-------
ISO
MT
PO
PERCENT ISOKINETIC
TOTAL MAS3 OF PARTICLES
PARTICLE DENSITY
GR
.Ob GH/CI
59.900 MG
1.00 GM/CC
68 OEG F, 89.
IN.HG.
I
ho
-------
IMPACTOP RESULTS AND EXAMPLE CALCULATIONS
PLANT-NAME AND CITY
ASARCO TACUMA
TEST DATE Ol/JO/83
TEST TEAM LtADER
00
RUN NO
PSB-3
SAMPLE LOCATION
NO « SEC tX
CALC. MASS LOADING
TOTAL MASS OF PARUCLES DIVIDED BY A VOLUME. UNITS GIVEN ARE GRAINS PER
ACTUAL* CUBIC FOOT(GR/ACF).GRAINS PER DRY STANDARD** CUBIC FOOT(GR/DSCF),
MILLIGRAMS PER ACTUAL CUBIC ME TEH(MG/ACM) AND MILLIGRAMS PER DRY STANDARD
CUBIC METEH(MG/OSCM.)
EXAMPLE CALCULATIONS
CML(CRXACF) • MT(GR) / IF(ACF)
CML » ,92fl / 17.083 *
CML(6R/DSCF) • MT(GB) / VMSTO(D3CF)
CML « - .92fl / 06.607 =
CML(MS/*CM) * MT(MG) / IF(ACM)
CML a 59.900 / 1.333 =
CML(MG/OSCM) * MT(MG) / VMSTO(DSCM)
CML n 59.900 / 1.331 =
0196 GR/ACF
.0198 GH/OSCF
43.9c!81 MG/ACM
05.3076 MG/OSCM
050 (MICROMETERS)
THE SIZE OF THE PARTICLES UN EACH STAGE ASSUMING A 50 PERCENT
COLLECTION EFFICIENCY DEFINITION
MASS (MILLIGRAMS)
THE MASS ON EACH STAGE COLLECTED
MG/DSCM/STAGE
EXAMPLE CALCULATIONS
MG/DSCM/STAGE(I) =
MG/DSCM/STAGE(1) *
CUM. PERCENT OF MASS
EXAMPLE CALCULATIONS
CUM X (6) = MASS(7)
THE MASS LOADING FOR EACH STAGE. UNITS GIVEN ARE MILLIGRAMS
PER DRY STANDARD CUBIC METER FOR EACH STAGE(MG/DSCM/STAGE)
MASS(l) / VMSTD(OSCM)
58^0 / 1.321 =
03.91
THE PERCENTAGE OF THE TOTAL MASS SAMPLED SMALLER
IN DIAMETER THAN THE COPRESPONUING 050 INDICATED
FOR THAT STAGE
CUM X (6) =
MASS18) * MASS(9)
MT (MG)
.20 + .20 »
59.90 (MG)
100 =
.60
* 100 =
2.IT
-------
CUM.(MASS/VOLUME)
I
M
THE CUMULATIVE MASS LOADING OF PARTICLtS SMALLER IN DIAMETER
THAN THE CORRESPONDING l>50. M43S/VULUME UNITS ARE
MG/USCM.GR/ACF,GN/OSCF.
EXAMPLE CALCULATIONS
CUM.(MGXACM) (5) = MAS3(6) + MAS3(7) » MASS(8) * MAS3(9)
IF(ACM)
CUM.(MGXACM) (5) = .30 * .80 + .c!0 »
1.33 (ACM)
.60
CEO.MEAN DIA.(MICROMETERS)
THE GEOMETRIC MEAN DIAMETER IN MICROMETEKS
FOH A PARTICULAR STAGE.
EXAMPLE CALCULATION
6EO.MEAN DIA.(J) e SURT( 050(J) • 050(J-1))
GEO.MEAN DIA.«>) = SUHTC i.oe • a.»5)
DM/DL06D(MG/03CM)
DM IS MG/DSCM/3TAGEU) AND DLUGO IS LOG I 0 (050 (J- I ) /
D50(J)) WHERE J IS THE CORRESPONDING STAGE NUMBER.
FOR STAGE 1 THE MAXIMUM PARTICLE OIAMF1ER IS USED.
FOR STAGE 9 (BACKUP FILTER) THE 050 13 A33UMEO AS
.5 « D50 OF STAGE 6.
EXAMPLE CALCULATION
DM/OLOGD(J) = MG/DSCM/STAGEU)
LOGl OSO(J-l) / D50U))
DM/DLOGD (3) r .UO
_______.._._._...-_.._-_. i
LOG( 9.^9 / 6.03 )
.00
DN/DLOGD THE NUMBER OF PARTICLES PER UNIT VOLUME FOH A STAGE.
EXAMPLE CALCULATION
DN/DL060(J) = DM/OLOGD(J)
5.23599E-10 * PD(GM/CC) • GEO.MEAN DIA.(J)
ON/DLOGD (3) = .00
10 * 1.00 • 1 ,U6
.00
• CALCULATED AT STACK CONDITIONS
•* CALCULATED AT STANDARD CONDITIONS
68 DEG.F AND 29. 9Z INCHES OF HG (760 MMHG)
.98
-------
FIELD OAT*
PLANT A3ARCU TACUMA
SAMPLING LOCATION NO « SEC EX
SAMPLE TYPE PAHT SIZE-BLOW
OPERATOR t>0
AMBIENT TEMP. (DEG.F) 55.
BAR. PRESS. (IN. HG) 29.70
STATIC PRESS. (IN. H20) -3.00
FILTER NUMBER(S) MARK III
STACK INSIDE DIM. (IN) 60.00 .00
PITOT TUBE COEFF. .B4
THERM. NO.
LEAKAGE .000 CFM a .0 IN.MG
METER CALIB. FACTOR .980
READ I RECORD DATA EVERY 5.0 MIUUTE3
TRAVERSE SAMPLE CLOCK GAS METER VELOCITY ORIFICE PRESSURE STACK
POINT TIME TIME READING HEAD DIFFERENTIAL TFMP
NO. (MIN.) (24-HR (CU.FT.) (IN.H20) (IN.H2U) (DEG.F)
> INIT 0
1 5.0
^ 10. 0
w I5-°
15.0
20.0
25.0
25.0
30.0
40.0
50.0
60.0
70.0
70.9
76.5
90.0
100.0
108.9
120.0
130.0
140.0
148.5
160.0
170.0
160. 0
190.0
199.9
VL. V'V» " /
1607
0
0
1622
1706
0
1716
1739
0
0
0
0
0
1026
1903
0
0
2036
0
0
0
211S
0
0
0
0
2211
DESIRED
615.937
618.320
620.710
623.048
628.738
631.170
633.577
640.409
642.620
647 .650
652.990
657.850
662.710
663. 137
667.191
6/2.720
677.550
6B1 .84Q
687.240
692.100
696.970
701 .097
706.630
711.510
716.400
721 .280
725.648
.450
.300
.400
.500
.300
.350
.500
.500
.500
.500
.500
.550
.500
.550
.550
.550
.550
.550
.550
.500
.550
.550
.550
.550
.450
.550
.62
.82
.8?
.82
.82
.82
.82
.82
.B2
.82
.82
.82
.62
.82
.82
.82
.82
.82
.82
.82
.82
.82
.82
.82
.62
.62
ACTUAL
.62
.82
.82
.82
.82
.82
.82
.82
.82
.62
.82
.82
.82
.82
.82
.82
.82
.82
.82
.82
.82
.82
.82
.82
.82
.«2
DATE 01/22/83
HUN NUMBER PSB-a
PHUBE LENGTH A TYPE 6* STEEL
NOZZLE : I.D. .118
ASSUMED MOISTURE 1.0
SAMPLE BOX NUMBER
METER BOX NUMHER F89
MtTER HEAD OIFF. 2.08
PPOBE HEATER SETTING o.
HEATER BOX SETTING 0.
DRY GAS METER PUMP IMPACTUR IMPINGES
TEMP VACUUM TEMP TEMP
(OEG.F) UN.HG) (DEG.F) (DEG.F)
INLET OUTLET
64.
62.
63.
63.
63.
63.
63.
68.
64.
62.
62.
63.
62.
58.
62.
62.
60.
69.
64.
62.
61 .
69.
63.
62.
61.
61.
46.
49.
50.
60.
53.
53.
60.
58.
61.
64.
65.
65.
67.
58.
54.
56.
59.
61.
62.
64.
65.
64.
65.
66.
66.
67.
54.
54.
54.
61.
56.
56.
61.
60.
61.
62.
63.
64.
65.
64.
60.
60.
60.
61.
62.
63.
63.
64.
65.
65.
65.
66.
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
64.
62.
63.
63.
63.
63.
63.
68.
64.
62.
62.
63.
62.
56.
62.
62.
60.
69.
64.
62.
61.
69.
63.
62.
61.
61.
49.
49.
49.
49.
50.
50.
51.
47.
47.
47.
47.
48.
46.
46.
45.
45.
45.
45.
45.
46.
46.
47.
47.
47.
45.
«5.
TOTALS
AVERAGE
199.9
97.189
.82
.82
63.
60.
61.
.0
63.
47.
PERCENT ISOKINETIC
98.6
-------
ASARCO TACOMA
NO 4 SEC EX
01/22/83
PSB-O
DO
b2.9F 17.2C
39.70
29.48
.148
.820
PLANT ft CITY
SAMPLING LOCATION
DATE
RUN NUMBER
OPERATOR
STACK TEMP.
BAR. PRESS. (IN. H6)
STACK PRESS. (IN. HG)
NOZZLEU.D.dN.)
METER HEAD DIFF.
CALC. MASS LOADING » 5.4737E-03 GR/ACF
IMPACTOR STAGE
STAGE INDEX NUMBER
.p MO (MICROMETERS)
to MASS (MILLIGRAMS)
M
**" MG/03CM/8TAGE
CUM. PERCENT OF MASS SMALLER THAN 050
CUM. (MG/ACM) SMALLER THAN 050
CUM. (MG/OSCM) SMALLER THAN 050
CUM. (GR/ACF) SMALLER THAN 050
CUM. (6R/03CF) SMALLER THAN 050
GEO. MEAN DIA. (MICROMETERS)
DM/DLOGD (MG/DSCM)
DN/DLOGO (NO. PARTICLES/DSCM)
IMPACTUH FLUWRATE(ACFMJ
AT IMPACTOH CONniT10N3
IMPACTOR TEMP.
PAHTICLE OEN3ITY(GM/CC)
MAX.PftWTICLE DIAM.MKP.U3
GAS COMPU3ITION(PEHCENT)!
C02
CO
N2
02
H20
31
1
10.40
31.40
1.15E+01
9.25
1.16E+00
1.18E+00
5.06E-OQ
5.14E-04
3.23E*01
I.17E+01
6.66E»OS
5.5576E
32
2
9.18
.UO
O.OOE»00
9.25
1.16E+00
1.18E+00
5.06E-04
5.14E-04
9.77E+00
O.OOE+00
O.OOE+00
SAMPLING OURATION(MIN.)
•03 GR/OSCF
S3 SO
3 0
5.93 3.79
.50 .30
.406
17 ,2C
1 .00
100.0
.00
.00
99.00
.00
1.00
199.90
I.2718E+OI MG/OSCM
38 FILTER
8 9
.39
.80 .80
1.252bE*01 MG/ACM
35 Sfc 87
5 b 7
2.Ob 1.00 .70
.20 .30 .30
1.83E-01 1.10E-01 7.33E-02 1.10E-01 1.10E-01 ^.93E-01 Z.93E-QI
7.80 6.94 6.3b 5.49 4.62 2.31
9.77E-01 B.69E-01 7.9bE-01 6.88E-OI 5.79E-01 2.90E-01
9.92E-01 8.82E-01 B.09E-01 b.98E-01 5.88E-01 2.94E-01
4.27E-04 3.80E-04 3.48E-04 3.01E-04 2.53E-04 1.27E-04
4.34E-04 3.85E-04 3.53E-04 3.05E-04 2.57E-04 1.28E-04
7.38E*00 4.74E+00 2.80E*00 1.43E*00 8.38E-01 5.23E-01 2.75E-01
9.bbE-01 5.6bE-01 2.77E-01 3.48E-01 7.28E-01 I.l3t»00 9.7JE-01
4.59E»06 1.01fc»07 2.42E*07 2.25E»08 2.3fcE»09 1 .51EMO 8.97E»tO
STANDARD CONDITIONS ARE 20 DEGC AND 760MM HG.
AERODYNAMIC DIAMETERS ARE CALCULATED HERE ACCORDING TO THE TASK GROUP ON LUNb DYNAMICS.
-------
>
I
AbAKU) IAIIJMA
NO U StC KX
oi /a50
GEO. MEAN OIA. (MICROMETERS)
DM/DUOGD (MG/DSCM)
DN/DLOGD (NO. PARTICLES/OSCM)
IMP ALT UP
A I I S'Par I uk LUND I T I HNS
-03
SI
1
10.as
3i.io
.00
GW/
55
3
0.
50
iMHALtljP ftMp. ha.4F If.aC
PAHTICL> Dh.Nbl 1 Y (f.M/CC ) 1.00
MAX.P«*IlCLt 01 AM. MICROS 100.0
GAS COMMUSI T IUN(P(: RCENT ) : COi? .00
L 0 .00
Nc? 99.00
ua .00
nau i.oo
SAMPLING UUPA F 1 ON (MI N . ) 199.91)
USL> i.ab^bE+oi MG/ACM 1.^7
S.90E-Ol
H.ttrM-lM H.09K-01 h.9Mt-01 b.tl^t-01
3.80K-01 3.1fl£-01 3.0IE-01 a.b3t-01
D1 3.S5E-00 3.05E-01 c
1 . I6E + 00 1 . Ibt+00
1.1BE+00 1.1HK+00
5.0bfc-0« 5.06t-oa
5.11E-01 b.iat-0«
3.ayt+01 9.M5H+00 /.a^t+00
1.17E+01 O.OOt+00 9.7bt-01
b.blb+05 O.OOt+00 <•
l.bat+00 9.15K-OI b.01E-OI 3^9E-01
3.bbt-0l 7.9,>E-yl 1.30E+00 9.73E-OI
a.OH+ofl 1.9Ht + 09 1
STANDARD CONDITIONS ARE 20 DEGC AND 760MM HP,.
AERODYNAMIC DIAMETERS ARE CALCULATED HE"H ACCOWDiNG TO
-------
IMPACHIR M
PLANT-NAME AND AODRtSS
ASARCO TACOHA
TEST PSB-«
NO « SEC EX
TFS1 TfcAM
00
TEST
TB
TF
TT
Y
ON
CP
PM
OATE
TIME-START
TIME-FINISH
NET TIME OF TEST, MIN.
METER CALIBRATION FACIOh
SAMPLING NOZZLE DIAMETEH
PITOT TUOE COEFFICIENT
AVERAGE ORIFICE PRESSURE
ENGLISH UNITS METWIC UMTS
01/VP/H3 Ul/rV/h3
1 h 0 1 \ b 0 7
c^
7«SU.38 MM-Hb
-76.80 M
70B.78 MM-HL.
1 1 . C
-------
I
NJ
130 PtRCENT ISOMNfTIC fn.f, qB-b
MT TOTAL MASS Uf PAWTICLf-5 .SiU (,k ^U.hOO Ml
pt> PARTlCLt DENSITY .Ob ()k/LI |-l)()
* b8 OEG F, ?9.9^ IM.HG.
-------
00
IMPACTUW RF.SUITS AND FXAMPLI CAl LULAT|HNS
PLANT-NAME AND CITY Ttsi IF.AM itADFk KUN MI SAMPLE LUCAIION
ASARCO TACOMA I,D PSH-U NO " st-L tx
TEST DATE C
CALt. MASS LUAUING TU1AL MASS OF PAkTlCLfS U1V1UF_D BY A VOLUME. 11141 1 S GIVLN AkE GRAINS PtH
ACIIIAL* CUBIC EUUT (Gk/ACI- ) .GRAINS PFH DkY bTANDAklx* CIIH1L FUMT(Gk/USCF),
MILLIGRAMS PER ACTUAI CUBIC MF.TFR (MG/AL") AND MILL IGRAM-I PE* DRY SIANIJARU
CUBIC ME lEk(MG/DbCM.)
EXAMPLE CALCULATIONS
CML(GR/ACF) = MT(GR) / IF(ACF)
CML = .530 / 97.b5U = .005b Gk/ACF
CML(GRXDSCF) * MT(GR) / VMSHULKSfF)
CML = .530 / 9b.077 = .005b Gk/USCF
CML(MGXACM) = MT(MG) / IF(ACM)
CML = 3«.bOO / 2.7ht? = I2.5
-------
CUM. (MAS5/VULUMF ) THE CUMULAIIVI MASS LUAhlM, OF P A w 1 1 r. I F S SMALLt^ IN UlAMe
1 M A N IMF I.UWHIIjPUNDlNI, 11 VJ . M A S S / Vlll U"H III) I 1 ;, Alvt Mf, / A I, M ,
Ml, /DSC M , (,W / Al.f ,f,W/DSI I .
