Deethanizer Overhead Separator F-513 <35>
<34>
F-514
<36>
*etela elar 1ari e3ri!erant *stem pa1a s -##.##o' pa1a pa1a ali alira ran n terb terben ent t 1a 1a 3ase 3ase,, ma ma memisaan pro1 Ammonia pro1 Ammonia liquid 1an 1an vapor Komposisi vapor 1an liquid 1an liquid 1apat 1apat 1ietai 1en!an ara berit ini + (o')= P (bar) = zi =
-70.46 27.58
o
' bar
= =
202.69 2758
mol/total mol
Komponen
Massa (!) "#4$
%M
mol
2
62.&029
28
2.2&79607
'2
&4&4.6089
#2.&50202#
'4
968&.5864
44 &6
605.099&500
'26
7#84.4057
#0
246.&468567
'#8
2.9705
0.0675&&4
i-'4&0
0.00#4
44 58
n-'4&0
0.0002
2* 2 +otal
0.0000586 0.00000#4
0.#&76
58 #4.08
0.4#65
&8
0.0242500
&8,546.4
en!an men!naan persamaan antoine
0.009#&92 885.7
Komponen
a
b
2
#5.4
-966.2
0
'2
&##.6
-47#5.0
0
'4
#&.#5
-.52
0
'26
44.0&0#
-2568.8
0
'#8
52.#785
-#490.6
0
i-'4&0
58.8
-4.7
0
n-'4&0
66.945
-4604.&
0
2*
78.7
-#8#9.9
0
2
65.9
-7227.5
0
en!an nilai a,b,,1,e,3 1ietai 1ari literatr Maa sesai 1en!an rms antoine 1iatas 1i1apatan Komponen 2
ln Psat
Psat (Kpa) &0.96 5778#.#8500&685
'2
5.59
'4
8.78 65#2.62006945&9
'26
5.5&
246.0524455#0#
'#8
#.&7
2#.789800427#
i-'4&0
&.05
2.86769#0
n-'4&0
0.86
2.#5844#9&28
2*
4.07
58.#452425409
2
-7.69
0.0004590847
267.&474062#9
en!an persamaan &&.65 *mit an ess 6t e1 1apat 1iari nilai oe3isien 3!asit
Tc (K)
Bo
Tr
2
&26.&5
&.6&
-0.&&
'2
#04.2
0.67
-0.7#
'4
&90.6
&.06
-0.#0
'26
#05.#
0.66
-0.7#
'#8
#69.8
0.55
-&.02
i-'4&0
408.&
0.50
-&.2&
n-'4&0
425.&
0.48
-&.#0
2*
#7#.5
0.54
-&.04
2
Komponen 2
647.&
Pc(bar)
0.#&
Pr
-2.62
ω
##.94
0.8&
0.04
'2
7#.8#
0.#7
0.22
'4
45.99
0.60
0.0&2
'26
48.72
0.57
0.&0
'#8
42.48
0.65
0.&52
i-'4&0
#6.48
0.76
0.&8
n-'4&0
#7.96
0.7#
0.20
2*
89.6#
0.#&
0.09
2
220.55
0.&#
0.25
*elan:tna men!itn! Ki masin!-masin! omponen 1en!an persamaan berit. oe3isien ati;itas = &
Maa 1iperole asil, Komponen 2
Ki 20.95&&9&08&&
'2
0.0968627289
'4
2.#686077&&9
'26
0.0892&40847
'#8
0.00862574#4
i-'4&0
0.00&0#97727
n-'4&0
0.000855&28#
2*
0.02&&549&0#
2
&.6645566#8-007
Komponen 2
0.00456777&2
'2
0.0066928652
'4
0.94&&782#74
'26
0.047559#022
'#8
&.#72722&28-006
i-'4&0
&.448868225-0&0
n-'4&0
7.0&070#564-0&2
2*
4.584278628-007
+rial
2
9.606&59&&9-0&2
mla
&.000000007#
asil
7.29440#970-009
Maa 1ietai nilai = > < =& <=&- <= 0.474424
0.525576
Ant men!etai omposisi vapor 1an liquid masin!-masin! omponen 1apat me
Komponen 2
i
?i
0.00456777&2
0.0002&80&96
'2
0.0066928652
0.069096#9#2
'4
0.94&&782#74
0.#97#550507
'26
0.047559#022
0.5##09&858#
'#8
&.#72722&28-006
0.000&59&425
i-'4&0
&.448868225-0&0 &.#9#447&&8-007
n-'4&0
7.0&070#564-0&2 8.&984228#5-009
2*
4.584278628-007
0.00002&67
2
9.606&59&&9-0&2
0.0000577&
0
&
&
Maa 1apat 1ietai omposisi mol vapor 1an liquid pa1a flash drum Tabe !"3# Komposisi Mol Ammonia Flash Drum BB Komponen
apor
i
mol
?i
2
0.00
0.00
0.0002&80&96
2
0.0&
0.00
0.069096#9#2
#
0.94
0.00
0.#97#6
&
465.5&
0
Komposisi massa vapor 1an liquid pa1a 3las 1rm Tabe !"35 Komposisi Massa Ammonia Flash Drum %M
Komponen
Mas (!)
apor (!)
"24$
"25$
28
2
62.&
0.0
2
2
&,4&4.6
0.0
&7.0#
#
9,68&.6
0.0
++<
&&,&58.#
0.0
&&,&58.#
0.
a 1ibtan Flash Drum nt
K Kpa
zi 0.0025 0.0#6# 0.68#2 0.2779 0.000& 0.0000 0.0000 0.0000 0.0000 &.0000
1
e
3
-4.#&849
0.000079#&9
2
-2&.267
0.0409&
&
-#.26
0.0000294&8
2
-4.976#5
&.46447-005
2
-6.&0875
&.&&869-005
2
-7.&066
&.0#662-005
2
-8.2549&
&.&5706-005
2
-&&.&99
0.0&8848
&
-7.&7695
4.0#&#-006
2
s
B1
0.&2 -0.8& 0.0& -0.82 -2.0& -#.&& -#.72 -2.&0
-22.40
n $%&i'ita'
$%&i'ita'
-0.056
0.95
-0.508
0.60
-0.&69
0.84
-0.692
0.50
-&.572
0.2&
-2.699
0.07
-#.&&&
0.04
-0.70&
0.50
-#.#09
0.04
smsi lartan i1eal maa
0.525576#7&4
!!naan persamaan
i1 mol 0.0 0 0.0 420.2
B
0.0 0 0.0 0.0
