Presentasi Peralatan Pabrik (Oil Refinery Unit) (1)

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1 1 CONFIDENTIAL 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 R usli

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Transcript of Presentasi Peralatan Pabrik (Oil Refinery Unit) (1)

Page 1: Presentasi Peralatan Pabrik (Oil Refinery Unit) (1)

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

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PERTAMINA |

Block Flowsheet

2

INPUT PROSES OUTPUT

Page 3: Presentasi Peralatan Pabrik (Oil Refinery Unit) (1)

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)

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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)

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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)

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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)

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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)

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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)

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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)

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PERTAMINA |

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