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"O-------- . Note';.--The four.: .data". pOTn'tS-bel owrwere_ort itheTSamerba sd sra j
--.-- j--a boveexcept-tha t-the-fOg-i n 'Cfise-X-I-was- set-at-5-vo -T-%-
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~V01j.UHE"% i chlor; HATED; 0 EGAN | CSMNfP E R/XftEu "PHASE 13CTTOOVEHOENIti:
44-
ii 'i' -10-
mi T
xim mi SL 050401
PPG Industries, Inc, Industrial Chemical Division Lake Charles, Louisiana
SERVICE
TB Chemicals
INDUSTRIES
PROCESS CALCULATIONS
By gMH
Job F-457
Dote -/?-76 Pane 12 of
EQUIP. NO.
Several waricvfians o'? Core XI in -4ie merno oP Alovepnber 4, is>v mere consiie< to tie+ermine -Wie e-PTec^ o-T change? marfe m Jh* e<ncen4Ta+ons o*P Co ^ oL and chlorinated otqcm-iics m the mixhife on 4he amovM of1 methane oddi-han HcessAr'* *fe produce o -foot *"*cV rort- eyplarivp moc-hjre m J4e P/T Phare X MCI abrarfec*' ven4-
-ftrrf fe4
variahanj- mver+i^c4ed the e-Pfe^tr o-P chcu-girg -He xigeH can cpn
4^Cthon iin -hv<? f/T ffoc-hx recondar-V) COn^enJpv i/e*4 (J25CV,).
CD /,, 5vb)%oziMescv
Tvol.Sf^mRSCV
9rot0/. a,.n nscv
mole/hr n*ole%
moleAt*- mole %
mde/V *ale%
CO
12.6
12.6
Ml
15.0
3.l
Ot
11.7
11.7
C0t 57.2 574
12.6 8.3 16.4 S7.2
12.6 83 16.5 57.4
12.6
3.6 21.1 57.2
12.6
3.6 2I.Z 57.4
P/T Phare I UCI ofcsorber *>+ analyses
d.o^.
5.2 5.2
S.Z 5.2
5.2 5.2
4Ja)
95.7
99-1
99n
() Hiis i Care xi. The 4CI in the P/r RScv mas S4.d wft4 Or- 59.1 TPP
In 4fcye carer c\?*ne the total males m the P/f ft'Scv vf>r* he*d constant
adjiffhng the nih-agen ooncv?4mftQii 4 make
the mereare or- deeveare m O^..
TV>e reronci s4 Orp variation r ,vivolvp? 4-he et-fects oT changing the Co ronee*v+m-Konj keeping -Wift total male! m 4he 4o4al moles In the T/T RScU conrtant V^, a4ju*Anj
the H\ concentrations
CO
Nj Oz CO, d.arg.
P/T Phare I HCf Atroche <- Vent
CD'"
moie/h r Wolf Ti
wale/hir WO)y.
wole /lir moieTi
12.6 12.6
15-0 15.1
9.0 9.0
i3.o 13.1
10.6 10.6
(6.6 16.7
M.7 11.7
11.7 II.7
11.7 H.7
57.2 57.4
57.2 57.4
57.X 57.4
5.2 5.2
5.2 5.2
5.2 5.2
i
mde/hr fM0l% 5.o 5.0
20.6 U.7 57.2
5.2
20.7 11.7 57.4 5.2
total
99.7
<0 Hus is care xi
99.7
99.7
99.7
SL 050403
E0-7(
PPG Industries, Inc. Industrial Chemical Division Lake Charles, Louisiana
SERVICE
Chemicals
INDUSTRIES
PROCESS CALCULATIONS
Ry emH
Job MSn
Date M-is-76 page
of
EQUIP. NO.
Hie n*x4 *e4 o voria+ions involves
e-COcte of chang-*^ He CO roncerctro.'han*
while Vteep'^S H1 moles/W Nv,Co*.aiA ckl.aij. cons-lan*.
There^orti, He 4oVo.\ moles
4rW' +he P/T f^-'SCV smi)> cticxe. Ho*ievpv; Ov wof Vcepf cA- +bp some eo*nf Allan aj Cos* /W
CO
Nt Oi. Co2 Cl-Aig.
