab Run Data Run Name Value UOM Comments Target Value 1Brick Production 20.26 tons/hr 20
1Lime Feed 240 lbs/hr 240



### Run Name Value UOM Comments Target Value 1Dry Sorbent Injection/Fabric Filter 0 0

Page 22 of 29

### Salisbury Plant 6

3/15/2011 Sampling / Stack Data Results Detail

LocationDiff Stack - Method 23 Average Run Number 1 2 2 Test Date 9/22/2010 9/23/2010 9/22/2010 Run Start Time Run Finish Time Net Traversing Points 2 1 2 Net Run Time, minutes 240 240 Nozzle Diameter, inches 0.289 0.289 0.289 Pitot Tube Coefficient 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.995 0.995 0.995 Barometric Pressure, inches of Mercury 29.31 29.33 29.320 Average Orifice Meter Differential, inches H2O 2.00 2.18 Dry Gas Meter Volume Sampled, cubic feet 184.450 0.000 191.080 125.177 Average Dry Gas Meter Temperature, °F 89.00 104.00 Dry Gas Meter Volume Sampled, dscf 173.777 175.433 174.605 Total Moisture Liquid collected, g 184.3 0 221.6 135.300 Volume of Water Vapor, standard cubic feet 8.68 0.00 10.43 6.370 Moisture Content of Stack Gas, % 4.76 5.61 5.185 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.000 Dry Mole Fraction 0.9524 0.9439 0.948 Carbon Dioxide, % 1.73 1.63 1.680 Oxygen, % 18.86 19.05 18.955 Carbon Monoxide & Nitrogen, % 79.41 79.32 79.365 Fuel Factor 1.18 1.13 Dry Molecular Weight, lb/lb-Mole 29.03 29.02 Wet Molecular weight, lb/lb-Mole 28.50 28.40 28.450 Flue Gas Static Pressure, inches of H2O 0.25 0.25 0.250 Absolute Flue Gas Pressure, inches of Mercury 29.33 29.35 Average Stack Gas Temperature, °F 381.00 386.00 Average Velocity Head, inches of H2O 0.42 0.44 0.430 Average Stack Gas Velocity, feet/second 46.68 47.99 47.335 Stack Cross-Sectional Area, square feet 38.944 38.944 38.944 38.944 Dry Volumetric Flow Rate, dry scfm 63,933.8 64,800.564,367.150 Actual Wet Volumetric Flue Gas Flow Rate, acfm 109,074.4 112,135.4110,604.900 Percent Isokinetic of Sampling Rate, % 96.8 96.4 96.600 Percent Excess Air, % 896.3 1,007.7 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Round Duct Diameter, inches 84.5 84.5 84.5 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



### Page 23 of 29

### Salisbury Plant 6

3/15/2011

LocationDiff Stack - Method 23 3 Average Run Number 3 Test Date 9/22/2010 Run Start Time Run Finish Time Net Traversing Points 2 Net Run Time, minutes 240 Nozzle Diameter, inches 0.289 0.289 Pitot Tube Coefficient 0.84 0.840 Dry Gas Meter Calibration Factor 0.995 0.995 Barometric Pressure, inches of Mercury 29.3 29.300 Average Orifice Meter Differential, inches H2O 2.15 2.150 Dry Gas Meter Volume Sampled, cubic feet 196.590 196.590 Average Dry Gas Meter Temperature, °F 98.00 98.000 Dry Gas Meter Volume Sampled, dscf 182.233 182.233 Total Moisture Liquid collected, g 214.5 214.500 Volume of Water Vapor, standard cubic feet 10.10 10.100 Moisture Content of Stack Gas, % 5.25 5.250 Moisture Saturation at Stack Gas Temperature, % 100.00 100.000 Dry Mole Fraction 0.9475 0.948 Carbon Dioxide, % 1.65 1.650 Oxygen, % 19.05 19.050 Carbon Monoxide & Nitrogen, % 79.3 79.300 Fuel Factor 1.12 Dry Molecular Weight, lb/lb-Mole 29.03 29.030 Wet Molecular weight, lb/lb-Mole 28.45 28.450 Flue Gas Static Pressure, inches of H2O 0.25 0.250 Absolute Flue Gas Pressure, inches of Mercury 29.32 29.320 Average Stack Gas Temperature, °F 382.00 382.000 Average Velocity Head, inches of H2O 0.43 0.430 Average Stack Gas Velocity, feet/second 47.31 47.310 Stack Cross-Sectional Area, square feet 38.944 38.944 Dry Volumetric Flow Rate, dry scfm 64,364.8 64,364.800 Actual Wet Volumetric Flue Gas Flow Rate, acfm 110,546.4 110,546.400 Percent Isokinetic of Sampling Rate, % 100.9 100.900 Percent Excess Air, % 1,010.5 1,010.500 F-Factor, dscfm/MMBtu @ %O2 0 0.000 Round Duct Diameter, inches 84.5 Rectangular Duct Width, inches 0 Rectangular Duct Length, inches 0 Fw 0 0.000 Fc 0 0.000



