PLANT4· 

FIELD DATA CALCULATIONS 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 1 
City, State Augusta, GA 

Process Tested DIFF Baghouse Outlet 

Specific Source Plant 4 

Air Pollution Controls D!FF Baghouse Outlet 

Test Methods 1-5, 26A 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENOIX PAGE No. 12 
1: 

~ 

" 2 

~ z 

? 

E 

01 

.. 

"' 

G) 

em 

,_ ~;2 

(J) -a·£ 

mS::m 

~z:s: m-ICil 

, s:"'"' .. - m"'o "'"'z • -i 

~cnrn 

. 0~~ c;;-u 

"'"' co 

;o<-

-<m 

"~ 

~ "' 

, 

" " m 

z 

0 

x 

m 

~ 

z 

-

" "' 

Method 1 -Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance- Far Wall to Outside of Port (in) 

Distance- Near Wall to Outside of Port (in) 

Inside Diameter of Stack (in) 

63.00 

4.25 Port Length 

58.75 

Port Diameter- For Ref. Only (in) 4.00 

Distance to Upstream Disturbance (It) 

Distance to Downstream Disturbance (It) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default is 1.0 inch) 

20.00 

18.00 

4.09 

3.68 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

Conversion Table for Decimal to Inch Fraction 

1/16 1/8 3/16 1/4 5/16 

0.06 0.13 0.19 0.25 0.31 

PROBE MARKINGS 

Decimal Inches 

Number of Traverse Points on a Diameter 

2 4 6 8 

12.83 8.19 6.84 6.13 

54.42 18.94 12.83 10.42 

48.31 21.64 15.65 

59.06 45.61 23.23 

54.42 44.02 

60.42 51.60 

56.83 

61.12 

10 

5.78 

9.07 

12.83 

17.53 

24.34 

42.91 

49.72 

54.42 

58.18 

61A7 

3/8 

0.38 

12 

5.48 

8.19 

11.18 

14.65 

18.94 

25.17 

42.09 

48.31 

52.60 

56.07 

59.06 

61.77 

"' 0 

, 

:0 

,... 

:0 "' 0 

" "' 
ATCPROJECT No. P-10142 

Pm{fnHg) 30.10 30.06 30.<)3 

Ps(GAUGE} -1.20 -1.20 -1.20 

Ps(fNHG) 29.95 29.91 29.87 

Tm(F} eo.on 89.67 95.08 

Tm(R} 539.6\l 549.36 554.77 

Vm(ft3) 29.15 21J.OO 31.73 

Vm STD(ft3} 28.55 2BA5 30.15 

1/tQ(ml} 42.00 33.00 32.00 

W$TD(ft3) 1.98 1.56 1,51 

VSTO{ft3} 30.53 30.00 31.66 

"" 6.49 5.19 4.17 %S\1Pl 100.00 100.00 100.00 

MD 0.935 0.948 0.952: 

MWD 28.94 28.94 2S.G4 

M 28.23 28.37 2S.42 

Tli(F} 275.21 200.36 283.42 

Ts(RJ 734.00 740,07 743.11 

SUMSQRTDP 12.77 12.77 13.26 

NDP 24.00 24.00 24.00 

;.,;:_ -AVGSQRTDP 0.53 0.53 0.55 

CP 0.1!4 0.84 0.84 

Vs (ft!s) 35.62 35.69 37.14 

DsOnJ 60.00 60.00 60.00 

As(fttj 19Jl3 19.63 19.63 

QS, FLOW. ACFM 41,966 42,050 43,749 

Q STD (ft31mfn) 30,183 29,992 31,035 

Q STD DRY, FLOW SCFM 28,225 28,436 29,555 

WT(gm)·PM 0.0080 0.0075 1).0035 

WT(gm)·HCL 0.0000 0.0030 0.0030 

WT(gm}·HF 0.0111 0.0357 0.0410 

WT(gm)·C12 2.27E-o4 1.82E-OS 1.76E-05 

"' 97.94 96.86 98.79 %C02 1.00 1.00 1.00 

"02 1~.41 19.50 19.46 

""" 0.00 0.00 0.00 %112 79.59 79.50 79.54 

PM (fbslhr} 1.046 {).992 0.454 

PM(kglhrj 0.4746 0.4499 0.2059 

ProctuctJon (tph} 6.75 8.75 6.75 

Production (Mg) 3.06E..03 3.06E.03 3.00E-03 

PM (kg/Mg of Product} 1.37E+04 1.37E+D4 1.43E+04 

PM (mg/dscm) 1.85E+07 1.66E+07 1.52E+07 

PM (mgldscm @ 7% 02} 1.73E+08 1.54E+08 1.57E+OS 

HCI {fbslhr) 7.86E..{)2 3..97E...01 3.B8E..Ot 

f/Cl(Ag!M 3..57E-02 1.80E-01 1.76E-Ot 

HCJ (kg/Mg of Product) 9.86E+03 9.80E+03 1.01E+04 

HCJ(ppm) 652.04 3266.69 307&.35 

HCI (ppm @ 1% 02) 6{)72.95 32433.61 29640.74 

HF(Ibslhr) 1.45E+OO 4.72E+00 5.32E:+OO 

HF(kgthr} S.57E-01 2.14E+OO 2.41E+OO 

HF (kgiMg of Product} 9.22E+03 9,29E+03 9.65E+03 

HF(ppm) 6592,01 21317.93 23116.82 

HF (ppm@ 7% 02) 61396.34 211658.63 222730.97 

CIZ {lb$/hr) 2.97E--02 2.41E-03 2.28E-03 

Cl2(kglhr) 1.35E..OZ 1.09E--o3 1.04E-03 

Cl2 fkB/Mg of Product) 2.61E-03 2.45E-03 1.14E-03 

C12(ppm) 478.98 38.54 35.16 

C/2 (ppm@ 7% 02} 4461.10 382,00 338.76 

QS,. FLOW. ACMM 1188 1191 1239 

QS, Fl..OW, DSCMM 799 805 837 

1 Thet>filtfcalllmoun-t of muistvre thl!lt Ts c.an b()/d. 

11 %M>-%$VP, %SVPwilf bill utUin<i fn Ci'llculllt/!1/la. 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

5.4S 

279.67 

739.3£1 

35.15 

42,5SS 

30,403 

2S,739 

fM0&3 

0.0022 

0.0"29J. 

~).0001 

1.00 

19.45 

0.831 

0.37GS 

6.7500 

3.0GE..03 

1.39E+04 

1.71E+G1 

1.64E+G8 

2.S3E·01 

1.311:~·01 

9.93E-t03 

2331.70 

2271!1.711 

3.83E+OO 

1.74E.j.OO 

9.39E+03: 

17008.92 

165261.31 

1.15E-02 

5.20E·03 

2.0TE·03 

184.23 

1727,51 

1206 

814 

APPENDIX PAGE No.4 
p 

SQ

TDP %02 %C02 

A1 77 247 0.39 1.00 0.624 19.5 1.0 

A2 78 245 0.38 0.97 0.616 

A3 78 245 0.37 0.95 0.608 

A4 78 244 0.37 0.95 0.608 

A5 78 248 0.36 0.92 0.600 

A6 78 245 0.36 0.92 0.600 

A7 78 245 0.37 0.95 0.608 19.6 1.0 

AS 78 244 0.36 0.92 0,600 

A9 79 243 0.36 0.92 0.600 

MIJ 79 245 0.33 0.85 0.574 

A11 79 244 0.33 0.85 0.574 

A12 79 244 0.33 0.85 0.574 

B1 79 245 0.37 0.95 0.608 19.5 1.0 

B2 80 245 0.38 0.97 0.616 

BJ 80 245 0.37 0.95 0.608 

B4 80 245 0.36 0.92 0.600 

B5 80 246 0.36 0.92 0.600 

86 80 245 0.36 0.92 0.600 

137 80 244 0.36 0.92 0.800 19.8 1.0 

88 81 245 0.36 0.92 0.600 

B9 81 245 0.35 0.90 0.592 

810 82 245 0.35 0.90 0.592 

811 82 245 0.34 0.87 0.583 

B12 83 244 0.34 0.87 0.583 19.4 1.0 

79.46 244.88 0.36 0.92 14.372 19.56 1.00 

corrected per 7 e-5b 19.47 Vm(ft3) Initial 398.71 % N2 (BY DIFFERENCE) 7!}.53 

Final 434.33 

Total 35.62 %Excess Air 1272.93 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 16 
POINT# Tm Ts dp dH SQRTDP %02 %C02 

A1 82 248 0.40 1.04 0.632 19.4 i.O A2 82 248 0.38 0.98 0.616 

A3 82 248 0.36 0.93 0.600 

A4 82 248 0.36 0.93 0.600 

A5 82 248 0.36 0.93 0.600 

Ali 83 248 0.35 0.91 0.592 AT 83 249 0.35 0.91 0.592 19.4 1.0 A8 83 249 0.34 0.88 0.583 

A9 83 249 0.34 0.88 0.583 A10 84 249 0.33 0.85 0.574 

A11 84 249 0.33 0.85 0.574 

A12 84 249 0.32 0.83 0.566 

81 85 248 0.39 1.01 0.824 19.6 1.0 82 86 248 0.38 0.98 0.616 

83 86 247 0.38 0.98 0.616 

B4 86 247 0.38 0.98 0.616 

85 66 247 0.36 0.93 0.600 

B6 86 247 0.36 0.93 0.600 

87 87 246 0.36 0.93 o.aoo 19.8 1.0 88 87 246 0.35 0.91 0.592 

89 87 246 0.34 0.88 0.583 

B10 87 248 0.34 0.88 0.583 

B11 87 246 0.34 0.88 0.583 

812 87 245 0.33 0.85 0.574 19.6 1.0 84.63 247.54 0.36 0.92 14.302 19.56 1.00 

corrected per 7e--5b 19.47 Vm(ft3) Initial 434.71 % N2 (BY DIFFERE:NC£} 79.53 Final 

Total 

ATC PROJECT No. P-10142 

469.66 

34.95 %Excess Air 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 201 0 

1272.93 

APPENDIX PAGE No. 17 
ATC PROJECT No. P-1 0142 

Pm{TnHg) 30.11 30.07 30.03 

Ps (GAUGE) 0.22 0.22 0.22 

Ps(INHG} 30.06 30.02 29.00 

Tm(FJ 79.46 84.63 89.50 

Tm{R} 539,15 544.32 549.19 

Vm(ft3) 35.62 34.00 35.90 

Vm STD(ftJ) 33.80 32.81 33.36 

Vl.Q(ml) 14,50 10.20 14.80 

WSTD(tt3) 0.68 OAB 0.70 

VSTD(ft3) 34.49 33.2ll 34.00 

%M UlB 1.44 2.05 

%SVP1 100.00 100.00 100.00 

MO 0.980 0.986 0.980 

MWO 28.94 26.94 28.93 

M 28.72 28.78 28.71 

Ts(F} 2.41.86 247.54- 248,83 

Ts(R) 704.57 701'.23 708.52 

SUMSQRTDP 14.37 14.30 14.56 

NDP 24.00 24.00 24.00 

AVGSQRTDP 0.80 0.60 0.61 

CP 0.84 0.64 0.84 

Vs (ffls) 38.85 38.72 39.53 

Ds(ln} 58,75 5S.75 58.75 

As (ft2} 18.83 18,83 18,83 

QS, FLOW. ACFM 43,880 43,735 44,650 

Q SID (ft3/min) 33,033 32,7$6 33,3:36 

Q STD DRY, FLOW SCFM 32,379 32,2$3 32,653 

WT(gm)·PM 0.0002. 0.0026 0.0000 

WT(gm}-HCL o.ooto 0.0011 0,0013 

Wf(gm)·HF 0.0015 0.0018 0,0023 

WT(gm)·CIZ 1.69E·05 1.876-05 LS1E:-05 

!OJ 108.$9 104.16 104.70 

%COZ 1.00 1.00 1.00 

"02 1f.IA-7 19.47 19.23 

%CO 0.00 0.00 O.OQ 

%N2 79.53 79.53 79.77 

PM(Ibslhr} 0.786 0,338 0.777 

PM (kg/h<} 0.3!564 0.1535 0.3524 

Producuon (tph} 6.15 6.75 6-.75 

Production (Mg} 3:06E.03 3.06E-03 3.06E-03 

PM (kg/Mg of Ptoduct) 1.43E.o-04 1.43E+04 1.46E+04 

PM (mgldscm) 1.95E>~-07 1.82E+07 1.76E+07 

PM (mgldscm @: 7% 02) 1.89E1{18 1.77E+08 1.46E+08 

HCI (lbslht) 1.25E-01 1.43E-01 1.65E-01 

HCI(kg!M 5.68E-02 6.49E-02 7.51E.02 

HCf {kg/Mg of Product) 1.08E+04 1.07E+04 1.0SE+04 

HCI(ppm) 005.30 1038.35 1166.51 

HCI (ppm @ 7% 02) 8783.15 10074.01 9866,51 

HF(Ibslhr) 1.93E-Ot 2.35E-01 3.01E-01 

HF(kglhf') 8.75E-02 t.o7E-01 1.37E-01 

HF (kg/Mg of Product) 1.05E-l-04 i.OSE-i-04 1.0'fE+04 

HF(ppm) 765,36 938.65 1184.00 

HF (ppm @ 7% 02) 7425.72 9007.38 9851.13 

C/2 (fbs!hr) 2.14E-03 2.43E-03 1.9£E-03 

Cl2{kgfhr) 9.71E-04 UOE-03 8.87E-04 

C/2 (kg!Mg of Product) 2.02E-03 8A9E-04 1.96E-03 

CJl{ppm) 30.12 34.3S 27.27 

Ct2 {ppm @ 7% 02) 292.19 333.08 2:26.73. 

QS, FLOW, ACMM 1243 1238 1264 

QS, R.OW, DSCMM 917 914 925 

1 Theontf!Cltt t~mount 

ofmo.Jstu~ that T;s c,:~~n hold, 

It ~llf:I>%SVP, "SYP wiff b& utill:z.Gd ln ettlcu/a.tio/1$, 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5. SALISBURY PlANT 6 

SEPTEMBER 2010 

,.., 

247.0S 

106.71 

39.03 

44,089 

33,042 

32,438 

0.0049 

0.0011 

o-.0019 

0.0000 

1.01} 

19.39 

o.a34 

G.M74 

6.7500 

3.06E-03 

1:.44E+04 

1.85E+07 

1,71E-tos 

1.45E-Of 

B.56E-02 

1.08E+04 

1043.39 

9574.66 

Z.43E·01 

UOE-01 

1.06E+04 

962.23 

8738.08 

2.1ae:.o3 

9.S7E-Q4 

1.61E--03 

3G.57 

284.0ll 

1248 

,. 

APPENDIX PAGE No. 14 
Run #2 

BEGINNING 

ENDING 

NET 

Run#3 

BEGINNING 

ENDING 

NeT 

ATC PROJECT No. P-10142 

1st Imp. 2nd Imp. 3rd/4th Imp. 

100 100 200 

106 100 200 

6 0 0 

1st Imp. 2nd Imp. 3rdl4th Imp. 

100 100 200 

111 100 200 

11 0 0 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

5th Imp. TOTALS 

300.0 

304.2 

4.2 10.2 

5th Imp. TOTALS 

300.0 

303.8 

3.8 14.8 

APPENDIX PAGE No. 15 
POINT# Tm Ts dp dH SQRTDP %02 %C02 

A1 87 249 0.39 1.04 0.624 19.1 1.0 A2 87 249 0.39 1.04 0.624 

A3 87 249 0.39 1.04 0.624 

A4 87 250 0.38 1.01 0.616 

A5 87 250 0.38 1.01 0.616 

A6 88 250 0.38 1.01 0.616 

A? 88 249 0.37 0.98 0.608 19.5 1.0 

A8 88 248 0.37 0.98 0.608 

A9 88 248 0.36 0.96 o.600 MO 89 247 0.32 0.85 0.566 

A11 89 247 0.32 0.85 0.566 

A12 89 247 0.32 0.85 0.566 

B1 89 251 0.37 0.98 0.608 19.3 1.0 82 89 251 0.37 0.98 0.608 

83 90 251 0.37 0.98 0.608 

B4 90 251 0.38 1.01 0.616 

135 91 250 0.38 1.01 0.616 

BIJ 91 249 0.39 1.04 0.624 

87 91 249 0.39 1.04 0.624 19.3 1.0 88 91 248 0.38 1.01 0.616 

89 92 248 0.38 1.01 0.616 

811) 93 248 0.36 0.96 0.600 

811 93 247 0.35 0.93 0.592 

812 94 246 0.35 0.93 0.592 19.4 1.0 89.51) 248.83 0.37 1).98 14.559 19.32 1.{)1) 

corrected per 7e-5b 19.23 Vm(ft3} Initial 469.99 % N2 (BY DIFFERENCE) 79.77 

Final 505.89 

Total 35.90 %&cess Air 1050.1)1 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5. SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 18 
PATM Avg. DH 

30.04 0.92 

2} ABSOlUTE STACK PRESSURE 

Ps =: P ATM + Ps{GAUGE)/13.6 

PATM Ps{GAUGE} 

30.04 0.22 

Pm 

30.11 

Ps 

30.05 

3) SAMPLE VOLUME AT STANOARD CONDITIONS 

VM STD = {VM}'(Y}'(f STD/TM)'(PMIP STD) 

Vm Tm y VmSTD 

35.62 539.1S 0.963 33.80 

ft3 

4) VOLUME OF WATER COLLECTED, CORRECTED TO STANDARD CONDITIONS 

W STO = W STOw+ WSTDsg 

W STDw= (.002B73)'{VLQw)'(T STD/P STD) 

W STDsg = (.002£68)'VlQsg)'(f STD/P STD) 

WHERE 0.002673 =- 0.04707 FT3/ML~IN. HG/17.64 DEG. R 

WHERE 0.002668 = 0.04715 FT3/G"1N.HG/17.64 OEG. R. 

VLQ {w) 

10.00 

VLQ {sg) 

4.50 

WSTD 

0.63 ff3 

5) TOTAl SAMPLE VOLUME AT STANDARD CONDITIONS 

V STD=Vm STD+W STD = 34.49 ff3 

6) PERCENT MOISTURE IN STACK GAS 

%M = {100)"{W STD)N STD = 1.98% 

7) MOLE FRACTION OF DRY GAS 

MD= 

{100~%M}1100 

=- 0.980 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 19 
%C02 %02 %CO 

1.0 19.5 0.0 

9) MOLECULAR WEIGHT OF THE WET GAS 

M = (MWD)'(MD) + 18(1-MO) = 

%N2 

79.5 

WHERE 18 =MOLECULAR WEIGHT OF WATER, G/G.MOLE 

10) STACK VELOCITY 

VS = (85.49)'(CP)'((TSI(PS)(M))'112'((SUM SQRT DP)IN DP)) 

where 85.49 = ftlsec"" [lbllb-mole~Jn.Hg)/(deg. 

R~ln H20)J"'.5 

CP 

0.$4 

T${R) 

704.57 

SUM SQRT 

14.37 

11} STACK VOLUMETRIC FLOW RATE 

QS = (60)'{VS)'(AS) 

AS Qnlet) 

18.83 

NOP 

24 

QS 

43,880 

MWD 

28.94 

28.72 

vs 

$8.85 

12) STACK VOL.UMETR!C FLOW RATe, STANDARD COt-m!T!ONS INClUDING MOISTURE 

Q STD = Q STD DRYIMD 33,033 

13) STACK VOLUME FLOW RATE STANDARD CONDITION$ ORY 

Q STD DRY~ 17.647*60*Md"Vs''A"{Ps!Ts{R)) = 32,379 

14) POlLUTANT MASS RATE, CONCENTRATION BASIS 

PMRC = (.1323)'(WT)'(Q STD)N STD 

WHERE 0.1323 =COMBINED CONVEtiSION FACTOR {60 M!N/HR*0.00220 LBS/GRAM} 

WT(GRAMS) 

0.0062 

15) PERCENT ISOKINETIC 

PMRC 

0.786 

%1 = {0.09450'Ts~vm 

std)/{Ps"Vs"'An"Tima~Md) 

Run Tii'M Area of Nozzle %1 

60 3.06!2-04 106.99 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 20 
City, State Augusta, GA 

Process Tested DIFF Baghouse Outlet 

Specific Source Plant 4 

Air Pollution Controls DIFF Baghouse Outlet 

Test Methods US EPA M29 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 32 
)> 

~ "0 

2 

~ 

~ 

]; 

0 

:;:: 

"' 

~ ern 

(/), -jl> 

l>(i 

(/)""' rn..:m 

~z:: rn-155 

;::(/)(!) 

OJ ... - rn"'o "'"'z - -l "'(l)m ;:)>.(/) 

oc-l 

(I)"U 

"'"' 

co 

,~ 

...:m 

.,;_, -u" 

~ 

"' 

~ m 

z 

0 

x 

111 

~ 

~ 

t:l 

Method 1 -Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance- Far Wall to Outside of Port (in) 

Distance - Near Wall to Outside of Port (in) 

Inside Diameter of Stack (in) 

63.00 

4.25 Port Length 

58.75 

Port Diameter- For Ref. Only (in) 4.00 

Distance to Upstream Disturbance (ft) 

Distance to Downstream Disturbance (ft) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default is 1 .0 inch) 

20.00 

18.00 

4.09 

3.68 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

Conversion Table lor Decimal to Inch Fraction 

1/16 1/8 3/16 1/4 5/16 

0.06 0.13 0.19 0.25 0,31 

PROBE MARKINGS 

Decimal inches 

Number of Traverse Points on a Diameter 

2 4 6 8 

12.83 8.19 6.84 6.13 

54.42 18.94 12.83 10.42 

48.31 21.64 15.65 

59.06 45.61 23.23 

54.42 44.02 

60.42 51.60 

56.83 

61.12 

10 

5.78 

9.07 

12.83 

17.53 

24.34 

42.91 

49.72 

54.42 

58.18 

61.47 

3/8 

0.38 

12 

5.48 

8.19 

11.18 

14.65 

18.94 

25.17 

42.09 

' 48.31 

52.60 

56.07 

59.06 

61.77 

"' 

0 

52 

r 

"' ;u 

0 

"' 

(I) 
Dn (in) 0.237 0.237 0.237 

An (ft2} 3.06E-04 3.06E-04 3.06E-04 

A VG DH (in H20) 0.99 0.96 0.95 

P A TIVI (in Hg) 30.01 29.99 29.94 

Pm (in Hg) 30.08 30.06 30.01 

Ps(GAUGE) 0,22 0.22 0.22 

Ps(IN HG) 30.03 30.01 29.96 

Tm(F) 99.75 108.04 101.83 

Tm(R) 559.44 567.73 561.52 

Vm (ft3} 36.45 35.78 35.17 

VmSTD(ft3) 33.31 32.19 31.94 

VLQ (m/) 22.00 25.00 20.50 

WSTD(ft3) 1.04 1.18 0.97 

VSTD(ft3) 34.35 33.37 32.91 

%M 3.02 3.53 2.94 3.16 

%SVP' 100.00 100.00 100.00 

MD 0.970 0.965 0.971 

MWD 28.94 28.94 28.93 

M 28.61 28.55 28.61 

Ts(F) 251.46 254.67 257.54 254.56 

Ts(R} 711.15 714.36 717.23 714.25 

SUMSQRTDP 14.49 14.28 14.30 

NDP 24.00 24.00 24.00 

AVGSQRTDP 0.60 0.60 0.60 

CP 0.84 0.84 0.84 

Vs (ftfs) 39.44 39.03 39.15 39.20 

Ds (In) 58.75 58.75 58.75 

As (ft2} 18.83 18.83 18.83 

QS, FLOW. ACFM 44,544 44,080 44,216 44,280 

Q sm (ft31mln) 33,189 32,674 32,590 32,818 

Q STD DRY, FLOW SCFM 32,188 31,520 31,633 31,780 

ATC PROJECT No. P-10142 

WT(gm) 0.0021 0.6231 0.0626 0.2293 

%1 106.05 104.66 103.48 

%C02 1.00 1.00 1.00 1.00 

%02 19.47 19.47 19.23 19.39 

%CO 0.00 0.00 0.00 

%N2 79.53 79.53 79.77 

1 Theoretical amount of moisture that rs can hold. 

lf%M>%SVP, %SVP wilt be utilized in calculations. 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

4';-:\: \ ' '" l\ ~~ D· 

APPENDIX PAGE No. 34 
A2 98 246 0.40 1.08 0.632 

A3 98 246 0.38 1.03 0.616 

A4 98 247 0.37 1.00 0.608 A5 98 248 0.35 0.95 0.592 

A6 9B 249 0.35 0.95 0.592 

A7 99 249 0.35 0.95 0.592 

A8 99 251 0.35 0.95 0.592 

A9 99 254 0.35 0.95 0.592 

MO 99 254 0.34 0.92 0.583 

A11 99 254 0.33 0.89 0.574 

A12 99 254 0.32 0.87 0.566 

B1 100 253 0.39 1.06 0.624 

82 100 254 0.39 1.06 0.624 

B3 100 255 0.38 1.03 0.616 

84 100 254 0.38 1.03 0.616 85 101 254 0.39 1.06 0.624 85 101 254 0.36 0.97 0.600 87 101 253 0.36 0.97 0.600 

88 102 253 0.37 1.00 0.608 

89 102 252 0.37 1.00 0.608 

B10 102 252 0.37 1.00 0.608 

811 102 252 0.35 0.95 0.592 

812 102 252 0.35 0.95 0.592 

99.75 251.46 0.36 0.99 14.485 

Vm(ft3) Initial 506.08 

Final 542.53 

Total 36.45 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No, 35 
A1 105 254 0.39 1.06 0.624 

A2 105 254 0.38 1.03 0.616 

A3 106 254 0.38 1.03 0.616 

A4 106 255 0.38 1.03 0.616 

A5 106 255 0.37 1.00 0.608 

A6 107 255 0.37 1.00 0.608 

A7 107 255 0.37 1.00 0.608 

A8 107 256 0.37 1.00 0.608 

A9 107 256 0.37 1.00 0.608 

A10 108 254 0.36 0.97 0.600 

A11 108 253 0.34 0.92 0.583 

A12 108 253 0.30 0.81 0.548 

81 108 254 0.38 1.03 0.616 

B2 108 254 0.37 1.00 0.608 

BJ 109 253 0.36 0.97 0.600 

B4 109 254 0.36 0.97 0.600 

B5 109 255 0.34 0.92 0.583 

86 110 255 0.34 0.92 0.583 

B7 110 255 0.34 0.92 0.583 

B8 110 256 0.34 0.92 0.583 

B9 110 257 0.33 0.89 0.574 

B10 110 257 0.33 0.89 0.574 

B11 110 254 0.32 0.87 0.566 

812 110 254 0.32 0.87 0.566 

1013.()4 254.67 ().35 0.96 14.283 

Vm(ft3) Initial 542.67 

Rna! 578.45 

Total 35.78 

ATC PROJECT No. P·10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 36 
A1 104 258 0.40 1.07 0.632 A2 104 258 0.40 1.07 0.632 

A3 103 258 0.37 0.99 0.608 

A4 103 258 0.37 0.99 0.608 

AS 103 258 0.36 0.96 0.600 

A6 103 258 0.36 0.96 0.600 A7 103 258 0.36 0.96 0.600 A8 103 258 0.30 0.80 0.548 

A9 103 258 0.30 0.80 0.548 

A10 102 259 0.34 0.91 0.583 

A11 102 259 0.30 0.80 0.548 

A12 102 257 0.29 0.78 0.539 

81 102 260 0.39 1.04 0.624 B2 102 259 0.39 1.04 0.624 

B3 102 258 0.39 1.04 0.624 

B4 101 257 0.38 1.02 0.616 

85 101 257 0.36 0.96 0.600 

Btl 101 257 0:39 1.04 0.624 

87 100 257 0.37 0.99 0.608 88 100 256 0.37 0.99 0.608 

B9 100 256 0.35 0.94 0.592 

B10 100 256 0.34 0.91 0.583 

811 100 256 0.33 0.88 0.574 

812 100 255 0.33 0.86 0.574 

101.83 257.54 0.36 0.95 14.3()1 

Vm(ft3) Initial 578.59 

Final 613.76 

Total 35.17 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 37 
Run#2 

BEGINNING 

ENDING 

NET 

Run#3 

BEGINNING 

ENDING 

NET 

ATC PROJECT No. P-10142 

1st Imp. 2nd imp. 3rd/4th Imp. 

