Boral Bricks,/he. 

Smyrna, Georgia 

Run Number 

Trigon pro;ed%? %G04-135 

Kiln No. 

SUMMARY OF RESULTS 

EPA METHOD 26A 

Determination of Hydrogen Halides & Halogens with Particulate Emissions 

2 3 Average 

Sample Identification 

Pl•r 

Pg 

Ps 

VM 

AH 

TM 

Vs• 

Vc 

Vwc 

Bws 

PMv 

M. FD 

%02 

%CO2 

%CO 

Md 

Ms 

Cp 

APS 

Ts 

Vs 

A 

QsD 

Q^ 

Qsw 

D, 

A• 

Net Time of Test, minutes 

Sample Time, 24-hour cIoek 

Barometric Pressure, in. Hg 

Static Pressure, in. Hg 

Stack Pressure, Absolute, in. Hg 

Actual Meter Volume Sampled, eu. ft. 

Avg. Delta H, in. H20 

Avg. Gas Meter Temp., Deg. F 

Volume Sampled at Stand. Con&, cu. ft. 

Volume of Water Collected, ml 

Volume of Water Vapor at Std. Cond.,SCF 

Moisture Content of Gas Stream 

Percent Moisture in Stack 

Mole Fraction of Dry Gas 

Percent Oxygen, Dry 

Percent Carbon Dioxide, Dry 

Percent Carbon Monoxide, Dry 

Mole. Wt. Stack Gas, Dry Basis, lb/tb mole 

MoM, Wt. Stack Gas, Wet Basis, lb/Ib mole 

Pitot Tube Constant 

Avg. Sqrt. Delta P, in. H20 

Avg. Stack Temp,, Deg. F 

Avg. StackVelocity, fl/sec 

Area Stack, R 

Gas Volume Flow, Dry Std. Cond. CFM 

Actual Gas Volume Fl0w, CFM 

Gas Volume Flow, Wet Std. Con&, CFM 

Sample Nozzle Diameter, inches 

Area of Nozzle, fi 

Percent tsokinetic 

4135-01 4135-02 4135-03 

11/2/2004 11/2/2004 11/2/2004 

60 60 60 

1005-1119 1210-1312 1350-1455 

29.10 29.10 29.10 29.10 

0.029 0.029 0.029 0.029 

29.129 29.129 29.129 29.129 

49.371 52.385 53.151 51.636 

2.25 2.35 2.20 2.26 

97.3 97.1 98.1 97.5 

45.756 48.572 49.179 47.836 

119.3 120.0 86.1 108.5 

5,62 5,65 4.05 5.11 

0.109 0.104 0.076 0.097 

10.9 10.4 7.6 9.7 

0.891 0.896 0.924 0,903 

14.75 14:69 14.65 14.70 

3.51 3.49 3.53 3.51 

0.00 0.00 0.00 0.00 

29.152 29.146 29.150 29.149 

27.933 27,984 28.301 28,073 

0.85 0.85 0.85 0.85 

0.698 0.701 0.682 0.693 

551.2 554.9 555.3 553.8 

56.5 56.9 55.0 56.1 

I0.50 10.50 10.50 10.50 

16117 16250 16195 16188 

35596 35815 34625 35346 

18096 18141 17530 17922 

0,310 0.310 0.310 0.310 

0.00052 0.00052 0.00052 0.00052 

94.8 99.8 101.4 98.7 

Tdgon Engineering Consultants, Inc. 
Boral Bricks, Inc. 

