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penjelasan tentang separator dalam refinery
PROJECT : P RO J . N O . : CLIENT : UNIT :
DATE : BY : REV : DOC NO.:
S.R. M.
HORIZONTAL THREE PHASE SEPRATOR SIZING SIZING CALCULATION SHEET (BUCKET & WEIR) In p u t Dat a Volumetric Flow Rate Density Viscosity Particle Dia. Oil in Vapor Oil in W ater W ater in Oil
Un i t m3/hr kg/m3 CP micron micron micron
Vap o r 2046 1.17 0.01 100 200 200
------m /s ec
21 31.29 0.004
------m /s ec
26 26.16 0.004
Tr i al Di am et er Inlet Nozzle Size Hv/D Ratio Crest Safety Height Vapor Space Crest Height W ier Height Vessel Cross sectional Area
mm mm ---mm mm mm mm m2
3000 250 0.2 100 600 2400 2300 7.07
Separation Separation Compartment BTM - LLIL LLIL - LIL LIL - NIL NIL - HIL HIL - HHIL HHIL - W IER To t al L i q u i d l ev el Hei g h t
mm mm mm mm mm mm mm
250 100 1000 650 100 200 2300
Light Droplet Rising Time heavy phase Cross Sec. Area Heavy Phase Velocity Lmin Lmin ligh lightt dro drop p thr throu ough gh heav heavy y ph ph
min m2 m/sec mm
5.5 3.1 0.006 2069
Heavy Droplet Settling time Light phase Cross Sec. Area Light Phase Velocity Lmin Lmin heav heavy y dro drop p thr throu ough gh ligh lightt ph ph
min m2 m/sec mm
3.8 2.7 0.005 1175
Sep ar at i o n Co m p . L en g t h
mm
2300
BTM - LLIL Hold up Time LLIL - LIL Hold up Time LIL - NIL hold up Time NIL - HIL hold up Time HIL - HHIL hold up Time HHIL - W IER hold up time Heav y Ph as e h o l d u p Ti m e L i g h t Ph as e Ho l d u p Ti m e
min min min min min min min min
0.61 0.35 5.16 5.31 0.77 1.47 5.16 5.31
L i g h t Ph as e Heav y Ph as e 50 70 800 1000 0.8 1
Light Dropl et Terminal Velocity Velocity 2
CRe Drag Coefficient Ter m i n al Vel o c i t y Heavy Heavy Dropl et Terminal Velocity 2
CRe Drag Coefficient Ter m i n al Vel o c i t y
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PROJECT : P RO J . N O . : CLIENT : UNIT :
DATE : BY : REV : DOC NO.:
S.R. M.
HORIZONTAL THREE PHASE SEPRATOR SIZING SIZING CALCULATION SHEET (BUCKET & WEIR) Bucket Compartment BTM - BTM Bucket B u c k et Wi er Hei g h t BTM Bucket - LLLL LLLL - LLL LLL - NLL NLL - HLL HLL - HHLL HHLL - W IER To t al L i q u i d l ev el Hei g h t
mm mm mm mm mm mm mm mm mm
300 2000 200 150 700 700 150 100 2000
B u c k et Co m p . L en g t h
mm
1000
BTM - LLLL Hold up Time LLLL - LLL Hold up Time LLL - NLL hold up Time NLL - HLL hold up Time HLL - HHLL hold up Time HHLL - W IER hold up time Ho l d u p Ti m e
min min min min min min min
0.49 0.42 2.34 2.48 0.49 0.31 4.82
Heavy Phase Compartment Wi er Hei g h t (b as ed o n NIL ) BTM - LLLL LLLL - LLL LLL - NLL NLL - HLL HLL - HHLL HHLL - W IER To t al L i q u i d l ev el Hei g h t
mm mm mm mm mm mm mm mm
2110 200 150 750 750 150 110 2110
Heav y Ph as e Co m p . L en g t h
mm
1100
BTM - LLLL Hold up Time LLLL - LLL Hold up Time LLL - NLL hold up Time NLL - HLL hold up Time HLL - HHLL hold up Time HHLL - W IER hold up time Ho l d u p Ti m e
min min min min min min min
0.30 0.34 2.48 2.94 0.57 0.41 5.42
m/sec m/sec ---sec m2 m/sec mm
0.012 0.32 1.00 1.87 1.03 0.55 1032
mm ----
6000 2.00
Vapor Side K vlaue Terminal Velocity Mesh Pad Correction Factor Drop out Time Av Cross sectional sectional Area Vapor Velocity L m i n l i g h t p h as e t h r . v ap o r Ves s el L en g t h L /D