P/T 0)
molt/W 12.6 13.0 H.7 57.2 S.2
maleV* 12.6 13.1 11.7 57.4 5.2
Phase X MCI Abfarbe*' Vent"
irtaifyV 15.0
13.0
male 7* 14.6 12.7
*xatePhv mole Yo p.O S.4 13.0 rj.&
12.0 M.7
11.2 |.7
57. Z 5.2
55S> 5.1
57.2 5.2
59.9 54
*nolei4v S.O 17.0 IO.fe 57.2 5.2
male T 5.5 14.7 M.7
528 5.7
99.7
102.4
95.6
91.0
^ 4tu is ease XI
Hip ne*4 vorio^ioo aw^med 4he co*po*i*+io*\ of vanalion vihich IS:
(JS>
CO Nv
l COi Cl .0/5. c4
mole/o 9J2 13.20 11-36
58.14
.24 2 J>4
The ne>4 voi'io'hon to l.o vnale/h*" "the
H>e Ni.
CO
Nv o,. cot
ct-oj.
/naleA. 17.6
14.0 11.7 572 4.2
motet''* 12.6 >4.1 11 .7 574 4.2
P/T Phase X PCI ahsorho*- vn4
common explosive li*n,+^
-toAa.1
99.7
.SL 050404
F0-7
PPG Industries, Inc. Industrial Chemical Division Lake Charles, Louisiana
SERVICE
Chtmiealc
industries
PROCESS CALCULATIONS By ______ Job P-4S7 Date D-is-?fa Page 14 of
EQUIP. NO.
The nex+
of Voriahon? imolwt <*ijvf+ing 4ke c hlovmaVed
Concrn-VruAiooS oAMe Iteepms -the -M-al
tOnshkn-b
eervfrahion
organic ( V>b
CPC 3 ni-Wojeo cOn-
CO Kx Ox
coi O.o^.
ntale/hr aa|*y*
(26
12.6
i?.o
13.1
11.7
11.7
67.2 57.4
5.2
6.2
Phase X MO Absorbe** Vd4
molftfir
12.6
12.6
male/hr maleTa
12.6
12.6
16.2
163
10.2
03
11.7 57.2
2.0
11.7 57.4
Z.O
U.7 67.1
8.0
11.7 57.4
80
|K<Mh* 12.6
7.2 11.7 67.2 M.o
mole% 12.6
1Z 11.7 674
II. J
@
mole K 12.6 17.3 11.7 67.4
l.o
4ofal
99.7
10 4,h, ; S Oise *1
$9.7
99.7
99.7
99*7 males ht<
The nc*^ *'*' of Vorm+ionr 15 -HP Saw as 4he -fit-S-f- -three varicihont
OjJ e/cffft H'lah A( MCI in Aa P/T R.SCV U
4o tc 75 7PD. The went"
from -the MCI abrovbev J-hereb^ changed yince -Hie
eon+en+ af dh Ptt RSCV
IS *e+ a* 5 voLTaf-fo*- case Xl) and onl*^ ",4 is varied -ft**- 4ho odhfir ea.se r.
CO Ml Oi CO^ cl.0^.
-Mai
CO r4i Ol CoL
tarfe.1
(D WOle/V MOlfli
12.5 13.0 11.7 57.2
5.2
12.6 13.1 11.7 57.45.2
99.7
toiole/hv* male % ^5v0lV-OtinftSCV>
14.5 14.6 9.2 9.2 13.6 13.6 57.2 57.4 5-2 5.2
rnole/V maleY.
(7<>|%axmffSC'/)
14.6 14.6
3.8 19-0
3.8 19.1
57.2 57.4
5.2 5.2
99.7
99.7
Vnole/V Omle% (avoiy.Oj ivsiscv)
14.5 14.5
l.l 1.1
21.7 57.2
21.8 57.4
5.2 5.2
99.7
(3VO)*40imfZ?CVj
mol&V 14.5 14.7 e.i 57.2 6.2
niolit. 14.5 14.8 8.1
57.4 6.2
99.7
<0 4W ir rose X| wt|L 59.1 TPP MCI m KCV
Ad >4W rases have 75 TPO e\ ffSCV N;_ v*es varied 4a Veep 4a4a) r>s^et c^\yh?n+. Po* coses IS-18 fhe "hs4c.l melfs m Jhe P/T JV3CV v<ay *sh a* 17Ml of* which 171.4 male/ we^ MCI .
st *>0.,
ED"7(
PPG Industries, Inc. Industrial Chemical Division Lake Charles, Louisiana
SERVICE
Chemicalc
INDUSTRIES
pKUOC-ii
By EMU Date
UHLUUlhi IWIVO
Job P-4S7 Page 15 of
EQUIP. NO.