Smyrna, Georgia 

MwHCI 

mu•HCl 

C• 

Cm 

C• 

Caw 

E 

P e3of•2 Trigon Project•o. 0•267-047135 

Kiln No.I 

SUMMARY OF RESULTS 

EPA METHOD 26A 

Determination of Hydrogen Halides & Halogens with Particulate Emissions 

P•t¢ Production Rate, tons/hr t2.66 

Run Number 

Front Half Analysis Non-Condensible Particulate Matter 

mR Non-Condensible Catch, mg 26.1 

C• Non-Condensible Concentration, gr/dsef 0.0088 

C• Non-Condensible Concentration, gr/aef 0.0081 

Caw Non-l•ondensible Emission Rate, lbs/hr 1.21 

E Non-Condensible Emission Rate, lbslton 0.096 

Hydrogen Chloride Concentrationand Emission Rate 

Molecular Weight of Hydrogen Chl'oride, g/mole 36.46 

Hydrogen Chloride Catch, ug 6,262 

Hydrogen Chloride Concentration, ppmv 3.19 

Hydrogen Chloride Concentration, mg/dsem 4.83 

Hydrogen Chloride Concentration, gr/dsef 0.0021 

Hydrogen Chloride Emission Rate, lbs/hr 0.29 

Hydrogen Chloride Emission Rate, lbs/ton 0.023 

Hydrogen Fluoride Concentration and Emission Rate 

Molecular Weight of Hydrogen Flouride, g/mole 20.01 

Hydrogen Flouride Catch, ug 2,61,175 

Hydrogen Fluoride Concentration, ppmv 242.37 

Hydrogen Fluoride Concentration, mg/dscm 201.58 

Hydrogen Fluoride Concentration, gr/dsef 0.0879 

Hydrogen Fluoride Emission Rate, lbs/hr 12.14 

Hydrogen Fluoride Emission Rate, lbs/ton 0.959 

M-wHF 

C, 

C^w 

E 

12.66 12.66 12.66 

2 3 Average 

53.5 18.o 

0,0170 0.0056 0,0105 

0.0157 0.0052 0.0097 

2.36 0.78 1.45 

0.187 0.062 0.115 

36.46 36.46 36.46 

6,563 7,232 6,686 

3.15 3.43 3.25 

4.77 5.19 4.93 

0.0021 0.0023 0.0022 

0.29 0.31 0.30 

0.023 0.025 0.024 

20.01 20.01 20.01 

290,946 313,750 288,624 

254.35 270.90 255.87 

211.54 225.31 212.81 

0.0922 0.0982 0.0928 

12.85 13.64 12.87 

1.015 1.077 1.017 

Trigon Engineering Consultants, Inc. 
Boral Bricks, Inc. 

S•myma, Georgia 

Page 4 of 227 Trigon Project No. 046-04-135 

Kiln No. 

SUMMARY OF RESULTS 

EPA METHOD 26A 

Determination of Hydrogen Halides & Halogens with Particulate Emissions 

Run Number 

Caw 

Sulfur Dioxide Concentrations and Emission Rates 

Cmeas SO2 Concentration, ppm dry 41.04 45.58 45.50 44.04 

Ca SO2 Concentration, lbs/dsef 6.81E-06 7,57E-06 7.55E-06 7.31E-06 

C^w SOz Emission Rate, lbs/hr 6.59 7.38 7.34 7. I0 

E SOz Emission Rate, [bs/ton 0.520 0.583 0.580 0.561 

Oxides of Nitrogen Concentrations and Emission Rates 

NOx C•neentration, ppm dry 31.52 32•52 31,73 31.92 

NOx Concentration, lbs/dscf 3.76E-06 3.88E-06 3,79E-06 3.81E-06 

NOx Emission Rate, lbs/hr 3.64 3.79 3.68 3.70 

NOx Emission Rate, lbs/ton 0.287 0.299 0.291 0.292 

Total Gaseous Organics Concentrations and Emission Rates 

MWC 

Cmeas 

Cc 

Cd 

CON 

CAN 

cAW 

E 

3 Average 

Mole Weight of Carbon, g/mole I2.01 t2.01 12.01 12.01 

Organic Concentration, ppm as propane (wet) 5.I0 2,10 1.30 2.83 

Organic Concentration, ppm as carbon (wet) 15.30 6.30 3.90 8.50 

Organic Concentration, ppm as carbon (dry) 17.18 7.03 4.22 9.48 

Organic Concentration, mg/dscm as carbon 8.58 3.51 2. 4.73 

Organic Concentration, gr/dsefas carbon 0.0037 0.0015 0.0009 0.0021 

Organic Emission Rate, lbs/hr 0.52 0.21 0.13 0.29 

Organic Emission Rate, lbs/ton 0.041 0.017 0,010 0.023 

Trigon Engineering Consultants, Inc. 
Boral Bricks, Inc. 

Smyrna, Georgia 

SUMMARY OFRJESULTS 

Trigon Project•. Pa 5 0f_227 046-04.135 

Kiln No. 

Example Calculations Run 1 

Stack Pressure, Absolute, in. Hg 

Volume Sampled at Stand. Cond., eu. ft. 

17.647 * Vu * (Pb,• + AH / 13:6) Vs.rD ................................. 

Tu + 460 

Volume of Water Vapor at Std. Cond.,SCT Vwc 0.04709 * Vc 

Moisture Conteat of Gas Stream 

Vwc 

Bws ................ 

Vsro + Vwc 

Percent Moisture in Stack 

100 * Vwc 

VsTo + Vwc 

Mole Fraction of Dry Gas 

100 PMv 

100 

Mole. Wt. Stack Gas, Dry Basis, Ib/lb mole Md 0.44 * %CO 2 + 0.32 * %02 + 0.28 * (100 %COa 

MoJe. •¢t. Stack Gas, Wet Basis, lb/lb mole Ms Md * (1 13,) + 18.0 * 

Avg. Stack Veloeity, i°dsee 

(Ts + 460) Vs 85.49 * C• * ziPS * SQRT ...................... 

(Ps *M,) Gas Volume Flow, Dry Std. Cond. CFM 

1058.82 * Vs * A * Ps * (1 B•) 

Ts + 460 

Actual Gas Volume Flow, CFM 

QA--Vs* A*60 

Gas Volume Flow, Wet Std. Cond., CFM Qsw Qm* [1/(t-B•s)] 

Area of Nozzle, ft 

A, ((D• / 2) • * 3.14159)/144 

EPA METHOD 26A 

Determination of Hydrogen Hatides & Halogens with Particulate Emissions 

29.t29 

45.756 

5.62 

0.109 

10.9 

0.891 

29.152 

27.933 

56.5 

16117 

35596 

18096 

0.00052 

Trigon Engineering Consultants, Inc. 
Boral Bricks, Inc. 

