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 TX 76234

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 TX 76234

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/NAIS 327121

Sampling Location Information:

AFS #: 4836300012 FRS #: 110000459245

SCC / Description 30500311 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 0 0 0 756 282 2 12

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 Runs

Test Run

Duration

Sample 

Location Points Comments

Kiln outlet % 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-PeCDD Method 23 3 240 0 12 sample points

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

HxCDD

Kiln outlet Method 23 3 240 0 12 sample points

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

HxCDD

Kiln outlet Method 23 3 240 0 12 sample points

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

HxCDD

Kiln outlet Method 23 3 240 0 12 sample points

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

HpCDD

Kiln outlet 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-PeCDF Method 23 3 240 0 12 sample points

Kiln outlet 2,3,4,7,8-PeCDF Method 23 3 240 0 12 sample points

Kiln outlet 1,2,3,4,7,8-HxCDF Method 23 3 240 0 12 sample points

Kiln outlet 1,2,3,6,7,8-HxCDF Method 23 3 240 0 12 sample points

Kiln outlet 2,3,4,6,7,8-HxCDF Method 23 3 240 0 12 sample points

Kiln outlet 1,2,3,7,8,9-HxCDF Method 23 3 240 0 12 sample points

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

HpCDF

Kiln outlet Method 23 3 240 0 12 sample points

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

HpCDF

Kiln outlet 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 Chloride Method 26A 3 60 0 12 sample points

Kiln outlet Chlorine Method 26A 3 60 0 12 sample points

Kiln outlet Hydrogen Fluoride Method 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

Filterable 

Particulate

Kiln outlet 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

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

Location Kiln 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 AM 12:55:00 

PM

8:00:00 AM

Run Finish Time 12:03:00 PM 4:40:00 PM 11:46:00 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
Location Kiln 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 AM 9:26:00 

AM

10:57:00 AM

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

AM

11:56:00 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

Location Kiln 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 PM 2:33:00 PM 4:20:00 PM

Run Finish Time 1:42:00 PM 3:27:00 PM 5:18:00 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 18
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-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 18
ng/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

2 Brick Produced 0 Tons/hr 7.7

3 Brick Produced 0 Tons/hr 7.7

4 Brick Produced 0 Tons/hr 7.7

5 Brick Produced 0 Tons/hr 7.7

6 Brick Produced 0 Tons/hr 7.7

7 Brick Produced 0 Tons/hr 7.7

8 Brick Produced 0 Tons/hr 7.7

9 Brick Produced 0 Tons/hr 7.7

1 Hydrate Lime Feed Rate 0 lbs/hr 34.04

2 Hydrate Lime Feed Rate 0 lbs/hr 34.04

3 Hydrate Lime Feed Rate 0 lbs/hr 34.04

4 Hydrate Lime Feed Rate 0 lbs/hr 34.04

5 Hydrate Lime Feed Rate 0 lbs/hr 34.04

6 Hydrate Lime Feed Rate 0 lbs/hr 34.04

7 Hydrate Lime Feed Rate 0 lbs/hr 34.04

8 Hydrate 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

2 DRY SCRUBBER 0 0

3 DRY SCRUBBER 0 0

4 DRY SCRUBBER 0 0

5 DRY SCRUBBER 0 0

6 DRY SCRUBBER 0 0

7 DRY SCRUBBER 0 0

8 DRY SCRUBBER 0 0

9 DRY SCRUBBER 0 0

Run Name Value UOM Comments

1 None 0

Monday, November 01, 2010 Page 15 of 18
1 0

2 None 0

3 None 0

4 None 0

5 None 0

6 None 0

7 None 0

8 None 0

9 None 0

Monday, November 01, 2010 Page 16 of 18
Sampling / Stack Data Results Detail

Location Kiln 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 AM 12:55:00 PM 8:00:00 AM

Run Finish Time 12:03:00 PM 4:40:00 PM 11:46:00 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 13,582.9 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

Percent Excess Air, % 506.9 540.9 540.9 529.567

F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000

Round Duct Diameter, inches 35 35 35

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10610 10610 10610 10,610.000

Fc 1040 1040 1040 1,040.000

Monday, November 01, 2010 Page 17 of 18
Location Kiln 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 AM 9:26:00 AM 10:57:00 AM

Run Finish Time 8:55:00 AM 10:25:00 AM 11:56:00 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 11,627.0 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

Percent Excess Air, % 487.4 483.5 551.4 507.433

F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000

Round Duct Diameter, inches 35 35 35

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10610 10610 10610 10,610.000

Fc 1040 1040 1040 1,040.000

Monday, November 01, 2010 Page 18 of 18
Location Kiln 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 PM 2:33:00 PM 4:20:00 PM

Run Finish Time 1:42:00 PM 3:27:00 PM 5:18:00 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 11,520.4 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

Percent Excess Air, % 566.9 620.2 537.2 574.767

F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000

Round Duct Diameter, inches 35 35 35

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10610 10610 10610 10,610.000

Fc 1040 1040 1040 1,040.000

Monday, November 01, 2010 Page 19 of 18