The -fbllaiMing add* 4*oeal He<na4n#f we<t rJ*N | pleVe
do.4. nfeW*r^ H on*
CO
pi O*. Co Cl.org.
molt % 7.0 18.7 11.7
5?.4
5.2
ole% 4.0
21.7 11.7 57.4 5.2
P/T fW I UCl Afc*o.'^OT Vfht
@U?
(V
12.6 17.8 M.7 574
.5
male 9^ 12.6 17.56
11.7 57.4
.75
wialeK 14.0 15.4 11.7 57.4
.5
male
45 21.2 11.7 57A
.2
<Z>
*no*r7. 17.6 15.3 11.7 57.4 3.0
moleX> *2.4,
12.3 11.7 57.4 6.0
*P- Basiy" *** ol+'ra,+iwey 4 HrowgV 6
<*> -Tor `
*c< altfma4wr 12 -Hiraigk 14
CV -IHes V4QJ a ffetia) aMernodvre in wW*cV He cc war edjvs^ei Upv*ar4
He mix t-rt -flan*<*able ^4 cnl<^ O.S
cVtlarincAed 0<jjiMCT s
CUq aidi'ho*' Cow Id Lf cWfcUec* CtV low* Organic Con ccnVroi.4ior>c.
+ Veep JVw*
All a^tve o!4-evr>c.4vpr (20-r?) ron-Vamed 5sn wolf.
Fr<y* previous ccdcolahcms i+ *is cfeHrmined Ha4 since He venf <Pi#n He UCl abrovVer
condenro^ Cuc Recover vrr.4) was more lean m-fiieI i4- neared lets oxygen +* prod-**
expioxiwe mix'W. TVieced*o<e , da.4a Pe4c vere ^eneraHd -from* o^evooVivey 2 (59.1 TPD UCl In P/T PSCV) end Ifa (7STtt> UCl in P/T RSeV.), wihicb COn-Wed 7 Vol.Y* O* lrs
He P/T R.5CV . Triese doVa Jg+s faUeYtahwpj ) vtpre enen*4ed
verging Hp mole*>
Oir^Oic5 condenjed |am H? PCI <;fc>SOvV>e- ven-V ,n He Te^rigeraW COrvJen/ev. Xr\
PhojC I dejign:
mole% condensed *
mole/Wr condensed ^ , Oo mole/V- ewVfrn$
X (ao =. 21.0 5.7
2> COndCnfcd
CO
Ox Cov d.or^
n*ale/Ji<r *4.5 3.8 19.0
57.2 4.11
*4.7 3.8
19.3 59.0
4.2
P/T MCI Recov^ru
@
30*t'JcTo cmJeiidl
Aislr/A. 14.5 3.8
maleY4.8 3.9
10.0 19.3
57.2 sa?
3.54 3.7
Vend- f AI4.16 feast?) @
46 molrY. condensed
mole/hr molcTo
14.5
14.8
3.8 3.9
19.0
19.5
57.2
58.8
2.86 3.0
doial 98.fci
98.14
1__________ ______ _______ ___________ _____
97.3fe
60 ma'eVa rand On
male/hr mate*
14.5
15,0
3.8 19.0 51. Z 2.o8
3.9 19.7
59.2 2.2
96.58
SL 050406
E0" 7
PPG Industries, Inc. Industrial Chemical Division Lake Charles, Louisiana
SERVICE
VS?
INDUSTRIES
PROCESS CALCULATIONS By ErttHJob P-4S7 Date U-ifl*76 Page ^ 6 of
EQUIP. NO.
2| inilt TC MivjfnriA
molo^hr tnaleIC
CO
12-6
12.8
Ni 8.3 8-4
Oi
16.4
16.6
CC^
67.2
58.0
cl^.
4.11
4.2
Wal
98.6/
P/T MCI Recovery \Je+faW, 2 basis,?
