### Name: Mike Shipley

Title: Company: Sign Date: Name: Title: Company: Sign Date: Permitted Facility Representative / Date Testing Company Representative / Date 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.

Monday, November 01, 2010 Page 1 of 18

### Facility Information:

Hanson Brick-Mineral Wells Facility
500 NE 14th NE

Mineral Wells TX76234 Contact:Paul Anderson Phone:817-690-8132 Fax: 940-325-9788 Email:Paul.Anderson@hanson.com Testing Company: Armstrong Environmental Inc
1748 Hlavek Road

Decatur TX76234 Contact:Tom Armstrong Phone:214-631-0021 Fax: 214-905-0634 Email:armst@ix.netcom.com

Air Permit Number: O1692 Permitted Source ID/Name: Kiln-2 Kiln-2 Permitted Maximum Process Rate: 11.24 Tons per hour Max. Normal Operation Process Rate: 7.7 Tons per hour Target Process Test Rate 7.7 Tons per hour

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: The source is a tunnel kiln. Emissions are controlled by a dry scrubber. Industry/SCC/NAIS327121

Sampling Location Information: AFS #:4836300012 FRS #:110000459245

SCC / Description30500311 Industrial Processes - Mineral Products - Brick Manufacture - Curing and Firing: Gas-fired Tunnel Kilns

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 Kiln outlet 35 756 282 2 0 12 0 0 Regulation Description Compound Limit Unit 30 TAC Sect 116.120(b) Sulfur Dioxide 24.31 lb/hr 30 TAC Sect 116.120(b) Carbon Monoxide 11.78 lb/hr 30 TAC Sect 116.120(b) Total Particulate 8.94 lb/hr 30 TAC Sect 116.120(b) Total PM10 8.94 lb/hr 30 TAC Sect 116.120(b) Nitrogen oxides (NOx) 2.36 lb/hr 30 TAC Sect 116.120(b) Sulfur Trioxide as H2SO4 1.42 lb/hr 30 TAC Sect 116.120(b) Total organic compounds (TOC) 0.55 lb/hr
30 TAC Sect 116.120(b) Hydrogen Chloride 0.29 lb/hr 30 TAC Sect 116.120(b) Hydrogen Fluoride 0.13 lb/hr



### Monday, November 01, 2010 Page 2 of 18

### 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.
There were no modifications or deviations. Test Parameter Information:

Target Parameter Test

Method Number of

Test RunsTest Run

DurationSample

Points Comments Location% H2O Method 1 - 4 3 240 0 12 sample points Kiln outlet Flowrate Method 1 - 4 3 60 0 12 sample points Kiln outlet 2,3,7,8-TCDD Method 23 3 240 0 12 sample points Kiln outlet 1,2,3,7,8-PeCDDMethod 23 3 240 0 12 sample points Kiln outlet 1,2,3,4,7,8-

HxCDD Method 23 3 240 0 12 sample points Kiln outlet

1,2,3,6,7,8-

HxCDD Method 23 3 240 0 12 sample points Kiln outlet

1,2,3,7,8,9-

HxCDD Method 23 3 240 0 12 sample points Kiln outlet

1,2,3,4,6,7,8-

HpCDD Method 23 3 240 0 12 sample points Kiln outlet

OCDD Method 23 3 240 0 12 sample points Kiln outlet 2,3,7,8-TCDF Method 23 3 240 0 12 sample points Kiln outlet 1,2,3,7,8-PeCDFMethod 23 3 240 0 12 sample points Kiln outlet 2,3,4,7,8-PeCDFMethod 23 3 240 0 12 sample points Kiln outlet 1,2,3,4,7,8-HxCDFMethod 23 3 240 0 12 sample points Kiln outlet 1,2,3,6,7,8-HxCDFMethod 23 3 240 0 12 sample points Kiln outlet 2,3,4,6,7,8-HxCDFMethod 23 3 240 0 12 sample points Kiln outlet 1,2,3,7,8,9-HxCDFMethod 23 3 240 0 12 sample points Kiln outlet 1,2,3,4,6,7,8-