100 100 200 

118 100 200 

18 0 0 

1st Imp. 2nd imp. 3rdl4th Imp. 

100 100 200 

114 100 200 

14 0 0 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

!Sth Imp. TOTALS 

300.0 

307.0 

7.0 25.0 

5th Imp. TOTALS 

300.0 

306.5 

6.5 20.S 

APPENDIX PAGE No. 38 
 0 " 

ATC PROJECT No. P-10142 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 42 
e co

sta

t, 

, 

s dete

ed by t

e 

o

o

g equat

o

!:lH = [846.72xD: x/).H: (1-Bwst X Jxflp MsT.Pm 

Modu/e/D 

Dn 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACTION,NOT"A.) 

Md 

Pbar 

PS(GAUGE) 

Ps 

rm,F 

Tm,R 

Ms 

Ts, F 

Ts,R 

Pm 

K 

BORAL BRICK 

9115/2010 

Run#1 Run#2 Run#3 

ATC3 ATC3 ATC3 

0.237 0.237 0.237 

1.937 1.937 1.937 

0.963 0.963 0.963 

0.84 0.84 0.84 0.04 0.04 0.04 

29.0 29.0 29.0 

30.01 29.99 29.94 

0.22 0.22 0.22 

30.03 30.01 29.96 

100 108 102 

559.69 567.69 561.69 

28.56 28.56 28.56 

245 255 255 

704.69 714.69 714.69 

30.12 30.08 30.06 

2.7052 2.7070 2.6759 

Terminology 

Ms=APPARENT STACK GAS MOLECULAR WEIGHT 

=Md(1-Bw)+18Bw 

Md=DRY GAS MOLECULAR WEIGHT (29) OR 

=(0.44*%C02)+(0.32*%02)+(0.28*(%N2+%CO)) 

Ps GAUGE=STACK STATIC PRESSURE (IN. H20) 

Ps=ABSOLUTE STACK PRESSURE (IN. Hg) 

Pm=METER ABSOLUTE PRESSURE (IN. Hg) 

= Pbar + (avg dH/13.6) 

1The method 5 sampling train is intended to operate at a sampling rate of 0.75 elm of dry air at 68 oF 

and 29.92 in. Hg. The orifice meter pressure differential that would produce such a sampling rate 

lhrouah the orifice is desianaled as 

The theoretical no.,.zle calculation is optional. If the tester feels comfortable choosing the 

nozzle size through other means (experience, prior testing, etc.), this is also acceptable. On (theoretical) 

is calculated on the assumption that a 0.75 cfm ftowrate is achieved at 68 °F and 29.92 in. Hg. 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 39 
PATM Av9. DH 

30.01 0.99 

2) ABSOlUTE STACK PRESSURE 

Ps = P ATM + Ps{GAUGE)/13.6 

PATM Ps(GAUGE) 

30.01 0.22 

Pm 

30.08 

Ps 

30.03 

3) SAMPLE VOLUME AT STANDARD CONDITIONS 

VM STD = (VM)'(Y)'(T STDITM)"(PM/P STD) 

Vm Tm y 

36.45 559.44 0.963 

VmSTD 

33.31 

ft3 

4) VOLUME OF WATER COLLECTED, CORRECTED TO STANDARD CONDITIONS 

W STD = W STOw t WSTDsg 

W STOw= (.002673)'(VLQw)'(T STD/P STD) 

W STOsg = (.002668)'VLQsg)'(T STOlP STD) 

WHERE 0.002673 = 0.04707 FT3/ML'IN. HG/17.64 DEG. R. 

WHERE 0.002668 = 0.04715 FT3/G'IN.HG/17.64 DEG. R. 

VLQ{w) 

10.00 

VLQ (sg) 

12.00 

WSTD 

1.04 ft3 

5) TOTAL SAMPLE VOLUME AT STANDARD CONDITIONS 

VSTD =Vm SID+ WSTO = 

6) PERCENT MOISTURE IN STACK GAS 

%M = (1 OO)"(VV STD)N STD = 

7) MOLE FRACTION OF DRY GAS 

0.970 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 40 
%C02 %02 %CO 

1.0 19.5 0.0 

9) MOLECULAR WEIGHT OF THE WET GAS 

M = (MWD)'(MD) + 18(1-MD) = 

%N2 

79.5 

WHERE 18 =MOLECULAR WEIGHT OF WATER, GiG-MOLE 

10) STACK VELOCiiY 

VS = (85.4S)'(CP)"([f$1(PS)(M))"112'((SUM SORT DP)/N DP)) 

where 85.49 = I!Jsec' [IMb-mole'in.HgY(deg. R'in H20)]'0.5 

CP 

0.84 

Ts(R) 

711.15 

SUM SORT 

14.49 

11) STACK VOLUMETRIC FLOW RATE 

QS = (60)'(VS)'(AS) 

AS (Inlet) 

18.83 

NOP 

24 

QS 

44,544 

MWD 

28.94 

28.61 

vs 

39.44 

12) STACK VOLUMETRIC FLOW RATE, STANDARD CONDITIONS INCLUDING MOISTURE 

Q STD = Q STD DRY/MD 33,189 

13) STACK VOlUME FLOW RATE STANDARD CONDITIONS DRY 

Q STO DRY= 17.647'60'Md'Vs'A'(Ps/Ts(R)) = 32,188 

14) POLLUTANT MASS RATE, CONCENTRATION BASIS 

PMRC = (.1323)'(WT)'(Q STD)N STD 

WHERE 0.1323 =COMBINED CONVERSION FACTOR (60 MINIHR'0.00220 LBS/GRAM) 

WT(GRAMS) 

0.0021 

15) PERCENTISOKINETIC 

PMRC 

0.268 

%1 = {0.09450*Ts*Vm std)t{Ps"'Vs~An"Tlme"Md) 

Run Tirne Area of Nozzle %1 

60 3.06E-()4 106.05 

16) CONCENTRATION, GR/SCFD 

Cs::: 15.43 gr/gm WTNm STD 

Cs= 0.0010 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 41 
Antimony (SO 7 440-3&.0 

Arsenic (As 7 44Q..38-2} 

Barium (Ba 7440-39-3) 

Beryllium (Be 7440-41-7} 

Cadmium (Cd 7440-43-9} 

Chromium (Cr 7440-47-3) 

Cobalt (Co 7440-48-4) 

Copper (Cu 7 440-50-8) 

Magnesium {Mg 7439-95-4} 

Manganese (Mn 7439-96-5} 

Mereury (Hg 7439-97-6) 

Nickel (Ni 7440-02-0) 

· Phosphorus {P 7723-14-0) 

Selenium {Se n82-49-2) 

Silver {Ag 7440-22-4) 

Thallium (TI7440-28-0) 

Zinc {Zn 744Q..66-6) 

ATC PROJECT No. P-10142 

3.21E-04 1.46E-04 

1.60E-04 7.28E-05 

1.81E-03 8.23E-04 

1.60E-05 7.28E-06 

9.71E-05 4.41E-05 

4.10E-04 1.86E-04 

2.26E-04 1.03E-04 

2.59E-04 1.17E-04 

9.43E-04 4.28E-04 

4.54E-04 2.06E-04 

5.08E-04 2.30E-04 

3.30E-04 1.49E-04 

4.91E-03 2.23E-03 

321E-04 1.46E-04 

1.60E-04 7.28E-05 

1.60E-04 7.28E-05 

l.OOE-03 4.55E-04 

7.84E-07 

3.92E-07 

4.42E-06 

3.92E-08 

2.37E-07 

i.OOE-06 

5.55E-07 

6.31E-07 

2.33E-06 

1.11E-06 

1.24E-06 

8.06E-07 

1.20E-05 

7.84E-07 

3.92E-07 

3.92E-07 

2.45E-06 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 2010 

2.61E-03 

1.30E-03 

1.48E-02 

1.30E-04 

7.90E-04 

3.34E-03 

1.84E-03 

2.10E-03 

7.60E-03 

3.69E-03 

4.13E-03 

2.68E-03 

3.99E-02 

2.61E-03 

1.30E-03 

1.30E-03 

8.15E-03 

2.39E-02 

1.19E-02 

1.35E-01 

1.19E-03 

7.23E-03 

3.05E-02 

1.68E-02 

1.92E-02 

6.95E-02 

3.38E-02 

3.78E-02 

2.45E-02 

3.65E-01 

2.39E-02 

1.19E-02 

1.19E-02 

7.46E-02 

APPENDIX PAGE No. 43 
y, 

, 

Process Tasted DIFF Baghouse Outlet 

Specific Source Plant 4 

Air Pollution Controls DIFF Baghouse Outlet 

Test Methods USEPA M23 

ATC PROJECT No, P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 53 
~ -u 

2 

~ :z 

? 

:!; 

" 

'" 

"' 

§ 

em 

~~ )>0 

"'""' qjS::m 

-l:Z'S: 

m-100 

.::"'"' 

m"'o 

"' ... - "'"'" - -< "'com 

~)>00 

or-< (ii-u 

"'"' 

c:o 

:U'-

-<m 

.,o 

s:;-< 

:"! 

"' 

l;; 

m 

" :z 

0 

x 

~ m 

z 

? 

"' .. 

Method 1 - Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance· Far Wall to Outside of Port (in) 

Distance • Near Wall to Outside of Port (in) 

Inside Diameter of Stack (in) 

63.00 

4.25 Port Length 

58.75 

Port Diameter· For Ref. Only (in) 4.00 

Distance to Upstream Disturbance (ft) 

Distance to Downstream Disturbance (ft) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default is 1. 0 inch) 

20.00 

18.00 

4.09 

3.68 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

Conversion Table for Decimal to Inch Fraction 

1/16 1/8 3/16 1/4 5116 

0.06 0.13 0.19 0.25 0.31 

PROBE MARKINGS 

Decimal Inches 

Number of Traverse Points on a Diameter 

2 4 6 8 

12.83 8.19 6.84 6.13 

54.42 18.94 12.83 10.42 

48.31 21.64 15.65 

59.06 45.61 23.23 

54.42 44.02 

60.42 51.60 

56.83 

61.12 

10 

5.78 

9.07 

12.83 

17.53 

24.34 

42.91 

49.72 

54.42 

58.18 

61.47 

3/8 

0.38 

12 

5.48 

8.19 

11.18 

14.65 

18.94 

25.17 

42.09 

48.31 

52.60 

56.07 

59.06 

61.77 

"' 

0 

5: 

r 

"' 

2l 

0 

" 

"' 
(

) 

An (ft2) 3.06E-04 3.06E·04 3.06E-04 

A VG DH (In 1120) 0.89 0.91 0.91 

P ATM (in Hg) 30.16 29.88 29.77 

Pm (In Hg) 30.23 29.95 29.84 

Ps(GAUGE) 0.22 0.22 0.22 

Ps(IN IJG) 30.18 29.90 29.79 

Tm(F) 77.15 95.19 98.31 

Tm(R) 536.84 554.88 558.00 

Vm (ft3) 134.36 138.63 135.63 

VmSTD(ft3) 128.55 127.15 123.25 

VLQ(ml} 76.50 78.40 78.40 

WSTD(ft3} 3.61 3.70 3.70 

VSTD {ft3) 132.16 130.85 126.94 

%M 2.73 2.83 2.91 2.82 

%SVP1 100.00 100.00 100.00 

MD 0.973 0.972 0.971 

MWD 28.97 28.98 29.00 

M 28.67 28.67 28.68 

Ts(F} 244.98 248.58 253.48 249-01 

Ts(R} 704.67 708.27 713.17 708.70 

SUMSQRTDP 28.28 28.26 28.00 

NDP 48.00 48.00 48.00 

AVGSQRTDP 0.59 0.59 0.58 

CP 0.84 0.84 0.84 

Vs (fils} 38.19 38.43 38.27 38.30 

Ds (in) 58.75 58.75 58.75 

As (ft2J 18.83 18.83 18.83 

QS, FLOW. ACFM 43,133 43,412 43,232 43,259 

Q STD (ft3fmin) 32,596 32,337 31,864 32,265 

Q STD DRY, FLOW SCFM 31,706 31,423 30.935 31,355 

WT(gm) O.OOE+OO 1.73E-14 5.97E·14 0.0000 

%1 103.88 103.67 102.06 

%C02 1.20 1.30 1.50 1.33 

%02 19.41 19.40 19.10 19.30 

%CO 0.00 0.00 0.00 

%N2 79.39 "19.30 79.40 

DIP (lbslhr) O.OOE+OO 5.66E-13 1.98E-12 8.49E-13 

DIF(kglhrJ O.OOE+OO 2.57E-13 8.99E-13 3.85E-13 

Production (tph) 4.82 4.82 4.82 4.82E+OO 

Production (Mg) 2.19E-03 2.19E-03 2.19E-03 2.19E-ll3 

DIF (kg/Mg of Product) O.OOE+OO 7.913E·15 2.731E-14 1.17E·14 

DIF (ngldscm) O.OOOE+OO 4.B04E-06 1.710E-05 7.30E-06 

DIP (ngldscm@ 7% 02) O.OOE+OO 4.45E-05 1.32E-04 5.89E-05 

QS, FLOW, ACMIVI 1221 1229 1224 1225 

QS, FLOW, DSCMM 898 890 876 888 

1 Theoretical amount of moisture that Ts can hold. 

If %M>%SVP, %SVP will be utilized in calcu!atlons. 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 55 
A1 64 245 0.37 0.95 0.608 19.5 1.2 

AI 64 245 0.37 0.95 0.608 

A2 64 245 0.38 0.98 0.616 

A2 65 246 0.38 0.98 0.618 

A3 65 247 0.36 0.93 0.600 

A3 66 248 0.36 0.93 0.600 

A4 66 250 0.35 0.90 0.592 

A4 67 250 0.35 0.90 0.592 

A5 68 251 0.34 0.87 0.583 

A5 68 252 0.34 0.87 0.583 

A6 69 252 0.32 0.82 0.566 

A6 70 252 0.32 0.82 0.566 

A7 71 252 0.36 0.93 0.600 

A7 72 251 0.36 0.93 0.600 

A8 72 249 0.32 0.82 0.566 

A8 72 247 0.32 0.82 0.566 

A9 72 245 0.32 0.82 0.556 

A9 73 244 0.32 0.82 0.586 

MO 73 244 0.30 0.77 0.548 

MO 74 244 0.30 0.77 0.548 

A11 75 242 0.30 0.77 0.548 

A11 76 242 0.30 0.77 0.548 

A12 77 242 0.29 0.75 0.539 

A12 78 242 0.29 0.75 0.539 

81 79 241 0.37 0.95 0.608 

81 80 241 0.37 0.95 0.608 

82 80 241 0.39 1.00 0.624 

82 80 241 0.39 1.00 0.624 

83 81 243 0.38 0.98 0.616 

83 81 243 0.38 0.98 0.616 

84 82 243 0.40 1.03 0.832 

84 82 243 0.40 1.03 0.632 t;t;;- _) 85 83 244 0.40 1.03 0.632 

85 64 244 0.40 1.03 0.632 

86 84 244 0.35 0.90 0.592 (7.._ 86 84 245 0.35 0.90 0.592 2"· ./ 87 84 242 0.32 0.82 0.566 

87 85 244 0.32 0.82 0.566 

88 85 243 0.37 0.95 0.608 ~~{ 88 85 245 0.37 0.95 0.608 D.;, 

89 86 245 0.37 0.95 0.608 

89 86 245 0.37 0.95 0.608 

810 88 245 0.35 0.90 0.592 6Ctl 

810 88 243 0.35 0.90 0.592 

811 88 242 0.34 0.87 0.583 / bS 

811 89 242 0.34 0.87 0.583 \ S,s 

812 89 242 0.30 0.77 0.548 

812 89 241 0.30 0.77 0.548 

77.15 244.98 0.35 0.89 28.282 19.50 1.20 

corrected per 7e..5b 19.41 

Vm(ft3} Initial 618.11 % N2 (BY DIFFERENCE) 79.39 

Final 752.45 

Total 134.36 %Excess Air 1250.48 .--"!>::'2~ •. 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT APPENDIX PAGE No. 56 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 
A1 85 247 0.36 0.94 0.600 

A2 86 246 0.40 1.05 0.632 

A2 86 245 0.40 1.05 0.632 

A3 87 247 0.40 1.05 0.632 

A3 88 250 0.40 1.05 0.632 

A4 88 250 0.36 0.99 0.616 

A4 88 251 0.38 0.99 0.616 

A5 88 250 0.36 0.94 0.600 

AS 88 250 0.36 0.94 0.600 

A6 88 249 0.34 0.89 0.583 

A8 88 247 0.34 0.89 0.583 

A7 89 247 0.30 0.79 0.548 

A7 89 246 0.30 0.79 0.548 

A8 90 245 0.35 0.92 0.592 

A8 91 245 0.35 0.92 0.592 

A9 92 245 0.32 0.84 0.566 

A9 92 245 0.32 0.84 0.568 

A10 92 246 0.33 0.86 0.574 

A10 93 246 0.33 0.86 0.574 

A11 93 247 0.30 0.79 0.548 

A11 94 245 0.30 0.79 0.548 

A12 94 245 0.28 0.73 0.529 

A12 94 245 0.28 0.73 0.529 

81 94 245 0.38 0.99 0.616 

81 94 245 0.38 0.99 0.616 

82 94 246 0.39 1.02 0.624 

82 94 247 0.39 1.02 0.624 

83 95 245 0.39 1.02 0.624 

83 97 245 0.39 1.02 0.624 

84 99 248 0.37 0.97 0.808 

84 99 249 0.37 0.97 0.608 

85 100 251 0.37 0.97 0.608 

85 101 252 0.37 0.97 0.608 

86 102 252 0.34 0.89 0.583 

BB 102 252 0.34 0.89 0.583 

87 102 252 0.33 0.86 0.574 

87 102 253 0.33 0.86 0.574 

88 103 252 0.34 0.89 0.583 

88 103 251 0.34 0.89 0.583 

89 103 251 0.32 0.84 0.566 

89 103 250 0.32 0.84 0.566 

810 104 254 0.33 0.86 0.574 

810 106 254 0.33 0.86 0.574 

811 106 255 0.36 0.94 0.600 

811 106 256 0.36 0.94 0.600 

812 106 256 0.30 0.79 0.548 

812 106 254 0.30 0.79 0.548 

95.19 248.58 0.35 0.91 28.263 19.40 1.30 

corrected per 1 e-5b 19.40 

Vm(ft3} Initial 752.54 % 1'12 (BY DIFFERENCE) 79.30 

Final 891.17 

Total 138.63 %Excess Air 1263.68 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 57 
Run #2 

1st Imp. 2ndlmp. 3rd Imp. 

BEGINNING 100 100 0 

ENDING 154 118 0 

NET 54 18 0 

Run#3 

tstlmp. 2nd Imp. 3rd Imp. 

BEGINNING 100 100 0 

lENDING 154 118 0 

NET 54 18 0 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

4111 Imp. TOTALS 

300.0 306.4 

6.4 78.4 

4th Imp. TOTALS 

300.0 306.4 

6.4 78.4 

APPENDIX PAGE No. 58 
Mf = [846. 72 x D,~ x Ml@ X c! (1- Bws ) 2 x MdTmP. J x !:.p 

MsJ'.Pm 

BORALBRICK 

Modu!e!D 

Dn 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACTION,NOT%) 

Md 

Pbar 

PS(GAUGE) 

Ps 

Terminology 

Tm,F 

Tm,R 

Ms 

Ts,F 

Ts,R 

Pm 

K 

9116/2010 

Run #1 

ATC3 

0.237 

1.937 

0.963 

0.84 

0.04 

29.0 

30.16 

0.22 

30.18 

80 

539.69 

28.56 

255 

714.69 

30.27 

2.5720 

Run #2 

ATC3 

0.237 

1.937 

0.963 

0.84 

O.G4 

29.0 

29,88 

0.22 

29.90 

90 

549.69 

28.56 

250 

709.69 

30.23 

2.6175 

Run 113 

ATC3 

0.237 

1.937 

0.963 

0.84 

0.04 

29.0 

29.77 

0.22 

29.79 

100 

559.69 

28,56 

250 

709.69 

29.95 

2.6801 

Ms=APPARENT STACK GAS MOLECULAR WEIGHT 

=Md(1-Bw)+18Bw 

Md=DRY GAS MOLECULAR WEIGHT (29) OR 

=(0.44'%C02)•(0.32*%02)+(0.28'(%N2+%CO)) 

Ps GAUGE=STACK STATIC PRESSURE (IN. H20) 

Ps=ABSOLUTE STACK PRESSURE (IN. Hg) 

Pm=METER ABSOLUTE PRESSURE (IN. Hg) 

= Pbar + (avg dH/13.6) 

1The method 5 sampling train is intended to operate at a sampling rate of 0.75 cfm of dry air at 68 

oF and 29.92 in. Hg. The orifice meter pressure differential that would produce such a sampling rate 

through the orifice is designated as I!H@. 

The theoretical nozzle calculation is optional. If the tester feels comfortable choosing the 

nozzle size through other means (experience, prior testing, etc.), this is also acceptable. Dn 

(theoretical) is calculated on the assumption that a 0.75 elm flowrate is achieved at 68 °F and 29.92 in. 

ATC PROJECT No. P-10142 

Hg. 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 59 
PATM Avg.DH 

30.16 0.89 

2) ABSOLUTE STACK PRESSURE 

Ps = P ATM + Ps(GAUGE)/13.6 

PATM Ps(GAUGE) 

30.16 0.22 

Pm 

30.23 

Ps 

30.18 

3) SAMPLE VOLUME AT STANDARD CONDITIONS 

VM STD = (VM)'(Y)'{T STDfTM)'(PMIP STD) 

Vm Tm y VmSTD 

PSTD= 

134.36 536.84 0.963 123.55 ft3 

4) VOLUME OF WATER COLLECTED, CORRECTED TO STANDARD CONDITIONS 

W STD = W STOw+ WSTDsg W STOw= (.002673)'(VLOw)'(T STOlP STD) W STDsg = (.002668)'\/LQsg)'{T STDIP STD) 

WHERE 0.002673 = 0.04707 FT31ML 'IN. HG/17.64 DEG. R. WHERE 0.002668 • 0.04715 FT31G'IN.HGI17.64 DEG. R. 