.Smyrna, Georgia 

P.age 6 o£227 Trigon rroject No. 04(5-04-135 

Kiln No. 

SUMMARY OF RESULTS 

EPA METHOD 26A 

Determination of Hydrogen Halides & Halogens with Particulate Emissions 

Peroent Isokinetic 

0.0945 * (Ts + 460) * VSTb 

0 * Vs * P.• * (1 B,,s) * A, 

Front Half Analysis Non-Condensible Particulate Matter 

Non-Condensible Concentration, gr/dscf 

(At Standard Conditions) 

Cs 0.0154 * m, / VSTD 

Non-Condensible Concentration, gr/aef 

(At Standard Conditions) 

C• 0.0154 * m,/VM 

Non-Condensible Emission Rate, lbs/hr 

(At Standard Conditions) 

CAw 0.00857 * C, * QsD 

Hydrogen Chloride Concentration and Emission Rate 

Hydrogen Chloride Concentration, ppmv 

C C,, / MwHCI * 24.05408 

Hydrogen Chloride Concentration, mg/dscm 

Cra mugHCl*0.001 /Vsr• * 0.0283160502 

Hydrogen Chloride Concentration, gr/dsof 

Cs 0.0154 * m,gHCl *0.001/VsrD 

Hydrogen Chloride Emission Rate, lbs/hr 

(At IStandard Conditions) 

C^w 0.00857 * C, * QsD 

NOX Concentration, pore dry 

C• Cna / MwCI2 * 24.05408 

NOX Concentration, Ibs/dscf 

Cm mnCl• *0.001/VsrD * 0.0283160502 

NOX Emission Rate, lbs/hr 

Cs 0.0154 * mnCl• *0.001/Vsr D 

NOX Emission Rate, tbs/hr 

E CAW/Prato= 

Standard Conditions 68 Dog. F, 29.92 in. Hg 

0.0088 

0.0081 

1.21 

3.19 

4.83 

0.0021 

0.29 

31.52 

3.76E-06 

3.64 

0.287 

Trigon Engineering Consultants, Inc. 
Run Number 

Date: 

0 

Ps 

V• 

AH 

-T• 

Vc 

Vwc 

B• 

PMv 

Mm 

%02 

%C0• 

%C0 

M• 

Cp 

APu• 

AP•x 

APS 

T.• 

Vs 

A 

SUMMARY OF RESULTS 

EPA METHOD 201A/202 

Determination of Particulate Emissions Less Than 10 and 2.5 Microns 

Kiln No. Exhaust 

Run Time 

Net Time of Test, minutes 

Barometric Pressure, in. Hg 

Static Pressure, in. Hg 

Stack Pressure, Absolute, in. Hg 

Actual Meter Volume Sampled, cu. ft. 

Avg. Delta H, in. H20 

Avg. Gas Meter Temp., Deg. F 

Volume Sampled at Stand, Cond., cu. 