*3> 30 male Y. Cwlrr>JJ
'ey 4S *.*!? HL oart4w*eA
12.6 8.3 16.4 57.2 364
12.8 8.5 16.7 68.3 3.7
tn ale/hr 12.6 8.3 164 57.2
2.86
maleY* J2.9 8.5 16.8 588
30
58.14
57.36
40 mJirY- CwAtdfl
idMw 12.6
e.7
t ir. 13.0
8.6
|6.4
n.o
57.2
59.2
2.08 2.2
56.S8
The
Qnol^yi5 gar ure4 4< de+e'i'twne vAucW aUyoV\ver jbouU le vr^l -hs re+
CH$, a<><li4ic*\ rel*.
AU?rnclivf 2 ; 8.U> vo|Y* a-f Jk* /let ak}a<lr^ ve^ * CIVq. cAArhon rale
- (.QS2Pj(py.7 molfs/UrO(379 sc4/W.o)e,? Go (tot/W
- 52.2 sc4*" CH*
AllfrAolm 32- ^37 vol^i orP Jkf MC\ Recovery Ve*4 * Cite- addthvf' ro^ie
AtiA|4ior\ - (.O977)(0a.Gt twole/b*X?7> fcf/tx.ailg ) Go h
= 58.0 Tc-f'w'
4Vn*>> Alt. 2
,( Go rtr* /kr)(5t.t. ICp/wn ) ( 375> ScP/wo'? ->Cs>8.Cl <*le/W?
JoO? - 9T87.
XRe ua
HK^'TrrVj Vf
"There fii*' / -Pt>v\ 44>e$e hwa c4 Verno4ivres i+- cars tf reeiN J'hosV rr>^e CWe. ctW4ion
it rexju\rcA 4o
Vj, net fteccsve*^ vev'4 rovi-xy>tojiue i.f-'ii0/*) M->a4 <s
ire<$uire.A 4a wvaL-e l4\e MCI AW sorter versV **-xflanre ( 8.2ft VO
Ucmce,
alle^na'hvps rwr a*. 4V\ ACl R.e<ji*iftv^
Wo u*eA 4-o 4*Vev>~v** Ctt^. oAtlvkai
Die faMov.iisj 4a\>le *yL CI+4 o^Ai^iort
ca^M-h/sey vicvtawT banr, alWnaWi d e4e**rrn CW< eiMi'Kan awi pir0e)Mte o* a**T * tlftmwftlblf rr\* 4u^e.
SL 050407
ED-7(
PPG Inaustries, Inc. Industrial Chemical Division Lake Charles, Louisiana
SERVICE
Chemicals
INDUSTRIES
rr\uc.c.oo i<hluulhi iuuo
By gfltti
Job r-isn
Dote M-S>-7fa Page.
of
EQUIP. NO.
Table 1 . CH4 Addfhon -hi produce tJoM.'flowwablt Mrrt+urer 1* P/T PPajq JT 4CI Recovery Ve*4
6e+
P/T RSCV Vol.%Ot TPDHCI
mole% organics condensed frorn HC1 absorber verf
Al+efna+ive Oiei +0
de+ernime CHt odd rfiorv
HCi Recover Ve+
CHc addi+ic
Seem
vol.VaCHs odd/tion 5CPM
A 7 75 B 7 75
C 7 75
D 7 75
E 7 59.1
P 7 55.1 G 7 59.1
H 7 59.1
X & 75
J&
75
K5
59.1
L5
59.1
21 30 45 50 21 30
45 60
21 30 21 30
28
623
(4.95
93
29
620
14.95
92
30
6(5
16.10
99
31
610
17.26
105
32
623
9.37
58
33
620
10.46
65
34
615
11.57
71
35
610
12.68
77
38
623
5.o
32
39
620
5.10
32
36
623
3.03
19
37
620
406
26
The -followmg -fe^jr oojes, Dibich cure w eluded m -H** aVove
wgff rvry V>c.je<4 o~
^I'leriNoAwK I Oni IS^ VjVitch CSrA-cmeci s VO I ./ C\ frt J+>e P/T P-SCV/ o\ 21
2a orjon 1 cf
i?w> J4p PCI abj^rlpt- veTo'f
AH: 1 bay 13
21 mle^
fifed
woleAuf nfaie^e
CO 12.6 17 .S
Nr 13.0 13.1
Or
11.7
11.9
COr 57.2 58.0
c\.or^. 4.11
4.2
P/t MCI eco\jcr^ Yem4
7 0 COndenye^
mote/nr matey.