VLQ (w) 

68.00 

VLQ (sg) 

8.50 

WSTD 

3.61 ft3 

5) TOTAL SAMPLE VOLUME AT STANDARD CONDITIONS 

V STD=Vm STD+WSTD = 132.1S ft3 

6) PERCENT MOISTURE IN STACK GAS 

%M = (100)"(W STD)N STD = 2.73.% 

7) MOLE FRACTION OF DRY GAS 

MD= = 0.973 

29.92 IN. HG 

ATC PROJECT No. P-1()142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 60 
y, 

Process Tested Dryer 

Specific Source Dryer 

Air Pollution Controls 

Test Methods US EPA M 23 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 61 
, 

~ "0 

:0 

2 

a 

~ 

!: 

:1 

t; 

§ 

em 

~;g 

"'"11 cn":O 

m:;;m 

~zs:: 

m-IW 

;;:"'"' 

oo"'-

m"'o 

;u<nz - -< "'cnm 

~)>(/) 

or -I 

[i;-o 

roll 

co 

~ffi ...,o 

:;;-I 

z 

-< 

"' 

, 

"0 

..., 

m 

z 

CJ 

x 

m 

~ 

z 

? 

"' 

N 

Method 1 - Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance - Far Wall to Outside of Port (in) 

Distance- Near Wall to Outside of Port (in) 

Inside Diameter of Stack (in) 

Port Diameter- For Ref. Only (in) 

Distance to Upstream Disturbance (ft) 

Distance to Downstream Disturbance (It) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default Is 1.0 inch) 

52.00 

0.00 Port Length 

52.00 

4.00 

10.00 

5.00 

2.31 

1.15 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

Conversion Table for Decimal to Inch Fraction 

1116 118 3/16 1/4 5116 3/8 

0.06 0.13 0.19 0.25 0.31 0.38 

PROBE MARKING$ 

Decimal inches 

Number of Traverse Points on a Oiameter 

;,)\-, 

2 4 6 8 10 12 

7.59 3.48 2.29 1.66 1.35 1.09 

44.41 13.00 7.59 5.46 4.26 3.48 

39.00 15.39 10.09 7.59 6.14 

48.52 36.61 16.80 11.75. 9.20 

44.41 35.20 17.78 13.00 

49.71 41.91 34.22 18.51 

46.54 40.25 33.49 ~ "' 

50.34 44.41 39.00 r 

47:74 42.80 !ll 

50.65 45.86 ~ 

48.52 "' 

50.91 
A3 82 

M 82 

A4 82 

AS 82 

A5 82 

A6 82 

A8 82 

A7 82 

A7 82 

A8 82 A8 82 A9 82 

A9 82 

A10 82 

A10 82 

A11 83 

A11 83 

A12 83 

A12 83 

B1 83 B1 83 

82 83 

82 83 

B3 83 B3 83 B4 83 

84 84 

85 84 

B5 84 

86 84 

86 84 87 84 87 84 

88 84 88 84 89 84 89 84 

81(} 84 

810 84 

811 84 811 84 

812 84 

812 84 

82.56 

Vm(tt3) 

ATC PROJECT No. P-10142 

122 0.66 1.59 0.812 

122 0.68 1.64 0.825 122 0.68 1.64 0.825 122 0.74 1.78 0.860 

122 0.74 1.78 0.860 122 0.74 1.78 0.660 

122 0.74 1.78 0.860 122 0.74 1.78 0.660 

122 0.74 1.78 0.860 

122 0.75 '1.81 0.866 

122 0.75 1.81 0.866 122 0.75 1.81 0.666 122 0.75 1.81 0.866 122 0.76 1.83 0.872 122 0.76 1.83 0.872 

122 0.77 1.85 0.877 

122 0.77 1.85 0.877 

122 0.76 1.83 0.872 

122 0.76 1.83 0.872 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 122 0.78 1.88 0.883 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 122 0.78 1.88 0.883 

122 0.78 1.88 0.663 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 122 0.78 1.88 0.883 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 122 0.78 1.88 0.883 

122 0.78 1.88 0.883 122 0.78 1.88 0.883 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 

122 0.75 1.81 0.866 122 0.75 1.81 0.866 

122.00 0.75 1.80 41.541 

Initial 467.99 

Final 641.43 

Total 173.44 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

20.90 0.00 

APPENDIX PAGE No. 64 
A3 82 

A3 82 

A4 82 

A4 82 

A5 82 

A5 82 

A5 82 

A6 82 

A7 82 

A7 82 

A8 82 

A8 82 

A9 83 

A9 83 

A10 83 

Mil 83 

A11 83 

A11 83 

A12 83 

A12 83 

81 84 

81 84 

B2 84 

82 84 

83 84 

83 84 

84 84 

84 84 

85 84 

85 84 

88 85 

86 85 

87 85 

87 85 

88 85 

88 85 

89 87 

89 87 

810 87 

810 87 

811 87 

811 88 

812 88 

812 88 

83.85 

Vm(ft3) 

ATC PROJECT No. P-10142 

124 0.66 1.59 0.812 

124 0.66 1.59 0.812 

124 0.66 1.59 0.812 

124 0.66 1.59 0.812 

124 0.72 1.73 0.849 

124 0.72 1.73 0.849 

124 0.72 1.73 0.849 

124 0.72 1.73 0.849 

124 0.72 1.73 0.849 

124 0.72 1.73 0.849 

124 0.76 1.83 0.872 

124 0.76 1.83 0.872 

124 0.76 1.83 0.872 

124 0.76 1.83 0.872 

124 0.76 1.83 0.872 

124 0.76 1.83 0.872 

124 0.76 1.83 0.872 

124 0.76 1.83 0.872 

124 0.76 1.83 0.872 

124 0.76 1.83 0.872 

124 0.77 1.85 0.877 

124 0.77 1.85 0.877 

124 0.79 1.90 0.889 

124 0.79 1.90 0.889 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.60 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.80 1.92 0.894 

124 0.78 1.88 0.883 

124 0.78 1.88 0.883 

124 0.78 1.88 0.883 

124 0.78 1.88 0.883 

124.00 0.76 1.82 41.684 

lnitial 842.37 

Final 818.41 

Total 176.04 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

20.90 0.00 

APPENDIX PAGE No. 65 
A3 87 

A3 87 

A4 87 

A4 87 

AS 87 

A5 87 

116 87 

A$ 87 

117 87 

AT 87 

A8 86 

A8 86 

A9 86 

A9 86 

1110 86 

A10 86 

A11 86 

A11 86 

A12 86 

A12 86 

81 86 

81 86 

82 86 

82 86 

83 86 

83 86 

84 86 

84 86 

85 86 

85 86 

86 86 

BB 86 

87 86 

87 86 

88 86 

88 86 

89 85 

89 85 

810 85 

810 85 

811 85 

811 85 

812 85 

812 85 

86.13 

Vm(ft3) 

ATC PROJECT No. P-10142 

124 0.66 1.59 0.812 

124 0.66 1.59 0.812 

124 0.67 1.61 0.819 

124 0.67 1.61 0.819 

124 0.67 1.61 0.819 

124 0.67 1.61 0.819 

124 0.74 1.78 0.860 

124 0.74 1.78 0.860 

124 0.74 1.78 0.660 

124 0.74 1.78 0.860 

124 0.74 1.78 0.860 

124 0.74 1.78 0.860 

124 0.77 1.85 0.877 

124 0.77 1.85 0.877 

124 0.77 1.85 0.877 

124 0.77 1.85 0.877 

124 0.77 1.85 0.877 

124 0.77 1.85 0.877 

124 0.77 1.65 0.877 

124 0.77 1.85 0.877 

124 0.77 1.85 0.877 

124 0.77 1.85 0.877 

123 0.77 1.85 0.877 

123 0.77 1.85 0.877 

123 0.82 1.97 0.906 

123 o,82 1.97 0.906 

123 0.82 1.97 0.906 

123 0.82 1.97 0.906 

123 0.82 1.97 0.906 

123 0.82 1.97 0.906 

122 0.82 1.97 0.906 

122 0.82 1.97 0.906 

122 0.82 1.97 0.906 

122 0.82 1.97 0.906 

122 0.82 1.97 0.906 

122 0.82 1.97 0.906 

122 0.82 1.97 0.906 

122 0.82 1.97 0.906 

122 0.80 1.92 0.894 

122 0.80 1.92 0.894 

122 0.80 1.92 0.894 

122 0.80 1.92 0.894 

122 0.78 1.88 0.883 

122 0.78 1.88 0.883 

123.25 11.76 1.83 41.837 

Initial 818.52 

Final 998.24 

Total 177.72 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

20.90 0.00 

APPENDIX PAGE No, 66 
AVG DH (In H2D) 1.80 1.82 1.83 

PATM(InHg) 30.16 30.16 30.16 

Pm(lnHg) 30.29 30.29 30.29 

Ps(GAUGE) 0.10 0.10 0.10 

Ps(/NHG) 30.17 30.17 30.17 

Tm(F) 82.56 83.85 85.13 

Tm(R) 642.25 543.54 545.82 

Vm (ft3) 173.44 176.04 177.72 

VmSTD(ft3) 170.97 173.12 174.06 

VLQ(ml} 134.00 137.00 139.00 

VV STD(ft3} 6.32 6.46 6.56 

V STD(ft3) 177.29 179.58 180.61 

%M 3.56 3.60 3.63 

%SVP1 12.06 12.74 12.48 

MD 0.964 0.964 0.964 

MWD 28.84 28.84 28.84 

M 28.45 28.45 28.44 

Ts(F) 122.00 124.00 123.25 

Ts(R} 581.69 583.69 582.94 

SUMSQRTDP 41.54 41.68 41.84 

NDP 46.00 48.00 48.00 

A'IGSQRTDP 0.87 0.87 0.87 

CP 0.84 0.64 0.84 

Vs (ftls) 51.16 51.43 51.59 

Ds (In) 52.00 52.00 52.00 

As (ft2) 14.74 14.74 14.74 

QS, FLOW. ACFM 45,251 45,489 45,628 

Q STD (ft31min) 41,414 41.489 41.670 

Q STD DRY, FLOW SCFM 39,938 39,996 40,157 

WT(gm) 7.46E-13 7.72E-14 6.53E-14 

%1 99.66 100.77 100.90 

%C02 0.00 0.00 0.00 

%02 20.90 20.90 20.90 

%CO 0.00 0.00 0.00 

%N2 79.10 79.10 79.10 

DIF (lbslhr) 2.31E-11 2.36E-12 1.99E-12 

DIF(kglhr) 1.05E-11 1.07E·12 9.o4E-13 

Production (tph) 4.82 4.82 4.82 

Production (Mg) 2.19E·03 2.19E-03 2.19E-03 

DIF (kg/Mg of Product) 3.4121E-13 3.531E-14 2.987E-14 

DIF (ngldscm) 1.541E·04 1.575E·05 1.325E·05 

OfF (ngldscm@ 7% 02) N/A NIA N/A 

QS, FLOW. ACMM 1281 1288 1292 

QS, FLOW, DSCMM 1131 1133 1137 

1 Thooretical amount of moisture that Ts can hold. 

ATC PROJECT No. P-10142 

If %M>%SVP, !Y!>SVP will be uttJJzed In cafculations. 

* Ambient oxygen concentrations, calculation not vafid 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 2010 

\ j "-() "110 L• '\ I ~'i v \_.] 3.60 123.08 582.77 51.40 45,455 41,524 40,030 2.96E-13 0.00 20.90 9.14E-12 4.14E·12 4.82E+OO 2.19E-03 1.35E-13 6.10E.05 NIA' 1287 1133 APPENDIX PAGE No. 63 
1st Imp. 2ndlmp. 

BEGINNING 100 100 

ENDING 220 100 

NET 120 0 

Run#J 

1stlmp. 2nd Imp. 

Bl:GINN!NG 100 100 

ENDING 222 100 

NET 122 0 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

3rd Imp. 4/h Imp. TOTALS 

0 300.0 

6 311.0 

6 11.0 137.0 

3rd Imp. 4/h Imp. TOTALS 

0 300.0 

8 309.0 

8 9.0 139.0 

APPENDIX PAGE No. 67 
Mi =[ 846.72xD: xMi@ xc!(l-BwS x ~:i~ JxL\p 

Module!D 

Dn 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACTION,NOT%) 

Md 

Pbar 

PS(GAUGE) 

Ps 

Tm,F 

Tm,R 

Ms Ts~F TsrR 

Pm 

K 

Terminology 

BORALBRICK 

9/16/2010 

Run#1 

ATC 1 

0.220 

1.980 

1.000 

0.84 

0.04 

29.0 

30.16 

0.10 

30.17 

85 

544.69 

28.56 

125 

584.69 

30.27 

2.4076 

Run#2 Run #3 

ATC 1 ATC 1 

0.220 0.220 

1.980 1.980 

1.000 1.000 

0.84 0.84 

0.04 0.04 

29.0 29.0 

30.16 30.16 

0.10 0.10 

30.17 30.17 

85 85 

544.69 544.69 

28.56 28.56 

125 125 

584.69 584.69 

30.29 30.29 

2.4058 2.4057 

Ms~APPARENT STACK GAS MOLECULAR WEIGHT 

=Md(1-Bw)+18Bw Md~DRY GAS MOLECULAR WEIGHT (29) OR 

~(0.44'%C02)+(0.32'%02)+(0.28.(%N2+%CO)) 

Ps GAUGE=STACK STATIC PRESSURE (IN. H20) 

Ps=ABSOLUTE STACK PRESSURE {IN. Hg) 

Pm=METER ABSOLUTE PRESSURE {IN. Hg) 

Pbar + (avg dH/13.6) 

1The method 5 sampling train is intended to operate at a sampling rate of 0. 75 cfm of 

dry air at 68 oF and 29.92 in. Hg. The orifice meter pressure differential that would produce 

such a sampling rate through the orifice is designated as IIH@. 

The theoretical nozzle calculation is optional. If the tester feels comfortable 

choosing the nozzle size through other means (experience, prior testing, etc.), this Is also 

acceptable. Dn (theoretical) is calculated on the assumption thai a 0.75 cfm flowrate is 

achieved at 68 "F and 29.92 in. Hg. 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 68 
30.16 1.80 

2) ABSOLUTE STACK PRESSURE 

Ps = PATM + Ps(GAUGE)/13.6 

PATM Ps(GAUGE) 

30.16 0.1 

30.29 

Ps 

30.17 

3) SAMPLE VOLUME AT STANDARD CONDITIONS 

VM STD = (VM)'(Y)"(T STDfTM)'(PMIP STD) 

Vm Tm y VmSTD 

173.44 542.25 1.000 170.97 ft3 

4) VOLUME OF WATER COllECTED, CORRECTED TO STAI\!DARO CONDITIONS 

W STD = W STOw+ WSTDsg 

W STDw = (.002673)'(VLQw)"(T STD/P STD) 

W STDsg = (.00266S)'VlQsg)'(T STDIP STD) 

WHERE 0.002673 = 0.04707 Ff3/ML'IN. HG/17.64 DEG. R. 

WHERE 0.002658 = 0.04715 FT3IG'IN.HGJ17.64 DEG. R. 

VLQ(w) 

122.00 

VLQ (sg) 

12.00 

WSTD 

6.32 ft3 

5) TOTAL SAMPLE VOLUME AT STANDARD CONDITIONS 

V STD =Vm STD+ WSTD = 177.29 ft3 

6) PERCENT MOISTURE IN STACK GAS 

%M • (100)'(VV STD)N STD = 3.56% 

1) MOLE FRACTION OF DRY GAS 

MD • (100-%M)/100 • o.9S4 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 69 
0.0 0.0 

9) MOLECULAR WEIGHT OF THE WET GAS 

M = (MWO)'(MO) + 18(1-MD) = 

79.1 

WHERE 18 =MOLECULAR WEIGHT OF WATER, GIG-MOLE 

10) STACK VELOCITY 

VS = (85.49)'(CP)'((TS/(PS)(M))'112"((SUM SORT DP)IN DP)) 

where 85.49 = f!lsec" Ubllb-mo!e"ln.Hg)/(deg. R"in H20)j"'.5 

CP 

0.84 

Ts (R) 

581.69 

SUMSQRT 

41.54 

11) STACK VOLUMETRIC FLOW RATE 

QS = (Sll)"(VS)"(AS) 

AS(lnleQ 

14.74 

NDP 

48 

QS 

45,251 

28.34 

2B.45 

VS 

51.1$ 

12) STACK VOLUMETRIC FLOW RATE, STANDARD CONDITIONS INCLUDING MOISTURE 

Q STD = Q STD DRY/MD 41,414 

13) STACK VOLUME FLOW RATE STANDARD CONDITIONS DRY 

Q STD DRY• 17.647"60"Md'Vs"N(Pslfs{R)) = 39,938 

14) POLLUTANT MASS RATE, CONCENTRATION BASIS 

PMRC = {.1323)"(WT).(Q STD)N STD 

WHERE 0.1323 • COMBINED CONVERSION FACTOR (60 MINIHR"0.00220 LBSIGRAM) 

Wf(GRAMS) 

0.0000 

15) PERCENT !SOKINETIC 

PMRC 

0.000 

%1 = (0.09450'Ts-"Vm std)/(Ps"Vs'"An"'Time"Md) 

Run Time Area of Nozzle 

240 2.64E-04 

ATC PROJECT No. P-10142 

%! 

99.66 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 70 
::; 

0 

"1J 

;o 

0 

~ 

m 

<:1 

z 

0 

I: 