EXAMPLE cALCULA T i UNS
CUM.JMG/ACM) (S) - MASb(f>) » MASS(7) * MASS(H) « MA So (4)
IF ( A I, MJ
CUM.(MG/ACM) (S) = .50 « .30 * .HO » .ttd
_ >eo
f . Ih I ,
t;l A . ( MJC^OMf. TEH3) IMF bFUMtTHIC MfAN DJAMflfW [II M 11. KilhF I h K S
F IIH » M AW I I f UL AP T t Al.l- .
EXAMPLE cALCIIL AT iori
(jFU.MEAN UIA.(J) = 5URT( IJSU(J) * L)SO(J-l))
(,Eii.MEAN uiA.fb) =
OM/OLOGO (M(,/D3CM) DM IS Ml,/03CM/S T AT.F ( J ) AND ULOr.D IS L lib 1 U ( DSU ( J - 1 ) /
U^OfJ)) WHEWE J IS THF CIIKMf SPUNUlNl, SlA(,F NUMHFH.
Fllk SlAl.t I IHE MAXIMUM PAW T I CLE |) I AMF I I- H IS USFII.
F OW SIAf,F 4 (HACKUF1 FILTfW) IHE O'jd IS AbhUMED A b
. vj * I)'3II UF STAf.t «.
EXAMPLE CALCULATION
UM/nLOGO(J) = MG/U^CM/STAGF(J)
LUG( DSUIJ-1) / DbU(J))
UM/OLOGD (i) = .IB
i .4H
LIH, ( l.r'b / b.Ol )
ON/OLOGD IHE NIJMHEW OF PARTICLES PEW UNIT VOLUME F UW A b'TAi;F.
EXAMPLE CALCULATION
DN/OLOGt) ( J ) - UM/Ul.UGU ( J )
S.rMV^E-I 0 * POU.M/LL) • OFU.MFAN I) I A . ( J )
ON/DLOGD (5) = .9R
3 . IMJ
- 1 0 * I . U'J • I . 4h
• CALCULATED AT SlACK CUNOIIIUNS
** CALCULATED AT STANI'AHf) rONUIMllllS
f>fl OFG.F AND ^4. <*t INCHES OF HI, ( / h II MMHI, )
-------
END OF PWUliHAM
tFILt FTN10 = CIUHUIOA.OLI)
F TNI 1=CIURU^I)A,OLU
END OF PROGRAM
SFILE FTN08=CIOROJUA,OLO
:FILE FTN()9 = CIDROai)A,OLD
:RUN C10W1PG
NJ
O
-------
ASARCO AVERAGE PAHTICLF SUt l> I S rk IHU t IONS
RHOs 1.00 GM/CC
MEAN CUMULATIVE u^Htk CONFIDENCE
INTERVAL OIAMETEH MASS CONCENTHA I 1 UN LIM1I
(MICkONS) (Mf./ACM) (M(i/ALM)
2.HIE-01
3.0hF -Ul
3.3bE-01
l.bHF -d 1
u .Obf -0 1
» .«bF-0 1
0.93E-01
b.O-JE-Ol
b.O IF -01
b.b3E-01
1 . 5UE-01
H.01E -l»l
H .78E-01
1
2
3
4
5
6
7
a
9
10
11
12
13
14
15
Ib
17
10
1 9
20
21
22
23
24
25
26
27
20
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
lit.
07
08
09
50
51
5?
2.50E-01
2.71E-01
2.95E-01
3.20E-01
3.47E-01
3.77E-01
4.09E-01
4.45E-01
4.83E-01
5.24E-01
S.69E-01
6.18E-01
6.71E-01
7.28E-01
7 .91E-01
8.58E-01
9.32E-01
.OIE+00
. 10E+OU
.19E+00
.29E+00
.«IE+00
.53E+OU
.66E+00
.80E+00
.95E+00
2.12E+00
2.30E+00
2.50F. + 00
2.71E+00
2.95E+00
3.20E+00
3.47F+00
3.77E+00
0.09E+00
0.45E+00
4.83E+OU
5.24E+00
5.69E+00
b. 18E+00
b.71E+00
7.28E*00
7.91E+00
8.58E+00
9.32E+00
. 0 1 E + 0 1
. IOE + 01
.19E+01
.29E+01 f
.01E+01 c
.53E + 01 i.
\ .hhE +01 2
2.73E-01
2.95E-01
3.20E-01
3.09E-01
3.8PE-01
0.20E-01
0.b2E-Ul
5.09E-01
5.61E-01
b.!7E-01
b.78E-01
7.03E-01
8. 1?E-01
8.8bE-01
9.37E-01
9.72E-UI
1 .03E+00
. 1 OE+00
. 1 7E+00
.23E+00
.29E+00
.33F+00
,3/F+OO
.OOE+00
.02E+00
.oaE+oo
,«bE +00
. aȣ +00
.09F +00
.51E+00
.52E+00
.50E+00
.55E+00
.57E+00
,5«e +00
.60E+00
,b2E*<)0
.60E+00
.66E+00
.69E+00
.71E+00
.73E+00
.76E+00
.7HE+00
.81F+00
,8aF +00
. fltiF + 00
.9SK +00
.OHE+00
. ^ « E + 0 U
. 5bE + '10
. 9 a F. + () 0
1 .OIE+00
1 .ObF+00
. 1 IE+00
.20E+UU
. £ 7 E + 0 0
.33E+00
.39E+00
.U3F+00
.07F+00
.50E+00
.53E+00
.55F+OU
.b7E+OU
,S»t +OU
.60F »UO
.blF+UU
,b3F ' + UU
+00
. b 7 E + 0 0
. 7 lE + UO
.73E+00
.75E+00
. 7 7 F. » 0 0
.7>yF +00
.6.JF+00
,8bF +00
.84E+00
.92F +00
.4bF +00
,9^F +00
.ObF +00
t>.aOF+00
00
.UHE+00
.SOE+00
,b,?E + 00
.baE+oo
,b3E»00
.b^E+OO
.bflE +00
.70E+00
.7 5E + 00
.7 7F +0(i
.H4E+00
. 9 7 E + 0 0
c?. I 7E + 00
r" .H^E + 00
-------
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
70
71
72
73
\ .HOE+oi
1.9bE+01
2.12E+01
2.3UE+01
2.50E+01
?.71E*01
?.<>5E»01
3.20E*01
3.17E+01
3.77E*01
0.09E+01
4.45E+01
a.83E»01
5.24E+01
5.69E«01
6.18E»Ol
6.71E*01
7.28E+01
7.91E+01
8.58E+01
«'.3aE»01
1. a^F +00
J^bF +00
.b9F
1 .ObF
1 .(Mt
1 .oil
1 .bOF
1 .HOt
1 .94F
<> . IMF
c-.^bF.
c-.baf.
<>. 7 IE
?.B7t
^.OdF
?. Ibt
3.a«E
.^.oot
+ 111,
+ OU
+ 00
+ OU
+ 01
+ 01
+ 0
+ 0
+ 0
+ 0
+ 0
+ 0
+ 0
+ 0
+ 0
+ 0
+ 0
+ 01
+ 01
+ 01
+ 01
11 + 0 0
hE +00
7
H
I
1
1
1
1
1
c1
e
t
c?
€>
£
2
i
.r"'t
.rtot
.0<4h
.cME
. 5Hfc
.bbE
. Mt
.«1F.
.09E
,c")E
,^lt
.bbE
.7 lit
.dSt
.4bfc
.07t
4
+
+
+
+
+
+
+
+
+
+
+
+
+
+
+
00
00
0 1
01
01
01
0 1
0 1
01
01
01
01
01
01
01
01
N)
to
-------
RHO« 1.00
INTERVAL
1
2
3
4
5
6
7
8
9
10
1 1
12
13
10
15
16
17
18
19
20
f 21
1 22
^ *3
^ 25
26
27
28
29
30
31
32
33
30
35
36
37
38
39
40
41
42
03
04
45
46
47
48
09
50
51
52
53
GM/CC
DIAMETER
2.50E-01
2.71E-01
2.95E-01
3.20E-01
3.47E-01
3.77E-01
4.U9E-01
4.45E-OI
4.B3E-OI
5.24E-01
5.69E-01
6. I8E-01
6.7 IE-01
7.28E-01
7.91E-01
8.58E-01
9.32E-01
.01E+00
,10E»UO
.19E+00
.29E+00
.01E»00
,53E»00
!ROE*OU
.95E+00
2.12E+00
2.30E+00
2.50E+00
2.71E«00
2.95E+00
3.20E+00
3.07E+00
3.77E+00
4.09E+OU
4.45E+00
4 .B3E+OU
5.20E+00
5.69E»OU
6. 18E+OU
h.7 1E+00
7 .2BE+00
7 .91E+UO
8.5flF»00
9.32E+00
.OIE+01
.10E»01
. 1 9E»0 1
.29E+0 1
.OIE+01
.53F+OI
.66E+01
.HUk »01
ASARCO AVERAGE PART ICLE Sin D 1 S T H 1 HUT I (IMS
HtCORDS EXCLUDED f-WOM MtAN
CUMULATIVE MASb cum h N m A T H>N
4
4
2
2
4
4
It
4
4
4
It
4
4
4
4
a
It
It
It
It
q
U
It
u
It
It
4
4
4
4
4
4
4
4
(I
(1
U
It
a
it
-------
5
-------
ASARCO AVERAGE PARTiCLt SI/E DISTRIBUTIONS
RHO* 1.00
INTERVAL
I
2
3
4
5
6
7
0
9
10
1 1
12
13
1 4
15
16
1 7
18
19
> 2°
1 21
M 22
u^ 23
24
25
26
27
28
29
30
31
32
33
3fl
35
36
37
36
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
GM/CC
DIAMETER
(MICRONS)
2.50E-01
2.7IE-OI
2.95E-01
3.20E-01
3.47E-01
3.77E-01
4.09E-01
4.45E-01
4.83E-01
5.24E-01
5.69E-01
6.18E-01
b.7 1E-01
7.28E-01
7.91E-01
8.5BE-01
9. J^E-01
.01E+00
. 10h + 00
. 19F. + 00
.29E+00
.41E+00
.53E+00
.66E+00
.80E+00
.95E+00
2. 12E + 00
2.30E+00
2.50E+00
2.71E+00
2.95E+00
3.20E+00
3.47E+00
3.77E+00
4.09E+00
4.45E+00
4.83E+00
5.24E+00
5.69E+00
6. 18E + 00
b.7 1E + 00
/ .2BE+00
7.91E+00
8.58E+00
9.32E+00
.01E+01
. 10E + OI
. 19E + 01
.29E+01
.41E+01
.53E+01
.6bE+01
. 8 0 E + 0 1
MEAN CUMULATIVE
MASS CONCENTHA 1 IUN
(PEPCt NT )
5.80E-U1
b.26E-0 1
6.80F -01
7.42F-01
8. 12E-01
8.92E-01
9.81E-01
.08F+00
.19E+00
.31E+00
.44E+00
.58E+00
.Iff +00
.BflF+00
.99E +00
2.0bE+00
? . \ 8E +00
2.35E+OU
2.49E +00
2.62E+00
2.73F+00
2.82E+00
f. .90E+00
2.97E+00
3.02E+00
3.07E+00
3 . 1 1 E + 0 0
3.14E+00
3. 1 7E+00
3.20E+OU
3.23E+00
3.2bE+Oo
3.29E+00
3.33E+00
3.3bE+Oo
3.40E+00
3.44E+00
3.49E+00
3.53E+00
3 . 5PE + 00
3.b3E+00
3.b8E+Ou
3.73E+00
3.79E*00
3.85E+00
3.91E+00
3. 99E+OU
4 . I 4 F + 0 U
4 . 4(?E +00
4.85E+00
5 . UOE + 00
b . 25E + 0 (J
7 . . 3SE + 00
3.40E+00
3.<*bE + 00
3.bOE+UO
3.5bE+00
bflE+00
7SE+00
3. 9 IF +00
u .bIE+00
b. 1HE + 00
b."5t +00
-------
S6
57
56
59
60
61
62
63
64
65
66
67
68
69
70
71
72
73
1 .95E + OI
d. I2E + 01
2.30F+01
2.71E*OI
3.«7E»01
3.77E»01
4.09E»01
6. I8E + 01
6.7 IE»01
7.28E*01
7.91E+01
e.aot
9. 7bt *0(1
I . MF +UI
1 .37F +n
I .7Pt+0
2.04E *0
2.1IF+OI
?.79E+0
3. 1 7E + 0
3.56E+0
3.96E+0
1 . ?«F »l)
fl.7^E+0
5.09F »0
5.77E+01
6.08E+01
6.36E+01
6.63E+01
6.87E+01
H.7Ht•
1 . 0
-------
RHQE 1.00
INTERVAL
1
2
3
a
5
6
7
0
9
10
11
12
13
14
15
16
17
10
19
> 20
1 21
NJ 22
^ 23
24
25
26
27
26
29
30
31
32
33
34
35
36
37
ASARCO AVERAGE PAHTICLE SIZE D IS 1 H 1 HIM IONS
GM/CC
OlAMEfEW
2
2
3
4
a
5
b
7
9
I
1
1
1
2
2
2
3
a
4
5
6
7
9
1
1
1
1
2
2
2
3
a
4
5
6
7
9
•
•
•
.
•
•
•
•
.
•
•
*
•
•
•
•
•
•
•
•
•
•
.
•
•
•
•
•
•
•
•
•
•
•
•
•
.
50E-01
95E-01
47E-01
09E-01
83E-01
69E-01
7 1E-OI
91E-01
32E-01
10E+00
29E+00
53E+00
80E+00
12E+00
50E»00
95E+00
47E+00
09E+00
83E+00
69E+00
71E»00
91E+00
32E+00
10E+01
29E+01
53E+01
80E+01
12E+01
50F+01
95E+01
47E»01
09E+01
83E»01
69E+01
71E+01
91E+01
32E+01
MEAN LHANbt
IN MASS CUNCFUl 4A 1 IUN
(MG/I3NM3)
b.7«E-01
7 .74E-01
1 .01E + 00
1 ,?7E + 00
1 .53E + 00
1 .79E + 00
2.04E+00
1 .OOE + 00
9.30E-01
1 .84E + 00
1 .35E+00
9.57E-01
b.blE-01
4.B1E-01
4.09E-01
4.15E-01
3.54E-01
5.2IE-01
S.b4E-01
b. 1 3E-01
b.6<»E-01
7.31E-01
8.?2E -0 1
1 . 33E + 00
4.7bE»00
8.R7E+00
1 .38E+01
1 ,9bE+01
0 ,?bF +0
0.72E+0
b.09E»0
5.2IE+0
b. 1 1E+0
4.73E+0
4.2 7E + 0
3.b4E+0
i . 0 3 E » 0
STANDAKU
UE
VI A t HI
IIPPE H
v
LUNF
I
IM i
|
( MI,/|)NM A ( Mb /UN M
U
5
7
9
. 1«F -0
. 7 1 F - 0
.4BE-0
,5e;t -0
7
1
1
1
•
•
*
.I9E+00 2.
. 4 b F t 0
.7 7E + 0
.9 7F-0
.BbF -0
J
1
1
3
1
E
.
4
4
4
+
4
^
+
4
+
4
*
.
_
.
.
.
.
.
.
.
.
.
+
.OBF+OO b.?8F+
. 7bE +01
) 1
.
.7«E +00 1 .
,7bE+00 f.
.33E+0
. 1 7E+0
.ObE+0
.99F+0
.9BE+0
.B9E+0
. 7bF +0
. a b E + 0
. 1 ? t +0
1 E + 0 1
.ObE+01
,96t+Ul
,b?t»0I
.
-------
ASARCO AVERAGE PARTICLE Sl^t I) I SlHIdul IONS
RHO« 1.00 GM/CC
INTERVAL OIAMETEW RECOHDS EXCLUDED FHOM MtAN
C H » N P, F IN MASS CONTHAMUN
I
NJ
NJ
CO
1
2
3
4
5
6
7
e
9
10
11
12
13
14
15
16
17
ie
19
20
21
22
23
a«
25
at.