Volume of Water Collected, ml 

Volume of Water Vapor at Std. Cond., SCF 

Moisture Content of Gas Stream 

Percent Moisture in Stack 

Mole Fraction of Dry Gas 

Percent Oxygen, Dry 

Percent Carbon Dioxide, Dry 

Percent Carbon Monoxide, Dry 

Mole. Wt. Stack Gas, Dry Basis, lb/lb mole 

Mole. Wt. Stack Gas, Wet Basis, lb/lb mole 

Pitot Tube Constant 

Delta P Minimum, in. H20 

Delta P Maximum, in. H•O 

Avg. Sqrt. Delta P, in. HaO 

Avg. Stack Temp., Deg. F 

Avg. Stack Velocity, if/see 

Area Stack, ft • 

2 

11/02/04 11/02/04 

0939-1147 1247-1351 

123.4 60.8 

29. I0 29.12 

0.029 0.029 

29,129 29.149 

56,851 29.143 

0.52 0.52 

84.8 84.9 

53,658 27.520 

124.9 88.7 

5.88 4.18 

0.099 0.132 

9.9 13.2 

0.901 0.868 

14.75 14.69 

3.51 3.49 

0.00 0.00 

29,152 29,146 

28,050 27.677 

0.85 0.85 

0.42 0.46 

0,53 0.54 

0,697 0.693 

554,0 563.1 

56.4 56.7 

10.499 10.499 

Page 7 of 227 

3 Avg 

11/02/04 

1444-q545 

56.6 80.3 

29.09 29.10 

0.029 0.029 

29.119 29.133 

25.710 37.235 

0.51 0.52 

86.8 85.5 

24.168 35.116 

63,1 92.2 

2.97 4.34 

0.109 0.113 

10.9 11.3 

0.891 0.887 

14.65 14.70 

3.53 3.51 

0.00 0.00 

29.150 29.149 

27.929 27.886 

0.85 0.85 

0.40 0.43 

0.56 0.54 

0.689 0,693 

550.5 555.9 

55.8 56.3 

10.499 10.499 
Run Number 

QsD 

QA 

Qsw 

N• 

O, 

Qs•sro• 

Dso 

SUMMARY OF RESULTS 

EPA METHOD 201Pd202 

Determination of Particulate Emissions Less Than 10 and 2,5 Microns 

Kiln No. Exhaust 

Gas Volume Flow, Dry Std. Cond,, CFM 

Actual Gas Volume Flow, CFM 

Gas Volume Flow, Wet .Std. Cond,, CFM 

Sample Nozzle Diameter, inches 

Area of Nozzle, ff• 

Percent Isokinetic 

Viscosity of Stack Gas, micropoise 

Reynolds Number 

Cunningham Correction Factor 

Total, Cyclone Flow Rate, Wet Cond., CFM 

Total Cyclone Flow Rate, Std Cond., CFM 

Particle Cut Diameter for Cyclone 

Particulate Cut for Cyclone IV 

Production Rate, tons/hr 

Page 8af227 

2 3 Avg 

16243 I5587 15929 15920 

35552 35706 35176 35478 

18023 17952 17888 17954 

0.240 0.240 0.240 0.240 

0,00031 0.00031 0.00031 0.00031 

89.5 97. 89.6 92. 

294.78 294,78 292.98 294.18 

2248 2396 2238 2294 

1.139 1.141 1.138 1.139 

0.952 1.037 0.943 0.977 

0,435 0.453 0.427 0.438 

9.47 8.93 9.48 9.29 

2.28 2.09 2.29 2.22 

12.66 12.66 12.66 12.66 
SUMMARY OF RESULTS 

EPA METHOD 201 A/202 

Determination of Particulate Emissions Less Than 10 and 2.5 Microns 

Kiln No. Exhaust 

Run Number 

Particulate Matter Greater Than 10 Microns Concentrations and Emission Rates 

m,, Greater than PM,3 Catch, mg 26.5 

C• Greater than PM,, Concentration, gr/dscf 0.00761 

C,,s Greater than PMjo Concentration, gr/aef 0.00718 

C^w Greater than PMtn Emission Rate, lbs/hr 1.059 

E Greater than PM•,• Emission Rate, lbs/ton 0.0836 

Page 9of227 

2 3 Avg 

7.2 8.7 14.1 

0.00403 0.00554 0.00573 

0.00380 0.00521 0.00540 

0.538 0.757 0.785 

0.0425 0.0598 0.0620 

Particulate Matter 10 Microns to 2,5 Microns Front-Half Concentrations and Emission Rates 

m, PMj,, to PM2.5 Front-Half, mg 2.8 3.0 

C, PM•o to PM2. Eront-HalfConcentration, gr/dscf 0.00080 0.00168 

C•, PMt•. to PMz5 Front-Half Concentration, gr/acf 0.00076 0.00159 

CAw PMt• to PM2.5 Front-Half Concentration, lbs/hr 0.112 0.224 

E PM•,, toPM2. • Front-Half Concentration, lbs/ton 0.0088 0.0177 

Particulate Matter Less Than 2,5 Microns Front-Half Concentrations and Emission Rates 

m,, PM2.• Front-Half Catch, mg 10.5 7.4 

C, PM.,.• Front-Half Concentration, gr/dscf 0.00301 0.00414 

C• PMa.s Front-Half Concentration, gr/acf 0.00284 0.00391 

C^w PM•.• Front-Half Emission Rate, lbs/hr 0.42 0.55 

E PM•.• Front-Half Emission Rate, tbs/ton 0.033 0.044 

Condensible Particulate Matter Concentrations and Emission Rates 

m,, Condensible Catch, mg 176.3 129.1 

C, Condensible Concentration, gr/dscf 0.05060 0.07224 

C, Condensible Concentration, gr/aef 0.04776 0.06822 

CAw Condensible Emission Rate, lbs/hr 7.04 9.65 

E Condensible Emission Rate, lbs/ton 0.5563 0.7622 

Total Particulate Matter Emission Rates 

Caw Total PM2.s Emission Rate, lbs/hr 7.46 10.20 

E Total PM•.• Emission Rate, lbs/ton 0.589 0.806 

C•,w Total PM• Emission Rate, lbs/hr 7,57 10.43 

E Total PM,• Emission Rate, lbs/ton 0.598 0.824 

CAw Total PM Emission Rate, lbs/hr 8.63 10.97 

E Total PM Emission Rate, lbs/ton 0.682 0.866 

2.6 2.8 

0.00166 0.00138 

0.00156 0.00130 

0.226 0.187 

0.0179 0.0148 

8.1 8.7 

0.00516 0.0041 

0.00485 0.00387 

0.70 0.56 

0.056 0.044 

84.2 t29.9 

0.05365 0.05883 

0.05043 0.05547 

7.32 8.01 

0.5785 0.6324 

8.03 8.56 

0.634 0.677 

8.26 8.75 

0.652 0.691 

9.01 9.54 

0.712 0.753 
SUMMARY OF RESULTS 

EPA METHOD 201A]202 

Determination of Particulate Emissions Less Than 10 and 2.5 Microns 

Kiln No, Exhaust 

Example Calculations Run 

Stack Pressure, Absolute, in. Hg 

Volume Sampled at Stand. Cond., cu. ft. 