17.6
17.8
17,0
13.3
11.7 S7.2
3.44
11.9 58.3
3.7
A Hr. ,s
% 21 f**leY* ca.i\dfriJeA.
rodte/V yytGiefl
14.S
14.7
9.2 93
13.6
13.8
SIX 4,it
58.0 4.2
30vH<te7a Conc-CnfCxi
rnaleA' 14 .S 9.2 13.6 57.2
3.C4
t4.8 9.4 l?.S 58-3 3.7
-W-cl 8.61
98.14
Pd.61
98.14
SL 050408
CD- 7i
r-rb industries, mu. Industrial Chemical Division Lake Charles, Louisiana
SERVICE EQUIP. NO.
Chemicals
INDUSTRIES
By-R/rtM
Job P-45'7
Date 11 -i5>-~>fa Page "* ^of
The -pollening ona.1^1 IS waV uied + cJe4*'mii^ -^if 7L CQrAe"feA
-firttw Hie
MCI
uent- *ba<<y'* -Ha+ rWaijii le c/ceA +<* *e+
CM4 cAArh** .Ve.
Comput-**" frarr*\ CMZl.4 Wj ujcA -ha C&\Ci/t<Ue J/k arvio^irv^ C r^amc*
cr\denxej 4vtsw fhe MCI Qbyov-bev- ven^ w CUy? XI C let analv|?$
6-4-TS
ct- 9-'ia -- see p. to o-P MtevMo or. P*o*r x V*C*
<io.LeA 11-4-76 0.
CO Nr
Ov COj.
WjO VC EC VDC 4rany
cr TE.I Pffi
itrf.y* 4Vo-- MCI ftbyarter
83 8.4 B.8 55.5 24 1-0
.1
2-? 3.8 7.1 2.7
.6
lb/V>r/K mole 1* ftom obyorbe^ UCI absorbed v*r
11.54\l.C%
334 338
U.O?
3S4
S4.4S S.37
3356 57
.64 40
.06 4
.96 93
I.S8 87
IS? 84
.83 |o5
.IS IS
wt>% I* l(|Uli 6>*
.4S .10 4-53 13.11 to.34 36.33 9.05
. lb/bv
nlf/|' *> hj | Ablr -
mole/Hv
CftoienfvA War v*nb^ tur^t kffc
l .64 .ol
- <C6
--
IZ .96 .11
34 i.sa .35 17 .87 .79 67 .83 .SI 13 .15 .14
Wet
4ol7
Js4(0 S.o9
141
(? C3> vAV. c^W^eA <CV\lb4J
357 Ib/h*- - (2S70C-3SS9+ .<^4s) - 164 lt*V
(4ol?lb/W )/C^.Tm lb/w*%l<0 = [Ou WvW/6r m WCI 0.t3**rb*v
The**
1.41 nt^lr/bv ^ )oq S-<*5 r4eAf
- 78 mole 7* otjovmcs iv* ttCl Writer V'CwV co*Ae*vS*<
Frtoiv* 4ite afoove analysis. aanr)^ec<r+ior U*e basts user*
c.lco\ati/ir (see
(nemo *"
J Cr-4 P/T fea-H<A `Ao-'Va, 54t F CU-iA L UJfurc AvO.V*r\ 10
Figav
4 veprereo'V CM4 oA<J+r<m W-es -Gw- -Wa PWo-re X IACI
C+tt 4Ve wet ab<rfaer> boyeA cm 7 - s vbt.V- ox^e* m -We P/T 2-rcv, resPe-
4ivrl^. DcrVa -Par -Wiese ctrvey
-VUe A^rec-VU^ ***, TaWe
SL 050409
E0'7
Table 2 . PARTIAL CONDENSER DATA FOR CASE XI - P/T PHASE I HCL ABSORBER VENT
PRESSURE
DEW POINT
BUBBLE POINT
T ItWK. 1NLKtMtN1b
? FINAL TEMPERATURE ] VAPOR CONDENSED
22.7 114.1 -204.0
10.0 40.0 6.39
PSIA DEG.F. DEG.F.