27
28
29
30
31
32
33
34
35
3«
37
2.50E-01
2.95E-01
3.47E-01
0.09E-01
0.83E-01
5.69E-01
6.71E-01
7.91E-U1
9.32t-01
1 .10E»00
1 .29E+00
I.53E»OU
1 .BOE+UO
2.iaE»oo
2.50E*00
2.95E+00
3.47E+00
4.09E»00
4.83E»00
5.69E+00
6.71E+00
7.91E*00
9.32F.*00
1 ,10E»01
1.29E*01
1.53E*01
1.80E+OI
2.12E»01
2.50E»01
2.95E»01
3.07E»01
4.09E*01
4.83E»01
5.b9E*01
6.71E+01
7.91E*01
9.32E»01
4
4
a
4
4
4
4
a 4
? 9
4
4
4
4
It
4
4
^ »
4
a
4
q
4
a
4
4
0
4
4
NONE
NONE
NONt
NONE
NONE
NONE
NONF
NONE
NONE
-------
ASARCO AVERAGE P'W'ICLE Sl/E u I s I M HLI I I ims
I
NJ
NJ
RHO= 1.00
INTERVAL
1
2
3
a
5
6
i
a
9
10
n
12
13
14
15
16
1 1
16
19
20
21
22
23
24
25
26
27
26
29
30
31
32
33
34
35
36
37
bM/C I
UlAMEUK
2.50E-01
2.95E-OI
3.47E-01
4.09E-01
4.83E-01
5.69£-01
6. ME-01
7.91E-01
9.32E-01
1 .10E+00
1 .29E + 00
I .53E + 00
1 .BOE + 00
2.12E+00
2.50E+00
2.95E+00
3.07E+00
4.09E+00
4.83E+00
5.69E+00
6.71E+00
7.916+00
9.32E+00
1 .IOE + 01
1 .29E + 01
1 .53E+01
1 .80E + 01
2.12E+01
2.50E+OI
2.95E+01
3.47E+01
4.09E+OI
4.83E+01
5.69E. + 0 1
6.7 tE+01
7.91E+01
9.32E+U 1
IN
CHANGE
(NO/DNM3)
7 .02E + 10
5. ?7E + 10
0
3.52E+
2.bit*
1 ,8bt +
.19E+09
.66E+09
,19t +09
, 14E + 08
,17t+08
.64E+07
,00t+07
.09E+07
.61t+07
9.58t»0b
6.3bE+Ob
0. 19E+Ob
2.83E+Ob
1 ,9aE+06
4. 19E + Ob
4.76E+06
1 .45E»Ob
8.b9E+05
4.91E+05
1 .411 «0b
7.Ibt+UU
STANUAWIi UPHEH CONMI'FNLE
Ul ¥ 1 A 1 ION
( N U / U N M } )
b. 3bt + 1 0
a . 3uF + i o
3.41E + I u
2.bbE + 1 u
c?.0b
4.13E+'«b
5 ,bc?t »0b
9 . 09E +Ub
1 .48E +0b
1 .bbt +0b
I .bbt +0b
a . 0 'E »Ub
^ . 37E +0b
1 . 39t »db
8. 3i?t + 0b
5.0bE+Ob
3.0UF»Ub
1 . 7«F +0b
9.U9t «0«
L 1 M I 1
I ND/ONM3 )
9.57E+ 0
1 .83E+ 0
b . ^ 1 E + U
0 . ?8E+ 0
?.'5/E+ 0
c'.bet* 0
1.82E+ 0
1.03E+09
a.SOE+09
1 . /OE + 09
b.9
-------
^SARCO AVERAGE PARTICLF SIZE DISTRIBUTIONS
RHO* I.00 GM/CC
INTERVAL DIAMETER RECORDS EXCLUDED FROM MtAN
CHANGF IN NUMdEH LONL t M f< A I I UN
>
NJ
IjO
o
I
2
3
4
5
6
7
8
9
10
11
12
13
14
IS
16
17
ia
1<»
eo
ZI
22
«>3
24
25
2b
27
26
2<»
30
31
32
33
34
35
36
37
2.50E-01
^.95E-01
3.47E-01
4.01E-01
0.83E-01
S.bVE-01
6. Mt-01
7.91E-01
9.32E-01
1 ,10E*00
1 ,2SE*00
1.53E+00
l.HOE»00
2.12E+00
2.50E*00
2.95E»00
3.47E*00
(I.OVE^OO
4.83E*00
5.69E»00
b.71E*00
7.91E*00
9.32E+00
1.10E+01
1.29E*01
1.53E»01
1.60E*01
2.12E«01
2.SOE*01
2.95t*01
3.47E»01
4.09E+OI
«.6iE*01
S.t9E»01
fc.71E+01
7.91E+01
9.3«JE + 01
4
1
U
a
u
u
0
? n
f «
a
u
4
-------
I) A 1 A
PL AN t AbAkLU
SAMPLING LOCATION NO M bE 1 lliili An Y tXHAUSI
SAMPLE TYPE MtlHOO t
UPtkATOH SLHtFI-EL
AMbltNl TEMP.(OFG.F) 04.
HAH.PRtSS. ( IN. HG ) iu.^b
MEIKW LALIH. FACTuR .4tf«
WtAD » kECUHl) OAl» FVtkY b.U MINIlHb
SAMPLE CLUCK GAS MtTtk UWY GAS M£ttl<
TIMt TIMt ^tAUl'Mb TfMP
(M1N.) (aq-HH (L'U.FI.) H'tb.F)
INLfc 1
0 IbOb b3H. « 1 *
5.0 IblO b«3.000 b«.
10.0 Iblb bUH . 00(1 b7.
Ib.O IbdO bbO.bOO bii.
80.0 Ibc'b bbb.OUO be*.
?b.O Ib30 bbH.OUO bl.
^ 30.0 Ib3b bb^.HOO 70.
1 3b.O 11)38 bbl.OOl Ml.
NJ
W TOTALS 3b.O c?5.bc?3
AVERAGE b^.«
U A 1 E
kllN NIIMHtk
HkUHt LtNGIH ^ lYPt
SAMPLE HUK NUMbtk
rif 1 t H HU» MIMHt ^
PkUHF 'HE A 1 Lk bF. 1 T I NG
IMP1NGEW
IbMP
(UEG.F )
bb .
bb.
bb.
bb.
bb.
bb.
bb.
bb.
01 / 1 «/
PbOc1-!
b F 1 b
Frtb
180. bB
68. ?B
10^.71
bu.HO
bLAbS
-------
SMLFUh DIllXIDt MKl> HAlA X KhMiL 1 > IAHIILAMUN
t V A Mt I Mill) b
PLANT- NAMt AND ADDRESS 11 b I ItAM LfcAnm
ASAHCU SLHEFt-tL
TEST PSU
I
NJ
Ul
to VT
PB
LNULISH UUlTb
U I / I
TEST UAIt
TH T1ME-3IARI
TF T1ME-FIMSH
TT NET llMt OF TEST, MIN.
Y METtR CALIBRATION FACIOR
VM VOLUME UF DRY GAS SAMPLED
AT MEIER CONDI I IONS
TM AVERAGE GAS MEtEK TEMP
VMSTD VOLUME OF OUT GAS SAMPLED
AT STANDARD CONDITIONS*
BAHOMtTRIC PRESSURE
VOLUME OF BARIUM PERCHLURATE l.b ML
T1TRANT USED FOR SAMPLE
VtB VOLUME OF BARIUM PERCHLURATE .Ib ML
T1IHAM FUR THE BLANK
VSOLN TOTAL VOLUME OF SOLUTION 11)00. ML
FOR THE SULFO* DIOXIDE
VA VOLUME OF SAMPLE ALIUUUT
Tl 1KAIED
02 OXYGEN , PERCENT
OS FLOW RATE
N NORMALITY OF UARIUM
IITRANT
CU-I- T
F
SLF
IN-HG
Mt fk 1C llfil I S
U I / I 4/Br!
Ibdb
Ibitt
.?c>3 CU-M
.MU SCM
/bB.bU MM-hb
l. ML
.0 X
.0 Stf-H
.U09/ MILLEUUI VALENTij/ML
CONCENTRATION OF SULFUR DIOXIDE .1
I»RY HAS1S, STND. CONDITIONS
SU?PPM CUNCENTrtATION OF SULFUR 10.b
UlOXlUE HY
* 1U*» (-*)) LB/USCF
S08HR LBS UF SULFUR OlnxloE ,(»U(i
PtH HOUK
i> «» . S ^ 1N.HU
-------
tXAMHLt SIJLFl/K IMUXlliF (. ALC I >L A I I HI Ib Ihbl Mi.H
N(J .<4 + 460 . J
VMSTU =
U.SCF
CONCbNTKAl ION OF SU2 AT STANUARO CUNUMIUNb
CSO? = 7.U6 * lU*«(-b) • N * (VT - VlH) * VSUL<\ / VA )/VMSII)
7.Ub • 10»*(-5) «.0097 * ( |.
-------
M 11U DATA
PLAN! ASAHCU
SAMPLINl. LUCAHdN Nil LI bECUMlAtV* hXHAUbl
SAMPLE rrPE bue-
UPbWAIUH bCHtFFEL
AMBIENT Ib'MP. (IJtG.h ) 49.
HAW.PMESS. ( IN.Hl,) 50. ^h
MEIEH LALIB. FACHlK .966
WtAI) & KtCUHIJ OAlA EVEWY b.U M I Ml 1 t b
SAMPLE CLUCK 1, AS MtttK I)HY U A S Mtlbk
11Mb TIMb NtAIHUb TLMH
IMIN.) (20-HH (CU.FI.) (l)b(i.F)
iNLbl
0 16«« 5b« (101
10.0 lbb« b/^.U»»0 bb.
t!0.0 1700 b^/.^OH n"i.
e'/.O 1 7 t! 0 585. '4 3 (1 bb.
TOTALS «?7.o
UA It 01 /I «/
KUN NUMHbH HbUd-d
HWUHt LbNGIH H lYPt 5 F I b
bAMPLE HUX NUMBbK
HETEM BOX NUMHtW FB5
HWUBb 'HtAltk btlTlNb ^^O.
IMP1NGEH PtKLtNT
ItMH OF
(UEb.F ) CUNb 1 AMI
K A 1 b
59. 117.50
59. 7 1 ,UO
b9. Ill .Oc!
59.
-------
b'lLFllK U1UXME FIELD DATA «, hEbULIS lAHULAMUN
t PA ML I HUD t
PLANT- NAME AND
ASARCU
TEST pso^-e
T t S I ItAM LbAutK
b'Lhtl- H e L
NO 4 SECI'MIAHY E X H A U S I
TtS! DA1E
I
N) PB
OJ
1/1 VT
VTB
TB TIME-START
TF 1 IMfh INISH
T T Nt T I I ME OF TEST, MIN.
Y METER CALIBRATION FACTOR
VM VOLUME OF DRY GAS SAMPLED
AT ME TER CONDI 1 IONS
TM AVERAGE GAS METER TEMP
VM3TD VULOME OF DRY GAS SAMPLED
AT STANDARD CONDITIONS*
HAROMETRIC PRESSURE
VOLUME OF BARIUM PE»CHLORA1E
TlIRANI USED FOR SAMPLE
VOLOME OF BARIUM PERCHLORATE
TI IRAN I F OR THE BLANK
VSOLN TOTAL VOLUME OF SOLUTION
FOR THE SOLFUR DIOXIDE
VA VOLUME OF SAMPLE ALIOOUT
TITRAIED
02 UXYG.EI* > PERCENT
Q3 FLOW KA IE
N NORMAL I T Y OF HARIUM
PERCHLUKATE TITRANT
CONCENTRATION OF SULFUR UlUXlUE
PRY HAS1S, SINO. CONDITlO^b
90
-------
SULFUIV IHiMIDF. C A L U HL A I I (jij Ji I t i> I I Mi . t' SU«?-tf
4 SetONOAKY EXHAUSI
VULUMt OF UHY (,Ab SAMfLtD A? SlAlvUAKU 1. UNI; I I 1 ON ',
VMSTU = 17.647 • VM • V * (PH ) / (TM •» U(.u.)
17
VMbfl) =
CONCtNlRAl ION OF S02 AT STANDARD CONOIIlUNS
CSU2 = ?.0b * !U«*(-5) * N * (VT - VlH) •
7.06 • 10«*(-5T
CSU2 =
)/VMSK)
LB/UStF
CONCENTRATION UK 302 BY VOLUME
=
-------
M t LL> 0 A I A
PLAMl Ab/\HUl
SAMPLING LUCATIUN MUM bt LU'JUANT fcxnniibT
b A K, P L E T T P E b U «?
1 ) P E n A T U W bLHtt-t-tL/AHltShtKGtk
AMH1ENI ItHP. (l)tb.F) bU.
bAk. PRESS. ( IN. Hi, ) 3U.^b
UtTEH CAL1B. f-AtlDH ,9b«
NtAO X KECUKU HAtA EVEHT b.U M1NUUS
SAMPLE CLUCK GAb METEk IJHY GAS MEtbw
! IME T 1ME Kt All 1 iJI, ft MP
(M1N.) (2P-HH (CU.hT.) llltG.F)
INLK 1
0 IBUO bHb.bd?
b.U 18Ub bn4.r>H3 ba.
1 U.U 1 8 1 U b43 . 1) 31? bH .
Ib.U 181 b b4b. 74b Ml.
^0.0 lH«iU bU(l.bbl) IS.
£b.O 18^5 bo7.H17 ?b.
^ 30.0 1839 blb.UBb 7n.
M
UlTOlALS 30. 0 a
-------
UIOX1MK F [ELM DAIA K, KFSULIH lADULAIlUU
tPA MtlHllU t
PLANT- NAMt AND ADDRESS
ASAKCU
TE3T PSOc>-3
NU« SECONDARY LXHAUbT
FfcSI HAM |_k Ai.lt K
SLHtFK-L/ANII-.SllhHbLK
TEST DATE
ENGLISH UNITS
0 I /!«/«<;
TB
TF
TT
Y
VM
TM
VMS TD
TIME-SIAHT
T1ME-F 1N1SH
NE 1 UMt OF TtST,
"E1EK CALIBRATION
1BOU
M1N. 30.U
FACTOR .VB8
VOLUME OF DRY GAS SAMPLED dl.S'il CU-FT
AT METEK CONDITIONS
AVERAGE GAS METtR
VOLUME OF DRY GAS
TEMP n.e F
SAMPLED d9.360 SLF
to PB
U)
00 VT
VTB
VSOLN
VA
oa
OS
N
CS02
SOZHR
Al STANDARD CONUITIONS*
BAROMETRIC PRESSURE
VOLUME OF BARIUM PERCHLURATE
TITRANT USED FOR SAMPLE
VOLUME OF BARIUM PEBCHLURATE
THHAM FOR THE HLANK
TOTAL VOLUME OF SOLUTION
FOR THE SULFUR DIOXIDE
VULUME OF SAMPLE ALIOUOt
T I THA ItU
OXYGEN , PERCENT
FLOW HATE
NORMAL1IY OF BARIUM
PEHCHLORATE TITRANT
CONCENTRATION OF SULFUR UIDXIOE
DRY BASIS, STNO. CONDlTlONb
CONCENTRATION OF SULFOR
DIOXIDE HY VOLUMfc
LHS OF SULFUR nillXlDE
PtK HOOK
METK[L UNI I b
U 1 / I 4/«r)
1800
I31*
i(J .U
CU-M
?\ .
.B31 bCM
MM-Hb
b.B ML
,lb ML
luoo. ML
-------
bULFuk U 111 XI Ob CALUILAllUNs
tXHAUbT
VULUMt uF UWT I,AS SAMHLID AT i, I .1 Nil A klj (_ L)N|> I I I dnh
VM5TU = 17.6U7 • VM * Y « (PH
|7.f)«7 • a9.b^9 •
VKSfU =
( 71.,? + UhO. )
USLb
CONCtN I hA t ION UF SU^ »T STANDARD CUNUHlUNb
= /.Oh • lU*M-5) • N * (VT - VTbJ « VbULlv / VA )/VMSIh
7.Ut> * 10«*(-5) *.OU97 « ( b.HO - ,lb) «10UO.O /
,b5V • 10**(-b) LH/USCF
NJ
UJ
CONCtNTHA f 1UN UF 3U^ BY VOLUME
30JPPM r a30.0 • (VT - VJB) • N « VSULN
---------------------------------
VMSTI) * VA
130.0 • ( 5.8 - .15 ) * .0097 *1UOU.U
SU2PPM r
CONCENTkArjON OF 30? IM LBS/HtV
30
-------
r
ItUJ DA I A
PI. AN I
SAr.PL IMi LUC* t ION
SAMHLt ITPt
UPbHA fUK
AMHltNl IEMP. (Ot'b.F )
Sb. ( IN.Hi; )
MEItW LALIH. FACl
ASAKCU
"n't sLr
.Slid
SLM
So.
