Gas Processing Simulation
Gas Processing Simulation
Gas Processing Simulation
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Instructor: Dr. Istadi (http://tekim.undip.ac.id/staf/istadi )<br />
Email: istadi@undip.ac.id
Software Simulasi<br />
• HYSYS<br />
• CHEMCAD<br />
• ASPEN PLUS
Schematic of typical glycol<br />
dehydration unit
Kondisi <strong>Gas</strong> Masuk<br />
• Tekanan gas inlet: 200 psia<br />
• Suhu gas masuk: 82 oF<br />
• Kandungan air gas masuk (kondisi jenuh): 151 lb/MMSCF<br />
• Kapasitas gas masuk pada kondisi design per unit adalah: 60 MMSCFD<br />
Komponen <strong>Gas</strong> Fraksi mol MMSCFD<br />
N 2 0,0044 0,264<br />
CO 2 0,0012 0,072<br />
CH 4 0,988 59,28<br />
C 2 H 6 0,0044 0,264<br />
C 3 H 8 0,0008 0,048<br />
i-C 4 H 10 0,0003 0,018<br />
n-C 4 H 10 0,0005 0,03<br />
n-C 5 H 12 0,0002 0,012<br />
i-C 5 H 12 0,0002 0,012<br />
Jumlah 1 60
SALES G AS<br />
12<br />
DRIED G AS<br />
5<br />
STRIPPING GAS<br />
SALES G AS 60 MMSCFD (8.1 L B/MMSCF )<br />
P= 198 psia, T= 89 oF<br />
28<br />
15<br />
8.1 lb/MMSCF )<br />
22<br />
5<br />
13<br />
TO ATMOSPHERE<br />
G AS-GL YCO L HE<br />
E-910<br />
20<br />
20<br />
EXCHANGER STRIPPER (op tional)<br />
22<br />
42<br />
27<br />
ST ILL COLUMN (packed)<br />
E-730<br />
11<br />
LEAN GL YCO L<br />
12<br />
35<br />
21<br />
G LYCO L REBOILER<br />
E-770<br />
by pass (igno re) 27<br />
18<br />
19<br />
CO NTACTO R<br />
V-690<br />
RICH G LYCO L<br />
33<br />
34<br />
36<br />
37<br />
10<br />
9<br />
1<br />
IN FLASH T AN<br />
24<br />
3<br />
14<br />
FL ASH TANK<br />
V-710<br />
21<br />
TO F LARE<br />
16<br />
TEG IN REGEN<br />
TO BLO W CASE<br />
7<br />
To Reb oiler F uel<br />
19 31<br />
6<br />
16<br />
ST RIPPER<br />
32<br />
30<br />
15<br />
CO NCENTRATED<br />
23<br />
MAKE UP TEG<br />
INLET G AS<br />
60 MMSCFD (151 lb/MMSCF)<br />
P= 200 psia, T= 82 oF<br />
17<br />
17<br />
39<br />
38<br />
SEPARATOR<br />
11<br />
14<br />
26 29<br />
13<br />
25<br />
SCRUBBER<br />
W ATER & SOL ID<br />
23<br />
24<br />
7<br />
G LYCO L CIRCULATING PUMP<br />
P-740<br />
10<br />
G LYCO L PLATE HE<br />
E-760<br />
TEG RECIRC. 2<br />
6<br />
1<br />
8<br />
41<br />
40<br />
18<br />
4<br />
4<br />
3<br />
26<br />
G LYCO L BO OSTER PUMP<br />
P-790<br />
9<br />
2<br />
TEG RECIRCULAT IO N<br />
18 gpm<br />
G LYCO L SURGE TANK<br />
EQ UIPPED W ITH CO IL HE<br />
V-780
Summary Hasil Simulasi<br />
<strong>Gas</strong> Inlet Properties<br />
DHP Properties<br />
Suhu<br />
Inlet<br />
<strong>Gas</strong><br />
Tekanan<br />
Inlet<br />
<strong>Gas</strong><br />
Tekanan<br />
<strong>Gas</strong> Out<br />
Kompres<br />
or<br />
Laju Alir<br />
Inlet <strong>Gas</strong><br />
Kadar Air<br />
Inlet <strong>Gas</strong><br />
Efisiensi<br />
Kontakt<br />
or<br />
overall<br />
Jumlah<br />
Tray<br />
Kontakt<br />
or<br />
Laju<br />
Alir<br />
Glycol<br />
Water<br />
Remova<br />
l Load<br />
Reboiler<br />
Duty<br />
Kadar Air<br />
Outlet<br />
<strong>Gas</strong><br />
( o F) (psia) (psia)<br />
(MMSCF<br />
D)<br />
(lb/MMSC<br />
F)<br />
(%) (gpm) lb H 2 O/h<br />
MMBtu/<br />
h<br />
(lb/MMSC<br />
F)<br />
82 200 - 60 151 39 8 18 357,3 0,5269 8,1<br />
104 583,7 - 60 151 15 9 18 363,2 0,7825 5,74<br />
88,2 156 - 45 162,4 13,9 8 7 187,3 0,2438 64,2<br />
88,2 156 - 45 162,4 30 8 18 269,6 0,3911 20,4<br />
88,2 156 - 52 162,4 65 8 18 335,7 0,4796 7,06<br />
88,2 156 300 45 130 43 8 18 233,3 0,3508 6,5<br />
88,2 156 - 45 162,4 30 8 18 269,6 0,3911 20,4<br />
88,2 156 - 45 162,4 30 12 18 286,9 0,4112 11,2<br />
88,2 80 - 45 162,4 30 8 18 258,6 0,3833 26,3<br />
88,2 80 - 52 162,4 30 8 18 294,0 0,4684 28,5<br />
88,2 80 - 52 162,4 30 8 20 296,4 0,4802 27,4<br />
88,2 80 - 52 162,4 30 8 35 303,6 0,5624 24,1<br />
88,2 80 - 52 420 30 8 46 788,7 1,2056 56<br />
88,2 80 - 52 420 30 12 49 839,2 1,2714 32,7