HpCDF Method 23 3 240 0 12 sample points Kiln outlet

1,2,3,4,7,8,9-

HpCDF Method 23 3 240 0 12 sample points Kiln outlet

OCDF Method 23 3 240 0 12 sample points Kiln outlet Total Dioxins Method 23 3 240 0 12 sample points Kiln outlet Total Furans Method 23 3 240 0 12 sample points Kiln outlet Total TEQ Method 23 3 240 0 12 sample points Kiln outlet Hydrogen ChlorideMethod 26A 3 60 0 12 sample points Kiln outlet Chlorine Method 26A 3 60 0 12 sample points Kiln outlet Hydrogen FluorideMethod 26A 3 60 0 12 sample points Kiln outlet Antimony Method 29 3 60 0 12 sample points Kiln outlet Manganese Method 29 3 60 0 12 sample points Kiln outlet Mercury Method 29 3 60 0 12 sample points Kiln outlet Lead Method 29 3 60 0 12 sample points Kiln outlet Cobalt Method 29 3 60 0 12 sample points Kiln outlet Filterable

Particulate Method 29 3 60 0 12 sample points Kiln outlet

Selenium Method 29 3 60 0 12 sample points Kiln outlet Chromium Method 29 3 60 0 12 sample points Kiln outlet Cadmium Method 29 3 60 0 12 sample points Kiln outlet Arsenic Method 29 3 60 0 12 sample points Kiln outlet Nickel Method 29 3 60 0 12 sample points Kiln outlet Beryllium Method 29 3 60 0 12 sample points Kiln outlet



### Monday, November 01, 2010 Page 3 of 18

### Monday, November 01, 2010 Page 4 of 18

### Monday, November 01, 2010 Page 5 of 18

### Sampling / Stack Data Results Summary



### LocationKiln outlet - Method 23 Average Run Number 1 2 3
Test Date 8/18/20108/18/2010 8/19/2010 Run Start Time 8:15:00 AM 12:55:00 PM8:00:00 AM

Run Finish Time 12:03:00 PM4:40:00 PM11:46:00 AM Net Run Time, minutes 240 240 240 Dry Gas Meter Volume Sampled, dscf 138.102 131.232 134.467 134.600 Moisture Content of Stack Gas, % 7.66 7.65 7.48 7.597 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 2.25 2.75 2.75 2.583 Oxygen, % 17.66 17.72 17.72 17.700 Average Stack Gas Temperature, °F 240.83 243.83 239.92 241.527 Dry Volumetric Flow Rate, dry scfm 11,409.3 13,390.5 13,582.9 12,794.233 Actual Wet Volumetric Flue Gas Flow Rate, acfm 16,816.1 19,818.5 19,954.8 18,863.133 Percent Isokinetic of Sampling Rate, % 96.5 78.1 78.9 84.500 F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000
Fw 10610 10610 10610 10,610.000
Fc 1040 1040 1040 1,040.000



### Monday, November 01, 2010 Page 6 of 18

### LocationKiln outlet - Method 26A Average

Run Number 1 2 3
Test Date 8/17/20108/17/2010 8/17/2010 Run Start Time 7:55:00 AM 9:26:00 AM10:57:00 AM

Run Finish Time 8:55:00 AM 10:25:00 AM11:56:00 AM

Net Run Time, minutes 60 60 60 Dry Gas Meter Volume Sampled, dscf 34.667 32.989 33.105 33.587 Moisture Content of Stack Gas, % 7.55 7.46 7.02 7.343 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 1.5 2 2 1.833 Oxygen, % 17.7 17.59 17.9 17.730 Average Stack Gas Temperature, °F 241.42 237.25 238.58 239.083 Dry Volumetric Flow Rate, dry scfm 12,058.5 11,539.3 11,627.0 11,741.600 Actual Wet Volumetric Flue Gas Flow Rate, acfm 16,547.5 16,884.2 16,964.4 16,798.700 Percent Isokinetic of Sampling Rate, % 91.7 91.2 90.8 91.233 F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000
Fw 10610 10610 10610 10,610.000
Fc 1040 1040 1040 1,040.000