UtCiih
DEG.F. WT. %
J COMPONENT 1
7
t CO NITROGEN 10 OXYGEN
- ii C02
u WATER VC
i EC ,s VDC ii TRANS J i? C I S
it TRI
17 PER
VAPOR FEED MOLE FR. WEIGHT FR.
0.1194 0.1208 0.1107 0.5445 0.0537 0.0064 0.0006 0.0096 0.0158 0.0087 0.0083 0.0015
0.0830 0.0840 0 0880 0.5950 0.0240 0.0100 0.0010 0.0230 0.0380 0.0210 0.0270 0.0060
LIQUID OUT MOLE FR. WEIGHT FR.
0.0005 0.0002 0.0002 0.0035 0.7774 0.0028 0.0006 0.0184 0.0532 0.0419 0.0788 0.0215
0.0004 0.0002 0.0002* 0.0039 0.3559 0.0045 0.0010 0.0453 0.1311 0.1034 0.2633 0.0909
VAPOR OUT MOLE FR. WEIGHT FR
0.1277 0.1293 0.1185 0.5825 0.0029 0.0067 0.0006 0.0090 0.0132 0.0064 0.0033 0.0000
0.0886 0.0897 ~ 0.0940" 0.6354
0.0013 0.0104
0.0010 0.0215 0.0316 0.0154 0.0108 0.0002
p i Jl :?
MOL. WT. DENSITY AT
| n 60 DEGF
i*
} . 15
n i'~ ________________
i 21
j?
30
40.26 lb/mole 0.1121 "LB/CU.FT.
' ----3--9---.-3--1.. LB/--M-DL---E-----------
40.33 LB/MDLE 0.1123 LB/CU.FT
1 if
1 f 1
Aj J j
*
Z R I E N! i PEP
ft. h-
r Hr!;:e i H I!_ SB COP E'EF VE NT-r iZPT DI L'JENT
V z. : id N 3 - MPY 19'3 -
_t: S - C'JFATE "NLV ST 7~ - hNI- 1 SIX
THI : i ; HU 31 z'
: tv sr : SM=
ZONTAI NIMG C03
: iu I c 0` 1L'- ` !=-02. D-'rs i : P`~ Z. _ E NTL S V 3 I . SI : thi: MILL
IM - LR ,, z[ OF :02- 2 I:-sts PEC ULT WILL. BE :on:' EPV RT IV t " INC E :02 I . S MUCH B ETTEF
EE UZED PETAPDANT
******************* ********************
*****-FAc TriM=,LE IC EXPLETIVE PEP S*****
* * * 4- ***********************
GAS SAMPLE UNDER ANALYSIS
COMPONENT
CO EDC
02 C02
N3 FUEL INERT OXIDIZER
PE-13 '.CAMPLE XTYF 11.10
4.70
11.3 0
37.70 14.70
13.30 73.40 11.30
OXY FREE
XSAMPLE MYFE
13.5?
5. 33
0. 0
35.43
13.37
17. 31
33. 03
0. 0
FUEL ONLY
FUEL'-.