I-XHAUM
TOTALS
AVERAliE
lfl.^03
HA It
01 /Id/He;
NIJMHtk
HWUHt LtNUIH *, TYPE
f- I GLASS
SAMPLt BOX
Me I EK BUX
PklJHt 'HEA1 tK bE I T ING
HtAU * HtLUWU DAIA
SAMPLE
1 1Mb
(MN. )
0
b.O
10.0
lb.0
do.o
db.O
EVEWY b.O MUJimb
CLOCK GAS ME TEW
T 1ME Wb AO 1 Nd
(2a-HH (CU.F 1 . )
r i 1 1 r K i
\s l_ UL T\ t
leab bib 190
l«bO bl H . ?9b
Iflbb bdd.<40(l
>90(l bdb.OOO
1900 bd9./U(l
191U bll.5V5
UK Y GAS -It Ft H
It'-IH
IDtG.F J
INLK !
1 1 .
/ 3.
7b.
/'.
'B.
IMP1NGEK PEHCENI
TEMP UF
(DEb^ ) CONblANI
Iv A 1 t
ft W 1 C
b«. 99. 0«?
b«. 99. Od
b«. 98. «»
b«. 101.63
b«. 1 01 .««
-------
bULFUR DIOXJOK MELD I) A I A n KhbliLlS I Ab liL A I I UN
t V A M t I M I J U fc
PLANT- NAME AND AUDREbS
A S A R C 0
TEST Psu£-« Nua SECONDARY
TEST H.AM LEAUtH
."iLHtFhtL/ANIEbHERbEh
TEST DATE
TB TIME-START
TF IIMt-F1N1SH
TT Nt! I1ME OF TESr, MIN.
Y METtR CALIBRATION FACTOR
VM VOLUME UF DHY GAS SAMPLED
AT ME IE* CONDITIONS
TM AVERAGE bAS METER TEMP
VMSTO VOLUME OF DRY GAS SAMPLED
AT STANDARU CONDITIONS*
PB BAROMETRIC PRESSURE
VT VOLUME OF BARIUM PERCHLORATE
T1IRANT USED FUR SAMPLE
VfB VULUME OF BARIUM PERCHLURATE
TI(RANT FUR THE HLANK
V30LN TUTAL VOLUME UF SOLUTION
FOR THE SULFUR DIOXIDE
VA VOLUME OF SAMPLE ALllJUOT
11IHA I ED
02 (IXYGEN , PERCENT
Q3 FLOW RAIE
N NORMAL 1 I Y OF HARIUM
E TITRANT
fc Nbl 1 SH UNI 1 b
0 1 / It/He!
UNlTb
SOPHPM
S08HR
* 1 0
cb.U
CU-h T
1410
CDNCENrkAT 1UN OF SULFUR U10XIUE
DHY HASIS, STNO. CONDITIONS
CONCENIKA f ION OF SULFUR
I) iOX I Ilk. HY VOLMMt
LHS UF bULFIJW DlllXIOF
PER HUUR
IP.
7
-------
bULFUH Ml)»ll)t L' ALL IIL A I 1 UNS I t S 1
AKY EXMAUbl
VOLUMt HI" UtVY l-AS Sft'iPLtL) »T SlANUAkn C Uul) 1 1 I (i
VMSTU = I?. 6«7 • VM * V * (PB J / (1M + UhO.)
17.b<4/ * IH.0*M-5) * N • (VT - VIH) • VSULIx
7. Ob • 10»*(-5) «.0097 * ( I. S3 -
--- -
I 7 .Vb
v« )/VMStn
lb) *1000.0 / c'O.U )
LH/USLf
CONCENTRATION C^ SO? BY VOLUME
S05PPM = «30.0 « (Vf - VT8) * N « VSOLN
VMS1D • VA
«30.0 * ( 1.5 - .15 ) * .0097 MOOO.O
I7.*»b • ^0.0
S02PPM =
lb.03
CONCENIMAT1UN UF 502 IN LBS/HH
30SHK = CSU£ * 10«*(-l>) * US
^b * IO**(-5) *
.0
.tMIO L8S/HR
-------
K L 11 I) A I A
PL AM
b A M P L 1 N b LUCATIUN
bAHHLE 1TPE
UPEkA I UK
AMblEM 1EMH.(UEG.F)
HAk .PkESb.(IN.Hb)
METEK LALIB. FACIDH
k E AII II k EIU k U I > A I A E V E k Y
A b A k I U
NU" bECUMUAKY EXHAIibl
SOc1
Au (ESHt ki,E k
SU.
.4Bfi
M]NUlt&
UA IE
kliN NUMHEk
HkUBE LEN(,1H ^ TYPE
ul /l<4/8c?
F T bLASS
bAMPLE BUI
Mf- IEk BOX NUMflEk
HHUHE 'HtAIEk bETTlNb
c'iU.
TOTALS
AVERAGE
SAMPLE
1 1ME
(MIN. )
0
10.0
6 M 1 . 0 f 0
ban. / is
IS.^B'3
DkY GAS ^E'EH
IEMH
(l)Eb.F)
INLE T
'«.
BO.
77.0
IMPIN6EH
TEMP
(OFG.F )
60.
60.
60.
PERCENT
(Jf
CONSTANT
U A 1 t
n B 1 C
99.95
100. Ob
-------
ShLFUw nillXlUt MtLU IIATA * NlSULTS IABMLAIIUU
t PA Mt T MUD f-
PLANf- NAME AND ADDRESS T t S I ItAM LtAUtK
ASARCU A^lESbtRkLR
TtST HSUc!-5> UU4 SECONDARY EXHAUST
t'MbLlSM UNITS
ItST DAIE
f'tTHR U'JlIb
01 /
TB
TF
TT
Y
VM
TM
VHSTD
T IME-STARl
T1ME-F [NISH
NET IlMt OF 1F.ST
13" !2"
fMIN. dO.U ^U.O
MtTEK CALIBRATION FACTOR .9«H ,VH«
VOLUME UF DRY GAS SAMPLED lb.283 CU-FT .U33 LU-M
Al MEItR CONDITIONS
AVERAGE GAS METfR TEMP 7/.0 F ^b.O t
VOLUME OF DRY GAS SAMPLED lb.015 SCF .«3b SCM
At STANDARD CONDITIONS*
P8 BAHOMtTRIC PRESSURE 30. 2b IN-HG fbrt.bU MM-Hb
VT
VTB
VSOLN
VA
02
US
N
VULUMt OF BARIUM
T1TRANT USED FOR
VULUME OF BARIUM
flfRAUT FUR THE
TUTAL VULUME OF
FOR THE SULFUR 0
VULUME UF SAMPLE
T 1 IKA TED
OXYbEN , PERCENT
FLOW RATE
NORMALITY OF BAR
PERCHLORAlE b.O ML
SAMPLE
PERCHLORATE .15 ML
BLANK
SOLUTION 10UO. ML
IOXIDE
ALIQUUI 20. ML
.0 X
.0 SLFH
IUM ,004/ MILLtOUl VftLtNTS/ML
C302
HfcWCHLURATE TITRANT
CONttNTRATION UF SULFUR OIOXlOE
DRY HASISr STNO. CONDITIONS
LUNLENTRATIUN OF SULFUH
Jt HY
302HR
LBS OF SULFUR OlUXlOt
MHUK
1.11 » 10*»(-5) LH/USUF
b7 .36
.000 LMS/HH
-------
bULt-Uk HIHKlUt I, ALLI'L A I I (lUb lhi>l Nti.KSIic'-b
N(J« StLUNDAkY tXHAUb'T
VOLUKt Hf UH1 bAb SAMpLhU AT SlANUAHU L I'NM I I KINS
VMSTU = 17.607 * VM « V * (HB J / (IM » thU.J
I7.6U7 « t'j.?8J * .9BH * iU.t-b
VMSTU = -------------------------------------- = Ib.Olb
( 7 / .u * y^y . )
CUNCtNIWAT lUn li F SUS AT 3T»NOAHO
= ?.0b • ItMM-S) • N • (VT - V7b) • VSULI< / VA ) / V H S I I)
7.Ub • 10«*{-S) «.00<»7 • ( 5.UO - .15) MUUO.U / «J U . 0 )
l.lUb • 10*«(-b) LH/USCF
CONCENTHA T 1UN UF 308 HY VOLUMt
«3U.U * (VI - VT8) • N • VSOLN
NJ
^ VMSTD • VA
• ( S.O - .IS ) « ,UU9f *1UOO.U
= b7..Jb HPM
CUNCtK IKAT ION OF 502 IN LBS/HB
30i?HK = CSV* • 10**(-5) « US
= 1.11 * 10**(-5) * .0 = .IIUU LHb/HK
-------
f
^ i tL\)
r A
PLANI
SAMPLING LUCATION
SAMPLE TYPE
UPEWAI OH
AMBItNT lEMP.(OFG.F)
HAK.PHtSS. ( IN.HC-)
ME ItH CAL IB. F AL TllH
HtAII K HECUHU HAlA EVEHY
ASArtLU INC
tlU u t XMAUJ- t
DA It
NUN NIIMBtK
PHUHt LtfNGlH *. TTPt
01/1
f I GLASS
ANftSbEKGtk
•DO.
30.^6
5AMPLt 8UX
Mt 1 1 H Bt)»
'HtAltW bfclTINt
. U MINUH.S
TOTALS
AVEHAGfc
SAMPLE
TIME
1 W 1 N . )
0
5.0
10.0
15.0
20.0
23.5
CLOCK
TIME
(2«-HH
r I f ir K )
\, l_ V\~ " /
202b
2031
203f>
?00 I
200b
2050
GAS ME1EH
KE AO INI,
(CU.K 1 . )
618. H15
652. bOO
b 5 b . c" 0 0
b59.9l 0
bbj.620
6b7 . J27
OH Y GAS Mt I EH
TEMP
lOtlj.F )
INLE I
6H.
bH.
t>1 .
bM .
bH.
IMPINtEH
TEMP
(OLG.F )
5«.
50.
50.
51.
50.
PEHCENT
OF
CONSTANT
Lf A 1 t
n w I t
102.23
97.23
1U0.21
100 .20
100.12
b« .0
50.
-------
UlUXint IJLLII UAIA n Rt.bULlj I A tiliL A I I UN
t H A "it I Mill/ b
PLANT- NAME AMJ ADDRESS
A3AHCU Hit
TEST P S U r? - b NU a EXHAUST
ItSI I E A M
AN I (• bHERI.b
TEST UAIE
ENGL 1 Sil UN II5
U I /!'»/•!c-
TB I1ME
TF T JME-F IN ISM
TT HiT 1 1ME OF TEST , MIN.
Y METER CALIBRATION FACTOR
VH VOLUME OF DRY GAS SAMPLED
Al MEIER CONDITIONS
TM AVERAGE GAS METtR TEMP
VMSTO VOLUME OF DRY GAS SAMPLED
AT STANDARD CONDITIONS*
PB BAROMETRIC PRESSURE
VT VOLUME OF BARIUM PEHCHLURATE
TITRANT USED FOR SAMPLE
VTB VOLOME OF BARIUM PESCHLURATE
TITRANT FOR T HE BLANK
VSOLN TOTAL VOLUME OF SOLUTION
FOR THE SULFUR DIOXIDE
VA VOLUME OF SAMPLE ALIOOOT
I I 1 R A I E U
08 OXYGEN , PERCENT
03 FLOW RATE
N NORMAL 1 IY OF HAHIUM
KtKCHLURATE TITRANT
C30«? CONCENTRATION OF SULFUR DIOXIDE
ORY BASIS, STND. CONDITIONS
S02PPM CONCEMRATION OF SULFUR
UlUXlUt HY VOLUME
302HR LBS OF SULFUR DIOXIDE
HOLIH
Id.
be.o
Me TKic UNi ri>
u l /1 y/tfr1
. •>
CU-F T
F
SCF
30.^b IN-Hl,
b.3 ML
I. Ib ML
1000. ML
c?o. ML
.U X
.0 SCFH
.U09/ MILLEIJUI VALENTS/ML
.// * 10*«(-b) LH/USCF
Mb.1^ PPM
.000 LbS/HR
.b
-------
P IdllXIOt LALUJLA I 1 UN5
U <4 t X H A I / S T
NU.P.SIlr'-b
VOLUME UH U»
-------
(tLJ
PL*'-!
SAMPL 1 NG LUCA I I (IN
SAMPLE I TPt
UPEPA TDK
AMb IENI IEMP. (DEK.F )
BAN.PWESS. ( IN.Mi;)
t XMAUb 1
10 .00
1)4 1 E
WUIv NUMHEW
PWUHE LtNC-IH K TYPE
Pbl V-7
"z F 1 OLASS
SAMPLE BUX
MEIH H BU« NIJMHEH Fob
P'Vlj'tt 'HhAtFk S E I T 1 NO c'bd.
METEH CALIO. FAI.
KEAU * WtCUP-U DA
SAMPLE
1 1ME
( M 1 N . )
1
0
5.u
10.0
Ib.O
c?0.0
S> TOTALS ?o.o
' AVEHAGE
ho
KJW .4hd
1A EVEwr b. 0 MINUItS
CLUCK bASMETEK DHYliAS^tlEK
TIME KEAiMUb TE'IP
(21-HK ICU.F I . ) (UtU.F )
ISU6 8,20.140
Ibl 1 Ht'O . 15d brf.
1 51 h 8c;n. i bd bt? .
1 5d 1 H3C1 . 1 bo b'J .
1^6 H3h.lbO -,C.
15.470
bl .0
IMPlNthH PERCENT
TEMP UF"
(Utb.F ) CUNbTAN 1
k A 1 E
bO. 99.19
bO. 1 UO. 1 4
bl . 100.19
bJ. 1 UO.fll
J 1 •
-------
SULFUK DIOXIDE F1KLD UAlA A WtSOLIS lAHIILAIlUN
Mh ! HIM) fc
PLANT- NAME AND ADDRESS
A3ARCO/-TACOMA, WASH
TEST PS02-7 NO «• EXHAUST
Itbl It AM LtAUtl<
ANltSht
TEST UATE
tfc TIME-START
TF llMt-F1NISH
TT NET TIME OF TEST. MIN.
Y METER CALIBRATION FACTOR
VM VOLUME OF DRY GAS SAMPLED
A1 METER CONDITIONS
TM AVERAGE GAS METER TEMP
"VMSTD VOLUME OF DRY GAS SAMPLEf)
Al S1ANDARD CONDITIONS*
PB BAROMETRIC PRESSURE
VT VOLUME OF BARIUM PERCHLORATE
TITRANT USED FOR SAMPLE
VTB VOLUME OF BARIUM PERCHLORATE
I1THANT FOR THE BLANK
VSOLN TOTAL VOLUME OF SOLUTION
FOR THE SULFUR DIOXIDE
VA VOLUME. OF SAMPLE ALIOUOT
I 1 (HATED
Oi OXYGEN , PERCENT
09 FLO* RATE
N NORMALITY OF BARIUM
PERCHLORATE TITRANT
CTD2 CONCENTRATION OF SULFUR DIOXIDE
DRY BASIS, STNO. CONDITIONS
S02PPM CONCENTRATION OF SULFUK
UIOX1UE HY VOLUMK
802HR LB3 OF SULFUR DIOXIDE
HUUW
ENGLISH UNITS
01
15Ub
ME Ik 1C UNlTb
U I
IbOb
15.970 CU-h T
bfl.O F
15.791 StF
30.00 IN-Hb
.3 ML
.20 ML
1000. ML
20. ML
.0 X
.0 SCFH
.0097 MRLEUUIVALENTb/ML
.03 * 10*«(-5) Lb/UStF
1.50 PPM
.000 LbS/HK
CU-M
t
bCM
MM-Hl,
IM.HIi. .UHT BASIS
-------
tKAMHLt SULt-UW IMOXlOt L*LCUL*IIUN5 ItbT (III . \ SUc1 - I
NO » tXHAUST
VOLUME IIH OKY GAS SAMPLED AT SIANUAhU L UNO 1 I I UNH
VMSIO r 17.647 • VM * r • (PH ) / (1M * <4fcU.J
17.647 » IS. 970 * .960 • 30.00
VM3TU =
U5LF
CONCtNlH* I ION OF
CS02 = 7.06 *
7.C'b
»! STUNOAHO CUNOJlIUNS
) • N * (VT - VIHJ * VSULN / VA )/vMSIO
(-5) *.0097 • ( ,3«? - .i^U) »IOOO.O
lb.79
* 10*«(-5) LB/03CF
CONCENTKATION OF 30? HT VOLUME
802PPM « 430.0 * (VI - VTB) • N * VSOLN
----------------------------- - ---
VM3»D * V»
130.0 • ( .3 - .20 ) • .009/ *100U.O
.....