s 

" N 

, 

c 

Glm 

c, 

~)> :Po 

"'1l;o 

m\:m 

-uz;:: -1-jmCiltn 

S:.r.,fa 

~~~ ;o 5Jl -i 

"'Cilm 

~);>00 

or- -I 

Oi1l 

"'" co 

;o~ 

..:m 

-oo 

\:-1 

z 

-1 

"' 

)> 

:;: 

m 

z 

0 

x 

~ m 

z 

? 

:1 

POI.l\JTANT 

PM 

HCI 

HCI 

"' "' "' Cl2 

OIOXIN/f!JAAN 

ANTIMONY jSb 7440-BG-01 

ARSENIC (A.s 74<1o-3a·2) 

BARIUM {58 7440-;1$-3} 

6Efl.'iWUM (&s! 7440-.41·7) 

CADMIUM (Cd 7440-43-9) 

CHROMIUM {Cl' 7440-47·3) 

CO!.W.T {Co 7441).46-4) 

COPPER (CU 7440·50-B} 

t.tAD {Pb 7439'·92·1) 

MAGNESIUM (Mg 7439-95-4) 

MANGANESE {Mo 7439--!16-5} 

Mereu I"{ {Hs 7439--97-6) 

NlCKa (N! 7440·02-0) 

PHOSPHORUS (P 1723-14-0) 

SEI.ENIUM !Se n82-49-2) 

SILVER (Ag 7440·22-4) 

THAU.IUM {TI7.:!40-28oOj 

ZINC {Zn7440--66-6) 

T~taiMeta!s 

0\FF 8AGHOUSE INUIT 

UNITS RUN#1 RUN#2 

!bs/1\r LOSE+OO 9.92E..01 

lbs/hr 7.86£..02 3.97£-01 

ppm 6.52E~02 3.17E+03 

!bs/hr 1.45E-~<OO 4.72E+OO 

ppm 6.SSE+03 2.13E+04 

!Wh< 2.971;:.02 2.41E.o.3 

ppm 4.79E+02 5.85E+Ol 

lbs/tlr 2.84E•l0 3A7E·10 

lb$/hr 3.30E..Q4 3.27E..Q4 

100/hr 1.55£..()4 1.54€·04 

!bs/hr 9.S9E'-o4 2.73E·03 

lbs/hr 1.65E-OS 1.6-JE-CIS 

lbsfhr 1.00E.o4 9.96E·IiS 

lbs/hr 6.1BE-o4 6.58E-o4 

ll:ts/hr Sl.61E-05 S.SOE-05 

!!1'$/hr l.OSE--04 2.18E·04 

lbs/hr l.QSE-\14 2.18E·0<1 

lbsfhr 3.17E.Q2 3.53E--02 

lbs/hr 8.1(lE-Q4 S.!lSE-o4 

lbs/hr 3.SSE-Q4 2.1SE·04 

lbs/llf 4.12£..04 4.351i·04 

lbs/hr S.57f-Q3 4,9;tE-03 

lbs/l!r 3.71E-<l4 4.61!E·04 

lbs/llr l.6$E-o4 1.64E-o4 

lbs/hr 1.6SE·C4 1.&1E-I» 

lb$/hr S.lOE-o<i 1.081;.03 

lbs/tu 4.32E·02 4.81E-<12 

BORALBRlCK 

EPA !CR EMISSION TEST SUMMARY 

AUGUSTA PLANT 4 

POLLUTANT EFFICIENCY CALCULATIONS 

IWN" AVERAGE 

4.54£·01 8.31f..01 

3-.S.Sl:..Ql 2.28£·0:1. HCI lb~/hr 1,2SE-o1 lAS.E.01 l.65E.01 1.441':.01 

:l.O&E+D3: 2.;m+0EJ HC! ppm SI.OSE.+Ol lME-o-03 l.l.9E+03 1.04E+<l3 

5.S:2E1-00 3.83£...00 HF '"""' 1.S3E..01 2:.!15E..01 3.01E.Ol 2A3i:-Ol 

2..31E+04 1.7010+04 "' ppm 7.651::+02. S.37&t02 l.1SEffi3: 9.52:1:«12 

2.2SE-o3 1.l.5E42 co lbs/hr 2.14E-03 :0A3E.OS !.>Sli-<>3 :l,,W£-03 

3,S2E...Ol 1.S4E+02 c" ppm 3.01E+01 3.43Ettll 2.73f+01 3.06E+Ql 

6.65E·1l 2.35E-10 OIOXlN/FURAN '"""' 0.00!<+00 5.6.SE·13 1.9SE·12 S.4SE-:13 

3.31E.(l4 3".29E..04 ANTIMONY (Sb 7440-31$-0) lbs/hr S.l6E...o4 3.22E.c4 3.:!4E-o4 3,2l£..Q4 

1.6&::..(15 1.15£-1)4 ARS~I•liC {As 744(0.38-2) liu/hr l.SSE...o4 l.lilE-04 1.82E-04 UOE-<>4 

2.93E-ro 2.<UE-tl3 SARIUM (Sa 7440-33.,j,~} tb$/hr .1.2$E.03 l..lSE-03 3,06!;-03 :;.,s;u;:~ 

1.65E--05 1,65€-0S BERYl.UUM (a<.t 7440-41·7) lb~/hr 1.5&:E·05 1.511:.05 1.62E-05 1.60£-0S 

1.01E-04 LOOHM CADMIUM (Cd 7440-4~9) lbs/hr 9.62E·OS &-67E..OS 9.85E-0-5 9,ne-os 

5.10E·04 5.99E..04 CHROMIUM (Ct7440-47•3} lbs/hr 3.a2E·04 3.89E-!l4 4.sm;.o4 4.10E-tl4 

9.64&05 9.60W.05 COMLT (Co 744(}-48-4) '"'"' 3.43E-o4 l.SBE--04 1.4SE-04 U6li·04 

1.79E-04 ;!:,0110-D<I COPPER (Cu 7440-SCI-8) IN/!'Ir 2.541':.04 l.Gll;.-()4 3.516-04 2.59E-o4 

1.65f2.04 l.BSS-<!4 u;AD (Pb 74SS..SH) !b~ht l,SSE-o.!l 1.61E-o4 1.75E-04 1.fiSE-Q4 

1.93E.Q2 2:.88£-1)2 MAGNESIUM {Mg 7439-95--4) lbs/nr M$E.Q3 3.9!JE.Q3 5.34E-03 3.$4E-Q3 

5.24E·04 7 .l3E-o4 MANGANESE {Mo 7439-96-!i) '"""' H41Hl4 3,12E--O¢ 5..WE..04 . 4.54E.Q4 "' 4.~E-<l4 3.-(;lE.-{14 Men:ury (Hg 14SHN:i) lbs/hr S.54E44 S.Si'E-o4 4.321::-IM 5.08E-o4 0 

4.41E-04 4.SOE-IM N!Cl{EI. (Ni 7440.02-0) ~ '"""' 3..69&-0<1 2.42E·04 3.7$5..().4 3,i30E-o4 

5.73E.03 5A4E..03 PHOSPHORUS {P 77.:!3·1-Hl) !bs/llr S.32E..03 4.S9E-Q3 4.51&03 4.9lE..03 ,.. 3.31E-04 3.89E-o4 SEL€NJUM (Se 71a2.·49·2) !bs/hr 3.15E.o4 3.2:2E-Q4 :3.24&-04 3.2lE-.04 "' ;o 

1.65E---04 1.6SE·04 SILVE~ (Ag 1440-22-4) lbsfhr 1.58E-04 1.51£-04 Hl2E-04 !.6oE-o4 0 

1.65E..Q4 1.65E-1» THAlUUM (l1744CI-2B-O) !bi/hr 1.58E..o4 1.61E-o4 i.62E-04 1.60E...:l4 :>< 

S.SSE-04 9.28£-04 ZINC {Zrl 744o-56-6-) '"""' l.U.E-D3- G.l$E·04 1.2SE..OS l.OOE-QS (/) 

3.24&02 4.12E.02 
HCI 

HF 

HF 

Cl2 

Cl2 

DIOXIN/FURAN 

ANTIMONY (Sb 7440-36-0) 

ARSENIC (As 7440-38-2) 

BARIUM (Sa 7440-39-3) BERYLliUM (Be 7440-41-7) 

CADMIUM (Cd 7440-43-9) 

CHROMIUM {Cr 7440-47-3) 

COBALT (Co 7440-48-4) 

COPPER (Cu 7440-50-8) 

LEAD (Pb 7439-92-1) 

MAGNESIUM (Mg 7439-95-4) 

MANGANESE (Mn 7439-96-5) 

Mercury (Hg 7439-97-6) NICKEL (Ni 7440-02-0) PHOSPHORUS (P 7723-14-0) 

SELENIUM (Se 7782-49-2) 

SILVER (Ag 7440-22-4) 

THALLIUM (TI 7440-28-0) 

ZINC (Zn 7440-66-6) 

Total Metals 

N/A" no rontrQI of pollutant demonstrated. 

ATC PROJECT No. P-10142 

pp

, 

N/A 

lbs/hr, %DE 86.69 95.02 

ppm, %DE 88.39 95.61 

lbs/hr, %DE 92.79 N/A 

ppm, %DE 93.71 10.92 

lbs/hr, %DE 100.00 99.84 lbs/hr, %DE 4.24 1.53 

lbs/hr, %DE 4.24 1.83 lbs/hr, %DE N/A 57.88 lbs/hr, %DE 4.24 1.83 lbs/hr, %DE 3.80 2.91 lbs/hr, %DE 33.19 41.77 lbs/hr, %DE N/A N/A lbs/hr, %DE N/A 26.15 lbs/hr, %DE 4.24 26.15 lbs/hr, %DE 92.15 88.70 lbs/hr, %DE 36.54 60.00 lbs/hr, %DE N/A N/A lbs/hr, %DE 10.44 44.50 

lbs/hr, %DE 6.17 0.41 

lbs/hr, %DE 14.82 30.60 lbs/hr, %DE 4.24 1.83 lbs/hr, %DE 4.24 1.83 lbs/hr, %DE N/A 42.78 

lbs/hr, %DE 67.69 71.11 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5. SALISBURY PLANT 6 

SEPTEMBER 2010 

94.34 92.02 

94.88 92.96 

14.04 53.41 

22.44 42.36 

97.02 98.95 

2.11 2.63 

N/A 3.04 N/A 57.88 

1.82 2.63 

2.48 3.06 

10.00 29.98 

N/A N/A 

N{A 26.15 

N/A 15.19 

72.33 84.39 

N/A 48.27 

7.59 7.69 

14.29 23.07 

21.29 9.29 

2.11 15.85 

1.82 2.63 1.82 2.63 

N/A 42.78 

44.67 61.16 

APPENDIX PAGE No. 72 
PLANTS 

FIELD DATA CALCULATIONS 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 73 
)> 

c: 

~ "1J 

~ ~ 

Q 

?r 

~ 

:< 

.. 

"' 

Qm c., 

~)> 

)>0 

CJ)'O;o 

mt;;m :!jz:S: 

m-100 ;g;CJ)(J) 

ro,::..O 

m"'z 

;::o ~Ul -l 

"'(J)m S!::r>cn or-! 

(ii"lJ 

ro:o 

co 

;o~ 

-<m -o" 

s;:-1 

z 

-1 

"' 

)> 

"1J 

'0 

m 

z 

~ 

m 

~ 

z 

? 

g: 

Method 1 - Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance- Far Wall to Outside of Port (in) 

Distance- Near Wall to Outside of Port (In) 

Inside Diameter of Stack (in) 

Port Diameter- For Ref. Only (in) 

Distance to Upstream Disturbance (ft) 

Distance to Downstream Disturbance (ft) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default is 1.0 inch) 

84.50 

9.50 Port Length 

75.00 

4.00 

25.00 

40.00 

4.00 

6.40 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

1 

8 

9 

10 

11 

12 

Conversion Table for Decimal to Inch Fraction 

1/16 i/8 3/16 1/4 5/16 

0.06 0.13 0. iS 0.25 0.31 

PROBE MARKINGS 

Decimal Inches 

Number of Traverse Points on a Diameter 

2 4 6 8 

20.45 14.53 12.80 11.90 

73.55 28.25 20.45 17.38 

65.75 31.70 24.05 

79.48 62.30 33.73 

73.55 60.28 

81.20 69.95 

76.63 

82.10 

10 

11.45 

15.65 

20A5 

26.45 

35;15 

58.85 

67.55 

73.55 

78.35 

82.55 

3/8 

0.38 

12 

11.08 

14.53 

18.35 

22.78 

28.25 

36.20 

57.80 

65.75 

71.23 

75.65 

79.48 

82.93 

to 

0 

$1 

r 

"' ;o 

0 

" 

CJl 
ATC PROJECT Noo P-10142 

34.08 

Vl.Q (ml) 48.00 37.00 48.00 

WSTD{ft3} 2.26 1.74 2.26 V STD (ft3) 37.71 36.72 36.34 

'"" 6.00 4.75 6.23 %SVP1 100.00 100.00 100.00 

MD 0.940 0.952 0.938 

MWD 29.05 29.05 29.05 

M 28.39 28.52 28.36 

Ts(F) 352.00 351.04 352.25 

Ts(R) 811.69 810.73 811:94 SUMSQRTDP 11.57 11.73 11.73 

NDP 24.00 24.00 24.00 AVGSQRTDP 0.48 0.49 0.49 CP 0.84 0.84 0.84 vsifltSJ 33.89 34.26 34.39 Ds (in} 75.00 75.00 75.00 

As(ff~ 30.68 30.68 30.68 QS, FLOW, ACFM 62,386 63,069 63,313 Q sro (ft3/mln} 40,447 40,945 41,015 Q STD DRY, FLOW SCFM 38,019 39,000 38,461 wr(gm}-PM 0.0000 0.0014 0.0004 WT(gm)-HCL 0.0003 0.0003 0.0003 wr(gm)-HF 0.0023 0.0021 0.0021 WT(gm) • CIZ 1.3SE~05 1.55E...05 f.61ENQ5 

%/ 106.18 102.12 100.91 

%C02 1.98 1.92 1.98 %02 18.39 18.50 18,41 %CO 0.00 0.00 0.00 

%N2 79.63 79.58 79.61 PM(Ibslhr) 0.000 0.207 0.060 PM(kg/hrj 0.0000 0.0937 0.0271 Production (tph) 14.65 14.65 14.65 Production (Mg) 6.85E...o3 8.65E-03 6.85E-03 

PM (kg/Mg of ProduCt} 5.10E-~-oo 5.16E.,.OO 5.18E+OO PM (mgldscm) 4.00E+04 4.05E+04 4.06E+04 PM (mg/dscm@ 7% 02) 2.22E+05 2.34E+05 2.27E+05 HCI (lbS/hr) 4.67E-02 4.18E-02 4.66E-02 

HCJ (kg/hr) 2.12E-02 U9E...02 2.11E-02 HCI (kg/Mg of Product) 1.13E+01 1.13E+01 1.13E+01 

HCI(ppm) 287.49 250.65 283.57 HCI (ppm @ 7% 02) 1593.61 1451.66 1584.45 

HF(Ibslhr) 3.21E-01 3.09E-01 3.17E-01 

HF(kg/hr) 1.45E-01 1.40E-01 1.44E-01 HF (kg/Mg ofProduct) 4.62E+OO 4.62E+OO 4.62E+OO 

HF(ppm) 1083.36 1016.88 1057.97 HF (ppm @ 7% OZ) 6005.29 5889.41 5911.47 Cl2 (lbslhr) 1.96E-03 2.29E-03 2.40E-03 

C/2 (kglhr} 8.88E-04 1.04E-03 1.09E-03 C/2 (kg/Mg of Product) 9.39E+03 9.49E+03 9.53E+03 

Cl2{ppm) 23.45 26.70 28.46 Cl2 (ppm @ 7% 02) 130.00 154.63 159.02 QS, FLOW, ACMM 1767 1786 1793 QS, FLOW, DSCMM 1077 1104 1089 

1 Theoretical amount of moisture that Ts can hofd. 

ff%M>%SVP, %SVP wlfl be utilized In calculations. 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SAliSBURY PlANT 6 

SEPTEMBER 2010 

5.66 

351.76 

811.45 

34.18 

62,923 

40,803 

38,493 

0.0006 

0.0003 

0.0022 

0.0000 

1.96 

18.43 

0.089 

0.0403 

14.6500 

6.65E-03 

5.14E+00 

4.04E+04 

2.2BE+05 

4.50E-02 

2.04E-02 

1.13E+01 

273,90 

1543.24 

3.15E-01 

1.43E-01 

4.62E+00 

1052.74 

5935.39 

2.22E-03 

1.01E-03 

9.47E+03 

26.20 

147.88 

1782 

1090 

APPENDIX PAGE No. 86 
A3 82 357 0.26 1.29 0.510 

A4 83 357 0.28 1.39 0.529 

A5 84 356 0.26 1.29 0.510 

A !I 86 356 0.24 1.19 0.490 

A7 89 355 0.28 1.39 0.529 18.5 2.0 

A8 90 350 0.25 1.24 0.500 

A9 90 350 0.22 1.09 0.469 

A10 91 345 0.21 1.04 0.458 

A11 92 345 0.20 0.99 0.447 

A12 93 340 0.18 0.89 0.424 

81 94 357 0.28 1.39 0.529 18.4 2.1 

B2 95 357 0.27 1.34 0.520 

83 96 357 0.26 1.29 0.510 

B4 96 357 0.25 1.24 0.500 

85 96 354 0.24 1.19 0.490 

85 97 352 0.23 1.14 0.480 

87 97 352 0.23 1.14 0.480 18.6 1.8 

88 97 351 0.21 1.04 0.458 

89 97 351 0.20 0.99 0.447 

810 97 350 0.18 0.89 0.424 

811 97 347 0.18 0.89 0.424 

812 97 341 0.16 0.79 0.400 18.5 1.9 

91.54 352.00 0.23 1.16 11.568 18.48 1.98 

corrected per 7 e-5b 18.39 

Vm(ft3) Initial 29.31 % N2 (BY DIFFERENCE) 79.63 

Final 

Total 

ATC PROJECT No. P-10142 

67.78 

38.47 %Excess Air 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

699.53 

APPENDIX PAGE No. 87 
A3 98 356 0.27 1.35 0.520 

A4 98 356 0.27 1.35 0.520 

A5 98 354 0,28 1.40 0.529 

A6 98 354 0.28 1.40 0.529 

A7 98 354 0.28 1.40 0.529 18.6 1.8 

A8 99 350 0.26 1.30 0.510 

A9 99 350 0.23 1.15 0.480 

A10 100 348 0.20 1.00 0.447 

A11 100 345 0.20 1.00 0.447 

A12 100 340 0.19 0.95 0.436 

81 100 356 0.29 1.45 0.539 18.4 2.1 

82 100 356 0.28 1.40 0.529 

B3 101 356 0.27 1.35 0.520 

B4 101 355 0.25 1.25 0.500 

85 102 355 0.25 1.25 0.500 

B6 102 354 0.23 1.15 0.480 

87 102 348 0.23 1.15 0.480 18.6 1.7 

88 102 347 0.20 1.00 0.447 

89 102 347 0.20 1.00 0.447 

1310 103 346 0.19 0.95 0.436 

811 103 344 0.19 0.95 0.436 

B12 103 340 0.17 0.85 0.412 18.6 1.8 

100.13 351.04 1),24 1.21) 11.730 18.50 1.92 

corrected per 7 e-5b 18.50 

Vm(ft3) Initial 67.85 % N2 (BY DIFFERENCE} 79.58 

Final 106.38 

Total 38.53 %Excess Air 737.31 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 88 
AS 103 356 0.26 1.31 0.510 

A6 104 354 0.28 1.41 0.529 

A7 104 354 0.27 1.36 0.520 18.6 1.9 

A8 105 354 0.26 1.31 0.510 

A9 105 351 0.23 1.16 0.480 

A10 105 351 0.22 1.10 0.469 

. A11 106 350 0.21 1.05 0.458 

A12 106 345 0.20 1.00 0.447 

81 106 357 0.28 1.41 0.529 18.5 2.0 

82 107 357 0.27 1.36 0.520 83 107 354 0.27 1.36 0.520 

84 108 354 0.28 1.41 0.529 85 108 353 0.24 1.21 0.490 86 108 353 0.24 1.21 0.490 

87 108 353 0.23 1.16 0.480 18.6 1.9 

88 108 352 0.20 1.00 0.447 

89 109 350 0.20 1.00 0.447 

810 109 350 0.18 0.90 0.424 

811 109 345 0.17 0.85 0.412 

812 110 341 0.17 0.85 0.412 18.6 1.8 

106.04 352.25 0.24 1.21 11.730 18.50 1.98 

corrected per 7e-5b 18.41 

Vm(ft3) Initial 106.44 % N2 (BY DIFFERENCE) 79.61 

Final 

Total 

ATC PROJECT No. P-10142 

144.41 

37.97 %Excess Air 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

707.05 

APPENDIX PAGE No. 89 
ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 90 
6Jf = [846. 72 X D:X AH@ X c! (1- Bwj X MdTm~ J X Ap Ms~Pm BORALBRICK 

Module ID 

Dn 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACTION,NOT"/o} 

Md 

Pbar 

PS(GAUG£) 

Ps 

Tm,F 

Tm,R 

Ms 

Ts,F 

Ts1 R 

Pm 

K 

Terminology 

9117/2010 

Run#1 Run#2 Run#3 

ATC3 ATC3 ATC3 

0.287 0.287 0.287 

1.937 1.937 1.937 

0.963 0.963 0.963 

0.84 0.84 0.84 

0.03 0.05 0.05 

29.0 29.0 29.0 

29.80 29.81 29.79 

0.28 0.22 0.22 

29.32 29.83 29.111 

80 100 105 

539.69 559.69 564.69 

28.67 28.45 28.45 

350 350 350 

809.69 809.69 809.69 

29.91 29.89 29.90 

4.9658 4.9830 5.0220 

Ms=APPARENT STACK GAS MOLECULAR WEIGHT 

=Md(i-Bw)+18Bw 

Md=DRY GAS MOLECULAR WEIGHT (29) OR 

=(0.44"%C02)+(0.32"%02)+(0.28*(%N2+%CO)) 

Ps GAUGE=STACK STATIC PRESSURE (IN. H20) 

Ps=ABSOLUTE STACK PRESSURE {IN. Hg) 

Pm=METER ABSOLUTE PRESSURE (IN. Hg) 

= Pbar + (avg dH/13.6) 

'The method 5 sampling train is intended to operate at a sampling rate of 0. 75 cfm of 

dl)l air at 68 oF and 29.92 in. Hg. The orifice meter pressure differential that would produce 

such a sampling rate through the orifice is designated as LIH@. 

The theoretical nozzle calculation is. optional. If the tester feels comfortable 

choosing the nozzle size through other means (experience, prior testing1 etc.}, this is also 

acceptable. Dn (theoretical) is calculated on the assumption that a 0. 75 cfm ftowrate is 

achieved at 68 °F and 29.92 in. Hg. 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 91 
Air Pollution Controls DIFF Baghouse Inlet 

Test Methods USEPA M 29 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 92 
Process Tested DIFF Baghouse Outlet 

Specific Source Plant 5 

Air Pollution Controls DIFF Baghouse Outlet 

Test Methods USEPA M 29 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 103 
~ a 

" e5 

~ 

~ z 

0 

:!:: 

s: 

... 

"' 

§ 

c:m 

~~ 

>fi 

(/)-o;o 

mS::m 

-oz;: -<..;-

ll1(/)(/) 

s:.j:>.~ 

ro,.o 

~Olz - -< "-'(l)m 

~)>en 

or-< 

(i)-o 

ro;o 

co 

,~ 

-<m 

s;; "~ 

":] 

"' 

)> 

" 

~ z 

0 

x 

~ m 

z 

5' 

z 

Method 1 -Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance- Far Wall to Outside of Port (in) 

Distance- Near Wall to Outside of Port (in) 

Inside Diameter of Stack (in) 

84.50 

9.50 Port Length 

75.00 

Port Diameter- For Ref. Only (in) 4.00 

Distance to Upstream Disturbance (ft) 

Distance to Downstream Disturbance (ft) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default is 1.0 inch) 

25.00 

40.00 

4.00 

6.40 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

Conversion Table for Decimal to Inch Fraction 

1116 118 3116 114 5116 

0.06 0.13 0.19 0.25 0.31 

PROBE MARKINGS 

Decimal Inches 

Number of Traverse Points on a Diameter 

2 4 6 8 

20.45 14.53 12.80 11.90 

73.55 28.25 20.45 17.38 

65.75 31.70 24.05 

79.48 62.30 33.73 

73.55 60.28 

81.20 69.95 

76.63 

82.10 

10 

11.45 

15.65 

20.45 

26.45 

35.15 

58.85 

67.55 

73.55 

78.35 

82.55 

3/8 

0.38 

12 

11.08 

14.53 

18.35 

22.78 

28.25 

36.20 

57.80 

65.75 

71.23 

75.65 

79.48 

82.93 

OJ 

0 

,-

~ 

"' "' fi 

"' en 
AVG DH (in H20) 1.22 1.20 1.17 

PATM(InHg} 29.75 29.72 29.72 

Pm(ln Hg} 29.84 29.81 29.81 

Ps(GAUGE) 0.28 0.22 0.22 

Ps(IN HG) 29.77 29.74 29.74 

Tm(F) 104.79 99.42 89,71 

Tm(R} 564.48 559.11 549.40 

Vm (ft3) 38.18 37.31 35.88 

VmSTD(ft3} 34.30 33.80 33.08 

VLQ(ml) 40.50 40.50 48.00 

WSTD(ft3} 1.91 1.91 2.26 

V STD (ft3) 36.21 35.71 35.35 

%M 5.27 5.35 6.40 5.67 

%SVP1 100.00 100.00 100.00 

MD 0.947 0.947 0.936 

MWD 29.05 29.05 29.05 

M 28.47 28.46 28.35 

Ts(F) 355.71 353.25 356.46 355.14 

Ts(R) 815.40 812.94 816.15 814.83 

SUMSQRTDP 11.80 11.78 11.73 

NDP 24.00 24.00 24.00 

AVGSQRTDP 0.49 0.49 0.49 

CP 0.84 0.84 0.84 

Vs (ftls) 34.64 34.55 34.55 34.56 

Ds (in} 75.00 75.00 75.00 

As (ft2) 30.68 30.68 30.68 

QS, FLOW, ACFM 63,772 63,595 63,592 63,653 

Q STD (ft3/mln) 41,088 41,050 40,887 41,00$ 

Q STD DRY, FLOW SCFM 38,922 38,856 38,269 38,682 

WT(gm) 0.0021 0.6231 0.0626 0.2293 

%1 100.37 99.08 98.45 

%C02 1.98 1.92 1.98 1.96 

%02 18.39 18.50 18.41 18.43 

%CO 0.00 0.00 0.00 %N2 79.63 79.58 79.61 

1 Theoretical amount of moisture that Ts can hold. 

If %M>%SVP, %SVP will be utilized in calculations. 

j 

v 

.Lu 

q 

D· 91.:::2> 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 105 
A2 101 360 0.26 1.31 0.510 

A3 102 360 0.28 1.41 0.529 

A4 104 360 0.28 1.41 0.529 

A5 104 360 0.27 1.36 0.520 

A6 104 361 0.28 1.41 0.529 

A7 104 361 0.25 1.26 0.500 

A8 105 361 0.24 1.21 0.490 

A9 105 360 0.24 1.21 0.490 

A10 105 355 0.20 1.00 0.447 

A11 105 354 0.19 0.95 0.436 

A12 105 353 0.19 0.95 0.436 

81 105 362 0.24 1.21 0.490 

82 106 360 0.26 1.31 0.510 

83 106 359 0.28 1.41 0.529 

84 106 357 0.30 1.51 0.548 

85 106 357 0.30 1.51 0.548 

86 106 357 0.26 1.31 0.510 

87 106 348 0.26 1.31 0.510 

88 106 347 0.24 1.21 0.490 

89 106 347 0.20 1.00 0.447 

811) 106 344 0.20 1.00 0.447 

811 106 344 0.18 0.90 0.424 

812 106 344 0.19 0.95 0.436 

104.79 355.71 ().24 1.22 11.804 19.50 1.20 

corrected per 7e-5b 19.51) 

Vm(ft3) Initial 145.04 % N2 (BY DIFFERENCE) 79.30 

Final 183.22 

Total 38.18 %Excess Air 1358.70 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 106 
A1 103 360 0.24 1.19 0.490 19.4 1.3 

A2 103 364 0.27 1.34 0.520 

A3 103 364 0.27 1.34 0.520 A4 103 360 0.28 1.39 0.529 

A5 102 359 0.27 1.34 0.520 A6 102 355 0.25 1.24 0.500 

A? 101 351 0.25 1.24 0.500 

AB 101 348 0.25 1.24 0.500 