70. 35
33.75
0. 0 0. 0 0. 0
MUTE: HCL 13 CONSIDERED S3 M3 SMIi CL 13 CONSIDERED Si 02
DEW POINT -- 33.33- F ST 34.70 Pi IS PELRTI VE VOLUME OF PAIRED FUELS - 143.33 \
PIS Inal gas sample LDUEF EXPLOSIVE LIMITS J- P'E P EXPLOSIVE LIMITS CUMMITH EXPLOSIVE LIMITS
'.FUEL 10. 03 13.33 10.34
'.OXIDIZER 43.73 3.33 3. 03
r UEL 3 ONLY IN 03 LD'-'E^ explosive limits UP r EPs EXPLOSIVE LIMITS
`.FUEL '.OXIDIZER
10.54
33. 43
73.35
20.35
-0. 03 C'J FT DILUTION OXIDANT PEP CU FT ORIGINAL GAS
MILL PRODUCE
0.?7 CU FT UPPER EXPLOSIVE LIMIT MIXTURE
0.57 CU FT DILUTION OXIDANT PER CU FT ORIGINAL GAS
UILi_ -r'OD'J_E
1.1-7 CU FT LOWER EXPLOC-IVE LIMIT MIXTURE
* -5S3 ISMF'LE 13 INCSFSELE OF BECOMING EXPLOSIVE WITHOUT THE ADDITION OP FUEL-*****
BY THE ADDITION OF 30.32 X GAS OF FOLLOWING MOLE FRACTION****
C3H2 C2H4 CH4 EDC COS
0.0 0.0 0.0 0.0 0.0
C3H3 C3H3 ETCL SL2 HCL
0-0 0.0 0.0 0.0 0.0
C3H3 H3 CO 03 N2
0. 0 0. 0 0. 0 0. 0 1.0000
C RI-E SI PER " TP I FHnSE I iHCL ABSORBER VENT-INERT DILUENT
VERSION 3 - MAY 1373 - RESULTS A CCUR ATE ONLY AT 77 F AND 1
COMPOSITION OF NON-EXFLD SIV E DIL UTED GAS SAMPLE
COMPONENT
,30 EDC 03 COS N3 FUEL INEPT OXIDIZER
AS-IS '.SAMPLE '.TYPE
3.43 3.53 3. 03 44.11 34.30
12. 03 73. 30
3. 03
RIP- r PEE XSAM5LE '.TYRE 14* 31
6* 31 0. 0 77 * 51 1. 7
21.22 73.73
0. 0
FUEL ONLY F'UELX
70.25 23.75
0. 0 0. 0 0. 0
NOTE: HC L IS CONSIDEREDt RI N AND CL2 IS CONSIDERED AS 03
DEW POINT - 53.55 F AT 24.7 0i PSIA
63
SL 050411
SL 050412
-64-
' I ; fO KE
X UfF
to
F.L
T&OETc
Hs rEn
IN C H * 7 X 14 INCHES
CO. UIOEWUSA.
A* tCO nU "/7oQUn
TABLE
LIMIT MIXTURES FOR FUEL GASES IN AIR
FUEL GAS
EXPLOSIVE LIMITS IN AIR
LOWER
UPPER
XFUEL *02 XFUEL *02
NITROGEN AS INERT DILUENT
EXTINCTION CCMMON EXPLO LIMIT
RATIO XFUEL *FUEL SN2
XC2
CARBGN CIOXICE AS INERT DILUENT EXTINCTION COMMON EXPLC LIMIT RATIO XFUEL XFUEL XCC2 *02
C2H2
2.5C 20.AO 81.00 3.98 100.00 LOO.CO 100.00 100.00 100.00 100.CC 1CC.CC 100.00 100.00 ICO.00
C3H6
2. 40 20. A3 1C.30 18.77 1A.10 6.62 2.81 39.69 12.03 7.80 11.36 3.54 27.66 14.40
C3H0
2.2C 20.A7 9.50 18.9A 1A.6A 6.39 2.95 43.20 11.27 7.97 11.14 3.75 29.90 13.89
i C2H4
3.10 2C.2E 32.00 1A.23 15. AO 6.G9 3.06 47.24 10.40 9.10 9.90 4.26 38.74 11.93
C2H6
3.00 20.30 12.50 18.31 11.75 7.8A 3.56 41,8 A 11.43 7.40 11.90 4.25 31.45 13.46
H2 A.00 20.05 75.OC 5.23 16.55 5.69 A.30 71.20 5,14 10.20 8.92 5.31 54.19 8.48
CM
5.30 15.82 1A.CC 16.00
6.00 14.28 5.93 35.57 12.24 3.20 23.80 6.66 21.3* 15.07
ETCL
3.80 20.13 15.AO 17.71 100.OC 1C0.0G 100.00 100.00 100.00 100.00 100.00 100.00 >00.00 100.00
CO
12.50 18.31 7 A .OC 5.AA
A. 15 19. Al 13.. 78 57.22 6.07 2.16 31.64 18.35 39.65 8.79
EDC