15.79 • 20.0
302PPM
CONCtNTKATlON OF 502 IN L83/HH
302HH = C302 • IO**(-5) • OS
SOdHH = .03 * IO**(-S) •
.0
LHS/HR
-------
ENO OF PHObHAM
iCOJ
CPU SEC. = U. LLAPStU MIN. = |. FHl, ^EB ,,,
HM
U1
NJ
-------
-------
TRAVERSE POINT LOCATION FOR CIRCULARJWCTS
Plant
Date
Sampling location
Inside of far wall /to outside
of nipple r/-/X
Inside of near wall to outsijd
nipple (nipple length)
Stack I.D.
of
Nearest upstream disturbance
Nearest downstream disturbance
Calculated by
dd
dd
Ffcu
I
0- -jj
• • — .
/
_ ^ — —
p/t<^
-------
CAS VELOCITY AND VOLUME DATA
SAMPLING LOCATION
STACK INSIDE DIMENSION (in.)
B-3
-------
CAS VELOCITY AND VOLUME DATA
1.
2.
PLANT AND CITY
A
<4^0
\
SAMPLING LOCATION
X/f V fe^r//)«v £"x/C^*r
CLOCK
TIME
75*77
i5 7 •« •»
RUN
NUMBER
f- 7
OPERATOR
5cXfc-7<^/
AMB. TEMP.
CF)
i «^ i-'
RUN DATE
,/
J'lll/ftf
14 17 40
BAR. PRESS
(in. Hg)
^1^*3
17 Jl 31
STATIC PRESS
(in. H-O)
-3*. ^>
SIDE 2
• . • * i
PITOT
TUBE Cp
.^y
MOISTURE
%
./.K
it
73
76
FIELD DATA
TRAVERSE
POINT
NUMBER
7 . i 9 .10
$ !
k
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-------
£
6AS VELOCITY AND VOLUME DATA
PLANT AND CITY
A***«o
RUN
_t/^Zj
DATE
*• /e\*
14
SAMPLING LOCATION
S/0 4 Z^ortjA^ e?*/*^'
CLOCK
TIME
/£U
43 / *6 *9
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NUMBER
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$Jie£ft1
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(in. Hg)
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WT.
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STACK INSIDE DIMENSION (in.)
DIAM OH SIDE 1
. ^ 6.tf . .
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W
MOISTURE
\
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73 76
FIELD DATA
TRAVERSE
POINT
NUMBER
7.1.9 ,10
(^ /
-2
.1
v
j»
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3
5
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S
1
POSITION
(in. )
n ,17 ,1 : t '<
VELOCITY
HEAD
(ip ) , in.HjO
?5.26«J71?8 ,J»
/ /
x 7
if- 1
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/;*{-
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STACK
TEMP. *F
38,59 ,40 .41
r?
•T7
-------
CAS VELOCITY AND VOLUME DATA
PLANT AND CITY
Xfw/?^
RUN DATE
.'
l./l/ r- 1 fr. luJ
SAMPLING LOCATION
rf/6 / JJV^W*^/ ttit*^
CLOCK
TIME
J^^\
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NUMBER
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OPERATOR
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AMB. TEMP.
CF)
.
-------
CAS VELOCITY AND VOLUME DATA
1.
2.
PLANT AND CITY
M-sfl^^>
\
SAMPLING LOCATION
fjo . if 5'e<^~'*
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(in.)
11 ,12 ,1 3 • 14
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(Ap ) , in.HjO
7 5,76 . J7 , ?« , 2»
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!'£
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GAS VELOCITY AND VOLUME DATA
1.
2.
PLANT AND CITY
A^lfic*
\ 1
CLOCK
SAMPLING LOCATION TIME
/(/*'
FIELD DATA
TRAVERSE
POINT
NUMBER
7.8,9 ,10
jP 7
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.9
V
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4
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4
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(in.)
i .1 1 ,1 :>•'<
VELOCITY
HEAD
(Ap ) , in.H,0
75, 26 .37, 28 ,29
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31 .39 .40 .41
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4o
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^71
^L
£r
-
ft -
B-8
-------
CAS VZLOCITY AND VOLUME DATA
PLANT AND CITY
RUN DATE
1.
14 17 40
SAMPLING LOCATION
CLOCK
TIME
44
RON
NUMBER
OPEJJAIOR
AMB. TEMP.
CF)
BAR. PRESS
(in. Hg)
STATIC PRESS
(in. H,0)
2.
7 T
II
31
13
II
MOLECULAR
WT.
stt&.
STACK INSIDE DIMENSION (in.)
HAM OH SIDE 1
/ ,— ,
. ev.c-', . ,
SIDE 2
— ^
, , • . .^
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TUBE Cp
•
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%
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70
73
FIELD DATA
TRAVERSE
POINT
NUMBER
7 . 1 . 9 .10
/!-/
z
*>
4-
6
(a
t>- i
7_
1
i
4
^
POSITION
(in.)
11 .17 ,13*14
VELOCITY
HEAD
(Ap ) , in.H20
;5,26*?7,71 ,?»
/,2°
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/x -V7
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£~e.
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<$4,
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-
f
B-9
-------
CAS VELOCITY AND VOLUME DATA
1.
PLANT AND CITY
;$^4/£.e^>-:~~"^
-S
OPERATOR
<^'/
7 '
MOLECULAR
WT.
."&*&
40 •>£ -,3 ««
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CLOCK
TIME
//^
46
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AMB. TEMP.
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21
STACK INSIDE DIMENSION
3IAM OR SIDE 1
. /£>. ^ . .
31 «!
RUN DATE
ijUii*l>&£»
14 17 •«
BAR. PRESS STATIC PRESS
(in. Hg) (in. H.,0)
i
5.0.V-3* ' a^e?
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(in.)
SIDE 2
,
«4
t
• , ^— •
*7
PITOT
TUBE Cp
70
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MOISTURE
%
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73 76
FIELD DATA
TRAVERSE
POINT
NUMBER
7.1.9 .10
£>-/
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3
4
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2
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(in.)
11 ,12 ,13 «H
1
VELOCITY
HEAD
(Apg) , in.HjO
2 1.26 «J7 . JS .79
/>^o>
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TEMP, «F
3I.J9.40 ,41
^
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^i
•5?
-
B-10
-------
CAS VELOCITY AND VOLUME DATA
PLANT AND CITY
RUN DATE
1.
, CU/te rt' A/^-r
17 40
SAMPLING LOCATION
4J
CLOCK
TIME
46
«9
RON
NUMBER
AMB. TEMP.
CF)
BAR. PRESS
(in. Hg)
STATIC PRESS
(in. HO)
2.
MOLECULAR
WT.
.a^r^
STACK INSIDE DIMENSION (in.)
3IAM OR SIDE 1
/^ ^> i — >
, c^; *-• <-< -: —
SIDE 2
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TUBE Cp
•
MOISTURE
«
JS.
70
73
FIELD DATA
TRAVERSE
POINT
NUMBER
7,1.9 .10
/L-l
•?
5
4
<
(s
^ - 1
7
^
*
^
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POSITION
(in.)
M .12 ,]3»H
-
-
VELOCITY
HEAD
(Aps) , in.H20
25.26.27, 26 ,2»
/t2&
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31,39.40.41
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£^~
•^4=
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•^ i.
^
B-ll
-------
CAS VELOCITY AND VOLUME DATA
PLANT AND CITY
RUN DATE
1.
45
SAMPLING LOCATION
;5
CLOCK
TIME
RUN
NUMBER
OPERAIOR
AKB. TEMP.
(•F)
BAR. PRESS
(in. Hg)
STATIC PRESS
(in. H20)
2.
It
11
15
MOLECULAR
WT.
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3IAM OR SIDE 1
£&m _
SIDE 2
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STACK
TEMP. »F
36.39.40.41
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S'y
5^
-
B-12
-------
CAS VELOCITY AND VOLUME DATA
RUN
NUMBER
AHB. TEKP .
CF)
BAR. PRESS
(an. Hg)
STATIC PRESS
(in. H20)
31
1«
MOLECULAR
WT.
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STACK INSIDE DIMENSION (in.)
3IAM OH SIDE 1
/ /~) r~)
i //V t ^^ • ^-^< ,
SIDE 2
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PITOT
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•
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t
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73
FIELD DATA
TRAVERSE
POIN'T
NUMBER
T . 1 . 9 ,10
/>-/
7
?
t
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r>- /
2
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V
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//
POSITION
(in. )
' i ,i: ,13 1 1*
VELOCITY
HEAP
(.1? ) , in.HjO
J 5i 7« • ? 7 , 78 ,29
// 2-o
//^O
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/, -s-o
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STACK
TEMP , *F
31,39,^0,41
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^^
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-
B-13
-------
CAS VELOCITY AND VOLUME »ATA
1.
2.
PLANT AND CITY
rr^AXcv
t
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LOCATION
/fa- V ^ct-s^Ajt* &dAu*r
jir tr-r-vstr-y ^
RUN
NUMBER
\f~9*
i
OPERATOR
&/cJ&f
7
MOLECULAR
WT.
.M.r*
40
44
CLOCK
TIME
xr^r
»4 4
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.¥,9
at
STACK INSIDE DIMENSION
51 AM OH SIDE 1
.£*.*. -
it »i
iV
RUN DATE
,/u,
&.;.$&
14 17 4B
BAR. VRESS STJ
(in. Hg) (
3W.L
31 JJ
(in.)
SIDE 2
64
• . i
*7
PITOT
TUBE Cp
.tf
70
MOISTURJ
%
,/J,
73
KTIC PRESS
in. HjO)
•^.<7
}«
E
76
FIELD DATA
TRAVERSE
POINT
NUMBER
7 . 1 . V ,10
-& /
4
?
-------
CAS VELOCITY AND VOLUME DATA
PLANT AND CITY
/^5.4/e^xf
»
SAMPLING LOCATION
A/°- ? Jecusdfi/** tf^C^arT"
CLOCK
TIME
RUN DATE
,/U/tf.
lJ »7
f/p
40
*9
RUN
NUMBER
OPERATOR
AMB. TEMP.
CF)
BAR. PRESS
(in. Hg)
STATIC PRESS
(in. HO)
2.
31
li
MOLECULAR
HT.
.^v.1?
STACK INSIDE DIMENSION (in.)
)IAM OK SIDE 1
. &o. D. .
SIDE 2
. • . i
PITOT
TUBE Cp
.fi/
MOISTURE
%
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70
73
76
FIELD DATA
TRAVERSE
POINT
NUMBER
7 . « . 9 .10
/
2.
J
V.
4
I,
/
J,
^
<+
4
L,
POSITION
(in.)
11 ,17 ,)3|U
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HEAD
(Ap ) , in.HjO
? J.J6.37, JB .Z»
tf.?
/. L
i 3
7; 3
/, ¥
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/,/
/..'J
/-.•f
A V
''V
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STACK
TEMP, *F
36 ,1 V .40 ,41
-------
CAS VELOCITY AND VOLUME DATA
PLANT AND CITY
RUN DATE
1.
>4 17
SAMPLING LOCATION
/t^ 4 ;
CLOCK
TIME
RUN
NUMBER
OPERATOR
AMB. TEMP.
CF)
BAR. PRESS
(in. Hg)
STATIC PRESS
(in. H20)
tt
ji
15
It
MOLECULAR
WT.
. *«.7$
STACK INSIDE DIMENSION (in.)
51 AM OR SIDE 1
.£.*>.*>.
SIDE 2
• . * i i
PITOT
TUBE Cp
.90
MOISTURE
%
./J).
70
73
76
FIELD DATA
TRAVERSE
POINT
NUMBER
7.1.9 .10
POSITION
(in.)
M
VELOCITY
HEAD
(Ap ) , in.HjO
7 i,26 «3 7 , 7B ,79
STACK
TEMP. »F
3« .} 9 .40 .41
B-16
-------
GAS VELOCITY AND VOLUME DATA
*9
RUN
NUMBER
OPERATOR
AMB. TEMP.
CF)
BAR. PRESS
(in. Hg)
STATIC PRESS
(in. H20)
2.
II
31
13
It
MOLECULAR
*rr.
. ^^c-7
STACK INSIDE DIMENSION (in.)
3IAM OR SIDE 1
. £.0. -r-r"
SIDE 2
1 . • , ./^
PITOT
TUBE Cp
• .
MOISTURE
t
/&
, f » i
40
31
*4 *7
70
73
76
FIELD DATA
TRAVERSE
POINT
NUMBER
7.1.9 .10
^ /
?
J
y-
?
is
h-r^
7^
^
4-
^
^
POSITION
(in.)
11,17, 3 «14
VELOCITY
HEAD
(Ap ) , in.HjO
? i.26 «J7y 78 ,2»
•2*10
y ,00
:?. TTc?
*.< , fao
1., ?0
i <7*>
4,+f
3. -*°
4,00
5, <^C?
STACK
TEMP. »F
3B .3 9 .40 .41
^/
<£?>
^"•^
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•55^
5i
^^
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^•V-
f^
-5^
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-,
B-17
-------
GAS VELOCITY AMD VOLUME DATA
2.
RUN
NUMBER
/-/3
OPERATOR
C^x/
1 7
MOLECULAR
WT.
.? 3.
t
f
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POSITION
(in.)
M .17 ,13.14
VELOCITY
HEAD
(Ap ) , in.HjO
? 5, 26 • 77 , J8 ,29
•3.1^>
^.'T'O
r"' ^r^^
4/x'SO
4'
-------
CAS VELOCITY AND VOLUME DATA
HUN
NUMBER
OPEJ»A
TOR
AMB. TEMP.
CF)
BAR. PRESS
(in. Hg)
STATIC PRESS
(in. H20)
2.
31
IS
MOLECULAR
WT.
.?$.*
STACK INSIDE DIMENSION (in.)
31 AM OR SIDE 1
/ _
^^
SIDE 2
>«-
. . . . ^
PITOT
TUBE Cp
•
MOISTURE
%
A?
. /• i
40
*7 70
73
76
FIELD DATA
TRAVERSE
POINT
NUMBER
7.1.9 .10
/!-'
7
•?
^
^
"^
h-l
i
^
+
4
tr
POSITION
(in.)
n .17 ,i3«u
VELOCITY
HEAD
(Ap ) , in.HjO
7 5, 26.77 , 2« . 7»
5/fo
f,f>/C>
Zs'Z'O
*>,£&
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•^xO-0
=?xtfo
4' "2-
STACK
TEMP, «F
3B .39.40 .41
•st-
^^
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<&£
-s^
•<2_
^4
«zV
^4
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<&z
-*
B-19
-------
CAS VELOCITY AND VOLUME DATA
1.
2.
PLANT AND CITY
£UAic*> -~TA^I^ / (£X&4o<.7 /O 54?
RUN DATE
V
14 17
<>_/:S&
RUN AMB. TEMP. BAR. PRESS STATIC PRESS
NUMBER OPEJWTOR <*F> (in. Hg) (in. H2O)
I/-/5<1_^4^ . 4^" 3r^.4r^ -
i '7 ^^ i§ si »»
MOLECULAR STACK INSIDE DIMENSION (in.) PITOT
WT" )IM<1 OR SIDE 1 SIDE 2 TUBE ^
MOISTURE
. L .
40 44 J8 *' *« *7 *° 73 76
<2*4*L_
18
FIELD DATA
TRAVERSE
POINT
NUMBER
7,8.9 ,10
b->
7
^
^f-
*7
Is
r - /
7
1,
t
-^
(^
POSITION
(in.)
I .1 2 ,13 t>4
VELOCITY
HEAD
(^p ) , in.HjO
75.76.77,78 .79
•2>, \0
^040
^^«=
f / 70
y f-o
<^, gc?
^ , 00
t,to
. £*
-------
CAS VELOCITY AND VOLUME DATA
PLANT AND CITY
RUN DATE
1.
»4 17
SAMPLING LOCATION
CLOCK
TIME
•6
*9
RUN
NUMBER
iA/£
OPE*3CrOR
/" ^^_ /
AMB. TEMP.
CF)
.4&
BAR. PRESS
(in. Hg)
35^-^3
STATIC PRESS
(in. H20)
— 3*2°
1 7 // It Jl JJ
MOLECULAR
WT.
.Z-.4.0
STACK INSIDE DIMENSION (in.)
51 AM OR SIDE 1
. rfb.^. . .
SIDE 2
— _
, . • , S^
PITOT
TUBE Cp
•
MOISTURE
%
y.e
11
40
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«l
*7 70
73
76
FIELD DATA
TRAVERSE
POINT
NUMBER
7.1.9 ..0
c-t
z
}
o-/
z
>
4f
^
IS
POSITION
(in.)
1 1 ,1 2 ,1 3 t '«
VELOCITY
HEAD
(Ap ) , in.H20
7 }. J6 •?? , JB ,79
•?,^o
"«, ^"c>
•?-«o
^.'x'O
3,-^e?
