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7/26/2019 PROCESO TRITON CHEA FASE 1+2-FEEDGAS
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Stream (Summary) UOM FEEDGAS
Name FEEDGAS
Description FEEDGAS
Phase Mixed
Thermodynamic System SRK01
Total Molar Rate !"mol # day $%0&&0'(()*(&)
Total Mass Rate ! # day 1%&+,,$,'1$&((
Temperat-re . )1'*****%*
Press-re /ar (%'$
Total Molec-lar ei!ht )$'*&(+0011
Total Speciic Enthalpy 2 # ! ))%&*)'$%)&
Total .p cal#!"K 0
!"mol # day
.3) 111*$,'1(&1%, N) (+()'&$(%0+$&,
MET4ANE %(11)&'&+&+)(
ET4ANE )*,+1'%*,1$%)+
PR3PANE 1$101'0,))
567TANE (1,$'+101+&,1,
67TANE (1,$'+101+&,1,
5PENTANE 1$,)'1&++$+*1)
PENTANE 1$,)'1&++$+*1)
.,8 11*&',&0(%%1+(
.&8 $%,%'(+0%+&$)
4)3 100(('1,,(+(1,
raction
.3) 0')10*%1%+*&
N) 0'00*1)(00*
MET4ANE 0',()&0%0$**
ET4ANE 0'0$$*)1%(%%
PR3PANE 0'0)+($1)11,
567TANE 0'00&+(+,1
67TANE 0'00&+(+,1
5PENTANE 0'00)*(%))++
PENTANE 0'00)*(%))++
.,8 0'00))$,(&$(
.&8 0'01010$0+(*
4)3 0'01+*)%&(+&
9apor Molar Rate !"mol # day $0,+&$'$%($%1)
9apor Mass Rate ! # day 1)$)1$+*'+1*+(
9apor Molec-lar ei!ht )('&0%(+0%&
9apor Mole Fraction raction 0'*$(*+0&101
9apor Speciic Enthalpy 2 # ! )(11($'0$1$
9apor .P cal#!"K 0'(,(%)(10*,
Vapor Composition raction
.3) 0')1&*110%(1
N) 0'00*$%&1*** MET4ANE 0',,+++)&%,,
Total Molar ComponentRates
Total Molar ComponentFractions
7/26/2019 PROCESO TRITON CHEA FASE 1+2-FEEDGAS
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ET4ANE 0'0$,*$(,()%
PR3PANE 0'0)&$100%,
567TANE 0'00,*&1&+)$
67TANE 0'00,,11,0+)
5PENTANE 0'00)01)1+*%
PENTANE 0'001+(0&,((
.,8 0'000++0&&(1
.&8 0'000)+$%*0$
4)3 0'000,01+(1*
Vapor Component Rate !"mol # day
.3) 110($%'&&1*)%)
N) (+%('1&%%1)+,(
MET4ANE %%*0(0')*(,1&,
ET4ANE )++,+'*1(&&*+(
PR3PANE 1%*(('1,()1)+
567TANE %$%%'+)$*+)+1,
67TANE %%$1'),)($((*,
5PENTANE 101*'*)*$)(&,+
PENTANE *%%'0%+((%$+(
.,8 ((,'(()+$*$),(
.&8 1((',$&((&00(+
4)3 %0$'0$+*$0(0*,
Total :i;-id Molar Rate !"mol # day )%+*('*0+($0$,
Total :i;-id Mass Rate ! # day 1),$0,,'%$))++
Total :i;-id Molec-lar ei!ht $)'*()*)$)&
Total :i;-id Mole Fraction raction 0'0($01*)+**
Total :i;-id Speciic Enthalpy 2 # ! $)0%&'+0,%%Total :i;-id .P cal#!"K 0'$,,(()&$,+
Total Liui! Composition raction
.3) 0'10,0&1&&,$
N) 0'000,0$+(1$
MET4ANE 0'1(&%+),*
ET4ANE 0'0$&%,%%*$)
PR3PANE 0'0+1,+01(,%
567TANE 0'0((,1*+0(,
67TANE 0'0$&$0*)+,$
5PENTANE 0'0%+)+()&+,
PENTANE 0'0(((1*0)$( .,8 0'0$%0%+&11
.&8 0'%,+(,%101,
4)3 0'000$,1*()*
!"mol # day
.3) )$%('$&$%+*1)
N) 1('(&,$)&*$,)
MET4ANE %$)1',*$++%%)+
ET4ANE 1%&0',*%0&&%((
PR3PANE 1*$1'&%*,1&+)(
567TANE 10,,'1+,1($*$)
67TANE 1%&('1&*1%,&,+
5PENTANE *1('&**%%)&%,
PENTANE 10,1'%++$((+*,
Total Liui! ComponentRate
7/26/2019 PROCESO TRITON CHEA FASE 1+2-FEEDGAS
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.,8 1),&'%$$1(%$+(
.&8 ++0('%*)0&*0(
4)3 1%'()&$&%)(&(
:i;-d Molar Rate !"mol # day 1(1,%'&,01%&,
:i;-id .p cal#!"K 0'(*&%**,((+
:i;-id Molec-lar ei!ht &,'*%*&*(,%
:i;-id Mole Fraction raction 0'0),,+$)+()
:i;-id Molar Enthalpy 2 # !"mol %($(,*&'*((
Liui! Composition raction
.3) 0'10,0&1&&,$
N) 0'000,0$+(1$
MET4ANE 0'1(&%+),*
ET4ANE 0'0$&%,%%*$)
PR3PANE 0'0+1,+01(,%
567TANE 0'0((,1*+0(,
67TANE 0'0$&$0*)+,$
5PENTANE 0'0%+)+()&+,
PENTANE 0'0(((1*0)$(
.,8 0'0$%0%+&11
.&8 0'%,+(,%101,
4)3 0'000$,1*()*
Liui! Component Rate !"mol # day
.3) 1$0)'%&$1**+(
N) +'$+0**(1(+)
MET4ANE )0+&'(*%0,*0)(
ET4ANE +1)'(+1%&0,&$)
PR3PANE 11$,'+*+0001,
567TANE ,%1'*+()0*,%+(
67TANE +1('$(&&(0)0(+ 5PENTANE $()')(*%%*)(1,
PENTANE ,)*'1(0()111,+
.,8 &$1'))&$+0%*,+
.&8 $)1+'+))**0%,+
4)3 &'*$*))%*1%+
Decant ater Mole Rate !"mol # day *&%1'1(+%1)*,
1+'01$%
ater Mole Fraction raction 0'01+%%(00$&
Decant ater Molar Enthalpy 2 # !"mol 1&%,,,&'0,*Decant ater .p cal#!"K 0'**$,)&$&&(
Liui!" Composition raction
Liui!" Component Rate !"mol # day
Liui!# Composition raction
Liui!# Component Rate !"mol # day
Decant ater Molec-latei!ht