17.647 * V• * (P•r + AH / 13.6) 

TM + 460 

Volume of Water Vapor at Std. Cond., SCF 

Vwc 0.04709 * Vc 

Moisture Content of Gas Stream 

Vwc 

Vs-m + Vwc 

Percent Moisture tn Stack 

100 * Vwc 

VsrD + Vwc 

Mole Fraction of Dry Gas 

100 PMv 

100 

Mote. Wt. Stack Gas, Dry Basis, Ib/lb mole 

Ma 0.44 * %CO• + 0.32 * %Oz+ 0.28 * (100 %CO• %O•) 

Mole. Wt. Stack Gas, Wet Basis, lb/lb mole 

M• lVI• * (1 B,,,) + 18.0 * 

Avg. Stack Velocity, ft/see 

(Ts + 460) 

Vs 85.49 * Cv * APS * SQRT 

(Ps * M,) 

Gas Volume Flow, Dry Std. Cond., CFM 

1058.82 * Vs * A * Ps * (1 B•n) 

Ts+460 

Actual Gas Volume Flow, CFM 

Q^=Vs *A * 60= 

Gas Volume Flow, Wet Std. Cond., CFM 

Qsw Qm* [I/(1-Bws)] 

Page 10of227 

29.129 

53.658 

5.88 

0.099 

9.9 

0.901 

29.I52 

28.050 

56.4 

16243 

35552 

18023 
SUMMARY OF RESULTS 

EPA METHOD 201 A/202 

Determination of Particulate Emissions Less Than 10 and 2.5 Microns 

Kilo No. Exhaust 

Area of Nozzle, ft2 

A,, ((D• 2) * 3.14159)/144 

Percent Isokinefic 

0.0945 * (Ts + 460) * 

0 * Vs* Ps* (1.- B•)* A, 

Viscosity of Stack Gas, micropoise 

IX Ct + C_• * (Ts +460) + C• * (TS +460)'+ C * Bws + C5 * (a/'d3• 100) 

Where: C1 51 

C2 0.207 

C3 3 •24E-05 

C4 -74. 43 

C5 53.147 

Total CyClone Flow Rate, Std Cond., CFM 

S(s'rD) 

0 

Total Cyclone Flow Rate, Wet Cond., CFM 

Ts + 460 

Qs (29.92/528) * Qs•sra• * * 

Bws Ps 

Reynolds Number 

Nr, 8.64E5 * ((Ps * Ms) / (Ts +460)) * (Qs •t) 

Cunningham Correction Factor 

C• + (0.0057193 * (Ix / (Ps * DS0)) * ((Ts +460) Ms)^0.5 

Particle Cut Diameter for Cyclone 

D50 I• * •0.2091 * ^0.709'1 

Ps *Ms Qs 

Where I]• =0.15625 

Particulate Cut for Cyelone IV 

Dso (IF Nre < 3162, 0.0024302 * (•t Qs)^1.1791 * (1 / C0^0.5 * ((Ts+460) / (Ps*Ms))'•0.6790, 

0.019723 * (• Qs)^0.8058 * (1/Cr)^0.5 * ((Ts+460) (Ps*Ms))'x0.3058.) 

PM2.5 Front-Half Concentration, gr/dscf 

(At Standard Conditions) 

Cs 0.0154 * m, / Vsro 

PM2.5 Front-Half Concentration, gr/aef 

(At Standard Conditions) 

C,, 0.0154 * m• / VM 

PM2.5 Front-Half Emission Rate, lbs/hr 

(At Standard Conditions) 

C^w 0.00857 * C• * Qs• 

Standard .Conditions 68 Deg. F, 29.92 in. Hg 

Page 1tof227 

0.00031 

89.5 

294.78 

0.435 

0.952 

2248 

t.139 

9.47 

2.28 

0.00301 

0.00284 

0.419 
Boral Bricks, Inc. 

Smyrna, Georgia 

Run Number 

SUMMARY OF RESULTS 

EPA METHOD 26A 

Determination of Hydrogen Halides & Halogens with Particulate Emissions 

2 3 Average 

Sample Identification 

Date: 

0 

P• 

Ps 

v• 

Vc 

Vwc 

Bws 

%C0_• 

%C0 

M• 

C• 

T• 

Vs 

A 

Qs,• 

Q• 

Q,• 

An 

Net Time of Test; minutes 

Sample Time, 24-hour clock 

Barometric Pressure, in. Hg 

Static Pressure, in. Hg 

Staek Pressure, Absolute, in. Hg 

Actual Meter Volume Sampled, eu. ft. 