3 /4c?
2. , o^>
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STACK
TEMP. »F
38.39 .40 .41
^^
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&*
f&-
£.**
^/
^?>
^3*
-------
CAS VELOCITY AND VOLUME DATA
PLANT AND CITY
RUN DATE
1.
>7 *«
SAMPLING LOCATION
CLOCK
TIME
42
RON
NUMBER
OPERATOR
AMB. TEMP.
(»F)
BAR. PRESS
(in. Hg)
STATIC PRESS
(in. H20)
2.
l
JS
It
MOLECULAR
WT.
./.K.7>
STACK INSIDE DIMENSION (in.)
5IAM OR SIDE 1
.Lv. . .
SIDE 2
• . • . i
PITOT
TUBE Cp
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MOISTURE
%
7.4
41
70
73
76
CoJ
FIELD DATA
TRAVERSE
POINT
NUMBER
±
±
POSITION
(in.)
VELOCITY ,
HEAD ,
(Ap ) , in.HO
^ ••••
STACK
TEMP, »F
lEJ
El
B-22
\i _
Vj
-------
PARTICUALTE/ARSENIC
B-23
-------
EMISSION TESTING FIELD DATA
17
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STACK
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-------
PARTICULATE/ARSENIC TRAIN SAMPLE RECOVERY AND INTEGRITY SHEET
Sample date | - (S
Sample location^ 4 .
Run No- /^ 1C -/
Recovery date /-
Recovered by
Particulate filter No. 0002501 ^articulate filter sample I.D.
MOISTURE
Final wt
Initial wt
Net wt
1st
impinger
fot g
/So g
•ID g
2nd
impinger
//7 g
/Jo g
3 7 q
Total
3rd
impinger
£&>£> g
Zoo g
2& g
moisture
4th 5th
impinger impinger Silica gel
fo~T g /?/ g .#20,9
Zoo
7
S7-L
g £c
g
g
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* g /r.t g
^0 % spent
RECOVERED SAMPLE
Acetone probe rinse
container I.D.
0.1 N NaOH probe rinse
container I.D.
HpO impinger
container I.D.
impinger
container I.D.
I R
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
Blank containers I.D.
Acetone
.
rt
0.1 N NaOH J5£9"7ft ^
H2°2
Samples stored and locked
Remarks
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
Received by
Remarks A** -
LABORATORY CUSTODY
Date
B-25
-------
Aftrt 4 tin
EMISSION TgSTING FIELD DATA
UK
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I I I I I I I l I I
Mil
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TCMTCMIVM
•9
-------
PARTICULATE/ARSENIC TRAIN SAMPLE RECOVERY AND INTEGRITY SHEET
ASftR
Sample location //Q
No. /%flt\ - /
Particulate filter
Sample date I
Recovery date
Recovered by
Particulate filter sample I.D. J>60J6
MOISTURE
Final wt
Initial wt
Net wt
1st
impinger
//-5 g
/So g
'•35 g
2nd
impinger
y T3 g
/ g
/O g
moisture
4th
impinger
/ff g
Zoo g
-5 g
/$>(j g
5th
impinger
y/7 g
2o6> g
~3 g
Silica gel
\5x$ . u g
3oc) g
Z/.6 g
% spent
RECOVERED SAMPLE
Acetone probe rinse
container I.D.
0.1 N NaOH probe rinse
container I.D.
impinger
container I.D.
HpOp impinger
container I.D.
_. . _. A
OC,6. In
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
Blank containers I.D.
Acetone Hloo fr *-
0.1 N NaOH
H20
n
n
Samples stored and locked
Remarks
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
Received by
Remarks
^
^
LABORATORY CUSTODY
Date
B-27
-------
EMISSION TESTING FIELD DATA
i i «» t i i i
SIACI IMIH
DIM*. (IKWS)
I I I I I I I I
«i«m«nni»m«M..
5315 Jl 54
OHV CAS MCTEB
Miricc PUSSUM
DirrCMMTIAL
(AMI .in.ll Olvi?
OUTLET
IT l.'f
-------
SAMFLC Ml
TtMTUMIVM
•r
-------
Plant
Sample location A
Run No. PRTL-
PARTICULATE/ARSENIC TRAIN SAMPLE RECOVERY AND INTEGRITY SHEET
Sample date
Recovery date
Recovered by
Particulate filter No.OooZSo% ^ Parti cul ate filter sample I.D.
Final wt
Initial wt
Net wt
1st
impinger
soo g
g
g
2nd
impinger
MOISTURE
3rd 4th
impinger impinger
_ g
_ g
15 g
110
2oo
10
g
g
g
"Zoo g
Total moisture
2n g
L. 9
5th
impinger
//o
g
g
g
Silica gel
-g S3.
% spent
RECOVERED SAMPLE
Acetone probe rinse
container I.D.
0.1 N NaOH probe rinse
container I.D.
H?0 impinger
container I.D.
hLO? impinger
container I.D.
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
Blank containers I.D.
Acetone
0.1 N NaOH
H2°2
Samples stored and locked
Remarks
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
LABORATORY CUSTODY
Received by
Remarks
Date
B-30
-------
1 i 1 I I I I I
d
MMIOI
"|n|'»h«|'»h«|"l'»|nH"l"l'^'T
nun tumid)
<>i«i(4i[i)|M[%4frs]n|<
i 1111 1111 111
MACI IHIH
OlMtl (IKNlt)
1 1 A I 1 I A*ftt| I I
ritoi
IIM
TM
"l'>l'«l'
fMf
im
JtliMiltl
i i i i i (
wiiu.
•0.
Mil
' I »
V> Iw*
III !M>I k
t
M>IMI n
T
J_L
mm
« N •
Mp
Mill Ui.
J«
l«»
IDU CMC!
cm
rwrw
11114
m
i;J*IJMJft
HI
jitj«i
MAI tn
•r.
•r
A i i
«cd«
Ml*
-L_i.
r>'*T46T4
3>l5J
55J34I ay
VELOCITY
(Miricc rustu
DirrtUHTIAL
<•»,). !•. 1,0
nWUATUM
BUY CAS MTIB
rrMPCRATUU
IMUT
IT. >.«r
In
OUTLXT
IT. i.»r
owt
VACVUH,
i*.M
TCMWM
•9
IHTIHCO
CftMM
r
te3 A
JT7
i
iro
11
LL
tt
4
°
.b
*
B^
A.o
JL7*
JA
oA
i
^2
il
JLL,
^2
J
•L
_k_
ilt
^S^
-------
PARTICULATE/ARSENIC TRAIN SAMPLE RECOVERY AND INTEGRITY SHEET
Plant
Sample location J^0 V
Run No. /VfcA- "2-— '
Particulate filter No.
1st
impinger
Final wt /£7 g
Initial wt /5o 9
Net wt -/& g
Acetone probe rinse
container I.D.
0.1 N NaOH probe rinse
container I.D.
HpO impinger
container I.D.
H?0? impinger
container I.D. -
Blank containers I.D.
Acetone
0.1 N NaOH _«,
•£*wC5c«^AjeJan/ £*ta*rTRecovery date //rfi
Recovered by Cpfrrf*
0(poZS7>^> ^Particulate filter sample I.D^
^•^/Sx*-
MOISTURE * (
2nd 3rd 4th 5th
impinger impinger impinger Impinger
/^ g fff g 777 g f?S g
/5o g ioo 9 "Zoo g Zx>o g
*/ g - r ^)g -3 (0)g -^ (o) g
Total moisture £,V g ^^
RECOVERED SAMPLE
Liquid level
./V/cZ— X> <^^ marked '
Liquid level
^73 -Hr *' marked K
^ Liquid level
St7V~4 ^ marked ^
_ . Liquid level
^?/-/7 ^ marked i/
Liquid level >
tf-loon marked ^
Liquid level
569 "7 # ^ marked X
r^
i
tjljj-A^
#~~j2#c~t
Silica gel
£ /If, ^--g
3oo 9
/^2^g
? % spent
^
/
/
/
Liquid level ^
H20 v5Cy# ft: u marked '
H2°2
xr/ 9/ A / Lic«uid level
DG»76. n L marked -^
/
Samples stored and locked
Remarks
r\S
Received by ^— ^^^
LABORATORY CUSTODY
^^ V^-A^c^Z^ Date ^27^f^-
/^
-»i-y / C^d/^-
Remarks A^t ^ • ^ ^^/^ (s
B-32
-------
i i i i i i i i i i i i i . i i i i i
•AMTLB MM
TtMTUATV**
•f
-------
EMISSION TESTING FIELD DATA
* tin
'N*N»|Hli
J i i i i i i i i i i i i i i i i i i i i i i i t i i i i i i i I j.
Mil
IOU1ION
.Mw[tiH"H'
1"I"I"H"
i i i ii i i i i i i i i i i i i i.i i i t i I i i i i i i i i i i i i i
Tin
liilnTHliiHM'^'H".*
511 53 JS4
oniricc mrssuu
DirrtUMTiM,
-------
PARTICULATE/ARSENIC TRAIN SAMPLE RECOVERY AND INTEGRITY SHEET
Plant
Sample location No 4- C
Run No. /V7TC-3
Sample date
Recovery
Recovered
/'2Z'
Particulate filter No. 353oL/£) ^Particulate filter sample
MOISTURE
1st
impinger
Final wt l/\
Initial wt tsc
Net wt ~31
Z- g
• g
\ g
2nd 3rd
impinger impinger
/^g 10?
/So g 2oo
/* g ?
g
g
g
4th
impinger
It / g
TOO g
~l g
5th
impinger Si
/4f g ^
Z^o g 2*
-3 g ^5
lica gel
£^3 g
^o g
Total moisture
^ 9 '3
spent
RECOVERED SAMPLE
Acetone probe rinse
container I.D.
0.1 N NaOH probe rinse
container I.D.
HpO impinger
container I.D.
HpOp impinger
container I.D.
Blank containers I.D.
Acetone
0.1 N NaOH
H2°2
Samples stored and locked
Remarks
A
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
Liquid level
marked
Received by
Remarks
LABORATORY CUSTODY
Date
/9f*>
B-35
-------
EMISSION TESTING FIELD DATA
oat net rutssuM
OirrCUHTlAL
MV CAS NCTCI
TCHfCKATUM:
-------
PARTICULATE/ARSENIC TRAIN SAMPLE RECOVERY AND INTEGRITY SHEET
n Sample date
Sample location No 4 C
No.
-------
P.S.D. BLOWING
B-38
-------
VMTttW IKMKW
i i i i i i i i i i i i i i i i
•(«• (IM.M1I
VMVlf IMtll
Ml HO I Ml M
f I I I I I M I I
»*170|>» i a 71331?
o* i rice rustuM
OirrEUMTIM.
•TACI
twmiM
M> «AS MCTCB
COMItMEM
TIHPCMTVIV
•P
-------
IMPACTOR EMISSION TESTING FIELD DATA
t cut
Ml
IOUIIM
vmi tm
• 11.... i..........
033?
•HMIM
VI
tUMt
Ml Si
(I* H 01
trn
MWI IMI«
•IMI. |I«CW(I
rn«t
IMt
C»
137®
nln HIM
111
»' I I I I I I I I I I I I I I I I I I I 1
i I I I A I I I ! I I I I I I !. | ! | | | I | | A . |
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•utt.
TTIT
i I 11 I I I I I
It) !ui
J_L
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*
I I
I (AC CMC!
M?
4111
A I I I I I
HUl HI
••t m
I I
M.V
•r
•I COW
Ml*
-------
ANDERSEN IMPACTOR RECOVERY AND INTEGRITY SHEET
Plant
Sample location
Run number
Nozzle rinse
container number
Acetone blank
container number
Filters
Stage
0
1
2
3
4
5
6
7
Backup
/o
-/
Sample date
Recovery date ///?/£5
Recovered by A(cP
RECOVERED SAMPLE
Liquid level
marked
Liquid level
marked
Filter number
Container sealed
:/_
53
500
Samples stored and locked
Remarks
LABORATORY CUSTODY
Received by A^L-^
Remarks /&'^,
Date
B-41
-------
IMPACTOR EMISSION TESTING FIELD DATA
•TACI
tCMMJIATVM
if_i.*r
-------
ANDERSEN IMPACTOR RECOVERY AND INTEGRITY SHEET
Plant
Sample location Ha.
Run number
Sample date
Recovery date
Recovered by
I fa
RECOVERED SAMPLE
f/g/fr
Nozzle rinse
container number
Acetone blank
container number
Filters
Stage
0
1
2
3
4
5
6
7
Backup
Samples stored and locked
Remarks
Liquid level
marked
Liquid level
marked <,
Filter number
Container sealed
- 1 1
3
o
LABORATORY CUSTODY
Received by
Remarks
Date
B-43
-------
IMPACTOR EMISSION TESTING FIELD DATA
Mince rwssuM
OirriUNTIAL
MI CAS NCTEft
TCMfLMTWU
-------
ANDERSEN IMPACTOR RECOVERY AND INTEGRITY SHEET
Plant /?5(\£CQ ~7^orr,^ _ Sample date
Sample location f\fCi T ^etovJary £\Hz(JT\' Recovery date > 1 1 y &3
Run number /%**£> ~O _ _ _ Recovered by
RECOVERED SAMPLE
Nozzle rinse / / ? 2 fl. Liquid level /
-3 '
.
container number T/<5-n marked
Acetone blank , Liquid level
container number y^Zoo f\ L marked
ain
Filters
Stage Filter number ' Contaiper sealed
0
1
2
3
4
5
6
7
Backup
Samples stored and locked
Remarks
LABORATORY CUSTODY
_/
Received by 7'^ ^-.
-------
IMPACTOR EMISSION TESTING FIELD DATA
« tilt
i|ii|ii|i4|i>|it|i>[n|it|;i|n|M|ii|n|it|ii|ii|»i|n|i«|ii|ii[ii
Mil
UWTUM; IOUIIM
wmt im
i TTTtido/ft/ii i i i i i i i
MiMliili'hi n '
ZZ2
«t[4l]4«J4t |«l|«l|l|»|n|M|l>
MltllllMlllllM Mill 14
I'M"!"!'
1 1 I I L
>/• ff&
3<+ \ ltf>t-
I I I t I I I I I
L£
•flMIM
im.|..|i.ht|n|.il.t|'i|.'|"l"N"l"l»^«|nl»|i»
11 •»
l*f)
MISS.
II" H,)
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rilii
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IHPACTOK TYPt
Sl«tl IMI
DIM!
nioi
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t»
nt
111*1
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p
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It Ml
I t » » I I I
I I I
J 1 I . I 1 l6
IIKW
llll»/t«l«l«l'l»l*l"i"b»l'»l"l'th»l"l'»p«
•ami.
i 'win I
(f)
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Mill Ui.
T
Id.
i ut CHtci
^nT
i
fdCTOH
t
MCK
MUI Ml
WAI ui
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••u
11 I I l I I I l
i 1 1
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fi
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ft
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n|>ijiiji'
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1 1
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-------
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l'i|i»|'«|"H"l'*l"H"l"H"M"l"l"H'*l t>\>t\it
0*11
IOOIIIM
-* ^-
33
nil* HlirlM " "I"
4j|«)U.|«\ |..|«>|««j««|-*|M|v|M|'va]->sU«js.U«|>»|»nlii]«;|«i|M|«%
..jujMlxluimMl.^^^..^^..!*!
t^rj*!"1 J-.jM-^fU >L*
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irn
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» »
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k » i
te
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CM urn*
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TfNPtHATOUt
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IT |.»r
111
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••••€
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TEMPERATURE
•r
CONDENSER
TEMPEMTORE
•r
' . .1 1.4
* •
-------
ANDERSEN IMPACTOR RECOVERY AND INTEGRITY SHEET
Plant A5AKCO Sample date
Sample location /Vo T- Ofx^wg/d-ri/ £*h&us~t~ Recovery date
j _ —
Run number PS£~H~ Recovered by _
RECOVERED SAMPLE
Nozzle rinse 4ia/ A • Liquid level
container number 7 I 1 k " marked
Acetone blank , Liquid level
container number y^oon marked i^
Filters
Stage Filter number '- - : r1 Container sealed
0
1
2
3
4
5
6
7
Backup
Samples stored and locked
Remarks
LABORATORY CUSTODY
v- -^
Received by '•-'-'- ^ 'i ^_ - ^^ /^ t- T.- Date
Remarks >" --. /x7
B-48
-------
P.S.D. SKIMMING
B-49
-------
IMPACTOR EMISSION TESTING FIELD DATA
« cm
111 II
1 1 1 1 M I
Mil
IOU> 110*
11
vmi im
•nwioi
'il"|'i|')|<«|'t|n|ii|n|n))i|ii|M|ii)n[n|i»|i>'
i i i i i i i i i
,
C')
III
Will
(II M 01
IMPACTW TYPE
11)11111
IMIH
OIWI
3HE*
i i i .i.