### Page 24 of 29

### Salisbury Plant 6

3/15/2011

LocationDiff Stack - Method 26A Average Run Number 1 2 3 Test Date 9/21/2010 9/21/2010 9/21/2010 Run Start Time Run Finish Time Net Traversing Points 2 2 2 Net Run Time, minutes 60 60 60 Nozzle Diameter, inches 0.289 0.289 0.289 0.289 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.995 0.995 0.995 0.995 Barometric Pressure, inches of Mercury 29.31 29.36 29.4 29.357 Average Orifice Meter Differential, inches H2O 2.05 1.99 2.00 2.013 Dry Gas Meter Volume Sampled, cubic feet 45.720 43.920 45.120 44.920 Average Dry Gas Meter Temperature, °F 75.00 85.00 97.00 85.667 Dry Gas Meter Volume Sampled, dscf 44.207 41.752 42.027 42.662 Total Moisture Liquid collected, g 33 59 49 47.000 Volume of Water Vapor, standard cubic feet 1.55 2.78 2.31 2.213 Moisture Content of Stack Gas, % 3.39 6.24 5.21 4.947 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9661 0.9376 0.9479 0.951 Carbon Dioxide, % 2.08 2.13 2.03 2.080 Oxygen, % 18.36 18.36 18.39 18.370 Carbon Monoxide & Nitrogen, % 79.56 79.51 79.58 79.550 Fuel Factor 1.22 1.19 1.24 Dry Molecular Weight, lb/lb-Mole 29.07 29.08 29.06 29.070 Wet Molecular weight, lb/lb-Mole 28.69 28.39 28.48 28.520 Flue Gas Static Pressure, inches of H2O 0.25 0.25 0.25 0.250 Absolute Flue Gas Pressure, inches of Mercury 29.33 29.38 29.42 29.377 Average Stack Gas Temperature, °F 365.00 371.00 376.04 370.680 Average Velocity Head, inches of H2O 0.42 0.4 0.4 0.407 Average Stack Gas Velocity, feet/second 46.08 45.33 45.37 45.593 Stack Cross-Sectional Area, square feet 38.944 38.944 38.944 38.944 Dry Volumetric Flow Rate, dry scfm 65,261.5 61,961.0 62,403.863,208.767 Actual Wet Volumetric Flue Gas Flow Rate, acfm 107,672.4 105,919.9 106,013.4106,535.233 Percent Isokinetic of Sampling Rate, % 96.5 96.0 96.0 96.167 Percent Excess Air, % 694.4 697.9 702.1 698.133 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Round Duct Diameter, inches 84.5 84.5 84.5 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



