presentasi peralatan pabrik (oil refinery unit) (1)
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1 1CONFIDENTIAL AND PROPRIETARY
TUGAS PERALATAN PABRIK“ Block Flow Sheet dan Process Flowsheet Pada Proses Oil Refinery Unit “
Padang,16 Februari 2016
Prepared By: (Kelompok 3)Hadi Ash Shidiq (1110912069)Dikky Andika (1110912068)M.Adri Dalnis (1110912043)Fhilip Perdana (0910912032)Dosen Pengampu : Dr.Eng.Meifal Rusli
PERTAMINA |
Block Flowsheet
2
INPUT PROSES OUTPUT
PERTAMINA |Source : RU II APR Extended Team
TOPPING UNIT-UNIT 100rs/pe-enj.bang
CRUDE OILS
H-1
HEATERS
STEAM
REBOILER
NAPHTHA
KEROSENE
LIGHT GAS OIL
HEAVY GAS OIL
LONG RESIDUE
FG.KO.DRUM
C-1 ABCKO.DRUMS
FLARE
E-1 A/B
E-3 A/B E-2 A/B E-11 A/B
E-5 E-12 A/B
E-6,13
E-4 A/B/C/D E-14 A-F
T-1
T-2A
T-2B
T-2C
D-1
D-2 D-3
D-5
FG & FLARE
E-8 A/B/C/D
FRACT.ACCUMULATOR
E-7 A-F
E-9
FEED PRODUCT
Memisahkan minyak mentah (crude oil) atas fraksi-fraksinya berdasarkan perbedaan titik didih dengan proses distilasi atmosferik pada temperatur 330 oC.
Feed Blending, %
SLC 85
Duri 15
Produk Yield,%
Naphtha 7
Kero 10
LGO 12
HGO 8
Residu 63
Process Flowsheet 1. CDU (Crude Distillation Unit)
PERTAMINA |Source : RU II APR Extended Team
EXISTING PLATFORMINGUNIT-301
r.sutontros/pe-enj.bang
T-1 T-2
PLATFORMATEHEAVYNAPHTHA
HIDROBONREACTOR HPS
HYDR. STRIPPER
HYDR STRIPPER RECEIVER
PLATF. HEATERS
PLATF. REACTORS
H2 Plant
FG
HPS STABILIZERSTAB. OHRECEIVER
STAB. REBOILER
E-9
E-4
E-3 ABC
E-2
E-1
E-8
E-7
E-6E-5
R-1
R-2 R-3 R-4
D-1
D-2
D-5
D-6
H-3 H-4
H-1H-2
H-6
C-1
PLATF.COMP.
HIDROBONHEATER
HYDROBONSTRIPPERREBOILER
RERUNSTABILIZER
FLAREFG
E-11
Mengkonversikan Low Octane Naphtha (Heavy Naphtha) menjadi komponen High Octane (High Aromatic Compound)
Feed Blending, %
H.Naphtha 100
FEED(9.3 MBSD) PRODUCT
Produk Yield,%
LPG 31,96
Reformate 55,4
2. PL I (Platforming I Unit 301)
PERTAMINA |Source : RU II APR Extended Team
CONTINOUS CATALYST REGENERATIONUNIT 310
rs/pe-enj.bang
Organic Chloride
Nitrogen
Vent
Hydrogen Rich Gasfrom Booster Compressor
Air
COALESCER
SURGEHOPPER
RecycleGas
Nitrogen
Vent
PLATF.REACTORS
ChlorinationHeater
LOCKHOPPER
No.2LOCK
HOPPERNo.1
No.1 No.2
REGEN COOLERBLOWER
CM-2REGEN BLOWER
OXYGENCONTROL SELECTOR
REGEN HEATER
AIR HEATER
REGENTOWER
CHLOR.BLOWER
CM-1
LIFT ENGAGERS
Nitrogen
DISENGAGINGHOPPER
DUST COLLECTOR
CM-3
LIFT GASBLOWER
H-3
H-1
CAT.COLLECTOR
FLOW CONTROLHOPPER
REGENERATEDCATALYST
PRODUCTFEED(8.8 MBSD)
Mengkonversikan Low Octane Naphtha (treated naphta dari NHDT) menjadi komponen High Octane (High Aromatic Compound).
Feed Blending, %
H.Naphtha 100
Produk Yield,%
LPG 9,0
Reformate 73,1
3. PL II (Platforming II Unit 300)
PERTAMINA |Source : RU II APR Extended Team
HEAVY VACUUM UNITUNIT 110
rs/pe-enj.bang
Flare
J-51/52/53
Water Swt Unit
Refinery Water
To Slop Tank
To SWS
LP SteamAtm
Fuel Gas
Feed WaterSteam
Condensate
FEED SURGE DRUM
1st & 2nd Stage DESALTER
VACUUM HEATERS
VACUUM TOWER
CONDENSATE RECEIVER KO DRUM
STEAM DISENGAGING DRUM
LVGO
VACUUM BOTTOM
HVGO
Grav. 34.5/.8524 K 12.25PP 80F FP 315F .S 0.09 BR 650-720F .
Grav. 31.0/.8708 K 12.25 .PP 80F FP 315F N2 600PPMS 0.09 BR 650-720F .
Grav. 18.8/0.9415 Visc. Kin.210 F 87.2S 0.17 K 12.22 N2 0.80 wt% .
