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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

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