A9 101 349 0.24 1.19 0.490 

A10 100 347 0.20 1.00 0.447 A11 100 345 0.20 1.00 0.447 A12 99 343 0.19 0.95 0.436 

81 99 365 0.25 1.24 0.500 

82 99 362 0.25 1.24 0.500 

B3 98 361 0.28 1.39 0.529 B4 98 359 0.29 1.44 0.539 Bfi 97 359 0.30 1.49 0.548 

Bll 97 358 0.26 1.29 0.510 

B7 97 352 0.26 1.29 0.510 

BB 97 345 0.21 1.04 0.458 

B9 97 345 0.21 1.04 0.458 

810 97 345 0.21 1.04 0.458 

B11 96 342 0.19 0.95 0.436 

B12 96 340 0.19 0.95 0.436 

99.42 353.25 0.24 1.20 11.780 19.40 1.30 

corrected per 7e-5b 19.4() 

Vm(ft3) Initial 183.41 % N2 (BY DIFFERENCE) 79.31) 

Final 220.72 

Total 37.31 %Excess Air 1263.88 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5. SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 107 
A2 92 360 0.28 1.37 0.529 

A3 92 360 0.28 1.37 0.529 

A4 92 360 0.26 1.27 0.510 

A5 91 359 0.26 1.27 0.510 

A6 91 358 0.27 1.32 0.520 

A7 90 358 0.27 1.32 0.520 

A8 90 355 0.24 1.17 0.490 

A9 90 353 0.22 1.08 0.469 

MO 90 347 0.19 0.93 0.436 

A11 90 345 0.20 0.98 0.447 

A12 90 344 0.19 0.93 0.436 

81 90 362 0.26 1.27 0.510 

82 90 364 0.26 1.27 0.510 

83 90 364 0.26 1.27 0.510 

84 90 364 0.25 1.22 0.500 

85 89 363 0.27 1.32 0.520 

86 89 362 0.27 1.32 0.520 

87 88 361 0.24 1.17 0.490 

88 88 358 0.20 0.98 0.447 

89 88 358 0.20 0.98 0.447 

810 87 348 0.21 1.03 0.458 

811 87 346 0.21 1.03 0.458 

812 87 346 0.21 1.03 0.458 

89.71 356.46 0.24 1.17 11.733 19.10 1.50 

corrected per 7 e-5b 19.10 

Vm{ft3) Initial 220.83 % N2 (BY DIFFERENCE) 79.40 

Final 256.71 

Total 35.88 %Excess Air 1026.00 

ATC PROJECT No. P·10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5. SALISBURY PlANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 108 
Run#2 

BEGINNING 

ENDING 

NET 

Run#3 

BEGINNING 

ENDING 

NET 

ATC PROJECT No. P-10142 

1st Imp. 2nd Imp. 3rdl41h Imp. 

100 100 200 130 100 200 

30 0 0 

1st Imp. 2nd Imp. 3rd/4th Imp. 

100 100 200 128 112 200 

28 12 0 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 2010 

5th Imp. TOTALS 

300.0 

310.5 

10.5 40.5 

5th Imp. TOTALS 

300.0 

308.0 

8.0 48.0 

APPENDIX PAGE No. 109 
!

i

H = [846. 72 X x !

i

H@ X c! ( 1-Bws )

x MdTmP.: J x !lp 

MsT..Pm 

Modu/eiD 

Dn 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACTION,NOT%) 

Md 

Pbar 

PS(GAUGE) 

Ps 

Tm,F 

Tm,R 

Ms 

Ts, F 

Ts, R 

Pm 

K 

BORAL BRICK 

9/17/2010 

Run#1 Run#2 Run #3 

ATC3 ATC3 ATC3 

0.287 0.287 0.287 

1.937 1.937 1.937 

0.963 0.963 0.963 

0.84 0.84 0.84 0.05 0.05 0.05 

29.0 29.0 29.0 

29.75 29.72 29.72 

0.28 0.22 0.22 

29.77 29.74 29.74 

105 100 90 

564.69 559.69 549.69 

28.45 28.45 28.45 

350 350 350 

809.69 809.69 809.69 

29.86 29.84 29.81 

5.0223 4.9755 4.8917 

Terminology 

Ms=APPARENT STACK GAS MOLECULAR WEIGHT 

=Md(1-Bw)+18Bw 

Md=DRY GAS MOLECULAR WEIGHT (29) OR 

=(0.44'%C02)+(0.32'%02)+(0.28'(%N2+%CO)) 

Ps GAUGE=STACK STATIC PRESSURE (IN. H20) 

Ps=ABSOLUTE STACK PRESSURE (IN. Hg) 

Pm=METER ABSOLUTE PRESSURE (IN. Hg) 

= Pbar + (avg dH/13.6) 

1The method 5 sampling train is intended to operate at a sampling rate of 0.75 cfm of dry air at 68 

oF and 29.92 in. Hg. The orifice meter pressure differential that would produce such a sampling rate 

throuqh the orifice Is desionated as 1\H,_ 

The theoretical nozzle calculation is optional. If the tester feels comfortable choosing the 

nozzle size through other means (experience, prior testing, etc.), this is also acceptable. Dn 

(theoretical) is calculated on the assumption that a 0. 75 cfm flowrate is achieved at 68 °F and 29.92 in. 

Ho 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 110 
2) ABSOLUTE STACK PRESSURE 

Ps = P ATM + Ps(GAUGE)/13.6 

PATM Ps(GAUGE) 

29.75 0.28 

Ps 

29.77 

3) SAMPLE VOLUME AT STANDARD CONDITIONS 

VM STO = (VM)"(Y)"(T STDffM)"(PMIP STD) 

Vm Tm y VmSTD 

38.18 564.48 0.963 34.30 

ft3 

4} VOLUME OF WATER COLLECTED, CORRECTED TO STANDARD CONDITIONS 

W STD::: W STOw+ WSTDsg 

W STDw • (.002673)'(VLOwt(T STDIP STD) 

W STDsg = (.002668)"\/LQsg)'(T STOlP STD) 

WHERE 0.002673 • 0.04707 FT31ML 'IN. HG/17.64 DEG. R. 

WHERE 0.002668 = 0.04715 FT3/G'IN.HGI17.64 DEG. R. 

VLQ (w) 

30.00 

VLQ (sg) 

10.50 

WSTD 

1.91 ft3 

5) TOTAL SAMPLE VOLUME AT STANDARD CONDITIONS 

V STD=Vm STD +W STD = 36.21 ft3 

6) PERCENT MOISTURE IN STACK GAS 

%M = (100)"(W STO)N STD = 5.27% 

7) MOLE FRACTION OF DRY GAS 

MD= (100--%M)/100"' 0.947 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 111 
1.2 19.5 0.0 

9) MOLECULAR WEIGHT OF THE WET GAS 

M = (MWD)"(MD) + 18(1-MD) = 

79.6 

WHERE 18 =MOLECULAR WEIGHT OF WATER, GIG-MOLE 

10) STACK VELOCITY 

VS = (85.49)"(CP)"((TSI(PS)(M))A1f2'({SUM SORT DP)IN DP)) 

where 85.49 = ftlsec~ (lbllb--mole"in.Hg}/{deg. R"in H20)]"0.5 

CP 

0.84 

Ts(R) 

815.40 

SUM SORT 

11.80 

11) STACK VOLUMETRIC FLOW RATE 

OS = (60)*(VS)*(AS) 

AS (Inlet) 

30.68 

NDP 

24 

QS 

63,759 

29.06 

28.48 

vs 

34.64 

12) STACK VOLUMETRIC FLOW RATE, STANDARD CONDITIONS INCLUDING MOISTURE 

Q STD = Q STD DRY/MD 41,080 

!3) STACK VOLUME FLOW RATE STANDARD CONDITIONS DRY 

0 STD DRY= 17.647'60'Md"Vs'A'(Ps1Ts(R)) = 38,914 

14) POLLUTANT MASS RATE, CONCENTRATION BASIS 

PMRC = (. 1323)'(WT)'(Q STD)N STD 

WHERE 0.1323 =COMBINED CONVERSION FACTOR (60 MIN/HR•o.00220 LBSIGRAM) 

WT(GRAMS) 

0.0021 

15) PERCENT ISOKINET!C 

PMRC 

0.315 

%1 • (0.09450'Ts'llm std)I(Ps"\\s'An'Time•Mct) 

Run Time Area of Nozzle %1 

60 4.49E-04 100.39 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 112 
ATC PROJECT No. P·10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 2010 

APPENOIX PAGE No. 113. 
Barium lBa 7440-39-3) 

Beryllium {Be 7440-41-7) 

Cadmium (Cd 7 440-43--9) 

Chromium (Cr 7440--47-3} 

Cobalt (Co 7440-48-4) 

Copper (Cu 7440-50-8) 

Magnesium (Mg 7 439-95-4 

Manganese (Mn 7 439-96-5) 

Mercury (Hg 7 439-97 -6) 

Nickel (Ni 7 440-02-0) 

Phosphorus (P 7723-14-0) 

Selenium {Se 7782-49-2) 

Silver (Ag 7 440-22-4) 

Thallium (TI 7 440-28-0) 

Zinc (Zn 7 440-66-6) 

ATC PROJECT No. P-10142 

1.42E-03 6.43E-04 

1.93E-05 8.76E-06 

1.17E-04 5.30E-05 

3.91E-04 1.77E-04 

1. i3E-04 5.11E-05 

3.32E-04 1.51E-04 

1.81 E-03 8.21E-04 

1.35E-03 6.10E-04 

1.03E-03 4.67E-04. 

2.90E-04 1.32E-04 

5.08E-03 2.30E-03 

3.97E-04 1.80E-04 

1.93E-04 8.76E-05 

1.93E-04 8.76E-05 

1.42E-03 6.42E-04 

1.32E-06 

1.81E-08 

1.09E-07 

3.66E-07 

1.05E-07 

3.11E-07 

1.72E-06 

1.26E-06 

9.63E-07 

2.71E-07 

4.75E-06 

3.71E-07 

1.81E-07 

1.81E-07 

1.32E-06 

EPA !CR. EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

9.23E-03 4.95E-02 

1.26E-04 6.74E-04 

7.61E-04 4.08E-03 

2.55E-03 1.37E-02 

7.33E-04 3.93E-03 

2.16E-03 1.16E-02 

1.18E-02 6.31E-02 

8.75E-03 4.69E-02 

6.70E-03 3.59E-02 

1.89E-03 1.01E-02 

3.31E-02 1.77E-01 

2.58E-03 1.39E-02 

1.26E-03 6.74E-03 

1.26E-03 6.74E-03 

9.21E-03 4.94E-02 

APPENDIX PAGE No. 114 
g

Specific Source Plant 5 

Air Pollution Controls DIFF Baghouse Outlet 

Test Methods USEPA M 23 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 126 
1: 

~ 

" 2 

m 

~ 

z 

? 

2: 

:1 

.... 

"' 

"'m c., 

~, 

»o 

"'""' m);rn 

-uzs: -<...,-

men~ 

s: .. - ~Qo~ ;o 91 -I 

"'"'m 

o_., ~F:~ 

gj, 

co 

,~ 

-<m 

.,o 

s;-< 

~ 

"' 

, 

:g 

m 

z 

0 

5< 

~ m 

z 

? 

"' ..., 

Method 1 ·Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance. Far Wall to Outside of Port (in) 

Distance· Near Wall to Outside of Port (in) 

Inside Diameter of Stack (in) 

84.50 

9.50 Port Length 

75.00 

Port Diameter. For Ref. Only (in) 4.00 

Distance to Upstream Disturbance (ft) 

Distance to Downstream Disturbance (ft) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default is 1.0 inch) 

25.00 

40.00 

4.00 

6.40 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

Conversion Table for Decimal to Inch Fraction 

1/16 1/8 3/16 1/4 5/16 

0.06 0.13 0.19 0.25 0.31 

PROBE MARKINGS 

Decimal Inches 

Number of Traverse Points on a Diameter 

:1. 4 6 8 

20.45 14.53 12.80 11.90 

73.55 28.25 20.45 17.38 

65.75 31.70 24.05 

79.48 62.30 33.73 

73.55 60.28 

81.20 69.95 

76.63 

82.10 

10 

11:45 

15.65 

20.45 

26.45 

35.15 

58.85 

67.55 

73.55 

78.35 

82.55 

3/8 

0.38 

12 

11.08 

14.53 

18.35 

22.78 

28.25 

36.20 

57.80 

65.75 

71.23 

75.65 

79.48 

82.93 

"' 0 

52 

r-

(D 

;o 

1'5 

@ 
(

g) 

29.91 29.84 

Ps (GAUGE) 0.22 0.22 0.22 

Ps(IN HG) 29.77 29.84 29.77 

Tm(F) 78.21 97.96 93.08 

Tm(R} 537.90 557.65 552.77 

Vm (ft3} 146.22 152.03 152.66 

Vm STD(fiJ} 137.83 138.58 140.05 

VI.Q (ml) 140.50 140.50 140.50 

WSTD(f/3) 6.63 6.63 6.63 

V STD (ft3} 144.46 145.20 146.68 

%M 4.59 4.56 4.52 4.56 

%SVP1 100.00 100.00 100.00 

MD 0.954 0.954 0.955 

MWD 29.06 29.10 29.09 

M 28.56 28.59 28.59 

Ts(F) 360.98 359.27 360.25 360.17 

Ts(R) 820.67 818.96 819.94 819.86 

SUMSQRTDP 23.90 24.07 24.35 

NDP 48.00 48.00 48.00 

AVGSQRTDP 0.50 0.50 0.51 

CP 0.84 0.84 0.84 

Vs (ftfs) 35.13 35.27 35.77 35.39 

Ds (in) 75.00 75.00 75.00 

As (f/2) 30.68 30.68 30.68 

QS, FLOW, ACFJ!I 64,668 64,933 65,839 65,147 

Q STD (f/3/min) 41,392 41,746 42,179 41,772 Q STD DRY, FLOW SCFM 39,493 39,841 40,274 39,869 

WT(gm) 1.21E-10 6.34E-11 4.50E-11 7.65E-11 

%1 99.37 99.03 99.01 

%C02 2.03 2.03 2.03 2.03 

%02 18.50 19.40 19.10 19.00 

%CO 0.00 0.00 0.00 

%N2 79.48 78.58 78.88 

D!F (lbslhr) 4.59E-09 2.41E-09 1.71 E-09 2.90E-09 

DIF{kg!hr) 2.08E-09 1.09E.Q9 7.77E-10 1.32E-09 

Production (tph) 14.65 14.65 14.65 1.47E+01 

Production (J!Ig) 6.65E-03 6.65E-03 6.65E-03 6.65E-03 

D!F (kg!Mg of Product) 1.82E-11 9.541E-12 6.772E-12 1.15E-11 

D!F (ngldscm) 3.100E-02 1.615E-02 1.135E-02 1.95E-02 

D!F (ngldscm@ 7% 02) 1.80E-01 1.50E-01 8.76E-02 1.39E-01 

QS, FLOW, ACMM 1831 1839 1864 1845 

QS, FLOW, DSCMM 1118 1128 1140 1129 

Theoretical amount of moisture that Ts can hold. 

If %M>%SVPv %SVP will be utilized in calculations . 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT . APPENDIX PAGE No. 128 

AUGUST A PlANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 
A3 93 360 0.28 1.38 0.529 

A3 94 364 0.28 1.38 0.529 

A4 94 364 0.31 1.53 0.557 

A4 94 364 0.31 1.53 0.557 

AS 95 364 0.31 1.53 0.557 

AS 95 364 0.31 1.53 0.557 

A6 95 364 0.24 1.18 0.490 

A6 95 363 0.24 1.18 0.490 

A7 00 363 0.24 1.18 0.490 18.5 2.0 

A7 96 363 0.24 1.18 0.490 

A8 96 364 0.26 1.28 0.510 

A8 97 364 0.26 1.28 0.510 

A9 97 364 0.28 1.38 0.529 

A9 97 362 0.28 1.38 0.529 

A10 97 362 0.28 1.38 0.529 

A10 97 362 0.28 1.38 0.529 

A11 97 362 0.21 1.04 0.458 

A11 97 362 0.21 1.04 0.458 

A12 97 362 0.21 1.04 0.458 

A12 97 360 0.21 1.04 0.458 

81 98 368 0.24 1.18 0.490 18.4 2.1 

81 98 368 0.24 1.18 0.490 

82 97 363 0.29 1.43 0.539 

B2 97 361 0.29 1.43 0.539 

83 98 359 0.30 1.48 0.548 

83 100 358 0.30 1.48 0.548 

84 100 358 0.31 1.53 0.557 

84 100 358 0.31 1.53 0.557 

85 100 358 0.25 1.23 0.500 

85 101 358 0.25 1.23 0.500 

B6 101 355 0.22 1.08 0.469 

86 101 355 0.22 1.08 0.469 

87 102 355 0.24 1.18 0.490 18.6 1.9 

87 102 354 0.24 1.18 0.490 

88 102 354 0.24 1.18 0.490 

88 102 354 0.24 1.18 0.490 zl /] \: 

89 102 356 0.22 1.08 0.469 "'-'. Q• 

89 102 356 0.22 1.08 0.469 ' C\ " 

810 103 354 0.22 1.08 0.469 ?60 l ~ 810 103 353 0.22 1.08 0.469 - L '-> 

B11 103 353 0.21 1.04 0.458 u l \q_ 811 103 353 0.21 1.04 0.458 ' . 

{X 812 103 352 0.20 0.99 0.447 '7 7_, 812 103 350 0.20 0.99 0.447 \c.\ lp c 0)5) 97.96 359.27 0.25 1.25 24.065 18.48 2.03 

rx corrected per 7e .. 5b 19.40 Vm(ft3) Initial 403.63 % N2 (BY DIFFERENCE) 78.58 

f' .l, \ Final 555.65 

\~/ ~ ~ 

Total 152.03 %Excess Air 1443.67 

~\j tl .. 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT APPENDIX PAGE No. 129 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 
0 0.520 

A3 93 360 0.27 1.30 0.520 

A4 93 360 0.32 1.54 0.566 

A4 93 359 0.32 1.54 0.566 

A5 93 359 0.33 1.59 0.574 

A5 93 359 0.33 1.59 0.574 

AG 93 359 0.30 1.45 0.548 

A6 93 359 0.30 1.45 0.548 

A7 93 359 0.26 1.25 0.510 18.5 2.0 

A7 93 358 0.26 1.25 0.510 

A8 94 350 0.26 1.25 0.510 

A8 94 351 0.26 1.25 0.510 

A9 94 351 0.27 1.30 0.520 

A9 94 361 0.27 1.30 0.520 

A10 95 359 0.24 1.16 0.490 

A10 95 359 0.24 1.16 0.490 

A11 95 358 0.22 1.06 0.469 

A11 95 358 0.22 1.06 0.469 

A12 95 358 0.22 1.06 0.469 

A12 95 358 0.22 1.06 0.469 

81 95 367 0.25 1.21 0.500 18.4 2.1 

81 95 367 0.25 1.21 0.500 

82 95 365 0.28 1.35 0.529 

82 95 385 0.28 1.35 0.529 

83 94 384 0.30 1.45 0.548 

83 94 354 0.30 1.45 0.548 

84 94 364 0.32 1.54 0.566 

84 93 364 0.32 1.54 0.566 

85 93 363 0.28 1.35 0.529 

85 93 363 0.28 1.35 0.529 

86 93 363 0.24 1.16 0.490 

86 92 363 0.24 1.16 0.490 

87 92 359 0.21 1.01 0.458 18.6 1.9 

87 92 359 0.21 1.01 0.458 

88 92 359 0.23 1.11 0.480 

88 91 359 0.23 1.11 0.480 

89 91 357 0.23 1.11 0.480 

89 91 356 0.23 1.11 0.480 

810 91 355 0.24 1.1B 0.490 

811) 90 355 0.24 1.16 0.490 811 90 354 0.20 0.96 0.447 

811 90 354 0.20 0.96 0.447 

812 90 354 0.20 0.96 0.447 

812 90 354 0.20 0.96 0.447 

93.08 360.25 1).26 1.25 24.355 18.48 2.03 

corrected per 7e·5b 19.10 

Vm(ft3) Initial 556.03 % N2 (BY DIFFERENCE) 78.88 

Final 708.89 

Total 152.66 %Excess Air 1108.53 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 130 
Run#2 

1st Imp. 2nd Imp. 

BEGINNING 100 100 

ENDING 213 114 

NET 113 14 

Run#3 

1st Imp. 2nd Imp. 

BEGINNING 100 100 

ENDING 213 114 

NET 113 14 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

3rd Imp. 4th Imp. TOTALS 

0 300.0 

0 313.5 

0 13.5 140.5 

3rd Imp. 4th Imp. TOTALS 

0 300.0 

0 313.5 

0 13.5 140.5 

APPENDIX PAGE No. 131 
flH = [846. 72 X D~ X MJ@ X c! (1- Bws )2 x MdTmP,. ]x f.l.p 

MsT.s~, 

ModuleiD 

Dn 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACTION,NOT%) 

Md 

Pbar 

PS (GAUGE') 

Ps 

Tm,F 

Tm,R 

Ms 

Ts,F 

Ts,R 

Pm 

K 

Terminology 

BORALBRJCK 

9/1812010 

Run#t 

ATC3 

0.287 

1.937 

0.963 

0.84 

0.05 

29.0 

29.75 

0.22 

29.77 

85 

544.69 

28.45 

360 

819.69 

29.86 

4.7846 

Run #2 Run#3 

ATC 3 ATC3 

0.287 0.287 

1.937 1.937 

0.963 0.963 

0.84 0.84 

0.05 0.05 

29.0 29.0 

29.82 29.75 

0.22 0.22 

29.84 29.77 

100 90 

559.69 549.69 

28.45 28.45 

360 360 

819.69 819.69 

29.84 29.91 

4.9317 4.8203 

Ms=APPARENT STACK GAS MOLECULAR WEIGHT 

=Md(1-Bw)+18Bw 

Md=DRY GAS MOLECULAR WEIGHT (29) OR 

=(0.44*%C02)+(0.32*%02)+(0.28*(%N2+%CO)) 

Ps GAUGE=STACK STATIC PRESSURE (IN. H20) 

Ps=ABSOLUTE STACK PRESSURE (IN. Hg) 

Pm=METER ABSOLUTE PRESSURE (IN. Hg) 

= Pbar + (avg dH/13.6) 

1The method 5 sampling train is intended to operate at a sampling rate of 0.75 cfm of dry air at 68 

oF and 29.92 in. Hg. The orifice meter pressure differential t11at would produce such a sampling rate 

through the orifice is designated as iiH@. 

The theoretical nozzle calculation is optional. If the tester feels comfortable choosing the 

nozzle size through other means (experience, prior testing, etc.), this is also acceptable. Dn 

(theoretical) is calculated on the assumption that a 0.75 cfm flowrate is achieved at 68 °F and 29.92 in. 

ATC PROJECT No. P-10142 

Hg. 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 132 
29.75 1.19 

2) ABSOLUTE STACK PRESSURE 

Ps • P ATM • Ps(GAUGE)/13.6 

PATM Ps(GAUGE) 

29.75 0.22 

29.84 

Ps 

29.77 

3) SAMPLE VOLUME AT STANDARD CONDITIONS 

VM STD • (VM)"(Y)'(T STDITM)'(PM/P STD) 

Vm Tm y VmSTD 

146.22 537.90 0.963 137.83 ft3 

4) VOLUME OF WATER COLLECTED, CORRECTED TO STANDARD CONDITIONS 

W STD = W STOw+ WSTDsg 

W STOw= (.002673)'(VLQw)"(T STD/P STD) 

W STDsg = (.002668)'VLQsg)'(T STOlP STD) 

WHERE 0.002673 • 0.04707 FT3/ML 'IN. HG/17,64 DEG. R. WHERE 0.002668 = 0.04715 FT3/G'IN.HG/17.64 DEG. R. 

VLQ (W) 

127.00 

VLQ (sg) 

13.50 

WSTD 

6.63 ft3 

5) TOTAL SAMPLE VOLUME AT STANDARD CONDITIONS 

V STD=VmSTD+W STD= 144.46 ft3 

6} PERCENT MOISTURE IN STACK GAS 

%M = (100)'(W STD)N STD = 4.59% 

7} MOLE FRACTION OF DRY GAS 

MD= {100-%M)/160 = 0.954 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 133 
2.0 18.5 0.0 

9) MOLECUlAR WEIGHT OF THE WET GAS 

M • (MWD)'(MD) + 18(1-MO) = 

79.5 

WHERE 18 = MOLECUlAR WEIGHT OF WATER. GIG-MOLE 

!OJ STACK VELOCITY 

VS = (85.49)'(CP)'({TS!(PS)(M))'112"((SUM SORT DP)/N DP)) 

where 85.49 = ftfsec .. pbilb--mole"'!n.Hg)J(deg. Win H20)1110.5 

CP 

0.84 

Ts(R) 

820.67 

SUMSQRT 

23.90 

11) STACK VOLUMETRIC FLOW RATE 

QS = (60)"(VS)'(AS) 

AS (inlet) 

30.68 

NDP 

48 

QS 

84,888 

29.06 

28.56 

vs 

35.13 

12) STACK VOLUMETRIC FLOW RATE, STANDARD CONDITIONS INCLUDING MOISTURE 

Q STD = Q STD DRY/MD 41,392 

13) STACK VOLUME FLOW RATE STANDARD CONDITIONS DRY 

Q STD DRY= 17.647'60'Md"Vs"A"(Ps!Ts(R)) = 39,493 

14) POLLUTANT MASS RATE, CONCENTRATION BASIS 

PMRC • (. 1323)'(Wl]'(Q STD)N STD 

WHERE 0.1323 • COMBINED CONVERSION FACTOR (60 MINIHR"0.00220 LBS/GRAM) 

WT(GRAMS) 

0.0000 

15) PERCENT ISO KINETIC 

PMRC 

0.000 

"lol = (0.09450~Ts*Vm std)/(Ps"Vs"An~Tlme~Md} 

Run Tlme Area of Nozzle %! 

240 4.49E-04 

ATC PROJECT No. P-10142 

99.37 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 134 
Specific Source Dryer 

Air Pollution Controls 

Test Methods US EPA M 23 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 135 
~ 

" 

" 

2 

m 

~ 

z 

? 

:!: 

~ 

t, 

8 

c:m 

m" -;> 

J>() 

{1)-u;o 

m>m 

"UZS: -<-;-

mm{/) 

s:,.!:>.f:Q 

~Jtoo 

"'"'z - -;

"'"''" ~>"' or-< 

(ii.v 

"'" 

c:o 

,~ 

-:rn 

.,n 

:;;-< 

~ 

"' 

~ rn 

z 

0 

x 

~ m 

fi 

~ 

Method 1 -Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance- Far Wall to Outside of Port (in) 