### Page 25 of 29

### Salisbury Plant 6

3/15/2011

LocationDiff Stack - Method 29 Average Run Number 1 2 3 Test Date 9/21/2010 9/21/2010 9/21/2010 Run Start Time Run Finish Time Net Traversing Points 2 2 2 Net Run Time, minutes 60 60 60 Nozzle Diameter, inches 0.289 0.289 0.289 0.289 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.995 0.995 0.995 0.995 Barometric Pressure, inches of Mercury 29.41 29.35 29.32 29.360 Average Orifice Meter Differential, inches H2O 2.00 2.00 2.01 2.003 Dry Gas Meter Volume Sampled, cubic feet 47.500 46.180 45.890 46.523 Average Dry Gas Meter Temperature, °F 101.00 106.00 101.00 102.667 Dry Gas Meter Volume Sampled, dscf 43.943 42.258 42.325 42.842 Total Moisture Liquid collected, g 51 50 60 53.667 Volume of Water Vapor, standard cubic feet 2.40 2.35 2.82 2.523 Moisture Content of Stack Gas, % 5.18 5.27 6.25 5.567 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9482 0.9473 0.9375 0.944 Carbon Dioxide, % 2.08 2.13 2.03 2.080 Oxygen, % 18.45 18.45 18.48 18.460 Carbon Monoxide & Nitrogen, % 79.47 79.42 79.49 79.460 Fuel Factor 1.18 1.15 1.19 Dry Molecular Weight, lb/lb-Mole 29.07 29.08 29.06 29.070 Wet Molecular weight, lb/lb-Mole 28.50 28.50 28.37 28.457 Flue Gas Static Pressure, inches of H2O 0.25 0.25 0.25 0.250 Absolute Flue Gas Pressure, inches of Mercury 29.43 29.37 29.34 29.380 Average Stack Gas Temperature, °F 389.00 388.00 389.00 388.667 Average Velocity Head, inches of H2O 0.41 0.41 0.41 0.410 Average Stack Gas Velocity, feet/second 46.26 46.28 46.44 46.327 Stack Cross-Sectional Area, square feet 38.944 38.944 38.944 38.944 Dry Volumetric Flow Rate, dry scfm 62,697.8 62,611.4 62,041.262,450.133 Actual Wet Volumetric Flue Gas Flow Rate, acfm 108,093.0 108,139.7 108,513.6108,248.767 Percent Isokinetic of Sampling Rate, % 99.9 96.2 97.2 97.767 Percent Excess Air, % 729.2 733.1 737.6 733.300 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Round Duct Diameter, inches 84.5 84.5 84.5 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



### Page 26 of 29

### Salisbury Plant 6

3/15/2011

LocationDIFF Stack - Method 5 Average Run Number 1 2 3 Test Date 9/21/2010 9/21/2010 9/21/2010 Run Start Time Run Finish Time Net Traversing Points 2 2 2 Net Run Time, minutes 60 60 60 Nozzle Diameter, inches 0.289 0.289 0.289 0.289 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.995 0.995 0.995 0.995 Barometric Pressure, inches of Mercury 29.31 29.36 29.4 29.357 Average Orifice Meter Differential, inches H2O 2.05 1.99 2.01 2.017 Dry Gas Meter Volume Sampled, cubic feet 45.720 43.920 45.120 44.920 Average Dry Gas Meter Temperature, °F 75.00 86.00 97.00 86.000 Dry Gas Meter Volume Sampled, dscf 44.207 41.675 42.028 42.637 Total Moisture Liquid collected, g 33 59 49 47.000 Volume of Water Vapor, standard cubic feet 1.55 2.78 2.31 2.213 Moisture Content of Stack Gas, % 3.39 6.25 5.21 4.950 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9661 0.9375 0.9479 0.951 Carbon Dioxide, % 2.08 2.13 2.03 2.080 Oxygen, % 18.36 18.36 18.39 18.370 Carbon Monoxide & Nitrogen, % 79.56 79.51 79.58 79.550 Fuel Factor 1.22 1.19 1.24 Dry Molecular Weight, lb/lb-Mole 29.07 29.08 29.06 29.070 Wet Molecular weight, lb/lb-Mole 28.69 28.39 28.48 28.520 Flue Gas Static Pressure, inches of H2O 0.25 0.25 0.25 0.250 Absolute Flue Gas Pressure, inches of Mercury 29.33 29.38 29.42 29.377 Average Stack Gas Temperature, °F 365.00 372.00 376.00 371.000 Average Velocity Head, inches of H2O 0.42 0.4 0.4 0.407 Average Stack Gas Velocity, feet/second 46.08 45.36 45.37 45.603 Stack Cross-Sectional Area, square feet 38.944 38.944 38.944 38.944 Dry Volumetric Flow Rate, dry scfm 65,261.5 61,920.9 62,406.863,196.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 107,672.4 105,990.0 106,013.4106,558.600 Percent Isokinetic of Sampling Rate, % 96.5 95.9 96.0 96.133 Percent Excess Air, % 694.4 697.9 702.1 698.133 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Round Duct Diameter, inches 84.5 84.5 84.5 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