Avg. Delta H, in. H20 

Avg. Gas Meter Temp., Deg. F 

Volume Sampled at Stand. Cond., cu. ft. 

Volume of Water Collected, ml 

Volume of Water Vapor at Std. Cond.,SCF 

Moisture Content of Gas Stream 

Percent Moisture in Stack 

Mole Fraction of Dry Gas 

Percent Oxygen, Dry 

Percent Carbon Dioxide, Dry 

Percent Carbon Monoxide, Dry 

Mote. Wt. Stack Gas, Dry Basis, Ib/lb mole 

Mole. Wt. Stack G•s, Wet Basis, lb/lb mole 

Pitot Tube Constant 

Avg. Sqrt. Delta P, in, H20 

Avg. Stack Temp., Deg. F 

Avg. Stack Velocity, ft/scc 

Area Stack, ft 

Gas Volume Flow, Dry Std. Cond. CFM 

Actual Gas Volume Flow, CFM 

G•s Volume Flow, Wet Std. Conck, CFM 

Sample Nozzle Diameter, inches 

Area of Nozzle, • 

Percent Isokinetic 

4135-07 4135418 4135-09 

11/2/2004 11/3/2004 I/3/2004 

60 60 60 

1620-1725 0745-0850 0937-1042 

29.09 29.12 29.12 29.11 

0.033 0.033 0.033 0.033 

29.123 29.153 29.153 29.I43 

53.865 50.236 50.690 51.597 

2.03 2.13 2.18 2.11 

99.7 99.8 102.4 100.6 

49.66t 46.364 46.570 47.532 

138.1 131.9 t37.8 135.9 

6.50 6.21 6.49 6,40 

0.116 0. t18 0.122 0.119 

,11.6 11.8 "12.2 11.9 

0.884 0.882 0.878 0.881 

14:19 14.22 14.28 14.23 

3.82 3.68 3.69 3.73 

0.00 0.00 0.00 0.00 

29.178 29.157 29.162 29.166 

27.884 27.839 27.797 27.840 

0.85 0.85 0.85 0.85 

0.652 0.668. 0.674 0.665 

534.1 "540.2 542.0 538.8 

52.4 53.9 54.5 53.6 

10.50 10.50 10.50 10.50 

15097 15390 15468 15318 

,33024 33930 34325 33760 

17073 17452 17624 17383 

0.310 0.310 0.310 0.310 

0.00052 0.00052 0.00052 0.00052 

109.9 100.6 100.6 103.7 

Trigon Engh•eering Consultants, Inc. 
Boral Bricks, Inc. 

Smyrna, Georgi a 

Trigon Project No. 

MwHCI 

m•HCI 

c• 

c, 

C^• 

E 

SUMMARY OF RESULTS 

EPA METHOD 26A 

Drtermination of Hydrogen Halides & Halogens with Particulate Emissions 

Prat• Production Rate, tons/hr 12.66 12£6 12.66 12.66 

Run Number 2 3 Average 

Front Half Analysis Non-Condensible Particulate Matter 

m, Non-Condensible Catch, mg 43.0 49.2 44.7 45.6 

C• Non-Condensible Concentration, gr/dsef 0.0133 0.0163 0.0148 0.0148 

Ca Non-Condensible ConCentration, gr/acf 0.0t23 0.0151 0.0136 0.0137 

C^• Non-Condensible Emission Rate, lbs/hr .1.73 2.16 1.96 1.95 

E Non-C0ndensible Emission Rate, lbs/ton 0.136 0.170 0.155 0.154 

Hydrogen Chloride Concentration and Emission Rate 

Moteeialar Weight of Hydrogen Chloride, g/mole 36.46 36.46 36.46 36.46 

Hydrogen Chloride Catch, ug 7,399 6,833 6,788 7•007 

Hydrogen Chloride Concentration, ppmv 3.47 3.43 3.40 3.43 

Hydrogen Chloride Concentration, mg/dscm 5.26 5.20 5.15 5.20 

Hydrogen Chloride Concentration, gr/dscf 0.0023 0.0023 0.0022 0.0023 

Hydrogen Chloride Emission Rate, lbs/hr ,0.30 0.30 0.30 0.30 

Hydrogen Chloride Emission Rate, lbs/ton 0.023 0.024 0.024 0.024 

Hydrogen Fluoride Concentration and Emission Rate 

Molecular Weight of Hydrogen Flouride, g/mole 20.01 20.01 20.01 20.01 

Hydrogen Flouride Catch, ug 326,342 324,853 317,623 322,939 

Hydrogen Fluoride Concentration, ppmv 279.03 297.51 289.60 288.71 

Hydrogen Fluoride Concentration, mg/dscm 232.07 247.44 240.86 240.13 

Hydrogen Fluoride Concentration, gr/dsef 0.t012 0.1079 0.1050 0.1047 

Hydrogen Fluoride Emission Rate, lbs/hr 13.09 ,14.23 ,13,92 13.75 

Hydrogen Fluoride Emission Rate, lbs/ton 1.034 1.124 1.100 1.086 

MwHF 

m•HF 

C• 

Cm 

c• 

E 

Page 13 of 227 

046-04-135 

Kiln No. 2. 