### LocationKiln outlet - Method 29 Average Run Number 1 2 3
Test Date 8/17/20108/17/2010 8/17/2010 Run Start Time 12:44:00 PM2:33:00 PM4:20:00 PM Run Finish Time 1:42:00 PM3:27:00 PM5:18:00 PM Net Run Time, minutes 60 55 60 Dry Gas Meter Volume Sampled, dscf 33.316 30.127 32.615 32.019 Moisture Content of Stack Gas, % 6.69 6.57 6.53 6.597 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 2.5 2.5 2.5 2.500 Oxygen, % 17.87 18.06 17.75 17.893 Average Stack Gas Temperature, °F 242.42 246.09 245.58 244.697 Dry Volumetric Flow Rate, dry scfm 11,684.0 11,791.2 11,520.4 11,665.200 Actual Wet Volumetric Flue Gas Flow Rate, acfm 17,080.6 17,305.1 16,888.2 17,091.300 Percent Isokinetic of Sampling Rate, % 90.9 88.9 90.3 90.033 F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000
Fw 10610 10610 10610 10,610.000
Fc 1040 1040 1040 1,040.000



### Monday, November 01, 2010 Page 7 of 18

### Monday, November 01, 2010 Page 8 of 18

### Emissions Summary



### Location: Kiln outlet - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.00000005 0.000000051 0.00000005 0.000 Eg/hr 2.48E-07 3.12E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.37E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.99E-02 5.73E-02 0.057 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

### Compound: 1,2,3,6,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

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



### Monday, November 01, 2010 Page 9 of 18RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

### Compound:2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057 

### Compound:2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000005 0.00000005 0.000 Eg/hr 2.48E-07 3.06E-07 3.03E-07 0.000 ng/dscm 1.28E-02 1.35E-02 1.31E-02 0.013 ng/dscm@7%O2 5.49E-02 5.90E-02 5.73E-02 0.057



### Monday, November 01, 2010 Page 10 of 18

### Compound:2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.00000005 0.00000001 0.00000001 0.000 Eg/hr 2.48E-07 6.12E-08 6.06E-08 0.000 ng/dscm 1.28E-02 2.69E-03 2.63E-03 0.006 ng/dscm@7%O2 5.49E-02 1.18E-02 1.15E-02 0.026 

### Compound:2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.00000001 0.00000001 0.00000001 0.000 Eg/hr 4.96E-08 6.12E-08 6.06E-08 0.000 ng/dscm 2.56E-03 2.69E-03 2.63E-03 0.003 ng/dscm@7%O2 1.10E-02 1.18E-02 1.15E-02 0.011 

### Compound:OCDD Average RunNumber 1 2 3 Mass_mg 0.00000001 0.00000031 0.00000015 0.000 Eg/hr 4.96E-08 1.90E-06 9.09E-07 0.000 ng/dscm 2.56E-03 8.34E-02 3.94E-02 0.042 ng/dscm@7%O2 1.10E-02 3.65E-01 1.72E-01 0.183 

### Compound:OCDF Average RunNumber 1 2 3 Mass_mg 0.00000001 0.00000001 0.00000001 0.000 Eg/hr 4.96E-08 6.12E-08 6.06E-08 0.000 ng/dscm 2.56E-03 2.69E-03 2.63E-03 0.003 ng/dscm@7%O2 1.10E-02 1.18E-02 1.15E-02 0.011 

### Compound:Total Dioxins Average RunNumber 1 2 3 Mass_mg 0.000000032 0.000000581 0.00000015 0.000 Eg/hr 1.59E-07 3.56E-06 9.09E-07 0.000 ng/dscm 8.18E-03 1.56E-01 3.94E-02 0.068 ng/dscm@7%O2 3.51E-02 6.82E-01 1.72E-01 0.296 

### Compound:Total Furans Average RunNumber 1 2 3 Mass_mg 0.000000032 0.000000066 0.000000082 0.000 Eg/hr 1.59E-07 4.04E-07 4.97E-07 0.000 ng/dscm 8.18E-03 1.78E-02 2.15E-02 0.016 ng/dscm@7%O2 3.51E-02 7.78E-02 9.40E-02 0.069 

### Compound:Total TEQ Average RunNumber 1 2 3 Mass_mg 0.0000000001 0.00000000082 0.00000000015 0.000 Eg/hr 4.96E-10 5.02E-09 9.09E-10 0.000