Distance- Near Wall to Outside of Port (in) 

Inside Diameter of Stack (in) 

52.00 

0.00 Port Length 

52.00 

Port Diameter- For Ret Only (in) 4.00 

Distance to Upstream Disturbance (ft) 

Distance to Downstream Disturbance (It) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default is 1.0 inch) 

10.00 

4.00 

2.31 

0.92 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

Conversion Table for Decimal to Inch Fraction 

1116 1/8 3116 114 5116 

0.06 0.13 0.19 0.25 0.31 

PROBE MARKINGS 

Decimal Inches 

Number of Traverse Points on a Diameter 

2 4 6 8 

7.59 3.48 2.29 1.66 

44.41 13.00 7.59 5.46 

39.00 15.39 10.09 

48.52 36.61 16.80 

44.41 35.20 

49.71 41.91 

46.54 

50.34 

.10 

1.35 

4.26 

7.59 

11.75 

17.78 

34.22 

40.25 

44.41 

47.74 

50.65 

3/8 

0.38 

12 

1.09 

3.48 

6.14 

9.20 

13.00 

18.51 

33.49 

39.00 

42.80 

45.86 

48.52 

50.91 

"' 

0 

~ r 

"' 

;o 

0 

"' 

(/) 
Pm(inHg) 30.29 30.29 30.29 

Ps(GAUGE) 0.10 0.10 0.10 

Ps (IN HG} 30.17 30.17 30.17 

Tm(F) 84.79 90.13 92.10 

Tm(R) 544.48 549.82 551.79 

Vm (ft3) 174.75 177.75 176.90 

VmSTD(ft3) 171.53 172.78 171.34 

VLQ(ml) 144.00 132.00 144.00 

WSTD(ft3) 6.79 6.22 6.79 

v sro (ftJ) 178.32 179.01 178.14 

%M 3.81 3.48 3.81 3.70 

%SVP 1 17.54 18.01 16.74 

MD 0.962 0.965 0.962 

MWD 28.64 28.84 28.84 

M 28.42 28.46 28.42 

Ts(F) 136.00 137.00 134.21 135.74 

Ts(R) 595.69 596.69 593.90 595.43 

SUMSQRTDP 41.16 41.00 41.18 

NDP 48.00 48.00 48.00 

AVGSQRTDP 0.86 0.85 0.86 

CP 0.84 0.84 0.84 

Vs (ft/s} 51.32 51.14 51.27 51.24 

Ds (in) 52.00 52.00 52.00 

As (ft2) 14.74 14.74 14.74 

QS, FLOW, ACFM 45,389 45,228 45,343 45,320 Q sro (ft31min) 40,563 40,353 40,645 40,520 Q STD DRY, FLOW SCFM 39,019 38,949 39,096 39,021 WT(gm) 4.56E-12 O.OOE+OO 1.39E-12 0.0000 

%1 102.34 103.27 102.03 

%C02 0.00 0.00 0.00 0.00 

%02 20.90 20.90 20.90 20.90 

%CO 0.00 0.00 0.00 

%N2 79.10 79.10 79.10 

D!F (lbs/hr) 1.37E-10 O.OOE+OO 4.20E-11 5.97E-11 

DIF(kglhr} 6.22E-11 O.OOE+OO 1.90E-11 2.71E-11 

Production (tph) 14.65 14.65 14.65 1.47E+01 

Production (Mg) 6.65E-03 6.65E-03 6.65E-03 6.65E-03 

D/F (kg/Mg of Product) 6.8622E-13 0 2.092E-13 2.98E-13 

D/F (ngldscm) 9.387E-04 O.OOOE+OO 2.864E-04 4.08E-04 

DIF (ng/dscm@ 7% 02) N/A NIA NIA N/A* 

QS, FLOW, ACMM 1285 1281 1284 1283 

QS, FLOW, DSCMM 1105 1103 1107 1105 

1 Theoretical amount of moisture that Ts can hold. 

If %M>%SVP, %SVP will be utilized In calculations. 

* Ambient oxygen concentrations, calculation not valid 

ATC PROJECT No. P-10142 EPA JCR EMISSION TEST PROJECT APPENDIX PAGE No. 137 

AUGUSTA PlANTS 4 & 5, SAliSBURY PlANT 6 

SEPTEMBER 2010 
A3 79 A4 79 

A4 82 AS 82 

A5 83 

A6 83 

A6 84 A7 85 A7 85 A8 85 

A8 85 

A9 85 

A9 86 

AIO 86 

A10 86 

A11 86 A11 86 A12 86 

A12 86 

81 86 

B1 86 B2 86 B2 86 

83 86 

B3 86 

84 86 

B4 86 

85 86 85 86 86 86 

86 86 

87 86 

B7 86 

88 88 

88 88 89 88 

89 88 

810 88 

810 88 

811 88 811 88 

812 88 

812 88 

84.79 

Vm(ft3) 

ATC PROJECT No. P-10142 

136 0.76 1.81 0.872 

136 0.76 1.81 0.872 

136 0.76 1.81 0.872 

136 0.76 1.81 0.872 

136 0.76 1.81 0.872 136 0.76 1.81 0.872 136 0.76 1.81 0.872 136 0.76 1.81 0.872 136 0.76 1.81 0.872 

136 0.76 1.81 0.872 

136 0.76 1.81 0.872 136 0.76 1.81 0.872 136 0.76 1.81 0.872 136 0.76 1.81 0.872 136 0.76 1.81 0.872 

136 0.76 1.81 0.872 

136 0.76 1.81 0.872 136 0.76 1.81 0.872 136 0.76 1.81 0.872 136 0.68 1.62 0.825 

136 0.68 1.62 0.825 

136 0.78 1.86 0.883 136 0.78 1.86 0.883 

136 0.78 1.86 0.883 

136 0.78 1.86 0.883 

136 0.78 1.86 0.883 

136 0.78 1.86 0.883 136 0.78 1.86 0.883 136 0.78 1.86 0.883 

136 0.78 1.86 0.883 136 0.78 1.85 0.883 

136 0.78 1.86 0.883 

136 0.78 1.86 0.883 

136 0.78 1.86 0.883 

136 0.78 1.86 0.883 

136 0.78 1.85 0.883 136 0.78 1.86 0.883 136 0.78 1.86 0.883 

136 0.78 1.86 0.883 

136 0.55 1.31 0.742 

136 0.55 1.31 0.742 136 0.42 1.00 0.648 136 0.42 1.00 0.648 

136.00 0.74 1.78 41.155 

Initial 10.36 

Final 185.10 

Total 174.75 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

20.90 1).00 

APPENDIX PAGE No. 138 
A3 89 

A3 90 

A4 90 

A4 90 

A5 90 

AS 90 

AS 90 

A6 90 

Al 90 

A7 90 

A8 90 

AB 90 

A9 90 

A9 90 

A10 90 

Af(l 90 

A11 90 

A11 90 

A12 90 

A12 90 

81 90 

81 90 

82 90 

82 90 

83 90 

133 90 

84 90 

134 90 

85 90 

85 90 

86 90 

86 90 

87 90 

87 90 

88 91 

88 91 

89 91 

89 92 

811! 92 

81() 92 

811 92 

811 92 

812 92 

812 92 

90.13 

Vm(ft3) 

ATC PROJECT No. P-10142 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.866 

137 0.75 1.79 0.666 

137 0.75 1.79 0.866 

137 0.64 1.53 0.800 

137 0.64 1.53 0.800 

137 0.76 1.81 0.872 

137 0.76 1.81 0.872 

137 0.76 1.81 0.872 

137 0.76 1.81 0.872 

137 0.76 1.81 0.872 

137 0.76 1.81 0.872 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.77 1.84 0.877 

137 0.60 1.43 0.775 

137 0.60 1.43 0.775 

137 0.50 1.19 0.707 

137 0.50 1.19 0.707 

137,00 0.73 1.75 41.001 

Initial 187.30 

Final 365.05 

Total 177.75 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 201 0 

20.90 0.011 

APPENDIX PAGE No. 139 
A3 92 A4 92 A4 92 

A5 92 

A5 92 

A6 92 A6 92 

Al 92 

A7 92 

A8 92 

A8 92 A9 92 

A9 92 

A1a 92 

A11J 92 

A11 92 

A11 92 

A12 92 

A12 92 

81 92 

81 92 

BZ 92 B2 92 

83 92 83 92 84 92 84 92 85 92 

85 92 

136 92 

136 92 137 92 

87 92 88 92 88 92 

89 92 89 92 

810 92 

81(} 92 

811 92 

811 92 

B12 92 

812 92 

92.10 

Vm(ft3) 

ATC PROJECT No. P-10142 

136 0.76 1.81 0.872 

136 0.77 1.64 0.877 

136 0.77 1.64 0.877 

136 0.76 1.81 0.872 

136 0.76 1.81 0.872 136 0.76 1.81 0.872 

136 0.76 1.81 0.872 

136 0.76 1.81 0.872 

136 0.76 1.81 0.872 

136 0.76 . 1.81 0.872 136 0.76 1.81 0.872 135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

135 0.76 1.81 0.872 135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

135 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.76 1.81 0.872 

132 0.74 1.77 0.860 132 0.74 1.77 0.860 

132 0.63 1.50 0.794 

132 0.63 1.50 0.794 

132 0.47 1.12 0.686 132 0.47 1.12 0.686 

134.21 0.74 1.76 41.176 

Initial 366.20 

Final 543.10 

Total 176.9(1 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

20.90 0.00 

APPENDIX PAGE No. 140 
Run#2 

tstlmp. 2nd Imp. 

BEGINNING 100 100 

ENDING 214 100 

NET 114 0 

Run#3 

1st Imp. 2nd Imp. 

BEGINNING 100 100 

ENDING 218 100 

NET 118 0 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

3rd Imp. 4th Imp. TOTALS 

0 300.0 0 318.0 0 18.0 132.0 

3rd Imp. 4th Imp. TOTALS 

0 300.0 0 326.0 0 26.0 144.0 

APPENDIX PAGE No. 141 
D.H =[846.72xD4 xMl xc2 (1-B )2 x MdT,,P, Jx A n @ p ws M.TP .p ,s· · s m 

ModuleiD 

Dn 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACTION,NOT%) 

Md 

Pbar 

PS(GAUGE) 

Ps 

Tm,F 

Tm,R 

Ms 

Ts,F 

Ts,R 

Pm 

K 

Terminology 

BORAL BRICK 

9118/2010 

Run #1 

ATC i 

0.220 

1.980 

1.000 

0.84 

0.04 

29.0 

30.16 

0.10 

30.17 

80 

539.69 

28.56 

125 

584.69 

30.27 

2.3855 

Run#2 Run#3 

ATC i ATC 1 

0.220 0.220 

1.980 1.980 

1.000 1.000 

0.84 0.84 

0.04 0,04 

29.0 29.0 

30.16 30.16 

0.10 0.10 

30.17 30.17 

90 90 

549.69 549.89 

28.56 28.56 

135 135 

594.69 594.69 

30.29 30.29 

2.3873 2.3874 

Ms~APPARENT STACK GAS MOLECULAR WEIGHT 

=Md(1-Bw)+18Bw 

Md=DRY GAS MOLECULAR WEIGHT (29) OR 

=(0.44'%C02)+(0.32*%02)+(0.28'(%N2+%CO)) 

Ps GAUGE~STACK STATIC PRESSURE (IN. H20) 

Ps~ABSOLUTE STACK PRESSURE (IN. Hg) 

Pm=METER ABSOLUTE PRESSURE (IN. Hg) ~ Pbar + (avg dH/13.6) 

1The method 5 sampling !rain is intended to operate a! a sampling rate of 0.75 cfm of dry air at 68 

oF and 29.92 in. Hg. The orifice meter pressure differential that would produce such a sampling rate 

through the orifice Is designated as 1\.H@. 

The theoretical nozzle calculation is optional. If the tester feels comfortable choosing the 

nozzle size through other means (experience, prior testing, etc.), this is also acceptable. On 

(theoretical) is calculated on the assumption that a 0.75 cfm ftowrate is achieved at 68 °F and 29.92 in. 

ATC PROJECT No. P-10142 

Hg. 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENOIX PAGE No. 142 
30.16 1.76 

~ ABSOLUTE STACK PRESSURE 

Ps = P ATM + Ps(GAUGE)/13.6 

PATM Ps(GAUGE) 

30.16 0.1 

30.29 

Ps 

30.17 

3) SAMPLE VOLUME AT STANDARD CONDITIONS 

VM STD = (VMr(Y)'(T STDffM)'(PMIP STD) 

Vm Tm y VmSTD 

174.75 544.48 1.000 171.53 ft3 

4) VOLUME OF WATER COLLECTED, CORRECTED TO STANDARD CONDITIONS 

W STD = W STOW+ WSTDsg 

W STOw= (.002a73)'(VLQw)'(T STOlP STD) 

W STDsg = (.002668)'\/LQsg)"(T STDIP STD) 

WHERE 0.002673 = 0.04707 FT31ML'IN. HG/17.64 OEG. R. 

WHERE 0.002668 = 0.04715 FTSIG'IN.HG/17.84 DEG. R. 

VLQ (w) 

122.00 

VLO (sg) 

22.00 

WSTD 

6.79 ft3 

5} TOTAL SAMPLE VOLUME AT STANDARD CONDITIONS 

VSTD •Vm STD + W STD= 178.32 ft3 

6) P>;RCENT MOISTURE IN STACK GAS 

%M • (100)•(VV STD)N STD" 3.81% 

7) MOLE FRACTION OF DRY GAS 

0.962 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 143 
%C02 %02 %CO 

0.0 20.9 0.0 

9) MOLECULAR WEIGHT OF THE WET GAS 

M = (MWD)"(MD) + 18(1-MD) = 

%N2 

79.1 

WHERE 18 =MOLECULAR WEIGHT OF WATER, GIG-MOLE 

10) STACK VELOCITY 

VS = (85.49)'(CP)"((TS!(PS)(M))"112'((SUM SORT OP)IN DP)) 

where 85.49 = fVsec" f!b/lb-mo!e~in.Hg)/(deg. R"ln H20}]"'0.5 

CP 

0.84 

Ts (R) 

595.69 

SUMSQRT 

41.16 

11) STACK VOLUMETRIC FLOW RATE 

QS = (60)'(VSr(AS) 

AS (lnle~ 

14.74 

NDP 

48 

OS 

45,389 

MWD 

28.84 

28.42 

vs 

51.32 

12) STACK VOLUMETRIC FLOW RATE, STANDARD CONDITIONS INCLUDING MOISTURE Q STD = Q STD DRYIMD 40,583 

13) STACK VOLUME FLOW RATE STANDARD CONDITIONS DRY 

Q STD DRY= 17.647'60'Md'Vs'A'(Psffs(R)) = 39,019 

14} POLLUTANT MASS RATE, CONCENTRATION BASIS 

PMRC = (.1323)'(WT)'(Q STD)N STD 

WHERE 0.1323 • COMBINED CONVERSION FACTOR (60 MINIHR'0.00220 LBSIGRAM) 

WT(GRAMS) 

0.0000 

15) PERCENT ISOKINETIC 

PMRC 

o.ooo 

%1:;:. (0.09450"Ts•vm std)/{Ps"Vs"'An"Time~Md) 

Run Time Area of Nozzle 

240 2.64E-04 

ATC PROJECT No. P-10142 

%1 

102.34 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 144 
PLANT6 

FIELD DATA CALCULATIONS 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PlANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 201 D 

APPENDIX PAGE No. 147 
Process Tested DIFF Baghouse Outlet 

Specific Source Kiln 6 

Air Pollution Controls DIFF Baghouse Outlet 

Test Methods 1-5, 26A 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 158 
~ ., 

;o 

2 

m 

~ z 

~ 

1: 

=: 

... 

"' 

8 

em "'., -jl> 

,o "'.,, 

m>m 

-uzs: 

;;:l~Ci5 

;;:""'"~ ,,.o 

~tnz - -l "'cnm 

~)>CI.l 

or-< (ii-u 

"'"' co 

,~ 

-<m 

.,o s;:-l 

:!i 

"' 

10 

., 

m 

z 

0 

x 

m 

~ 

z 

~ 

~ 

18 

Method 1 - Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance- Far Wall to Outside of Port (in) 

Distance - Near Wall to Outside of Port (in) 

Inside Diameter of Stack (in) 

84.50 

9.50 Port Length 

75.00 

Port Diameter- For Ref. Only (in) 4.00 

Distance to Upstream Disturbance (It) 

Distance to Downstream Disturbance (ft) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default is 1.0 inch) 

25.00 

40.00 

4.00 

6.40 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

7 

8 

9 

10 

ii 

12 

Conversion Table lor Decimal to Inch Fraction 

1116 1/8 3/16 1/4 5/16 

0.06 0.13 0.19 0.25 0.31 

PROBE MARKINGS 

Decimal inches 

Number of Traverse Points on a Diameter 

2 4 6 8 

20.45 14.53 12.80 11.90 

73.55 28.25 20.45 17.38 

65.75 31.70 24.05 

79.48 62.30 33.73 

73.55 60.28 

81.20 69.95 

76.63 

82.10 

10 

11.45 

15.65 

20.45 

26.45 

35.15 

58.85 

67:55 

73.55 

78.35 

82.55 

3/8 

0.38 

12 

11.08 

14.53 

18.35 

22.78 

28.25 

36.20 

57.80 

65.75 

71.23 

75.65 

79.48 

82.93 

"' 0 

:0 

)> 

r 

2l "' 

0 

"' 00 
ATC PROJECT No. P-10142 

Ps(INHG) 29.33 29.38 29.42 

rm(F) 74.96 85.58 97.17 

Tm{R} 534.65 545.27 556.86 

Vm {ft3) 45.72 43.92 45.12 

Vm STD(ft3} 44.23 41.73 42.04 

VLQ(ml) 33.00 59.00 49.00 

W STD(f13) 1.56 2.78 2.31 

v sro {ff31 45.79 44.51 44.35 

%M SA-O 6.25 5.21 

%SVP1 100.00 100.00 100.00 

MD 0.966 0.931l 0.948 

MWD 29.07 29.07 29.06 

M 28.69 28.38 28.48 

Ts(F} 365.25 371.79 376.04 

Ts(R) 824.94 831.48 835.73 

SUMSQRTDP 15.53 15.25 15.12 

NDP 24.00 24.00 24.00 

AVGSQRTDP 0.65 0,64 0.63 

CP 0.84 0.84 0.84 

V.s {ftls) 46.02 45.57 45.19 

Os (in) 75.00 75.00 75.00 

As (ft2J 30.66 30.68 

QS, FLOW, ACFM 84,715 83,884 83,184 

Q STD (tt3/min) 53,149 52,303 51,673 

Q $TD DRY, FLOW $CFM 51,343 49,034 48,981 

WT(gm)-PM 0.0015 0.0000 0.0010 

0.0003 0.0003 0.0002 

WT(gm}·HF 0.0000 0,0000 0.0000 

WT(gm)-Cf2 0.1348 0.0000 0.0064 

'" 96.75 95,58 96.39 %C02 2.00 2.13 2.03 

%02 18.36 18,36 18.39 

%CO 0.00 0.00 0.00 

%N2 79.58 79.51 79.59 

PM (lbs/hr) 0.246 0.000 0.154 

PM (kglhr} 0.1115 0.0000 0.0699 

ProducUon (tph) 20.26 20.26 20.26 

Production (Mg) 9.19E*03 9.19E-03 9,19E-03 

PM {kg!Mg of Product) 1.74E-04 O.OOE+OO i.09E-04 

PM (mgldscm) 1.2SE4-00 O.OOE+OO BAOE-01 

PM (mgldscm@ 7% 02} 7.00E+OO O.OOE-+00 4.ase.;.oo 

HCI (Jbslhr) 5.07E*02 3.93E..Q2 3.35E..02 

HCI(kglhr) 2.30E·02 1.78E-02 1.52E..(l2 

HCJ (kg!Mg of Product) 3.59E-05 2.755..05 2.36E..05 

HCJ (ppm} 223.24 \76.05 151.57 

HCI (ppm @ 7% 02) 1222.89 984.40 838.49 

HF (lbslhr) 4.41E·03 4.68E-03 4.305-03 

HF (kglhr) 2.00E*03 2.12E-03 1.95E*03 

HF (kg!Mg of Product) 3.12E·06 3.28E-06 3.04E-06 

HF(ppm) 10.66 11.50 10.69 

HF (ppm@ 7% OZ) 231.42 249.66 232.28 

Cl2 (Jbs/hr} 2.07E+01 2.24E-03 9.8SE-01 

C/2 (Kglhr) 9.39E+OO 1.02E-03 4.48E-01 

Cl2 {Xg!Mg of Product) 1.47E-02 1.57E-06 a.97E.04 

Cl2(ppm) 177371.92 19.49 8704.72 

C/2 (ppm @ 7% 02) 118251.80 12.99 5798.54 

QS, FLOW, ACMM 2399 2375 2355 

QS, FLOW. DSCMM 1454 1388 1387 

• TheororlcM of moisture that Ts can hold. 

If %M>%SVP, %SVP w!Ji be utilized In calcu/atlons, 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

4.95 

371.03-

830.72 

45.59 

83,928 

52,375 

49,78S 

0.0009 0,0003 0.0000 0.0471 

2.08 

18.37 

0.133 

0,0605 

20.2& 

9.19E·03 

9.43E·OS 7.06S-Q1 

3.8SE+OO 

4.UE..02 

1J37E-02. 

2.SOE..05 

183.62 

1008.59 

4.46E-03 

2.02E-03 

3.14E..06 

10.95 

237.79 

7.23E+OO 

3.286+00 

5.12E·03 

$2.032.04 

41354.44 

2376 

1410 

APPENDIX PAGE No.160 
A5 73 365 0.42 2.05 0.648 

A6 73 365 0.42 2.05 0.648 

A7 73 365 0.44 2.15 0.663 18.4 2.2 

A8 74 364 0.45 2.20 0.671 

A9 75 364 0.40 1.95 0.632 

A10 75 364 0.41 2.00 0.640 

A11 76 360 0.41 2.00 0.640 

A12 76 360 0.43 2.10 0.656 

81 76 369 0.39 1.90 0.624 18.5 2.0 

82 76 368 0.40 1.95 0.632 

83 76 368 0.43 2.10 0.656 

84 77 368 0.43 2.10 0.656 

85 77 370 0.44 2.15 0.663 

86 77 370 0.45 2.20 0.671 

87 77 370 0.45 2.20 0.671 18.5 2.0 

88 77 370 0.45 2.20 0.671 

89 77 365 0.42 2.05 0.648 

810 77 364 0.40 1.95 0.632 

811 77 360 0.39 1.90 0.624 

812 77 360 0.38 1.85 0.616 

74.96 365.25 0.42 2.05 15.534 18.45 2.08 

corrected per 7e-5b 18.36 Vm(ft3) Initial 750.26 % N2 (BY DIFFERENCE) 7$.56 Final 

Total 

ATC PROJECT No. P-10142 

795.98 

45.72 %Excess Air 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

695.04 

APPENDIX PAGE No. 161 
A4 82 372 0.42 2.07 0.646 

A5 83 375 0.42 2.07 0.648 

A6 83 375 0.45 2.22 0.671 

A7 84 369 0.43 2.12 0.656 18.4 2.2 

A8 84 369 0.43 2.12 0.656 

A !I 85 368 0.40 1.97 0.632 

A10 85 366 0.40 1.97 0.632 

A11 86 366 0.39 1.92 0.624 

A12 86 359 0.39 1.92 0.624 

81 87 365 0.38 1.87 0.616 13.4 2.1 

82 87 375 0.37 1.82 0.608 

83 87 378 0.37 1.82 0.608 

84 87 380 0.42 2.07 0.648 

85 87 381 0.42 2.07 0.648 

86 87 377 0.42 2.07 0.648 

87 88 375 0.43 2.12 0.656 18.6 2.0 

88 88 375 0.43 2.12 0.656 

89 88 378 0.40 1.97 0.632 

810 88 379 0.37 1.82 0.608 

811 88 365 0_38 1.87 0.616 

812 88 364 0.36 1.77 0.600 

85.58 371.79 0.40 1.99 15.251 18.45 2.13 

corrected per 7e-5b 18.36 

Vm(ft3) Initial 796.03 % N2 (BY DIFFERENCE) 79.51 

Final 

Total 

ATC PROJECT No. P-10142 

839.95 

43.92 %Excess Air 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

698.53 

APPENOIX PAGE No. 162 
A4 95 380 0.38 1.92 0.616 

A5 95 378 0.40 2.02 0.632 

A6 95 378 0.44 2.23 0.663 

Al 95 378 0.44 2.23 0.663 18.5 2.0 

A8 96 378 0.44 2.23 0.663 A9 96 374 0.41 2.08 0.640 

MO 96 374 0.41 2.08 0.640 

A11 97 370 0.41 2.08 0.640 A12 97 366 0.38 1.92 0.616 

B1 97 377 0.36 1.82 0.600 18.5 2.0 B2 97 380 0.36 1.62 0.600 

83 98 381 0.36 1.82 0.600 

84 99 380 0.40 2.02 0.632 

B5 99 :lao 0.40 2.02 0.632 B!i 99 379 0.41 2.08 0.640 

87 99 379 0.41 2.08 0.640 18.6 1.9 88 99 375 0.43 2.18 0.656 

B9 100 374 0.44 2.23 0.663 

810 100 370 0.40 2.02 0.632 

811 100 368 0.36 1.82 0.600 

812 100 364 0.36 1.82 0.600 

97.17 376.04 0.40 2.01 15.123 18.48 2.03 

corrected per '1 e-5b 18.31} 

Vm(ft3) Initial 839.63 % N2 (BY DIFFERENCE) 79.59 

Final 

Total 

ATC PROJECT No. P-10142 

884.75 

45.12 %Excess Air 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

700.83 

APPENDIX PAGE No. 163 
[ Ml= 

846.72xDn

xM

/@xc

(1

B .)

' P ws M TP r S s m 

Module ID 

Dn 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACT/ON,NOT"/o) 

Md 

Pbar 

PS(GAUGE) 

Ps 

Tm,F 

Tm,R 

Ms 

Ts, F 

Ts, R 

Pm 

K 

BORAL BRICK 

912112010 

Run#1 Run#2 Run#3 

ATC4 ATC4 ATC4 

0.289 0.289 0.289 

1.951 1.951 1.951 

0.995 0.995 0.995 

0.84 0.84 0.84 

0.05 0.05 0.05 

29.0 29.0 29.0 

29.31 29.36 29.40 

0.25 0.25 0.25 

29.33 29.38 29.42 

80 85 100 

539.69 544.69 559.69 

28.45 28.45 28.45 

365 365 365 

824.69 824.69 824.69 

29.42 29.46 29.51 

4.8798 4.9267 5.0614 