### Page 27 of 29

### Salisbury Plant 6

3/15/2011

LocationDryer - Method 23 Average Run Number 1 2 3 Test Date 9/23/2010 9/23/2010 9/23/2010 Run Start Time Run Finish Time Net Traversing Points 2 2 2 Net Run Time, minutes 240 240 240 Nozzle Diameter, inches 0.237 0.237 0.237 0.237 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.963 0.963 0.963 0.963 Barometric Pressure, inches of Mercury 29.32 29.36 29.4 29.360 Average Orifice Meter Differential, inches H2O 1.58 1.65 1.66 1.630 Dry Gas Meter Volume Sampled, cubic feet 173.440 176.040 177.720 175.733 Average Dry Gas Meter Temperature, °F 77.00 95.00 102.00 91.333 Dry Gas Meter Volume Sampled, dscf 161.568 158.915 158.652 159.712 Total Moisture Liquid collected, g 128.2 131 136.1 131.767 Volume of Water Vapor, standard cubic feet 6.03 6.17 6.41 6.203 Moisture Content of Stack Gas, % 3.60 3.74 3.88 3.740 Moisture Saturation at Stack Gas Temperature, % 12.75 12.73 13.06 12.847 Dry Mole Fraction 0.964 0.9626 0.9612 0.963 Carbon Dioxide, % 0 0 0 0.000 Oxygen, % 20.9 20.9 20.9 20.900 Carbon Monoxide & Nitrogen, % 79.1 79.1 79.1 79.100 Fuel Factor Dry Molecular Weight, lb/lb-Mole 28.84 28.84 28.84 28.840 Wet Molecular weight, lb/lb-Mole 28.45 28.43 28.42 28.433 Flue Gas Static Pressure, inches of H2O 0.16 0.16 0.16 0.160 Absolute Flue Gas Pressure, inches of Mercury 29.33 29.37 29.41 29.370 Average Stack Gas Temperature, °F 123.00 123.00 124.00 123.333 Average Velocity Head, inches of H2O 0.5 0.51 0.51 0.507 Average Stack Gas Velocity, feet/second 42.44 42.85 42.87 42.720 Stack Cross-Sectional Area, square feet 13.813 13.813 13.813 13.813 Dry Volumetric Flow Rate, dry scfm 30,102.8 30,390.9 30,350.230,281.300 Actual Wet Volumetric Flue Gas Flow Rate, acfm 35,173.4 35,513.2 35,529.835,405.467 Percent Isokinetic of Sampling Rate, % 100.8 98.2 98.2 99.067 Percent Excess Air, % -118,750.0-118,750.0 -118,750.0

- 118,750.000 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Round Duct Diameter, inches Rectangular Duct Width, inches 39 39 39 Rectangular Duct Length, inches 51 51 51 Fw 0 0 0 0.000 Fc 0 0 0 0.000



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### Salisbury Plant 6

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