### Monday, November 01, 2010 Page 11 of 18ng/dscm 2.56E-05 2.21E-04 3.94E-05 0.000 ng/dscm@7%O2 1.10E-04 9.66E-04 1.72E-04 0.000



### Location: Kiln outlet - Method 26A Compound:Chlorine Average RunNumber 1 2 3 Mass_mg 0.12 0.11 0.1 0.110 Eg/hr 2.50E+00 2.31E+00 2.11E+00 2.307 ppm 4.15E-02 3.99E-02 3.62E-02 0.039 ppm@7%O2 1.80E-01 1.68E-01 1.68E-01 0.172 

### Compound:Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 0.84 2.06 0.82 1.240 Eg/hr 1.75E+01 4.32E+01 1.73E+01 26.000 ppm 5.65E-01 1.45E+00 5.77E-01 0.864 ppm@7%O2 2.45E+00 6.09E+00 2.67E+00 3.737 

### Compound:Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 0.143 0.158 0.147 0.149 Eg/hr 2.98E+00 3.32E+00 3.10E+00 3.133 ppm 1.75E-01 2.03E-01 1.88E-01 0.189 ppm@7%O2 7.60E-01 8.52E-01 8.71E-01 0.828



### Location: Kiln outlet - Method 29 Compound:Antimony Average RunNumber 1 2 3 Mass_mg 0.000005 0.000005 0.000005 0.000 Eg/hr 1.05E-04 1.17E-04 1.06E-04 0.000 mg/dscm 5.30E-06 5.86E-06 5.41E-06 0.000 mg/dscm@7%O2 2.43E-05 2.87E-05 2.39E-05 0.000 

### Compound:Arsenic Average RunNumber 1 2 3 Mass_mg 0.000005 0.000005 0.000005 0.000 Eg/hr 1.05E-04 1.17E-04 1.06E-04 0.000 mg/dscm 5.30E-06 5.86E-06 5.41E-06 0.000 mg/dscm@7%O2 2.43E-05 2.87E-05 2.39E-05 0.000 

### Compound:Beryllium Average RunNumber 1 2 3 Mass_mg 0.000012 0.000012 0.00012 0.000 Eg/hr 2.53E-04 2.82E-04 2.54E-03 0.001 mg/dscm 1.27E-05 1.41E-05 1.30E-04 0.000 mg/dscm@7%O2 5.83E-05 6.90E-05 5.74E-04 0.000



### Monday, November 01, 2010 Page 12 of 18

### Compound:Cadmium Average RunNumber 1 2 3 Mass_mg 0.000005 0.000005 0.000005 0.000 Eg/hr 1.05E-04 1.17E-04 1.06E-04 0.000 mg/dscm 5.30E-06 5.86E-06 5.41E-06 0.000 mg/dscm@7%O2 2.43E-05 2.87E-05 2.39E-05 0.000 

### Compound:Chromium Average RunNumber 1 2 3 Mass_mg 0.000008 0.000011 0.000008 0.000 Eg/hr 1.68E-04 2.58E-04 1.70E-04 0.000 mg/dscm 8.48E-06 1.29E-05 8.66E-06 0.000 mg/dscm@7%O2 3.89E-05 6.31E-05 3.82E-05 0.000 

### Compound:Cobalt Average RunNumber 1 2 3 Mass_mg 0.000006 0.000005 0.000005 0.000 Eg/hr 1.26E-04 1.17E-04 1.06E-04 0.000 mg/dscm 6.36E-06 5.86E-06 5.41E-06 0.000 mg/dscm@7%O2 2.92E-05 2.87E-05 2.39E-05 0.000 

### Compound:Filterable Particulate Average RunNumber 1 2 3 Mass_mg 73.2 47.18 69.9 63.427 Eg/hr 1.54E+03 1.11E+03 1.48E+03 1,376.667 mg/dscm 7.76E+01 5.53E+01 7.57E+01 69.533 mg/dscm@7%O2 3.56E+02 2.71E+02 3.34E+02 320.333 

### Compound:Lead Average RunNumber 1 2 3 Mass_mg 0.000005 0.000005 0.000005 0.000 Eg/hr 1.05E-04 1.17E-04 1.06E-04 0.000 mg/dscm 5.30E-06 5.86E-06 5.41E-06 0.000 mg/dscm@7%O2 2.43E-05 2.87E-05 2.39E-05 0.000 