LUtlN M* 1TM
i i i
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MUM.
iin M
la
#
1 1
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)I]M|I\
1 1
Mitt
* M •
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in.
ItM CNCCK
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M 1
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s
CUKB TIM
•JMTLIMCN. l>« *»r
.CU>C«)
COKDCNSER
TEMPERATURE
•r
-------
IMPACTOR EMISSION TESTING FIEtD D*TA
» cm
h'l'»l"J'M'*l"l"i'»H»l"l>i|M|»|ii|i.|,i|H[H»-'P7nT
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s
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I I I I I I i 1 I I i
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(•f)
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1 1 L.I
33
JL_L
A 1 1
1 i
-LJL
I LI 1A 1 A I
-------
ANDERSEN IMPACTOR RECOVERY AND INTEGRITY SHEET
Plant Pl5ft?CQ
Sample location /V0. 4
Run number
Nozzle rinse
container number
Acetone blank
container number
Sample date /// // /•£
Recovery date
Recovered by
RECOVERED SAMPLE
Liquid level /
nwrkprl /
marked
Liquid level
marked
Filters
Stage
0
1
2
3
4
5
6 ?
7
Backup
Samples stored and locked
Remarks
Filter number
^077
Container sealed
Ij
/
LABORATORY CUSTODY
Received by
Remarks
Date
B-52
-------
xr*vj r J-IJAJL/ i_/i-* JL r-*
«\Mf » CIT?
»J»J«j»l»IM»l'M"l'i|'iH';l'«l''H'«H"l"liit'«l"l'»l»'l"N)i|i.|ii|ii
0*11
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1MTVI 1T*1
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—* • ii i ——t—t • *t i.'—i—' i * j^—'—'—'—^—•—*—*—* ' i
>«|trlllk«|»|ri[i||ii|p<|M|i[«t|4l[«l
,t*I*4Mh
-------
ANDERSEN IMPACTOR RECOVERY AND INTEGRITY SHEET
Plant _
Sample location //c
Run number
TOCO^J^
v^gilo i^J^fV £
Nozzle rinse
container number
Acetone blank
container number
Sample date /
Recovery date
Recovered by McP
RECOVERED SAMPLE
Filters
Stage
0
1
2
3
4
5
6
7
Backup
Samples stored and locked
Remarks
Filter number
lo
/7
Liquid level
marked
Liquid level
marked t
Container sealed
ntan
/ .
Received by
Remarks -.
LABORATORY CUSTODY
;
^^-' —/U"{!V._ Date
B-54
-------
XMfACTOR EMISSION TESTING FIELD DATA
.]Hil.JiUl.ji|t|..r.|.il.iH..|..|.,|..|..H''l"I^M|tt|M|,,|,.HH''l»l..
Mil
VWVtIM. IOCMIM
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l"l"l"l
.1 i I I t j i i i i i i i i i i i | _t
•Ml •.
E
VtMIM
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CM
SUIIt
f»lii
(I* «20)
IKPACTOK
MAtI IMIK
PIMI (IKNttl
IM1
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*
>•;
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H 14 ttktUilMllI
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KC
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im cmct
i«. Ht] cm
MCt«
UT
M»1
Ml*
jjirt
it it nil* n
M it hi
fafl
I i 1 I I I I I
il
)»I»Ti
W
ti t/M w '
I I I
l_l 1.
1 1 A
1 ii
nk
73|33|? 4
34
17
C14KJI TIM
MMTUHCN. (14 kr
CM mtnm MAD lac
O
vtuxrtTf
OBiricc russuM
oirrtUHTiAL
UNI .in.NOi
STACK
DAT CAS NCTCB
TrMPLAATUU
DCS I UP ACTUAL
IT. ».»f
VACUUH.
I W ACTOR
TEMPERATUBB
OUTLET
«T
out
CONUEN8EK
TEMPERATUM
•r
V7
W
w
T
-
V7
r
i
97-
(Ji
#
/-«Z
l.t
j
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60
-
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2JL
73
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5
ttL
» i .* I 4
* t
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Sample location ^/0 ~4 ^^uj^ry C*h°.(jsl Recovery date
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SF6 TRACER GAS INJECTION DATA
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Date
Plant
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B-71
-------
SF6 TRACER GAS INJECTION DATA
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B-72
-------
Date
SF6 TRACER GAS INJECTION DATA
RUN NO.
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B-73
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date
/-
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_psi
Time
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Time
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X
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B-74
-------
SF6 TRACER GAS INJECTION DATA
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Time
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B-75
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date
/-
Plant
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/y/
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psi
Time
(24-h)
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Time
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Time
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B-76
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date
Plant
Injection location
Barometric
Operator
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in.Hg Ambient temperature, °F
psi
Time
(24-h)
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Time
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B-77
-------
SF6 TRACER GAS INJECTION DATA
Date
/-
53-
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Plant
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time, min
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injection rate is the average of initial and final.
B-78
-------
Date /-//-^3
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psi
Time
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Time
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Time
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rate,
cc/min
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time, min
^ 5'
2_'iO^
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injection rate is the average of initial and final.
B-79
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date
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B-80
-------
Date
/' / ? ~
SF6 TRACER GAS INJECTION DATA
RUN N
Plant
Injection location
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psi
Time
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Time
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Average
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time, min
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B-81
-------
Date
SF6 TRACER GAS INJECTION DATA
RUN NO.
Plant
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Time
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Time
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Injection
time, min
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-82
-------
SF6 TRACER GAS INJECTION DATA
RUN NO
Date
Injection location
Barometric j>r§ssure
Operator
in.Hg Ambient temperature,
Regulator pressure
psi
Time
(24-h)
Calibration data
Time
Bubble meter rate., cc/min
Initial
Time
Final
Average
Injection
rate,
cc/min
Injection
time, min
31.0
-t
ft$
/o o
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-83
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
in.Hg Ambient temperature, °F
Date
Injection location
Barometric pr^-fsufe
Operator
Regulator pressu
Psi
Z-
I
I
r
Time
(24-h)
[){)fy
Calibration data
Bubble meter rate, cc/min
Time
fr.dfr
/} 3/
/2,2^
fett
Initial
^
/
/
y^,6^0
Time
//f^
/y?, O<3
1 2 1 L/ &
/
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date
Injection location
Barometric pn
Operator
in.Hg Ambient temperature, °F
Regulator pressu
psi
Calibration data
Time
(24-h)
Time
Bubble meter rate, cc/min
Initia
Time
Final
Average
Injection
rate,
cc/min
Injection
time, min
// '-
B/ z
C\ \
b/ ?
7^66
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-85
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date
Plant
Injection location
Barometric p/essure
Operator
/yy£ iMf^^A^
in.Hg Ambient temperature, °F
Regulator pressure
Time
(24-h)
Cal ibration data
Time
Bubble meter rate, cc/min
Initial
Time
Final
Average
Injection
rate,
cc/min
Injection
time, min
/z.^
-5P
*>
/J.4-1
r*
~7 1
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-86
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date ;
' ^ /I /?
Injection location ynfr/g. (_^
Barometric
Operator
Plant
in.Hg Ambient temperature, °F
Regulator pressure
ir
_psi
Time
(24-h)
Calibration data
Time
Bubble meter rate, cc/min
Initia
Time
Final
Average
Injection
rate,
cc/min
Injection
time, min
. 31
ML
&2-1-
5?
/£_
t(r L
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-87
-------
Date
SFg TRACER GAS INJECTION DATA
RUN NO. */-
Plant
Injection location
Barometric D-ressure
Operator
in.Hg Ambient temperature, °F
Regulator pres^fre
psi
Time
(24-h
Cal ibration data
Time
Bubble meter rate, cc/min
Initial
Time
Final
/
Average
Injection
rate,
cc/min
Injection
time, min
Jl.tc'l
1
tic
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-88
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date / Z.f-
Injection location
Plant
Barometric peessure
in.Hg Ambient temperature, °F
Regulator pressu
psi
Time
(24-h)
Calibration data
Time
Bubble meter rate, cc/min
Initia
Time
Final
Average
Injection
rate,
cc/min
Injection
time, min
A?..? 3
no
'v 33, 3'L, 35 :
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-89
-------
TRACER SAMPLE COLLECTION DATA
B-90
-------
SF, TRACER GAS BAG SAMPLING FIELD DATA
b
RUN NO. •?flt[f'*VAi4
Date /-/x ^1 Plant ^,4/2^
Sampling location /A 7 "fc.c~t£c/4t~f ^J^A^^T"
Barometric pressure ^ 13. in.Hg
Ambient temperature, °F ^^ Stack temperature. °F
Operator
Sample bag
Time
(24-h)
tffl
/fS*
/^s^
/y.5%
/&-%
/(, DC
/del
1 L o ^
/ t ^_-/
/4 ^^
/(O^
5^c^re/
S^~g> / y.
leak checked Sample train leak checked ^
Traverse
point
/!£?£.' 1 5)^3
Jc-pfl-1-
Jcpt-3
fic~Pf.' V
Acpz-f
A i pz - t
4c?£-7
rf ( PZ--^
AtPR-1
AtP^w
AP /
2 ^^^^~
t A f *~~/\
/ / r*~ / *^-' '
/ **) s y"^"^7
/o /J'V
i,^ / £*t
/, j~b / (D ^
/J^/ S~^
/ ^ -\ / A.^^V
/'JD / t>6
/, ^o/j-y
/,, 25 / 6*1
f ^/ ^
/
/
/
/
/
y
Rate roeier
flovrrate,
'J, $
-J,V
'#
-*i.y
-A>?
-*.?
-^.y
-^/
~2-tf
.-2-f
Average
Q - Q
af n™ - ^ av9-\ inn (Mnst hp
-------
SF6 TRACER GAS BAG SAMPLING FIELD DATA
RUN NO.
Date
Plant
Sampling location
/y^ 7 ^
Barometric pressure
Ambient temperature, °F
Operator
Sample bag leak checked
c
,0*;
«i
ft
m
5
• /
ll
1\
Time
(24-h)
!*,&
+?M-
niJ
MIL.
Traverse
point
6)
a")
r//J c 4
Dev. = (
Q - Q
100
Stack temperature, °F
Sample train leak checked
AP
n /bo
MA
Rate meter
flow rate,
cm3/min
Average
(Must be <10%)
in.Hg
Dev.
B-92
-------
SF6 TRACER GAS BAG SAMPLING FIELD DATA
RUN NO.
Date /' /V /J Plant -/hrfjc^
Sampling location /fv, f S6i»*bit)/*>f t~jJl#vdr~
Barometric pressure 3 - 4
rl^ ^ i» ' 4
V
in.H20 Z
/ ' ~-
>{ ? A^
/ 9 7^
/ /A-3
/?X$7/-
/ ? / i ".5
// y/s?>
'
Rate meter
flow rate,
cm3/min
Average
% Dev.a
Q - Q
( **±.) 100
B-93
-------
Date / •
SF6 TRACER GAS BAG SAMPLING FIELD DATA
RUN NO.
Plant
Sampling location //fl, 7
Barometric pressure
Ambient temperature, °F
Operator
Sample bag leak checked
Time
(24-h)
Traverse
4
g-i
Stack temperature, °F
Sample train leak checked
AP
_££
Dev. = ( av9') 100
^avg.
Rate meter
flow rate,
cm3/min
Average
(Must be <10%)
in.Hg
Dev.
B-94
-------
SF, TRACER GAS BAG SAMPLING FIELD DATA
D
RUN NO.
Date f'/T't^- Plant ^/^4^j^>
Sampling location /y£>, *f~ ^}E.u>t)s/Ai**f ^>(A/)<^y\
/
Barometric pressure ^Oi3^b in.Hg
Ambient temperature, °F rO Stack temperature. °F
^
II
il
Operator
Sample bag
Time
,(24-h)
«t/^
££$ 1
0 1 7^~)
. ^ • i ^**~ * f_ •*
Cs*cr—< dy i
Jo^L_
^^2^
£^•££1
leak checked Sample train leak checked
Traverse
(*/3) C (-^
(
-------
SF6 TRACER GAS BAG SAMPUflG FIELD DATA
RUN NO.
Date /' / 7
Plant
-r-f
Sampling location
Barometric pressure
Ambient temperature, °F
Operator
Stack temperature, °F
Sample bag leak checked
Sample train leak checked
Time
(24-h)
/ft/1
nu
Traverse
fil
(5)
tt-t
(l)
(i)
)
L-3
L-V
AP
// /T7
Rate meter
flow rate,
cm3/min
in.Hg
Dev.
LL-J
y&
sS ' I X>»'<
5y/s
- T.3
Q - Q
Average
-) 100
=10%)
-------
I SF, TRACER GAS BAG SAMPLING FIELD DATA
D
RUN NO.
Date
Plant
Sampling location
Barometric pressure
Ambient temperature, °F
Operator
Stack temperature, °F
Sample bag leak checked
Sample train leak checked
in.Hg
B-97
-------
SF6 TRACER GAS BAG SAMPLING FIELD DATA
RUN NO. j
Date
Plant
Sampling location
Barometric pressure
Ambient temperature, °F
Operator
Sample bag leak checked
Time
(24-h)
/V-0-!
Traverse
point
Ql-Z
fcA
in.Hg
Stack temperature, °F
Sample train leak checked
2
Rate meter
flow rate,
cm3/min
Dev.
Q - Q
avS
) 100
Average
B-98
-------
SF6 TRACER GAS BAG SAMPLING FIELD DATA
RUN NO.
Date
Plant
Sampling location
T/
Barometric pressure
Ambient temperature, °F
Operator
Sample bag leak checked
in.Hg
Stack temperature, °F
Sample train leak checked I
Time
(24-h)
Traverse
point
AP
Rate meter
flow rate,
cm3/min
% Dev.
7
, U
B
Z
tef^
-?
- (-
Q - Q
av9-
) 100
Average
(Must be
B-99
-------
Date T//9/33
SF, TRACER GAS BAG SAMPLING FIELD DATA
0
RUN NO.
Plant
Sampling location
Barometric pressure
a?.
in.Hg
Ambient temperature, °F
Operator
Stack temperature, °F
Sample bag leak checked
Time
(24-h)
: zc.
Traverse
point
sp
sf
Sample train leak checked
AP
in.H20 /
Rate meter
flow rate,
cm3/min
Dev.
/o;33
Q - Q
avS
) 100
144
Average
be <10%)
B-100
-------
Date
SF6 TRACER GAS BAG SAMPLING FIELD DATA
RUN NO.
Plant
Sampling location =*r y f/T/^f<->^S7^
Barometric
pressure S 9. ?O in_Hg
Ambient temperature, °F *S~C> 5
lofcif
^
Operator
Sample bag
Time
(24-h)
/Z'06>
AL °^
[(Z "- 1 4>
/? - / <^
/Z < ?<£
fL'- Z'L-
fZ LL\
(7 \Z1
C /^/t7Tps<$^aPC^?^^
>tack temperature, °F
^0
leak checked ^^"^ Sample train leak checked ^/^
Traverse
point
3iT- 52- -/
3p~ BZ--Z—
3^ _ C / - /
3^-- c/ -^_
^«T- c^ -/
?\J ~ C^> - "£__
^L-- j^/-y
3 if " bi -Z_
AP
in.H20 /
/ T s
/, 3 / ^ Z~
'i3^/ fe?"^
I ^^ / I**^ (-*r-^
I ^*^ / ^ ^? ^^^^
\,i$/ c?t^
/'&>/ 6> /
/3 / 67^
Az5/ (^3
Rate meter
flow rate,
cm3/min
'' / -V
<, ve^^U-
r
Average
Q - Q
aY nou - t av9-\ inn fMust bp <-in^
% Dev.a
)
avg,
B-101
-------
SFC TRACER GAS BAG SAMPLING FIELD DATA
b
RUN NO.
Date
Plant
£te&g_
f-(Ol^>H
6^0^
r~
Sampling lo
Barometric
Ambient tern
Operator
Sample bag
Time
(24-h)
/!> ' ( 3
t3> (°\
(3;Z/
( 3 "- £3
( V-2-3
/3; 3-0
1 1) • ^ ^>
/ 3 '1^
cation T £r?r/S'*iS£>~7~'
pressure '£c7-~i?<-:> in.Hg
perature, °F v5~C> Stack temperature, °F 4v^^
?. /4^T^/^«i^c
leak checked ' — ' Sample train leak checked — "
Traverse
point
3^S- &z--^
3^- /SZ-^
3A3T-CI-3
3A5- C( -V
3AT - C fe>'3
3/VS- C^-V
^^S- 6v-^
i^s- D'-y
AP
in.H20/
3 •£>/""?/
3 -o/ ~7 ^7
3o/ 2^4
/.^/ tG"
/, / / txS
Rate meter
flow rate,
cm3/min
"^
^rH4H ^i^U^-
\ ^^^7
i ^_ e i\
A
L /-cs-J
r ^^^ - 1 j"
J
Average
n n
% Dev.a
-) 100
"avg.