Trigon Engineering Consultants, Inc. 
Boral Bricks, Inc. 

Smyrna, Georgia 

Trigon Project No. 

SUMMARY OF RESULTS 

EPA METHOD 26A 

Determ•ation of Hydrogen Halides & Halogens with Particulate Emissions 

Run Number 2 3 Average 

Sulfur Dioxide Concentrations and Emission Rates 

Cmeas SO 2 Concentration, ppm dry 41.45 43.33 50.45 45.08 

C a SO 2 Concentration, lbs/dscf 6.88E-06 7. t9E-06 8.37E-06 7.48E-06 

C^w Sea Emission Rate, lbs/hr 6.23 6.64 7.77 6.88 

E SO2 Emission Rate, lbs/ton 0.492 0.525 01614 0.544 

Oxides of Nitrogen Concentrations and Emission Rates 

Cme•s NOx Concentration, ppm dry 30.09 29.24 30.48 29,94 

C NO× Concentration, lbs/dscf 3.59E-06 3.49E-06 3.64E-06 3.57E-06 

C•w NOx Emission Rate, lbs/hr 3.25 3.22 3.38 3.29 

E NOr Emission Rate, lbs/ton 0.257 0.255 0.267 0.260 

Total Gaseous Organics Concentrations and Emission Rates 

MWC Mole Weight of Carbon, g/mole 

Cmeas Organic Concentration, ppm as propane (wet)- 

Cc 

Cd 

CON 

CAN 

CAW 

E' 

12.01 

2.50 

Organie Concentration, ppm as carbon (wet) 7.50 

Organic Concentration, ppm as carbon (dry) 8.48 

Organic Concentration, mg/dsem as carbon 4.24 

Organic Concentration, gr/dsef as carbon 0.0019 

Organic Emission Rate, lbsthr 0.24 

Organic Emission Rate, lbs/ton 0.019 

12.01 12.01 12.01 

3.30 4.10 3.30 

9.90 12.30 9.90 

11.23 14.0I 11.24 

5.6t 7.00 5.61 

0.0025 0.0031 0.0025 

0.32 0.41 0.32 

0.026 0.032 0.025 

Kiln No. 2 

Trigon Engineering Consultants, Inc. 
Run Number 

Date: 

SUMMARY OF RESULTS 

EPA METHOD 201A/202 

Determination of Particulate Emissions Less Than 10 and 2.5 Microns 

Kiln No, 2 Exhaust 

Run Time 

.Net Time of Test, minutes 

Barometric Pressure, in. Hg 

Static Pressure, in. Hg 

dtaek Pressure, Absolute, in. Hg 

Actual Meter Volume Sampled, cu. 

Avg, Delta H, in. H20 

Avg. Gas Meter Temp., Deg. F 

Volume Sampled at Stand. Cond., eu. ft. 