### Compound:Manganese Average RunNumber 1 2 3 Mass_mg 0.000024 0.000092 0.000036 0.000 Eg/hr 5.05E-04 2.16E-03 7.63E-04 0.001 mg/dscm 2.54E-05 1.08E-04 3.90E-05 0.000 mg/dscm@7%O2 1.17E-04 5.29E-04 1.72E-04 0.000 

### Compound:Mercury Average RunNumber 1 2 3 Mass_mg 0.00000423 0.00000505 0.00000517 0.000 Eg/hr 8.90E-05 1.19E-04 1.10E-04 0.000



### Monday, November 01, 2010 Page 13 of 18

### Process Run Data mg/dscm 4.48E-06 5.92E-06 5.60E-06 0.000 mg/dscm@7%O2 2.06E-05 2.90E-05 2.47E-05 0.000 

### Compound:Nickel Average RunNumber 1 2 3 Mass_mg 0.000005 0.000013 0.000009 0.000 Eg/hr 1.05E-04 3.05E-04 1.91E-04 0.000 mg/dscm 5.30E-06 1.52E-05 9.75E-06 0.000 mg/dscm@7%O2 2.43E-05 7.44E-05 4.30E-05 0.000 

### Compound:Selenium Average RunNumber 1 2 3 Mass_mg 0.000018 0.000007 0.000015 0.000 Eg/hr 3.79E-04 1.64E-04 3.18E-04 0.000 mg/dscm 1.91E-05 8.21E-06 1.62E-05 0.000 mg/dscm@7%O2 8.76E-05 4.02E-05 7.15E-05 0.000



### Monday, November 01, 2010 Page 14 of 18

### Process Run Data

APCD Run Data

Process Lab Run Data 

### Run Name Value UOM Comments Target Value 1 Brick Produced 0 Tons/hr 7.7


### 2Brick Produced 0 Tons/hr 7.7
3 Brick Produced 0 Tons/hr 7.7
4Brick Produced 0 Tons/hr 7.7


### 5 Brick Produced 0 Tons/hr 7.7
6Brick Produced 0 Tons/hr 7.7
7 Brick Produced 0 Tons/hr 7.7


### 8Brick Produced 0 Tons/hr 7.7
9Brick Produced 0 Tons/hr 7.7
1 Hydrate Lime Feed Rate 0 lbs/hr 34.04


### 2Hydrate Lime Feed Rate 0 lbs/hr 34.04
3 Hydrate Lime Feed Rate 0 lbs/hr 34.04
4Hydrate Lime Feed Rate 0 lbs/hr 34.04


### 5 Hydrate Lime Feed Rate 0 lbs/hr 34.04
6Hydrate Lime Feed Rate 0 lbs/hr 34.04
7 Hydrate Lime Feed Rate 0 lbs/hr 34.04