Nitrogen
Flare
Tempered Water Supply
Tempered Water Return
CHARGE84.5% LSRC .15.5% PEDADA .
Grav. 26.6/.895 .PP 110F MW 522 .K 12.36 .Visc Kin 135F 7.1cst .BR oF 490-1115(73%) .
V-3
V-4
V-5A
V-5B
V-5B
H-1B
H-1A
V-1
V-2
V-11
V-6V-9
V-10
E-6
E-5
E-4E-3
E-7
E-9
E-51/52/53
E-2,3
TEMPERED WATER EXPANSION DRUM
CONT & . INTERMITTNBLOWDOWN
FEED(106 MBSD) PRODUCT
Pemisahan fraksi-fraksi minyak bumi ( LSWR ex-CDU) berdasarkan titik didih pada tekanan vacum (< 1 atm). Prinsip dasar : Titik didih semua material akan turun Jika tekanan turun P~T
Feed Blending, %
LSWR 100
Produk Yield,%
LVGO 7,8
HVGO 51,5
S.Residue 40,7
4. HVU (Heavy Vaccum Unit 110)
PERTAMINA |Source : RU II APR Extended Team
Konversi secara thermal cracking minyak berat (heavy oil / short residue) menjadi coke, gas oil, naphtha, LPG dan gas
FEED(35.3 MBSD) PRODUCT
Feed Blending, %
S.Residue 100
Produk Yield,%
LPG 6,4
C.Naphtha 14,5
LCGO 35,9
HCGO 30,8
G. Coke 17,1
5. DCU (Delay Coking Unit 140)
PERTAMINA |Source : RU II APR Extended Team
HC UNIBON/UNIT 211-212REACTOR SECTION
rs/pe-enj.bang
V-1
V-2
V-3
sws
Flare
C-2 C-2 C-2
FRESHFEED
SURGEDRUM
POWERRECYCLETURBIN P-3
E-1 E-2
E-4
E-3
V-8
C-1
V-27 V-28 V-29
V-9 V-10
H-1
E-1
V-25 V-24
ToDebut Column
at Fract.Section
V-26Filter
HVGO & HCGO
From Bott. Fractionator
RECYCLE FEED SURGE DRUM
AMINE LPG AMINE LPGFLARE
BACKWASHDRUM
REACTOR CHARGEHEATER
FRESH FEED REACTORS
RECYCLE REACTOR
HPSEPARATOR
RECYCLE COMPRESSOR
1ST 2ND 3RD STAGESUCTION DRUMS
MPFLASH DRUM
HPFLASH DRUM
H2 Make Up from Hydrogen Plants
Feed PropertiesGrav 31 S 0.31%Aromatics 0.06%BR, HVGO 690 -1080F (362-576)
HCGO 585 - 930 F (304-494)
CATALYST : DHC-8CoMo&Tungsten onSilica Alumina Base
FEED(31.5 MBSD)
Mengolah minyak fraksi berat (HVGO & HCGO) menjadi minyak fraksi ringan menggunakan katalis dalam lingkungan gas H2
Feed Blending, %
HVGO 86.7
HCGO 14.3
6. HCU (Hydro Cracker Unibon Unit 211/212)-(Reactor Section)
PERTAMINA |Source : RU II APR Extended Team
HC UNIBON - FRACTINATION SECTIONUNIT 211 & 212
rs/pe-enj.bang
E-10 E-29 E-11
CBA
V-19 V-23V-21V-13
V-14V-12H-2 H-3
LP STEAM LP STEAMMP STEAM
FGAmine LPG
Amine LPG
LIGHT NAPHTHA
SWS SWS WASHWATER
HEAVY NAPHTHA
LIGHT KEROSENE
HEAVY KEROSENE
RECYCLE FEEDTo V-25
GAS OIL/DIESELGrav.834Br 310-371F(153-186C)S 5ppm wtFP 121C An.Pt.210CPP 7C
Amine LPGFROM LP FLASH DRUMat Reactor Section
DEBUTREBOILER DEBUTANIZER
DEBUT OHRECEIVER
PRODUCT FRACTIONATOR
DIESEL, H.KERO & L.KEROSTRIPPERS
PROD.FRACT.RECEIVER
NAPHTHA SPLITTER
NAPH.SPLITRECEIVER
L.NAPHTHASPLITTER
L. NAPHTHA STRIP.RECEIVE
R
V-16 V-17 V-18
V-20 V-22
Grav.45.4/.80MW 191 K 12.17 BR 177-310CArom.10%vol An.Pt.72C S 5ppm wtFP 63C
Grav 58/.747 k 12.35 MW 139Br 149-177F Sm.Pt. 27mm
Grav 59.5 BR 95-134C
Grav.82.2/.662MW 79.3 K 12.61
RON Clear 75,+3cc/USG 93Vap.Press 11.7 psia
Ar. 1.0 BR 40-75C
SWS E-21 E-25
E-21,24
E-25,28
PRODUCT
Produk Yield,%
LPG 4,29
LN 10,47
HN 13,69
LK 8,81
HK 14,6
Diesel 44,92
Net UCO 14,3
HCU (Hydro Cracker Unibon Unit 211/212)-(Fractionator Section)
PERTAMINA |
Terima Kasih
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