Terminology 

Ms=APPARENT STACK GAS MOLECULAR WEIGHT 

=Md(1-Bw)+188w 

Md=DRY GAS MOLECULAR WEIGHT (29) OR 

=(0.44*%C02)+(0.32*%02)+(0.26*(%N2+%CO)) 

Ps GAUGE=STACK STATIC PRESSURE (IN. H20) 

Ps=ABSOLUTE STACK PRESSURE (IN. Hg) 

Pm=METER ABSOLUTE PRESSURE (IN. Hg) 

= Pbar + (avg dH/13.6) 

'The method 5 sampling train is intended to operate at a sampling rate of 0.75 cfm of dry air at 68 

oF and 29.92 in. Hg. The orifice meter pressure differential that would produce such a sampling rate 

throuoh the orifice is desiqnated as LlH,.. 

The theoretical nozzle calculation is optional. If the tester feels comfortable choosing the 

nozzle size through other means (experience, prior testing, etc.), this is also acceptable. On 

(theoretical) is calculated on the assumption that a 0. 75 elm flowrate is achieved at 6B °F and 29.92 in. 

Ho 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 164 
29.31 2.05 

2) ABSOlUTE STACK PRESSURE 

Ps = P ATM •· Ps(GAUGE)/13.6 

PATM Ps(GAUGE) 

29.31 0.25 

29.46 

Ps 

29.33 

3) SAMPLE VOLUME AT STANDARD COIIDITIONS 

VM STD = (VM)•(Y)•(T STDITM)•(PMIP STD) 

Vm Tm y VmSTD 

45.72 534.65 0.995 44.23 

ft3 

4) VOLUME OF WATER COLLECTED, CORRECTED TO STANDARD CONDITIONS 

W STD = W STOw+ WSTDsg 

W STOw= (.002673)'(VLQw)'(T STDIP STD) 

W STDsg = (.002668)'VLQsg)'(T STOlP STD) 

WHERE 0.002673 = 0.04707 FT3fML•JN. HG/17.64 DEG. R. 

WHERE 0.002668 • 0.04715 FT3JG•JN.HG/17.64 DEG. R. 

VLQ {w) 

25.00 

VLQ {sg) 

s.oo 

WSTD 

1.56 ft3 

5) TOTAL SAMPLE VOLUME AT STANDARD CONDITIONS 

V STD =Vm STD + WSTD= 45.79 ft3 

6) PERCENT MOISTURE IN STACK GAS 

%M = (100)•(W STD)N STD = .3.40tlfo 

7) MOLE FRACTION OF DRY GAS 

MD== (100-%M)/100 = 0.966 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 165 
2.1 18.4 0.0 

9) MOLECULAR WEIGHT OF THE WET GAS 

M = (MWDt(MD) + 18(1-MD) = 

79.6 

WHERE 18 =MOLECULAR WEIGHT OF WATER, GIG-MOLE 

10) STIICK VELOCITY 

VS = (85.49)'(CP).((TSI(PS)(M))'112.((SUM SORT DP)IN DP)) 

where 85.49 = ftlsec"' [lbflb-mole;O"in.Hg)/(deg. R*in H20}111 0.5 

CP 

0.84 

Ts (R) 

824.94 

SUM SORT 

15.53 

11) STACK VOLUMETRIC FLOW RATE 

QS = (60)'(VS)'(AS) 

AS (lnleQ 

30.68 

NDP 

24 

QS 

84,715 

29.07 

28.69 

vs 

48.02 

12) STACK VOLUMETRIC FLOW 1<1\TE, STANDARD CONDITIONS INCLUDING MOISTURE 

Q STD = Q STD DRY/MD 53,149 

13) STACK VOLUME FLOW RATE STANDARD CONDITIONS DRY 

Q STD DRY= 17.647'60'Md'Vs•A'(Pstrs(R)) = 51,343 

14) POLLUTANT MASS RATE, CONCENTRATIOM BASIS 

PMRC = (.1323)'(WT)•(Q STD)N STD 

WHERE 0.1323 =COMBINED CONVERSION FACTOR (60 MINIHR'0.00220 LBSIGRAM) 

WT(GRAMS) 

0.0016 

15) PERCENTISOKINETIC 

PMRC 

0.246 

%1 = {0.09450"Ts*Vm 

Run rime Area of Nozzle 

60 4.56E-04 

ATC PROJECT No. P-10142 

%! 

96.75 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No.166 
Process Tested DIFF Baghouse Outlet 

Specific Source Kiln 6 

Air Pollution Controls DIFF Baghouse Outlet 

Test Methods US EPA M29 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 179 
E' 

:!'< 

0 

" 2 

m 

~ z 

? 

!' 

~ 

" .,. 

"' 

Glm 

c., 

~,. 

>c; 

w""' mr;;m "Uz;: -<-;- mwW 

S::,::..SQ 

"'"'0 

~Olz - -; "'wm 

~)>(/) 

or-< 

1ii-u 

"'"' co 

,~ 

-<m 

,o 

r;;-< 

~ 

"' 

'" ., 

m 

z 

0 

x 

~ m 

z 

0 

~ 

gj 

Method 1 - Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance- Far Wall to Outside.of Port (in) 

Distance - Near Wall to Outside of Port (in) 

Inside Diameter of Stack (in) 

84.50 

9.50 Port Length 

75.00 

Port Diameter- For Ref. Only (in) 4.00 

Distance to Upstream Disturbance (ft) 

Distance to Downstream Disturbance (ft) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default is 1.0 inch) 

25.00 

40.00 

4.00 

6.40 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

1 

8 

9 

10 

11 

12 

Conversion Table for Decimal to Inch Fraction 

1/16 1/8 3/16 1/4 5116 

0.06 0.13 0.19 0.25 0.31 

PROBE MARKINGS 

Decimal Inches 

Number of Traverse Points on a Diameter 

2 4 6 8 

20.45 14.53 12.80 11.90 

73.55 28.25 20.45 17.38 

65.75 31.70 24.05 

79.48 62.30 33.73 

73.55 60.28 

81.20 69.95 

76.63 

82.10 

10 

11:45 

15.65 

20.45 

26.45 

35.15 

58.85 

67.55 

73.55 

78.35 

82,55 

3/8 

0.38 

12 

11.08 

14.53 

18.35 

22.78 

28.25 

36.20 

57.80 

65.75 

71.23 

75.65 

79.48 

82.93 

Ol 

0 

,... 

~ 

Ol 

;o 

0 

"' (f) 
AVG DH (in H20) 2.06 2.04 2.01 

PATM(in Hg) 29.41 29.35 29.32 

Pm (in Hg) 29.56 29.50 29.47 

Ps(GAUGE) 0.25 0.25 0.25 

Ps(IN HG) 29.43 29.37 29.34 

Tm(F) 101.04 106.00 101.08 

Tm(R) 560.73 565.69 560.77 

Vm (ft3) 47.50 46.18 45.89 

Vm STD(ft3) 43.97 42.28 42.34 

VLQ(ml) 51.00 50.00 60.00 

WSTD (ft3) 2.40 2.39 2.86 

VSTD (ft3) 46.37 44.67 45.19 

%M 5.Hl 5.34 6.32 5.62 

%SVP; 100.00 100.00 100.00 

MD 0.948 0.947 0.937 

MWD 29.07 29.08 29.06 

M 28.50 28.49 28.36 

rs (F) 389.25 388.29 389.63 389.05 

Ts(R) 848.94 847.98 849.32 848.75 

SUMSQRTDP 15.42 15.32 15.29 

NDP 24.00 24.00 24.00 

AVGSQRTDP 0.64 0.64 0.64 

CP 0.84 0.84 0.84 

Vs (fils) 46.41 46.16 46.21 46.26 

Ds (in) 75.00 75.00 75.00 

As (ft2) 30.68 30.68 30.68 

QS, FLOW, ACFM 85,438 84,963 85,064 85,155 

Q STD (ft3/mln) 52,265 51,927 51,854 52,016 

q Q STD DRY, FLOW SCFM 49,555 49,155 48,576 49,095 rL ( 

.-v·'> 

t)' 

(/ 

o.t 

ATC PROJECT No. P-10142 

WT(gm) 0.0021 0.6231 0.0626 0.2293 

%! 99.65 96.61 97.89 

%C02 2.08 2.13 2.03 2.08 

%02 18.45 18.45 18.48 18.46 

%CO 0.00 0.00 0.00 %N2 79.47 79.42 79.49 

1 Theoretical amount of moisture that Ts can hofd. 

lf%M>%SVP, %SVP will be utilized in calculations. 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 181 
A3 98 390 0.41 2.05 

0.640 

A4 98 391 0.42 2.10 0.648 

A5 99 391 0.43 2.15 0.656 

A6 99 391 0.43 2.15 0.656 

A7 99 391 0.43 2.15 0.656 19.1 1.5 

A8 100 391 0.44 2.20 0.663 

A9 100 390 0.44 2.20 0.663 

A10 101 390 0.40 2.00 0.632 

A11 101 390 0.40 2.00 0.632 

A12 101 389 0.39 1.95 0.624 

81 102 390 0.38 1.90 0.616 19.0 1.6 

82 102 391 0.38 1.90 0.616 

83 102 391 0.42 2.10 0.648 

B4 102 391 0.42 2.10 0.648 

85 102 390 0.42 2.10 0.648 86 103 387 0.43 2.15 0.656 

87 103 387 0.45 2.25 0.671 19.0 1.7 

88 103 387 0.44 2.20 0.663 

89 103 388 0.41 2.05 0.640 

811) 103 388 0.39 1.95 0.624 

811 104 384 0.39 1.95 0.624 

812 104 384 0.39 1.95 0.624 

101.04 389.25 0.41 2.06 15.417 19.03 1.60 

corrected per 7 e-5/:J 19.03 

Vm(ft3) Initial 884.91 % N2 (BY DIFFERENCE) 79.38 

Final 932.41 

Total 47.50 %Excess Air 985.75 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 182 
A3 103 389 0.41 2.05 0.640 

A4 103 389 0.42 2.10 0.648 

A5 104 390 0.45 2.25 0.671 

A6 105 390 0.45 2.25 0.671 

A7 105 387 0.40 2.00 0.632 19.0 1.5 

A8 105 388 0.41 2.05 0.640 

A9 105 388 0.41 2.05 0.640 

A10 106 388 0.39 1.95 0.624 

A11 106 388 0.39 1.95 0.624 

A12 107 385 0.39 1.95 0.624 

81 107 390 0.38 1.90 0.616 19.1 1.5 

82 108 390 0.38 1.90 0.616 

83 108 389 .,Q,,38 1.90 0.616 

84 108 391 0.4o· · 2.00 0.632 

85 109 391 0.40 2.00 0.632 

86 108 387 0.42 2.10 0.648 

87 108 387 0.42 2.10 0.648 18.9 1.7 

B8 107 387 0.46 2.30 0.678 

89 107 386 0.45 2.25 0.671 

810 107 386 0.38 1.90 0.616 

811 107 387 0.39 1.95 0.624 

812. 107 388 0.39 1.95 0.624 

106.1)0 388.29 0.41 2.04 15.322 19.05 1.53 

corrected per 7 e-5b 19.05 

Vm(ft3) Initial 933.61 % N2. (BY DIFFERENCE} 79.43 

Final 

Total 

ATC PROJECT No. P-10142 

979.78 

46.18 %Excess Air 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

993.12 

APPENDIX PAGE No. 183 
0.41 2.03 0.640 

A5 100 387 0.45 2.22 0.671 

AS 101 388 0.45 2.22 0.671 

A7 101 389 0.47 2.32 0.686 19.1 1.5 

A8 102 389 0.40 1.98 0.632 

A9 103 390 0.41 2.03 0.640 

A10 103 391 0.41 2.03 0.640 

A11 103 390 0.38 1.88 0.616 

A12 102 388 0.38 1.88 0.616 

81 102 392 0.37 1.83 0.608 19.0 1.5 

82 102 394 0.37 1.83 D.608 

83 101 394 0.38 1.88 0.616 

84 101 394 0.40 1.98 0.632 

85 101 393 0.41 2.03 0.640 

86 101 393 0.41 2.03 0.640 

87 101 389 0.41 2.03 0.640 18.9 1.6 

88 101 388 0.46 2.27 0.678 

89 101 390 0.45 2.22 0.671 

810 100 386 0.39 1.93 0.624 

811 100 388 0,37 1.83 0.608 

1312 100 387 0.37 1.83 0.608 

101.08 389.63 0.41 2.01 15.287 19.08 1.48 

corrected per 7e-5b 19.08 Vm(ft3) Initial 980.03 % N2 (BY DIFFERENCE) 79.45 

Final 1025.91 

Total 45.89 %Excess Air 1004.05 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PlANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 184 
BEGINNING 

ENDING 

NET 

Run#J 

BEGINNING 

ENDING 

NET 

ATC PROJECT No. P-10142 

100 100 200 

750 

650 -100 -200 

1stlmp. 2nd Imp. 3rdl4th Imp. 

100 100 200 

760 

660 -100 -200 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

300.0 

-300.0 50.0 

5th Imp. TOTALS 

300.0 

-300.0 60.0 

APPENDIX PAGE No. 185 
[

(

)

p MsT.Pm 

Module ID 

Dn 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACT/01\1,1\/0T'/a) 

Md 

Pbar 

PS(GAUGE) 

Ps 

Tm,F 

Tm,R 

Ms 

is, F 

Ts, R 

Pm 

K 

BORAL BRICK 

9121/2010 

Run#1 Run#2 RunttJ 

ATC4 ATC4 ATC4 

0.289 0.289 0.289 

1.951 1.951. 1.951 

0.995 0.995 0.995 

0.84 0.84 0.84 

0.05 0.05 0.05 

29.0 29.0 29.0 

29.41 29.35 29.32 

0.25 0.25 0.25 

29.43 29.37 29.34 

100 105 105 

559.69 564.69 564.69 

28.45 28.45 28.45 

375 380 390 

834.69 839.69 849.69 

29.52 29.58 29.50 

5.0001 4.9975 4.9440 

Terminology 

Ms=APPARENT STACK GAS MOLECULAR WEIGHT 

=Md(1-Bw)+18Bw 

Md=DRY GAS MOLECULAR WEIGHT (29) OR 

=(044*%C02)+(0.32*%02)+(0.28.(%N2+%CO)) 

Ps GAUGE=STACK STATIC PRESSURE (IN. H20) 

Ps"ABSOLUTE STACK PRESSURE (IN. Hg) 

Pm=METER ABSOLUTE PRESSURE (IN. Hg) 

= Pbar + (avg dH/13.6) 

1The method 5 sampling train is intended to operate at a sampling rate of 0.75 cfm of dry air at 68 

oF and 29.92 in. Hg. The orifice meter pressure differential that would produce such a sampling rate 

throuah the orifice is desionated as L'.H.,. 

The lheoreticaU1ozzle calculation is optional. If the tester feels comfortable choosing the 

nozzle size through other means (experience, prior testing, etc.), this is also acceptable. Dn 

(theoretical) is calculated on the assumption that a D. 75 cfm flowrate is achieved at 68 °F and 29.92 in. 

Ho 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 186 
Ps

 P ATM + Ps(GAUGE}I13.6 

PATM Ps{GAUGE) 

29.41 0.25 

29.43 

3} SAMPLE VOLUME AT STANDARD CONDITIONS 

VM STD "'{VM)~(Yt(T STD/TM)*{PMIF' STO) 

Vm Tm y VmSTD 

47.50 560.73 0.995 4-3.97 

ft3 

4) VOLUME OF WATER COLLECTE01 CORRECTED TO STANDARD CONDITIONS 

W STD "' W STOw+ WSTOsg 

W STDw = (.002673)~(VLQw}"•(T STOlP STD) 

W STDsg ""(.002668)~VLQsg)~(T STD/P STD} 

WHERE 0.002673 = 0.04707 FT31ML*IN. HG/17.64 DEG. R 

WHERE 0.002668 = 0.04715 FT31G"IN.HGf17.64 DEG. R. 

VLQ (w} 

40.00 

VLQ (sg) 

11.00 

WSTD 

2.40 ft3 

5) TOTAL SAMPLE VOlUME AT STANDARD CONDITIONS 

VSTD=-VmSTD+WSTD= 46.37 ft3 

8) PERCENT MOISTURE IN STACK GAS 

%M = (100)"{VV STD)N STD = 5.19% 

7) MOLE FRAC'fiON or DRY GAS 

MD"' (10Q.-%M)/100 = 0.948 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 187 
9) MOlECUlAR WEIGHT OF THE WET GAS 

M = (MWDt(MD) + 18(1~MD) = 

WHERE 18 =MOLECULAR WEIGHT Of WATER, GfG-MOLE 

10} STACK VELOCITY 

VS "" (85A9)~(CP)"({TS/{PS)(M))I\if2~((SUM SORT DP)IN DP}) 

where 85.4-9 ""ft!sec~ UbJ!b-moJe•!n.Hg)/(deg. R~in H20)J"0.5 

CP 

0.84 

Ts (R) 

848.94 

SUM SQRT 

15.42 

11) STACK VOLUME:TRJC FLOW RATE 

QS, (60)"{VS)'(AS) 

AS {tn!et) 

30.68 

NOP 

24 

QS 

85.477 

28.41 

VS 

46.44 

12) STACK VOLUMETRIC FLOW RATE, STANDARD CONO!TlONS INCLUDING MOISTURE 

Q STD"' 0 STD DRY/MD 52,289 

13} STACK VOLUME FLOW RATE STANDARD CONDITIONS DRY 

Q STD DRY= 17.647~60#Md'Vs~A'"{P$1Ts{R)) =- 49,577 

14) POLLUTANT MASS RATE,. CONCENTRATION BASiS 

PMRC = (.1323}"(WT)"(Q STD)N STD 

WHERE 0.1323 =COMBINED CONVERSION FACTOR (GO MINIHR~0.00220 LBS/GRAM) 

WT(GRAMS} 

0.0021 

15) PERCENT ISOKINET!C 

PMRC 

0.313 

%1 = {0.09450"Ts*Vm std)/(Ps~vs•Arnime'Md) 

Run Time Area of Nozzle %! 

60 4.56E-04 

ATC PROJECT No. P-10142 

99.-61 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 188 
Run# 

ATC PROJECT No. P-10142 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 189 
Arsenic (As 7440.38-2) 

Barium (Ba 7 440-39-3) 

Beryllium {Be 7440-41-7} 

Cadmium {Cd 7440..43-9) 

Chromium (Cr 744Q-47-3) 

Cobalt (Co 7 440-48-4) 

Copper (Cu 7440-50-8) 

Magnesium {Mg 7439-95-4) 

Manganese {Mn 7439-96-5) 

Mercury (Hg 7439-97-5) 

Nickel (NI 7440-02-0) 

Phosphorus {P 7723.-14-0) 

Selenium (Se 7782-49-2) 

Silver {Ag 7440<22-4} 

Thsllium (11 7 ..:140..28-0) 

Zinc {Zn 7440-66-6) 

ATC PROJECT No. P-10142 

1.40E-04 6.37E-05 

1.66E-03 7.53E-04 

1.98E-05 8.99E-06 

1.18E-04 5.34E-05 

4.73E-04 2.15E-04 

1.18E-04 5.34E-05 

2.79E-04 1.26E-04 

9.79E-04 4.44E-04 

1.04E-03 4.73E-04 

5.51E-04 2.50E-04 

1.16E-03 5.24E-04 

5.91E-03 2.68E-03 

4.17E-04 1.89E-04 

1.98E-04 8.99E-05 

1.98E-O'I 8.99E-05 

9.76E-04 4.43E-04 

9.43E-08 

1.13E-06 

1.34E-08 

7.98E-08 

3.23E-07 

7.98E-08 

1.89E-07 

6.75E-07 

7.04E-07 

3.74E-07 

7.94E-07 

4.01E-06 

2.83E-07 

1.34E-07 

1.34E-07 

6.60E-07 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010' 

7.22E-04 3.83E-03 

8.51E-03 4.51E-02 

1.02E-04 5.39E-04 

6.04E-04 3.20E-03 

2.43E-03 1.29E-02 

6.05E-04 3.21E-03 

1.43E-03 7.59E-03 

5.01E-03 2.65E-02 

5.36E-03 2.84E-02 

2.83E-03 1.50E-02 

5.91E-03 3.14E-02 

3.04E-02 1.61E-01 

2.14E-03 1.13E-02 

1.02E-03 5.39E-03 

1.02E-03 5.39E-03 

5.01E-03 2.66E-02 

APPENDIX PAGE No. 190 
Specific Source Kiln 6 

Air Pollution Controls DIFF Baghouse Outlet 

Test Methods USEPA M23 

ATC PROJECT No. P-1 0142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 201 0 

APPENDIX PAGE No. 201 
)> 

~ 

" :0 

2 

m 

<:1 

if 

E 

:1 

... 

N 

a 

c:m 

(l)v 

-<" "o 

ro""' mS::m 

-oz;:: 

-<-<- men[/) 

~~§ "'"'z ..... Nrom 

~):>Cf.l 

or-< c;;-o 

"'"' co 

:o~ 

-:m 

-o<:1 

~ .... 

"' 

)> 

" " m 

z 

0 

x 

m 

~ 

z 

~ 

N 

0 

N 

Method 1 -Sampling and Velocity Traverses for Stationary Sources 

(Circular Stack) 

Distance- Far Wall to Outside of Port (in) 

Distance- Near Wall to Outside of Port (in) 

Inside Diameter of Stack (in) 

84.50 

9.50 Port Length 

75.00 

Port Diameter- For Ref. Only {in) 4.00 

Distance to Upstream Disturbance (It) 

Distance to Downstream Disturbance (ft) 

Diameters Upstream 

Diameters Downstream 

Minimum Distance to Stack Wall 

(Default is 1.0 inch) 

25.00 

40.00 

4.00 

6.40 

1.00 

Traverse 

Point 

Number 

1 

2 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

Conversion Table for Decimal to Inch Fraction 

1116 1/8 3116 1/4 5/16 

0.06 0.13 0.19 0.25 0.31 

PROBE MARKINGS 

Decimal inches 

Nu.mber of Traverse Points on a Diameter 

2 4 6 8 

20.45 14.53 12.80 11.90 

73.55 28.25 2045 17.38 

65.75 31.70 24.05 

79.48 62.30 33.73 

73.55 60.28 

81.20 69.95 

76.63 

82.10 

10 

11.45 

15.65 

20.45 

26.45 

35.15 

58.85 

67.55 

73.55 

78.35 

82.55 

318 

0.38 

12 

11.08 

14.53 

18.35 

22.78 

28.25 

36.20 

57.80 

65.75 

71.23 

75.65 

79.48 

82.93 

0 

c 

, 

, 

r 

0 

, 

( 

> 0 
Pm(inHg) 29.46 29.49 29.46 

Ps(GAUGE) 0.25 0.25 0.25 

Ps(INHG} 29.33 29.35 29.32 

Tm(F) 89.81 104.33 97.85 

Tm(R} 549.50 564.02 557.54 

Vm (ft3) 184.45 191.08 196.59 

VmSTD(ftJ} 173.63 175.42 182.38 

VLQ(ml) 184.30 221.60 214.50 

VV STD (ft3} 8.69 10.45 10.12 

VSTD (ft3) 182.32 185.87 192.49 

%M 4.77 5.62 5.26 5.22 

%SVP, 100.00 100.00 100.00 

MD 0.952 0.944 0.947 

MWD 29.03 29.02 29.03 

M 28.50 28.40 28.45 

Ts(F) 381.38 386.92 381.92 383.40 

Ts(R) 841.07 846.61 841.61 843.09 

SUMSQRTDP 31.04 31.64 31.57 

NDP 48.00 48.00 48.00 

AVGSQRTDP 0.65 0.66 0.66 

CP 0.84 0.84 0.84 

Vs (ft!s} 46.57 47.71 47.44 47.24 

Ds (In) 75.00 75.00 75.00 

As (ft2) 30.68 30.68 30.68 

QS, FLOW, ACFM 85,732 87,824 87,333 86,963 

Q STD (ft31mln) 52,756 53,727 53,688 53,390 

Q STD DRY, FLOW SCFM 50,241 50,706 50,867 50,604 

WT(gm} 2.32E-12 2.76E-12 3.66E-12 0.0000 

%1 97.04 97.14 100.67 

%C02 1.73 1.63 1.65 1.67 

%02 18.86 19.05 19.05 18.99 

%CO 0.00 0.00 0.00 

%N2 79.41 79.33 79.30 

0/F (lbslhr) 8.88E-11 1.06E-10 1.35E-10 0.000 

DIF (kglhr) 4.03E-11 4.79E-i 1 6.13E-i1 0.0000 

Production (!ph) 20.26 20.26 20.26 20.2600 

Production (Mg) 9.19E-03 9.19E-03 9. 19E-03 9.19E-03 

DIF (kg!Mg of Product} 2.5245E-13 3.003E-13 3.983E-13 3.17E·13 

D!F (ng/dscm) 4.718E-04 5.556EHQ4 7.086E-04 5.79E-04 

DIF {ngldscm@ 7% 02] 3.22E-03 4.17E-03 5.32E-03 4.24E·03 

QS, FLOW, ACMM 2428 2487 2473 2462 

QS, FLOW, DSCMM 1423 1436 1440 1433 

1 Theoretical amount of moisture that Ts can hold. 

lf YcM>%SVP~ %SVP will be utilized in calculations. 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 203 
A2 81 372 0.40 1.94 0.632 

A3 82 373 0.41 i.99 0.640 

A3 83 374 0.41 1.99 0.640 

A4 83 375 0.42 2.04 0.648 

A4 84 376 0.42 2.04 0.648 

A5 84 377 0.42 2.04 0.648 

A5 85 378 0.42 2.04 0.648 

A6 86 380 0.45 2.18 0.671 

A6 86 380 0.45 2.18 0.671 

A7 86 381 0.46 2.23 0.678 19.0 1.7 

A7 87 381 0.46 2.23 0.678 

A8 88 382 0.46 2.23 0.878 

A8 88 383 0.46 2.23 0.678 

A9 89 384 0.46 2.23 0.678 

A9 89 385 0.46 2.23 0.678 

A10 90 385 0.42 2.04 0.648 

A10 90 384 0.42 2.04 0.648 

A11 90 384 0.37 1.80 0.608 

A11 90 364 0.37 1.80 0.608 

A12 91 863 0.36 1.75 0.800 

A12 91 383 0.36 1.75 0.800 

81 91 390 0.41 1.99 0.640 18.9 1.7 

81 91 389 0.41 1.99 0.640 

82 92 389 0.43 2.09 0.656 

82 92 389 0.43 2.09 0.656 

83 92 388 0.44 2.14 0.863 

83 92 388 0.44 2.14 0.863 

84 92 389 0.46 2.23 0.878 

84 93 389 0.46 2.23 0.878 