### 8Hydrate Lime Feed Rate 0 lbs/hr 34.04
9 Hydrate Lime Feed Rate 0 lbs/hr 34.04

Run Name Value UOM Comments Target Value 

### 1 DRY SCRUBBER 0 0
2DRY SCRUBBER 0 0
3 DRY SCRUBBER 0 0


### 4DRY SCRUBBER 0 0
5 DRY SCRUBBER 0 0
6DRY SCRUBBER 0 0


### 7 DRY SCRUBBER 0 0
8 DRY SCRUBBER 0 0
9DRY SCRUBBER 0 0

Run Name ValueUOM Comments 

### 1 None 0 Monday, November 01, 2010 Page 15 of 18

### 1 0



### 2None 0 3 None 0 4None 0 5 None 0 

### 6None 0 7 None 0 8None 0 

### 9None 0

Monday, November 01, 2010 Page 16 of 18

### Sampling / Stack Data Results Detail



### LocationKiln outlet - Method 23 Average Run Number 1 2 3 Test Date 8/18/2010 8/18/2010 8/19/2010 Run Start Time 8:15:00 AM12:55:00 PM8:00:00 AM Run Finish Time 12:03:00 PM4:40:00 PM11:46:00 AM Net Traversing Points 12 12 12 Net Run Time, minutes 240 240 240 Nozzle Diameter, inches 0.253 0.253 0.253 0.253 Pitot Tube Coefficient 0.84 0.998 0.998 0.945 Dry Gas Meter Calibration Factor 0.998 0.998 0.998 0.998 Barometric Pressure, inches of Mercury 29.2 29.2 29.2 29.200 Average Orifice Meter Differential, inches H2O 1.16 1.10 1.12 1.127 Dry Gas Meter Volume Sampled, cubic feet 147.448 143.432 144.810 145.230 Average Dry Gas Meter Temperature, °F 90.67 103.63 95.38 96.560 Dry Gas Meter Volume Sampled, dscf 138.102 131.232 134.467 134.600 Total Moisture Liquid collected, g 243.3 230.9 230.9 235.033 Volume of Water Vapor, standard cubic feet 11.45 10.87 10.87 11.063 Moisture Content of Stack Gas, % 7.66 7.65 7.48 7.597 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9234 0.9235 0.9252 0.924 Carbon Dioxide, % 2.25 2.75 2.75 2.583 Oxygen, % 17.66 17.72 17.72 17.700 Carbon Monoxide & Nitrogen, % 80.09 79.53 79.53 79.717 Fuel Factor 1.44 1.16 1.16 Dry Molecular Weight, lb/lb-Mole 29.07 29.15 29.15 29.123 Wet Molecular weight, lb/lb-Mole 28.22 28.30 28.32 28.280 Flue Gas Static Pressure, inches of H2O -0.32 -0.32 -0.32 -0.320 Absolute Flue Gas Pressure, inches of Mercury 29.18 29.18 29.18 29.180 Average Stack Gas Temperature, °F 240.83 243.83 239.92 241.527 Average Velocity Head, inches of H2O 0.401 0.394 0.402 0.399 Average Stack Gas Velocity, feet/second 41.95 49.44 49.78 47.057 Stack Cross-Sectional Area, square feet 6.681 6.681 6.681 6.681 Dry Volumetric Flow Rate, dry scfm 11,409.3 13,390.5 13,582.912,794.233 Actual Wet Volumetric Flue Gas Flow Rate, acfm 16,816.1 19,818.5 19,954.818,863.133 Percent Isokinetic of Sampling Rate, % 96.5 78.1 78.9 84.500 Percent Excess Air, % 506.9 540.9 540.9 529.567 F-Factor, dscfm/MMBtu @ %O2 8710 8710 87108,710.000 Round Duct Diameter, inches 35 35 35 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10610 10610 1061010,610.000 Fc 1040 1040 10401,040.000



### Monday, November 01, 2010 Page 17 of 18

### LocationKiln outlet - Method 26A Average

Run Number 1 2 3 Test Date 8/17/2010 8/17/2010 8/17/2010 Run Start Time 7:55:00 AM9:26:00 AM10:57:00 AM Run Finish Time 8:55:00 AM10:25:00 AM11:56:00 AM Net Traversing Points 12 12 12 Net Run Time, minutes 60 60 60 Nozzle Diameter, inches 0.253 0.253 0.253 0.253 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.998 0.998 0.998 0.998 Barometric Pressure, inches of Mercury 29.2 29.2 29.2 29.200 Average Orifice Meter Differential, inches H2O 1.20 1.11 1.15 1.153 Dry Gas Meter Volume Sampled, cubic feet 37.147 36.015 36.400 36.521 Average Dry Gas Meter Temperature, °F 92.71 103.00 107.08 100.930 Dry Gas Meter Volume Sampled, dscf 34.667 32.989 33.105 33.587 Total Moisture Liquid collected, g 60.1 56.6 53.1 56.600 Volume of Water Vapor, standard cubic feet 2.83 2.66 2.50 2.663 Moisture Content of Stack Gas, % 7.55 7.46 7.02 7.343 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9245 0.9254 0.9298 0.927 Carbon Dioxide, % 1.5 2 2 1.833 Oxygen, % 17.7 17.59 17.9 17.730 Carbon Monoxide & Nitrogen, % 80.8 80.41 80.1 80.437 Fuel Factor 2.13 1.66 1.50 Dry Molecular Weight, lb/lb-Mole 28.95 29.02 29.04 29.003 Wet Molecular weight, lb/lb-Mole 28.12 28.20 28.26 28.193 Flue Gas Static Pressure, inches of H2O 28.98 -0.34 -0.31 9.443 Absolute Flue Gas Pressure, inches of Mercury 31.33 29.18 29.18 29.897 Average Stack Gas Temperature, °F 241.42 237.25 238.58 239.083 Average Velocity Head, inches of H2O 0.415 0.406 0.410 0.410 Average Stack Gas Velocity, feet/second 41.28 42.12 42.32 41.907 Stack Cross-Sectional Area, square feet 6.681 6.681 6.681 6.681 Dry Volumetric Flow Rate, dry scfm 12,058.5 11,539.3 11,627.011,741.600 Actual Wet Volumetric Flue Gas Flow Rate, acfm 16,547.5 16,884.2 16,964.416,798.700 Percent Isokinetic of Sampling Rate, % 91.7 91.2 90.8 91.233 Percent Excess Air, % 487.4 483.5 551.4 507.433 F-Factor, dscfm/MMBtu @ %O2 8710 8710 87108,710.000 Round Duct Diameter, inches 35 35 35 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10610 10610 1061010,610.000 Fc 1040 1040 10401,040.000