6.20 19.63 16.00 17.58
A.3C IB. 86 7.36 31.6A 12.77 2.41 29.31 8.75 21.10 14.66
TABLE 2 - LIMIT MIXTURES FOR FUEL GASES IN CXYGEN
FUEL GAS
EXPLOSIVE LIMITS IN 02
LOWER
UPPER
XFUEL 102 XFUEL X02
NITRCGEN AS INERT DILUENT
EXTINCTION COMMON EXPLO LIMIT
RATIO XFUEL XFUEL XN2
IG2
CARBON CIOXICE AS INERT DILUENT EXTINCTION COMMON EXPLO LIMIT RATIO XFUEL XFUEL XC02 X02
C2F2 C3H6 C3H8 C2H4 C2F6 H2 CM ETCL CC
ECC
2.80 2.10 2.30 3.00 3.00 4.00 5.10 4.00 15.50 6.00
57.2C S7.SC S7.7C S7.CC S7.CC 56.CC S4.5C 56.CC 84.5C S4.00
94.CC 53.CO 55.CC 6C.CC 66.CO 54. CO 61.CC 67.CO 54.CC 56.CC
1.00 41.00 45.00 2C.C0 34.00
6.00 39.00 33.00
6.00 42.CO
ICO.00 30.31 29. C9 28.28 23.63 21.06 13.ec
100.CC 5.82
10.65
100.00 3. 19 3.32 3.42 4.C2 4.53 6.76
1CC.CC 14.67 8.43
100.00 2.81 2.95 3.C6 3.56 4.30 5.93
100.00 13.78 7.36
100.00 85.16 85.81 86.54 85.01 90,56
B1.B3 100.00
80.15 79.87
100.00 12.03 11.27 10.40 11.43 5.14 12.24
100.00 6.07
12.77
'
A VALUE OF EXACTLY 100.0 INDICATES THAT NO DATA IS AVAILABLE THIS WAS NECESSARY FOR PROGRAMMING REQUIREMENTS
65
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SL 05041A
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Tncin.\ye< T^ei
;
= CHo
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io,4? C^-isKi.d) M-53H t 14)
4 (.113)0.IS)] /.SG$ Ol= U,74 val.%
X -3
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SL 050415
OXYGEN X
n HI 12
INCINERATOR S/ENTS -- P^fsSE X Mc^ E-SGa^ERY B^-PAS^E^
FLOW* 135300 SCPH nN+T.
TOTAL. = 13578
o2= 533 4.0
ctm -
839
6.2
OTHET^ aE6 - IO 13
COt - 3602
7,5
26.5
INcR.Tr = 1336 3.8
WCI = &ZSO 46,0
trial. %
4.7 8.43.0 22.9 13.3 47.7
Moi.f0\ l* PIT M<
1 3 5 7 9
IWJ hr Oi t*
t IT rx.
Vo\,% Ol M 4u Inciripr;,
7 267 464 650 854
1.5 3.1 4.7 63
7.9
fcOvN - 135Soo sc?4 *4,4.
TOTA*-= IBS 78
Oc - 598 44 CtH4 = 635 4.7 otWcR.oB6= 1 O 13 7.5
CO5, = 5602 26.5 - io-so 10.9
MC - 6250 45.0
ral.%
5.2 63 3.0 22.9 14.8 47. S
1
1 3 5 7 S>
87 267 454 649 853
2.1
3.6 5.2
63 84
FLOW? IICBOOSCFH Totals I 1495 Ox' 507
CxUn ~ 635 OTHcROrj3= 1013
COi - 3602 IN5ETS= /5-71
MC 1 = 41 67
w4.%
44 5.6 S3 31.3 13.7 36.3
trial %
82 7.5 3.6 27.2 18.6 37.9
1
5 7 9
70 2 13 363 szo
6 SB
2.3
3,8 5.2 6.8 63
Flow- H4JQO SCf-i-1 TCtPlL ? 11495 Oi - 447 Cxl<4 = 839 02.67 lOto Coti 36oZ INcETS - 1427 MCI - 4167
3.9 7.3
83 31.3 12.4 36.3
mol.Ji
4.6 9.9 3.<o 27.1 16.9 __3__7_._9_ L
Flow? 5? 8<=o5CF(-/
TOTAU? 941 1
3 56 CiM*i = 83S) OTVttR 026- 10 13
35 3.9
to. 8
COi = 36 02 InERtt c 15 18 lA Cl = 2o33
33.3 I6.1 22. )
*-al V,
45 123 4.4 33.4 ^7 | 23.3
I 3 6 7
9
'
1 3 6 7 9
70 1.6 2 1 3 3.1 363 4.6 5 20 6.2 683 7-7
S2 t.s 160 3.2 272 45 339 6.0 5 it 7,5
SL 050416