85 93 389 0.47 2.28 0.686 

85 93 385 0.47 2.28 0.686 

86 93 385 0.47 2.28 0.686 

86 93 385 0.47 2.28 0.686 

87 64 383 0.41 1.99 0.640 18.9 1.8 87 94 383 0.41 1.99 0.640 

88 94 383 0.40 1.94 0.632 

88 94 382 0.40 1.94 0.632 

89 95 382 0.40 1.94 0.832 

89 95 382 0.40 1.94 0.832 

810 95 381 0.39 1.89 0.624 

810 95 381 0.39 1.89 0.624 

811 98 375 0.37 1.80 0.608 

811 96 375 0.37 1.80 0.608 

812 96 375 0.37 1.80 0.608 

812 96 375 0.37 1.80 0.608 

89.81 381.38 0.42 2.03 31.037 18.95 1.73 

corrected per 7 e--sb 18.86 

Vm(ft3) Initial 26.14 % N2 (BY DIFFER£NCE} 79.41 

Final 210.59 

Total 184.45 %Excess Air 895.83 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 204 
A3 100 385 0.42 2.10 0.648 

A3 100 385 0.42 2.10 0.648 

A4 101 386 0.42 2.10 0.648 

A4 101 386 0.42 2.10 0.648 

AS 102 386 0.42 2.10 0.648 

A5 102 387 0.42 2.10 0.648 

AS 102 387 0.45 2.26 0.671 

A6 103 387 0.45 2.26 0.671 

A7 104 389 0.47 2.36 0.686 19.1 1.5 A7 104 390 0.47 2.36 0.666 

A8 104 391 0.50 2.51 0.707 

A8 104 391 0.50 2.51 0.707 

A9 104 390 0.45 2.26 0.671 

A9 104 390 0.45 2.26 0.671 

A10 105 388 0.42 2.10 0.648 

A10 105 388 0.42 2.10 0.648 

A11 105 388 0.39 1.95 0.624 

A11 105 384 0.39 1.95 0.624 

A12 105 384 0.39 1.95 0.624 

A12 105 382 0.39 1.95 0.624 

81 105 390 0.40 2.00 0.632 19.0 1.7 

81 105 391 0.40 2.00 0.632 

82 105 391 0.40 2.00 0.632 

82 105 392 0.40 2.00 0.632 

83 105 392 0.41 2.05 0.640 

83 106 394 0.41 2.05 0.640 

84 106 394 0.45 2.26 0.671 

84 106 392 0.45 2.26 0.671 

85 106 391 0.48 2.41 0.693 

85 106 390 0.48 2.41 0.693 

86 106 389 0.50 2.51 0.707 

86 106 385 0.50 2.51 0.707 

87 106 387 0.49 2.46 0.700 19.0 1.7 

87 106 387 0.49 2.46 0.700 

88 106 387 0.49 2.46 0.700 

88 107 385 0.49 2.46 0.700 

89 107 385 0.46 2.31 0.678 

89 107 385 0.46 2.31 0.678 

810 107 382 0.44 2,21 0.663 

810 107 382 0.44 2.21 0.663 

811 107 380 0.44 2.21 0.663 

811 107 379 0.44 2.21 0.663 

812 107 379 0.39 1.95 0.624 

812 107 379 0.39 1.95 0.624 

104.33 386.92 0.44 2.18 31.644 19.05 1.63 

corrected per 7eu5b 19.05 

Vm(ft3) Initial 211.25 % NZ (BY DIFFERENCE) 79.33 

Final 402.33 

Total 191.08 %Excess Air 1006.98 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 205 
386 0.38 1.88 0.616 

A3 101 386 0.41 2.03 0.640 

A3 100 386 0.41 2.03 0.640 

A4 100 385 0.41 2.03 0.640 

A4 100 385 0.41 2.03 0.640 

A5 101 388 0.43 2.13 0.656 

A5 101 388 0.43 2.13 0.656 

A6 100 387 0.46 2.28 0.678 

A6 100 389 0.46 2.28 0.678 

A7 100 384 0.48 2.38 0.693 19.0 1.7 

A7 100 384 0.48 2.38 0.693 

AB 99 384 0.48 2.38 0.693 

AB 99 383 0.48 2.38 0.693 

A9 99 383 0.46 2.28 0.678 

A9 99 382 0.46 2.28 0.678 

MO 99 379 0.43 2.13 0.656 

MIJ 98 379 0.43 2.13 0.656 

A11 98 379 0.44 2.18 0.663 

A11 98 374 0.44 2.18 0.863 

A12 98 374 0.37 1.83 0.608 

A12 98 373 0.37 1.83 0.608 

81 98 385 0.40 1.98 0.632 19.2 1.6 

81 98 385 0.40 1.98 0.632 

82 97 384 0.39 1.93 0.624 

82 97 384 0.39 1.93 0.624 

83 97 384 0.39 1.93 0.624 

83 97 386 0.39 1.93 0.624 

84 97 386 0.44 2.18 0.663 

84 97 382 0.44 2.18 0.663 

85 96 382 0.47 2.33 0.686 

85 96 383 0.47 2.33 0.686 

86 96 381 0.50 2.48 0.707 

86 96 381 0.50 2.48 0.707 

87 96 381 0.46 2.28 0.678 19.1 1.6 

87 96 381 0.46 2.28 0.678 

86 96 380 0.47 2.33 0.686 

88 96 376 0.47 2.33 0.686 

89 96 376 0.46 2.28 0.678 

89 95 378 0.46 2.28 0.678 

810 95 379 0.46 2.28 0.678 

810 95 380 0.46 2.28 0.678 

811 95 375 0.44 2.18 0.663 

811 95 375 0.44 2.18 0.663 

812 94 375 0.39 1.93 0.624 

812 94 374 0.39 1.93 0.624 

97,85 381.92 0.43 2.15 31,568 19.05 1.85 

corrected per 7e~5b 19.05 

Vm(ft3) Initial 403.43 % N2 (BY DIFFERENCe) 79.30 

Final 600.02 

Total 198.59 %Excess Air 1010.50 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5. SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 206 
a p ws M TP . 

s s 117 

BORALBRICK 

Modu/e/D 

Dn 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACTION,NOT%} 

Md 

Pbar 

PS(GAUGE) 

Ps 

Tm,F 

Tm,R 

Ms 

Ts,F 

Ts,R 

Pm 

K 

Terminology 

9/2212010 

Run#1 Run #2 Run#3 

ATC4 ATC4 ATC4 

0.289 0.289 0.289 

1.951 1.951 1.951 

0.995 0.995 0.995 

0.84 0.84 0.84 

0.05 0.05 0.05 

29.0 29.0 29.0 

29.31 29.33 29.30 

0.25 0.25 0.25 

29.33 29.35 29.32 

90 105 100 

549.69 564.69 559.69 

28.45 28.45 28.45 

385 380 380 

844.69 839.69 839.69 

29.42 29.46 29.49 

4.8526 5.0114 4.9568 

Ms=APPARENT STACK GAS MOLECULAR WEIGHT 

=Md(1·Bw)+18Bw 

Md=DRY GAS MOLECULAR WEIGHT (29) OR 

=(0.44'%C02)+(0.32'%02)+(0.28.(%N2+%CO)) 

Ps GAUGE=STACK STATIC PRESSURE (IN. H20) 

Ps=ABSOLUTE STACK PRESSURE (IN. Hg) 

Pm=METER ABSOLUTE PRESSURE (IN. Hg) 

= Pbar + (avg dH/13.6) 

'The method 5 sampling train is intended to operate at a sampling rate of 0.75 cfm of dry air at 68 

oF and 29.92 in. Hg. The orifice meter pressure differential that would produce such a sampling rate 

through the orifice is designated as LIH@. 

_The thef'.!ffi!l!£.~i nozz~~ c~aif'&iation is .Q.QtionaL If the tester feels comfortable choosing the 

nozzle size through other means (experience, prior testing, etc.), this is also acceptable. On 

(theoretical) is calculated on the assumption that a 0.75 cfm flowrate is achieved at 68 'F and 29.92 in. 

ATC PROJECT No. P-10142 

Hg. 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 207 
2i ABSOLUTE STACK PRESSURE 

Ps = P ATM + Ps{GAUGE}/13.6 

PATM Ps(GAUGE) 

29.31 0.25 

Ps 

29.33 

3) SAMPLE VOLUME AT STANDARD CONDITIONS 

VM STD • (VM)'(Y)'(T STDITM)"(PMIP STD) 

Vm Tm y VmSTD 

184.45 549.50 0.995 17:3.63 ft3 

4) VOlUME OF WATER COLLECTED, CORRECTED TO StANDARD CONDITIONS 

W STD • W STDw + WST!Jsg 

W STOw • ( 002673)"(\/l_Qw)"(T STOlP STD) 

W STDsg • (.002668)'\/LQsg)"(T STOlP STD) 

WHERE 0.002673 = 0.04707 FT3/Ml'"IN. HG/17.64 DEG. R WHERE 0.002668 = 0.04715 FT3/G"IN.HGI17.64 DEG. R. 

VLQ (w) 

167.00 

\/l_Q (sg) 

17.30 

WSTD 

8.69 

S) TOTAL SAMPLE VOLUME AT STANDARD CONDITIONS 

V STD= Vm STO +W STD = 182.32 ft3 

6) PERCENT MOISTURE lN STACK GAS 

%M = (100)*{W STD}N STD = 4.77% 

1) MOLE FRACTION OF DRY GAS 

MD"' {100-%M}/100"' 0.952 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 208 
9) MOLECULAR WEIGHT OF THE WET GAS 

M = (MWD)"(MD) + 18(1-MD) = 

WHERE 18 =MOLECULAR WEIGHT OF WATER, GiG-MOLE 

10) STACK VELOCITY 

VS = (8S.49)'(CPt((TSI(PS)(M))~112'((SUM SQRT DP)IN OP)) 

where 85.49 :o. ftfsec~ [!b/lb-mole"lo.Hg)J(deg_ R*in H20)]"0.5 

CP 

0.84 

Ts (R) 

841.07 

SUM SORT 

31.04 

11} STACK VOLUMETRIC FLOW RATE 

QS = (60)WS)'(AS) 

AS (!nlet) 

30.68 

NDP 

48 

QS 

85,732 

28.50 

VS 

4G.57 

12) STACK VOLUMETRIC F!...,OW RATE, STANDARD CONDITIONS INCLUDING MOtSTURE 

Q SiD= Q STD DRY !MD 52,756 

13) STACK VOLUME FLOW RATE STANDARD CONDITIONS DRY 

Q STD DRY= 17.64r60"Md"Vs"A*(Psfrs{R)) = 50,241 

14) POLLUTANT MASS RATE, CONCENTRATION BASIS 

PMRC = (.1323)'(WT)'(Q STD)N STD 

WHERE 0.1323 "='COMBINED CONVERSION FACTOR (60 M!N/Hf\"0.00220 LBSJGRAM) 

WT(GRAMS) 

0.0000 

15) PERCENT ISOKINETIC 

PMRC 

0.000 

%1 = 

(0.09450"Ts~vm 

std)/(Ps~vs~An~Time"Md} 

Run Time Area of Ncu!e %1 

240 4.58E-04 

ATC PROJECT No. P-10142 

97.04 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 209 
Specific Source Dryer 

Air Pollution Controls 

Test Methods US EPA M 23 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 210 
Pm (In lfg} 29.44 29.48 29.52 

Ps(GAUGE) 0.16 0.16 0.16 

Ps(/NHG) 29.33 29.37 29.41 

Tm(F) 76.75 94.77 102.58 

Tm(R) 536.44 554.46 562.27 

Vm (ft3) 173.44 176.04 177.72 

vm sro (ftJJ 161.74 159.07 158.58 

VLQ(ml) 128.20 131.00 136.10 

WSTD(ft3} 6.05 6.18 6.42 

VSTD(ft3) 167.79 165.24 165.00 

%M 3.60 3.74 3.89 3.74 %SVPJ 12.74 12.94 13.22 

MD 0.964 0.963 0.961 

MWD 28.84 28.84. 28.84 

M 28.45 28.43 28.41 

Ts(F) 122.98 123.60 124.44 123.67 

Ts(R) 582.67 583.29 584.13 583.36 SUMSQRTDP 33.96 34.26 34.23 

NDP 48.00 48.00 48.00 

AVGSQRTDP 0.71 0.71 0.71 

CP 0.84 0.84 0.84 

Vs (ftls) 42.46 42.84 42.81 42.70 

Ds(ln} 51 X39 51 X 39 51 X 39 

As (f!2} 13.81 13.81 13.81 

CIS, FLOW, ACFM 35,192 35,500 35,479 35,390 Q STD (ft3/m/n) 31,263 31.546 31,525 31,445 Q STD DRY, FLOW SCFM 30.136 30,367 30,299 30,267 WT(gm} 9.00E-14 4.92E-14 2.03E·13 0.0000 

%1 100.88 98.46 98.38 

%C02 0.00 0.00 0.00 0.00 

%02 20.90 20.90 20.90 20.90 \/ %CO 0.00 0.00 0.00 

j/0 q,.l... %N2 79.10 79.10 79.10 DIF (lbslhr) 2.22E-12 1.24E·12 5.13E·12 2.86E·12 ( \. DIF(kglhl) 1.01E-12 5.64E-13 2.33E·12 1.30E-12 '\' / Producnon (tph) 20.26 20.26 20.26 2.03E+01 I Production (Mg) 9.19E-03 9.19E-03 9.19E-03 9.19E.03 

{J DIF (kg!Mg of Product) 9.7935E·15 5.354E-15 2.209E-14 1.24E-14 

~· 

DIF (ng!dscm) 1.965E-05 1.092E-05 4.520E-05 2.53E-05 

~~ \t DIF (ngldscm@ 7% 02} #DIV/0! #OIV/0! #OIV/0! #DIV/01 QS, FLOW, ACMM 996 1005 1005 1002 QS, FLOW, DSCMM 853 860 858 857 

~ 1\Q 1 Theoretical amount cf moisture that T.s can hold. % Jfo/~>%SVP1 %SVP wm be utilized In calculatfons. 1'-y Q\. t· ' ']! 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT APPENDIX PAGE No. 211 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 
70 

A3 70 

A3 70 

A4 70 

A4 70 

A5 71 

As 71 

A6 72 

A6 72 

81 73 

81 74 

82 74 

82 74 

83 74 

83 75 

84 75 

84 76 

B5 76 

B5 77 

B6 77 

B6 77 

C1 78 

C1 78 

C2 79 

C2 79 

C3 80 

C3 80 

C4 80 

C4 80 

C5 80 

C5 81 

C6 81 

CB 81 

D1 81 

D1 81 

02 81 

02 82 

03 82 

D3 82 

04 82 

D4 82 

D5 82 

D5 82 

D6 82 

D6 82 

76.75 

Vm(ft3) 

ATC PROJECT No. P-10142 

123 0.43 1.35 0.656 

122 0.47 1.48 0.686 

122 0.47 1.48 0.686 

122 0.49 1.54 0.700 

123 0.49 1.54 0.700 

123 0.53 1.67 0.728 

123 0.53 1.67 0.728 

123 0.57 1.79 0.755 

123 0.57 1.79 0.755 

123 0.50 1.57 0.707 

123 0.50 1.57 0.707 

123 0.44 1.38 0.663 

123 0.44 1.38 0.663 

123 0.49 1.54 0.700 

122 0.49 1.54 0.700 

123 0.50 1.57 0.707 

124 0.50 1.57 0.707 

124 0.52 1.63 0.721 

124 0.52 1.63 0.721 

123 0.54 1.70 0.735 

123 0.54 1.70 0.735 

123 0.49 1.54 0.700 

123 0.49 1.54 0.700 

123 0.45 1.41 0.671 

122 0.45 1.41 0.671 

122 0.45 1.41 0.671 

123 0.45 1.41 0.671 

124 0.50 1.57 0.707 

124 0.50 1.57 0.707 

124 0.55 1.73 0.742 

123 0.55 1.73 0.742 

123 0.58 1.82 0.762 

123 0.58 1.82 0.762 

123 0.48 1.51 0.693 

123 0.48 1.51 0.693 

123 0.48 1.51 0.693 

123 0.48 1.51 0.693 

123 0.43 1.35 0.656 

123 0.43 1.35 0.656 

122 0.50 1.57 0.707 

123 0.50 1.57 0.707 

123 0.57 1.79 0.755 

123 0.57 1.79 0.755 

123 0.57 1.79 0.755 

123 0.57 1.79 0.755 

122.98 0.50 1.58 33.965 20.90 0.00 

corrected per 7e~5b 20.90 lnit!a! 467.99 % N2 (BY DIFFERENCE) 79.10 Final 641.43 

Total 173.44 %Excess Air 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

·118750.00 

APPENDIX PAGE No. 212 
A3 90 

A3 90 

A4 90 

A4 91 

AS 91 

A5 91 

A6 91 

A6 92 

81 92 

81 93 

82 94 

82 94 

B3 94 

83 94 

84 94 

B4 95 

BS 95 

B5 95 

86 95 

86 95 

C1 95 

C1 96 

cz 96 

C2 96 

C3 97 

C3 97 

C4 98 

C4 98 

C5 98 

C5 98 

co 98 

C6 98 

01 98 

01 98 

D2 98 

02 98 

03 98 

D3 99 

D4 99 

D4 98 

D5 98 

D5 98 

06 98 

D6 99 

94.77 

Vm(ft3} 

ATC PROJECT No. P-10142 

663 

124 0.49 1.58 0.700 

124 0.49 1.58 0.700 

123 0.49 1.58 0.700 

123 0.49 1.58 0.700 

123 0.55 1.78 0.742 

123 0.55 1.78 0.742 

123 0.56 1.81 0.748 

122 0.56 1.81 0.748 

124 0.53 1.71 0.728 

124 0.53 1.71 0.728 

122 0.42 1.36 0.648 

122 0.42 1.36 0.648 

123 0.48 1.55 0.693 

123 0.48 1.55 0.693 

123 0.49 1.56 0.700 

123 0.49 1.58 0.700 

124 0.54 1.75 0.735 

125 0.54 1.75 0.735 

125 0.54 1.75 0.735 

125 0.54 1.75 0.736 

124 0.50 1.62 0.707 

124 0.50 1.62 0.707 

124 0.50 1.62 0.707 

124 0.50 1.62 0.707 

123 0.47 1.52 0.686 

123 0.47 1.52 0.686 

123 0.51 1.65 0.714 

123 0.51 1.65 0.714 

123 0.57 1.84 0.755 

123 0.57 1.84 0.755 

123 0.60 1.94 0.775 

124 0.60 1.94 0.775 

124 0.50 1.62 0.707 

124 0.50 1.62 0.707 

124 0.49 1.58 0.700 

125 0.49 1.58 0.700 

125 0.43 1.39 0.656 

125 0.43 1.39 0.656 

124 0.51 1.65 0.714 

124 0.51 1.65 0.714 

125 0.56 1.81 0.748 

124 0.56 1.81 0.748 

122 0.58 1.88 0.762 

122 0.58 1.88 0.762 

123.60 0.51 1.65 34.259 20.90 0.00 

corrected per 7e.-5b 20.90 Initial 642.37 % N2 (BY DIFFERENCE) 79.10 Final 818.41 

Total 178.04 %Excess Air 

EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

-11875().00 

APPENDIX PAGE No. 213 
A3 104 124 0.52 1.70 0.721 

A3 105 124 0.52 1.70 0.721 

A4 105 124 0.53 1.73 0.728 

A4 105 124 0.53 1.73 0.728 

AS 105 123 0.56 1.83 0.748 

AS 105 123 0.56 1.83 0.748 

A6 105 123 0.56 1.83 0.748 

A6 105 122 0.56 1.83 0.748 

81 104 125 0.52 1.70 0.721 

B1 104 126 0.52 1.70 0.721 

B2 104 126 0.45 1.47 0.671 

B2 104 126 0.45 1.47 0.671 

83 104 125 0.46 1.50 0.678 

B3 104 125 0.46 1.50 0.678 

B4 104 125 0.47 1.53 0.686 

B4 104 124 0.47 1.53 0.686 

BS 104 124 0.53 1.73 0.728 

B5 103 123 0.53 1.73 0.728 

B6 103 123 0.54 1.76 0.735 

B6 103 123 0.54 1.76 0.735 

C1 103 125 0.49 1.60 0.700 

C1 103 125 0.49 1.60 0.700 

C2 103 124 0.51 1.66 0.714 

C2 103 124 0.51 1.66 0.714 

C3 103 126 0.51 1.66 0.714 

C3 102 126 0.51 1.66 0.714 

C4 102 126 0.41l 1.57 0.693 

C4 102 127 0.48 1.57 0.693 

C5 102 126 0.55 1.79 0.742 

C5 101 125 0.55 1.79 0.742 

C6 101 124 0.56 1.83 0.748 

C6 101 124 0.56 1,83 0.748 

01 100 126 0.50 1.63 0.707 

01 100 126 0.50 1.63 0.707 

D2 100 125 0.48 1.57 0.693 

02 100 125 0.48 1.57 0.693 

03 100 125 0.48 1.57 0.693. 

DJ 100 124 0.48 1.57 0.693 

04 100 124 0.43 1.40 0.656 

04 100 124 0.43 1.40 0.656 

05 100 123 0.54 1.76 0.735 

D5 100 123 0.54 1.76 0.735 

D6 99 123 0.57 1.86 0.755 

06 99 123 0.57 1.86 0.755 

102.58 124.44 0.51 1.66 34.228 20.90 0.00 

corrected per 7e--5b 20.90 

Vm(ft3} Initial 818.52 % N2 (BY DIFFERENCE) 79.10 

Fin a! 996.24 

Total 177.72 %Excess Air -118750.00 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 214 
BEGINNING 100 100 

ENDING 218 103 

NET 118 3 

Run#3 

1stlmp. 2nd Imp. 

BEGINNING 100 100 

ENDING 227 100 

NET 127 0 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

0 300.0 

0 310.0 

0 10.0 131.0 

3rd Imp. 4th Imp. TOTALS 

0 300.0 

0 309.1 

0 9.1 136.1 

APPENDIX PAGE No. 215 
@ 

ws 

M TP :r

s s m 

Modu/e/D 

On 

dH@ 

Y, gamma factor 

Cp 

Bw(FRACT/ON,NOT"/o) 

Md 

Pbar 

PS(GAUGE) 

Ps 

Terminology 

Tm,F 

Tm,R 

Ms 

Ts,F 

Ts,R 

Pm 

K 

BORALBRICK 

9/23/2010 

Run#1 

ATC3 

0.237 

1.937 

0.963 

0.84 

0.04 

29.0 

29.32 

0.16 

29.33 

80 

539.69 

28.56 

125 

584.69 

29.43 

3.1432 

Run #2 

ATC 3 

0.237 

1.937 

0.963 

0.84 

0.04 

29.0 

29.36 

0.16 

29.37 

95 

554.69 

28.56 

125 

584.69 

29.44 

3.2343 

Run #3 

ATC3 

0.237 

1.937 

0.963 

0.84 

0.04 

29.0 

29.40 

0.16 

29.41 

100 

559.69 

28.56 

125 

584.69 

29.48 

3.2629 

Ms=APPARENT STACK GAS MOLECULAR WEIGHT 

~Mct(1-Bw)+18Bw 

Md~DRY GAS MOLECULAR WEIGHT (29) OR 

=(0.44.%C02)+(0.32*%02)+(0.28.(%N2+%CO)) 

Ps GAUGE=STACK STATIC PRESSURE (IN. H20) 

Ps=ABSOLUTE STACK PRESSURE (IN. Hg) 

Pm=METER ABSOLUTE PRESSURE (IN. Hg) 

= Pbar + (avg dH/13.6) 

'The method 5 sampling train is intended to operate at a sampling rate of 0.75 elm of 

dry air at 68 oF and 29.92 in. Hg. The orifice meter pressure differential that would produce 

such a sampling rate through the onfice is designated as IIH@. 

_The ih§wretlcal nozzle cafcuiat.ion is option_ai._ lf the tester feels comfortable 

choosing the nozzle size through other means (experience, prior testing, etc.), this is also 

acceptable. On (theoretical) is calculated an the assumption that a 0.75 elm llowrate is 

achieved at 68 'F and 29.92 in. Hg. 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 216 
2) ABSOLUTE STACK PRESSURE 

Ps = P ATM + Ps(GAUGE)/13.6 

PATM Ps(GAUGE) 

29.32 0.16 

Ps 

29.33 

3} SAMPLE VOLUME AT STANDARD CONDITIONS 

VM STO • (VM)"(Y)'(T STOITM)"(PMIP STD) 

Vm Tm y VmSTD 

173.44 536.44 0.963 161.74 

ff3 

4) VOLUME OF WATER COLLECTED, CORRECTED TO STANDARD CONDITIONS 

W STD = W STOw+ WSTDsg 

W STOw •(.002673)'(VLQw)'(T STOlP STD) 

W STDsg = (.002668)'1/LQsg)'(T STOlP STD) 

WHERE 0.002673 • 0.04707 FT3/ML'IN. HG/17.64 DEG. R. 

WHEHE 0.002688 = 0.04715 FT3/G'IN.HGI17.64 DEG. R. 

VLQ (w) 

120.00 

VLQ (sg) 

8.20 

WSTD 

6.05 ft3 

5} TOTAL SAMPLE VOLUME AT STANDARD CONDITIONS 

VSTD= Vm STD+ WSTD= 1$7.79 ft3 

6) PERCENT MOISTURE IN STACK GAS 

%M = (100)'(VV STD)N STD = 3.SO% 

7) MOLE FRACTION OF DRY GAS 

MD= (100-o/oM)/100"' 0.964 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 217 
9) MOLECULAR WEIGHT OF THE WET GAS 

M • (MWD)'(MO) + 18(1-MD) = 

WHERE 18 =MOLECULAR WEIGHT OF WATER, GIG-MOLE 

10) STACK VELOCITY 

VS = (85.49)'(CP)'((TSI{PS)(M))'112'((SUM SQRT DP)IN DP)) 

where 85.49 = ftlsec" [lh/1b-mole""in.Hg)/(deg. Win t-120)1"'0.5 

CP 

0.84 

Ts(R) 

582.67 

SUMSQRT 

33.96 

11} STACK VOLUMETRIC FLOW RATE 

QS = (60)"(VS)'(AS) 

AS (inlet) 

13.81 

NDP 

48 

OS 

35,192. 

28.45 

vs 

42..46 

12) STACK VOLUMETRIC FLOW RATE, STANDARD CONDITIONS !MCLUD!NG MOISTURE 

Q STD = Q STD DRY/MD 31,263 

13) STACK VOLUME FLOW RATE STANDARD CONDITIONS DRY 

Q STD DRY= 17.647'60"Md"Vs'A'(Ps1Ts(R)) = 30,136 

14) POLLUTANT MASS RATE, CONCENTRATION BASIS 

PMRC = (.1323)'{WT)'(Q STD)N STD 

WHERE 0.1323 • COMBINED CONVERSION FACTOR (60 MIN/HR'0.00220 LBSIGRAM) 

WT(GRAMS) 

0.0000 

15) PERCENT !SOKINET!C 

PMRC 

0.000 

%1 = {0.09450*Ts~vm std)/(Ps"Vs"Att"Time"Md) 

Run Time Area of Nozzle %1 

240 3.06E-04 100.88 

ATC PROJECT No. P-10142 EPA ICR EMISSION TEST PROJECT 

AUGUSTA PLANTS 4 & 5, SALISBURY PLANT 6 

SEPTEMBER 2010 

APPENDIX PAGE No. 218