### Monday, November 01, 2010 Page 18 of 18

### LocationKiln outlet - Method 29 Average

Run Number 1 2 3 Test Date 8/17/2010 8/17/2010 8/17/2010 Run Start Time 12:44:00 PM2:33:00 PM4:20:00 PM Run Finish Time 1:42:00 PM3:27:00 PM5:18:00 PM Net Traversing Points 12 11 12 Net Run Time, minutes 60 55 60 Nozzle Diameter, inches 0.253 0.253 0.253 0.253 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.998 0.998 0.998 0.998 Barometric Pressure, inches of Mercury 29.2 29.2 29.2 29.200 Average Orifice Meter Differential, inches H2O 1.16 1.18 1.14 1.160 Dry Gas Meter Volume Sampled, cubic feet 36.566 33.288 36.110 35.321 Average Dry Gas Meter Temperature, °F 106.08 109.91 111.00 108.997 Dry Gas Meter Volume Sampled, dscf 33.316 30.127 32.615 32.019 Total Moisture Liquid collected, g 50.7 45 48.4 48.033 Volume of Water Vapor, standard cubic feet 2.39 2.12 2.28 2.263 Moisture Content of Stack Gas, % 6.69 6.57 6.53 6.597 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9331 0.9343 0.9347 0.934 Carbon Dioxide, % 2.5 2.5 2.5 2.500 Oxygen, % 17.87 18.06 17.75 17.893 Carbon Monoxide & Nitrogen, % 79.63 79.44 79.75 79.607 Fuel Factor 1.21 1.14 1.26 Dry Molecular Weight, lb/lb-Mole 29.11 29.12 29.11 29.113 Wet Molecular weight, lb/lb-Mole 28.37 28.39 28.38 28.380 Flue Gas Static Pressure, inches of H2O -0.33 -0.31 -0.33 -0.323 Absolute Flue Gas Pressure, inches of Mercury 29.18 29.18 29.18 29.180 Average Stack Gas Temperature, °F 242.42 246.09 245.58 244.697 Average Velocity Head, inches of H2O 0.415 0.424 0.404 0.414 Average Stack Gas Velocity, feet/second 42.61 43.17 42.13 42.637 Stack Cross-Sectional Area, square feet 6.681 6.681 6.681 6.681 Dry Volumetric Flow Rate, dry scfm 11,684.0 11,791.2 11,520.411,665.200 Actual Wet Volumetric Flue Gas Flow Rate, acfm 17,080.6 17,305.1 16,888.217,091.300 Percent Isokinetic of Sampling Rate, % 90.9 88.9 90.3 90.033 Percent Excess Air, % 566.9 620.2 537.2 574.767 F-Factor, dscfm/MMBtu @ %O2 8710 8710 87108,710.000 Round Duct Diameter, inches 35 35 35 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10610 10610 1061010,610.000 Fc 1040 1040 10401,040.000



### Monday, November 01, 2010 Page 19 of 18