B-102
-------
SF6 TRACER GAS BAG SAMPLING FIELD DATA
RUN NO.
Date
Plant
Sampling location
vr
Barometric pressure
Ambient temperature, °F
Operator
Stack temperature, °F
•">
Sample bag leak checked
Sample train leak checked
*avg.
in.Hg
B-103
-------
SF6 TRACER GAS BAG SAMPLING FIELD DATA
RUN NO.
Date
?€>**'$
Sampling location
Barometric pressure
Ambient temperature, °F
Operator _
Plant
Sample bag leak checked
in.Hg
Stack temperature, °F
Sample train leak checked w-
Time
(24-h)
Traverse
point
AP
in.H20
/
7S
Rate meter
flow rate,
cm3/min
Dev.
f L :•
, "75'
r
.//
t : c v
II
Q - Q
av9
Average
) 100
B-104
-------
SF, TRACER GAS BAG SAMPLING FIELD DATA
o
RUN NO.
Date //
Plant
Sampling location
Barometric pressure
in.Hg
Ambient temperature, °F
Operator
Stack temperature, °F 6>
Sample bag leak checked
Sample train leak checked
Time
(24-h)
Traverse
point
AP
in.H0
L
Rate meter
flow rate,
cm3/min
Dev.
P77
ZJ
3s
^'/ 73
T27
SI
70
(S^T
a% Dev. =
Q - Q
^±) 100
Average
(Must be
B-105
-------
SF6 TRACER GAS BAG SAMPLING FIELD DATA
RUN NO.
Date
Plant
Sampling location
Barometric pressure
Ambient temperature, °F
Operator _
Stack temperature, °F
Sample bag leak checked
Sample train leak checked
Time
(24-h)
Traverse
point
AP
1n-,H«°/fs
Rate meter
flow rate,
cm3/min
in.Hg
Dev.
.6 / 69
3-7
3.37
n •,
3-y 77^7
it
Q - Q
av9
) 100
avg.
Average
be
B-106
-------
TRACER ANALYTICAL DATA SUMMARY
B-107
-------
Client
PN 1¥?0- 7
LABORATORY DATA
Analysis
Date
"Analyst
Calibration Number
AIR SAMPLE ANALYSES
SF6 TRACER
Sample I.D.
Atten.
Peak
Height
Response
Concen-
tration
v/v
(rV
3-00X10'%
Lit* iv
7
10
^7.0
3 00%
3.00*10
%
*
. CM
-------
Client IAI i--ffiI f
PN ?y?
-------
Client Us L
PN 1KO 1
UBORATORY DATA
Analysis
Date
Analyst
Calibration Number
AIR SAMPLE ANALYSES
SF6 TRACER
Sample I.D.
Atten.
Peak
Height
Response
Concen-
tration
v/v
C
a
r.-/
K
IL
v7
75 7/7 s 7
CM
V?
C /
^ 3
AJ
77 1/77-0
C
/g//7
B-110
-------
Client t/c
/ 7)
PN V/10'7 Date /-/7-frJ
Analyst £.*L'£
LABORATORY DATA
Analysis
Calibration Number /V7-%3
AIR SAMPLE ANALYSES
SF6 TRACER
Sample I.D.
Atten.
Peak
Height
Response
Concen-
tration
v/v
-------
Client
PN 3V
UBORATORY DATA
Analysis
Date
Analyst
Calibration Number /-If'
AIR SAMPLE ANALYSES
SF6 TRACER
Sample I.D.
Atten.
Peak
Height
Response
Concen-
tration
v/v
33-
61 -
fH*
3
/re/ -
/353-P
i
JO/ 3
ls/6-l
/W.y
I-I7XIO
'
!(.(.*<<
//
n
Ci I
1.27X10"^
12.
CI-3L
733/710
/j
&.
/)/ -
17
3s,
5V-0
19
O-/
c/~a.
5 O.
ry
V/
B-112
-------
Client U* LPf) / /)
PN 3V7fl 7 Date
Analyst r-./fdr,
LABORATORY DATA
Analysis
Calibration Number I -
AIR SAMPLE ANALYSES
SF6 TRACER
Sample I.D.
Atten
Peak
Height
Response
Concen-
tration
v/v
3V/
7
5/°
(0? l.
7/
/6
-/ti,
mi
mo*
/•£>** l0~
it Cr
/&
Ik
S'S
3-
hi t
y
77,7/7??
c
}L
I' -
3 - /
3/^7
C/ 3
/-37YIO'
7/ir
If?
C! H
f-">3x.
3
Mfm*
/} / -
l-lfXio*
t*/K
B-113
-------
Client
PN
LABORATORY DATA
Analysis
Date
Analyst
Calibration Number j-3-0-
AIR SAMPLE ANALYSES
SF6 TRACER
C. U I
Atten
Peak
Height
Response
oncen-
ration
v/v
*
f
/
h '- f.
r ^ ,y
V
I
.
-------
Client
PN
LABORATORY DATA
-^ -^—--^ Analysis
Date
Analyst Gftt'C
5
Calibration Number / -3-0-
AIR SAMPLE ANALYSES
SF6 TRACER
Sample I.D.
Atten.
Peak
Height
Response
Concen-
tration
v/v
33-
It
?0 0
/G
32
Y
/zoo
/£
c;
"
6f
f/s'2.
7
-'
s-
12 it-
71
1
t
X7//7
B-115
-------
EXAMPLE SF6 STRIP CHART PRINTOUTS - JANUARY 1983
CALIBRATION
BACKGROUND
INJECTION SAMPLES
B-116
-------
B-117
-------
B-118
-------
.r. '
-4---
--1—
100
-= 7u-y*
t - :-: t -••-.. _-.!
i££l*J{t ~~:~^{
~~is
i '
. j.
tf
jf$fl t^fc
ttfAflX
.^^.
i
-r-
80—- -
B-119
-------
B-120
-------
100 -'.'j -
r
B-121
-------
. _ _. I , :
B-122
-------
B-123
-------
B-124
-------
B-125
-------
B-126
-------
^trr
. 1 . .
B-127
-------
B-128
-------
B-129
-------
B-130
-------
B-131
-------
1
B-132
-------
'-(00
i
B-133
-------
Client
•PN
Date
LABORATORY DATA
Bottle Volume
Flow Rate:
Analyst
^/^//^.^
Gas Change Time(Tor):_
Initial Cone. (Co) ' tt-'Jltxio-i
CALIBRATION BY
EXPONENTIAL DILUTION
Time
, i,ru& j.}
i/
N
(TD/TGC)
At ten.
Peak
Height
Response
Cone
0
12
/3
M.
5~
2.
2-
imi
11
U.3
3-
ZV20
n
iL
S'O
/o
J/
33
13
//•=>'
87. /
627
73
/3
V
o
tto
n
3'
3P-
33
/.yyx of
'"
I 3.Q\/0
'1
77
7-3/x/o""
/is'
Figure 5-10.
GC calibration data stieet.
B-134
-------
10,000
to
I
M
U)
Ui
1000-
SF6 CALIBRATION JANUARY 19, 1983
m = .86787899
b = 10.054926
r = .99996
100-
5F6 CONCENTRATION, v/v
Example SFfi calibration curve - working range
-------
DECEMBER 1982 PRELIMINARY TEST DATA
SFg INJECTION
SF6 SAMPLE COLLECTION
SF6 ANALYTICAL SUMMARY
B-136
-------
CAS VELOCITY AND VOLUME DATA
1.
2.
PLANT AND CITY
JU+U0 7^4+M U?~J
\ J
SAMPLING LOCATION
t/oA 4*.l~*f £>**?*-
CLOCK
TIME
fl&^
4J 66 t<>
RUN
NUMBER
\tf~l
OPERATOR
14 }7 40
BAR. PRESS
(an. Hg)
^ , • '
17 21 31
'£
STATIC PRESS
(in. H20)
. •
33 36
MOLECULAR
WT.
.V."*
STACK INSIDE DIMENSION (in.)
5IAM OH SIDE 1
. i.om .
SIDE 2
i . • . i
PI TOT
TUBE Cp
.5?
MOISTURE
t
+/.*,
70
FIELD DATA
TRAVERSE
POINT
NUMBER
7 L« • 9 ''°
^:/
3
POSITION
(in. )
1 .'^ .13*14
//.D
•\;
VELOCITY
HEAD
p ) , in.H20
75.26»77.?8 i2938i39.40.4l
STACK
TEMP, °F
7./3
i i j T_i«
"w:
23.3
3-137
76
'u;
i
'/ *#)
-------
CAS VELOCITY AND VOLUME DATA
1.
PLANT AND CITY
RUN DATE
01/M
/ 40
SAMPLING LOCATION
CLOCK
TIME
2.
RUN
NUMBER
W-l
—V :
OPERATOR
CAu^^u
AMB. TEMP.
CF)
Stf .
BAR. PRESS
(in. Hg)
Jo^f
STATIC PRESS
(in. H20)
~7.*r
21
MOLECULAR
WT.
.^f.
STACK INSIDE DIMENSION (in.)
DIAM OP. SIDE 1
SIDE 2
, , • . •
PITOT
TUBE Cp
.^
MOISTURE
t
•^/.^?
40 44 ij «1 64 47 70 73 7^
FIELD DATA
TRAVERSE
POINT
NUMBER
7.8.9 .10
POSITION
(in.)
1 ,1 2 ,1 3 t U
VELOCITY
HEAD
(Ap ) , in.H^O
2 5. 26 • 2 7 , 28 , ?9
. .*.£.?
STACK
TEMP, "F
36,39.40.41
3-138
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date
Plant
Injection location
-ho
2?
BarometHp^jfressure
Operatoi"
in.Hg Ambient temperature, °F
Regulator pressure
res;
Time
(24-h)
/Zil~-
Calibration data
Time
Zll&S
7JO.lt?
2I\,0
Bubble meter rate, cc/min
Initial
^^
/^
z &4
Time
2^1/4-
?. O
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-139
-------
Date /2-
Injection location
SF6 TRACER GAS INJECTION DATA
RUN NO.
Plant
/T5rf/Z&& -
.^-— -s
Barometrip'pressure
r"~p7>^-
in.Hg Ambient temperature, °F
Regulator prssure
res
psi
Time
(24-h)
/^/
Calibration data
Bubble meter rate, cc/min
Time
/?#£/
1&* .
/&&
Initial
^
^
3.&
Time
/7^^^
/*Z.10
/?3£*
Final
/
/
s.4&
Average
3,^3
Injection
rate,
cc/min
3,43,
Injection
time, min
Z&&
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-140
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date
Plant
Injection location
Barometric^p^essure
Operator
ot ^ «~b
7/4CQ/v\A
AT OF
in.Hg Ambient temperature, °F
Regulator pressure
psi
Time
(24-h)
/^33
Cal ibration data
Bubble meter rate, cc/min
Time
53.ZS
5U*
te.3b
<#.^
Initial
y
/
/
/&.{(
Time
b0.°1
^.<&-
<&.&<+-
6-e^
Final
/
/
/
.&?-
Injection
rate,
cc/min
X^-^7^
Injection
time, min
2-
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date
Injection location
Barometric
Operator
J3o. (6 in.Hg Ambient temperature, °F
Regulator pressure
psi
Time
(24-h)
/^/^
Calibration data
Bubble meter rate, cc/min
Time
^,^-5"
*X3<>
3?. 15.
^32-
Initial
S
/^
/
/0,/i
Time
^^^,cf&
5f.o5-
5-? <^
5-SfV-
Final
X
x^
X"
/0-/X
Average
/
/€>*/¥-
Injection
rate,
cc/min
/#>/^
Injection
time, min
^^ c?
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-142
-------
SF6 TRACER GAS INJECTION DATA
RUN NO.
Date
Plant
Injection location
Barometric
Operator
A
. /O
in.Hg
Ambient temperature, °F
Regulator pressure
Time
(24-h)
tftl
Cal ibration data
Time
Z2 ?&
22. 1)
21 &
ZZ^e
Bubble meter rate, cc/min
Initial
/
/
/
2-&,tv
Time
26,34
2^.53
^5,^Z
•zs.v-o
Final
Z3.42-
Average
2^^(
Injection
rate,
cc/mi n
Z^^'
Injection
time, min
/^f, ^
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-143
-------
Date
Injection location
X"
Barometric/pfessu/e
Operator
SF6 TRACER GAS INJECTION DATA
RUN NO.
Plant
• / O
in.Hg Ambient temperature, °F
Regulator pressure
psi
Time
(24-h)
/?tt
Cal ibration data
Bubble meter rate, cc/min
Time
M
tw
nn-
/'(,?&
Initial
^
/
/
3c>yk
Time
tftf
/4M
tf,^
W,t2>
Final
/
/
/
SOtt
Average
-$& ^
Injection
rate,
cc/min
2>c (c~)r
Injection
time, min
y»?,o
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-144
-------
Date
SF, TRACER GAS INJECTION DATA
D
RUN
Plant
Injection location L\lcx-c>A/5T/?e~r/4-ts(-1
Barometric pressure J$<^ / O
Operator C_-/^fe
/
£~
in.Hg Ambient temperature, °F
5&
/^^5
/^^
Initial /
/
/
3c^
Time
/^^
/^^/
/^/=?2_
/^^^
Final
/
/
/
3o,^?4-
^Average
f
^0.^ \
Injection
rate,
cc/min
2>0.^l
Injection
time, min
/$5>.O
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-145
-------
SFg TRACER GAS INJECTION DATA
RUN NO.
Date
Injection location
Barometric/pressure
Operator
- 2L&
in.Hg Ambient temperature, °F
Regulator pressure
psi
Time
(24-h)
tfw
Calibration data
Bubble meter rate, cc/min
Time
tf./3
/3.CS
J'),lt>
tf.n
Initial
/-
/
/
S\tf
-------
Date
SFC TRACER GAS INJECTION DATA
D
RUN NO.
Plant
ST
Injection location j
Barometric
Operate
ure
in.Hg Ambient temperature, °F
Regulator pressure
psi
Time
(24-h)
/C'^
Calibration data
Bubble meter rate, cc/min
Time
?v,(tf
70.^/
2 S.b '<-
•JCkt-
Initial
/
/
/
_^>S
^Time
2? &
7?,^
Zo.^-
2? 13o
Final
/
/
/
Z^.^5
Average
.?<3.^V
Injection
rate,
cc/min
? -, .^7V
Injection
time, min
W,o
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-147
-------
Date
SF6 TRACER GAS INJECTION DATA
RUN
Plant
Injection location
Barometric
Operator'
CutXA/tJ -J-
in.Hg
Ambient temperature,
Regulator pr/ssure
psi
Time
(24-h)
/f^3
f
Calibration data
Bubble meter rate, cc/min
Time
-10^
tc-bl
•20bD
?o^\
Initial
/
/
X
^."7?
Time
/&*?'
/^.^
/f3^
fazb
Final
/
/
/
3?.?t
Average
30. 7*
Injection
rate,
cc/min
Tn.1*-
Injection
time, min
££.o
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-148
-------
SFg TRACER GAS INJECTION DATA
RUN NO.
Date
Plant
Injection location
Barometric pressure
Operator
in.Hg Ambient temperature, °F
Regulator pressure
psi
Time
(24-h)
Calibration data
Time
Bubble meter rate, cc/min
Initial
Time
Final
Average
Injection
time, min
503- Z-
A
Note:
ThP tracer qas injection rate is set immediately before the actual source
niection and checked at the end of the source injection. The source
niction rate is the average of initial and final.
B-149
-------
Date
SF6 TRACER GAS INJECTION DATA
RUN NO.
Plant
Injection location
Barometric pressure
Operator
l-T-P^T t-/
in.Hg Ambient temperature, °F
.
Regulator pressure
Time
(24-h)
'r- -z,
— - *— it
^y-'i
L '/' 2
.'/- ?
,v f
Calibration data
Bubble meter rate, cc/min
Time
-jpi^
a - -
/r :'S
f. 7V,
///
^
M
^/f
I
Initial
X
/
/
Z'/"-53
(-If)
(cC1
fcl
&(
^
Time
/^.•??
/5,5r
X-5.57-
(5,(-l
Final
3^,^
Average
3*/.cr /
Injection
rate,
cc/min
3^ ^ /
Injection
time, min
34-^-^
Note: The tracer gas injection rate is set immediately before the actual source
injection and checked at the end of the source injection. The source
injection rate is the average of initial and final.
B-150
-------