Volume of Water Collected, ml 

Volume of Water Vapor at Std. Cond., SCF 

Moisture Content of Gas Stream 

Percent Moisture in Stack 

Mole Fraction of Dry Gas 

Percent Oxygen, Dry 

Percent Carbon Dioxide, Dry 

Percent Carbon Monoxide, Dry 

Mole. Wt. Stack Gas, Dry Basis, lb/Ib mole 

Mole. Wt. Stack Gas, Wet Basis, lb/lb mole 

Pitot Tube Constant 

Delta P Minimum, in. HzO 

Delta P Maximum, in. H20 

Avg. Sqrt. Delta P, in. H20 

Avg. Stack Temp., Deg. F 

Avg. Stack Velocity, ft/see 

Area Stack, • 

Page t5 of 227 

2 3 Avg 

11/02/04 11/03/04 11/03/04 

1639-1747 0745-0849 0955-1 t00 

61.5 60.0 62.5 61.3 

29.09 29.12 29.12 29.11 

0.033 0.033 0.033 0.033 

29.123 29.153 29.153 29.143 

29.539 27.494 28.897 28.643 

0.51 0.50 0.50 0.50 

84.1 82.4 88.1 84.9 

27.906 26.081 27.127 27.038 

70.7 69.7 69.2 69.9 

3133 3.28 3.26 3.29 

0.107 0.112 0.107 0.109 

10.7 11.2 10.7 10.9 

0.893 0.888 0.893 0.891 

14.19 14.22 14.28 14.23 

3.82 3.68 3.69 3.73 

0.00 0.00 0.00 0.00 

29.178 29.157 29.162 29.166 

27.987 27.910 27.965 27.954 

0.85 0.85 0.85 0.85 

0.43 0.43 0.40 0.42 

0.49 0.49 0.44 0,47 

0.681 0.677 0.653 0.670 

539.7 537.8 535.2 537.6 

54.8 54,5 52.4 53.9 

10.499 10.499 10.499 10.499 
Run Number 

Q•, 

Q, 

Qsw 

D• 

A, 

N• 

C, 

Q• 

Prate 

SUMMARY OF RESULTS 

EPA METHOD 201A/202 

Determination of Particulate Emissions Less Than 10 and 2.5 Microns 

Kiln No. 2 Exhaust 

Gas Volume Flow, Dry Std. Cond., CFM 

Actual Gas Volume Flow, CFM 

Gos Volume Flow, Wet Std. Cond., CFM 

Sample Nozzle Diameter, inches 

Area of Nozzle, 1l 2 

Percent Isokinetic 

Viscosity of Stack Gas, mieropoise 

Reynolds Number 

Cunningham Correction Factor 

Total.Cyclone Flow Rate, Wet Cond., CFM 

Total Cyclone Flow Rate, Std Cond., CFM 

Particle Cut Diameter for Cyclone. 

Particulate Cut for Cyclone tV 

Production Rate, tons/hr 

Page 16 of 227 

2 3 Avg 

15847 15728 15245 15606 

34502 34343 33033 33959 

17737 17707 17076 17507 

0.240 0.240 0.240 0.240 

0.00031 0.00031 0.00031 0.00031 

95.7 92.4 95.2 94.5 

290.01 289,12 288.78 289.30 

2400 2313 2305 2339 

1.136 1.136 1.135 1.136 

0.988 0.949 0.940 0.959 

0.454 0.435 0.434 0.441 

9.09 9.32 9.37 9.26 

2.13 2.22 2.24 2.20 

12.66 12.66 12.66 12.66 
SUMMARY OF RESULTS 

EPA METHOD 201AJ202 

Determination of Particulate Emissions Less Than 10 and 2.5 Microns 

Kiln No. 2 Exhaust 

Run Number 

Particulate Matter Greater Than I0 Microns Concentrations and Emission Rates 

m,, Greater than PM•, Catch, mg 5.1 

C• Greater than PMu, Concentration, gr/dscf 0.00281 

C•, Greater than PMu• Concentration, gr/aef 0.00266 

Caw Greater than PMu, Emission Rate, lbs/hr 0.382 

E Greater than PMu• Emission Rate, Ibs/ton 0.0302 

Page 17 of 227 

2 3 Avg 

6.9 3.4 5. 

0.00407 0.00193 0.00294 

0.00386 0.00181 0.00278 

0.549 0.252 0,395 

0.0434 0.0199 0.0312 

Particulate Matter 10 Microns to 2.5 Microns Front-Half Concentrations and Emission Rates 

m, PM•o to PM2.s Front-Half, mg 1.7 1.6 

C, PM•0 to PM2. Front-Half Concentration, gr/dscf 0.00094 0.00094 

C•, PM,• to PM2.s Front-Half Concentration, gr/aef 0.00089 0.00090 

Caw PMu• to PM2. • Front-Half Concentration, lbs/hr 0.127 0.127 

E PM•o to PM2. Front-Half Concentration, lbs/ton 0.0101 0.0101 

Particulate Matter Less Than 2.5 Microns Front-Half Concentrations and Emission Rates 

PM•.• Front-Half Catch, mg 

PM• Front-Half Concentration, gr/dsef 

PMz• Front-Half Concentration, gr/aef 

CAw PM2.s Front-Half Emission Rate, lbs/hr 

E PM•.• Front-Half Emission Rate, lbs/ton 

Condensible Particulate Matter Concentrations and Emission Rates 

m• Condensible Catch, mg 

C• Condensible Concentration, gr/dscf 

C• Condensible Concentration, gr/aef 

C•w Condensible Emission Rate, lbs/hr 

E Condensible Emission Rate, lbs/ton 

Total Particulate Matter Emission Rates 

CAw 

C^w 

E 

E 

1.7 1.7 

0.00097 0.00095 

0.00091 0.00090 

0.126 0.127 

0.0100 0.0100 

72.6 87.9 79.5 80.0 

0.04007 0.05190 0.04513 0.04570 

0.03785 0.04923 0.04237 0.04315 

5.44 7.00 5.90 6.1 

0.4298 0.5526 0.4657 0.4827 

5.64 7.49 6.40 6.51 

0.445 0.592 0.506 0.514 

5.76 7.62 6,53 6,64 

0.455 0.602 0.516 0.524 

6.15 8.17 6,78 7,03 

0.485 0.645 0.535 0.555 

Total PM•.s Emission Rate, lbs/hr 

Total PMa.• Emission Rate, lbs/ton 

TeCtal PM.•.Emission Rate, lbslhr 

Total PM• Emission Rate, Ibs/ton 

Total PM Emission Rate, lbs/hr 

Total PM Emission Rate, lbs/ton 

2.6 6.2 6.8 5.2 

0.00143 0.00366 0.00386 0,00299 

0.00136 0.00347 0.00362 0.00282 

0.19 0.49 0,50 0.40 

0.015 0.039 0.040 0.031