2012 Ethylene Plant for Itb

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Ethylene Plant Consist of ISBL process units and supporting facilities designed to produce polymer grade ethylene, polymer grade propylene, hydrotreated pyrolysis gasoline and other by-products

description

proses pembuatan etilen oleh ITB

Transcript of 2012 Ethylene Plant for Itb

Page 1: 2012 Ethylene Plant for Itb

Ethylene PlantConsist of ISBL process units and supporting facilities designed to

produce polymer grade ethylene, polymer grade propylene,

hydrotreated pyrolysis gasoline and other by-products

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ISBL Facilities 100

Pyrolysis (cracking) and quench, gas turbine intergration, gasoline fractionation, pyrolysis fuel oil stripping, process water stripping and dilution steam generation

200 Charge gas compression, acid gas removal by caustic wash,

charge gas drying and condensate stripping 300

Charge gas chilling, demethanization, ,ethane refrigeration, methanation and hydrogen purification by ethane wash

400 Deehanization, acetylene hydrgenation, ethylene fractionation,

ethylene product delivery system, depropanization, C3 hydrogenation, propylene fractionation and debutanization

500 Propylene refrigeration

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ISBL Facilities (continue) 600

Ethylene refrigeration 700

Utilities distribution 800

Heavy NGL feed treatment 900

Spent caustic pretreatment Spent caustic oxidation

1100 C4/C5 Hydrogenation

1200 Pyrolysis gasoline hydrogenation and fractionation

1800 Storage tank yard

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ETHYLENE PLANT

PFO Stripper

GasolineFractionator

Furnace

Heavy Naphtha

Light Naphtha

C4 Recycle

C2 / C3 Recycle

Quench Tower

PFO

Crack Gas

Charge GasCompressor

1st, 2nd, & 3rd

Caustic WaterWash Tower

Charge GasCompressor

4th & 5th

Charge GasDryer

Chilling Train

Hydrogen MethaneSeparator No. 1

Demethanizer

AcetyleneConverter

Ethylene DryerEthylene

Fractionator

Hydrogen MethaneSeparator No. 2

MethanatorHydrogen

DryerEthane Wash

Tower

HP Methane

96 % H2

99 % H2

HP Ethylene

Ethane Recycle

Deethanizer

DepropanizerNo. 2

DepropanizerNo. 1

Debutanizer

C4/C5Reactor

PyGasReactor

PropyleneDryer

MAPDConverter

PropyleneFractionator No. 2

PropyleneFractionator No. 1

Depentanizer BTX Tower

Heavy Gasoline

Propylene

C3 LPG &C3 Recycled

Crude C4

C4 Recycled

C5 mix with Naphtha

PyGas

C9+

HOT SECTION COLD SECTION

AREA 100

AREA 200 AREA 300

AREA 400

AREA 1100

AREA 1200

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GENERAL PROCESS DESCRIPTIONHOT SECTION

PFO Stripper

GasolineFractionator

Furnace

Heavy Naphtha

Light Naphtha

C4 Recycle

C2 / C3 Recycle

Quench Tower

PFO

Heavy Gasoline

Crack Gas

To Compressor

Crack the feed into valuable product

Cooling fns effluent, separate product from

heavy co-products

Stripped lighter heavy co-product from PFO

Stripped lighter heavy co-product from PFO

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GENERAL PROCESS DESCRIPTIONCOLD SECTION

To Quench Tower

Charge GasCompressor

1st, 2nd, & 3rd

Caustic WaterWash Tower

Charge GasCompressor

4th & 5th

Charge GasDryer

Chilling Train

Hydrogen MethaneSeparator No. 1

Demethanizer

Deethanizer

AcetyleneConverter

Ethylene DryerEthylene

Fractionator

Hydrogen MethaneSeparator No. 2

MethanatorHydrogen

DryerEthane Wash

Tower

HP Methane

96 % H2

99 % H2

HP Ethylene

Ethane Recycle

To Hot Distillation

Compress the charge gas from 0.3 KG to 37 KG for

separation

Cold Distillation : -H2-CH4 separator, Demethanizer, Deethanizer, Ethylene Fractionator.-Operating T < ambient T-Separate cracked gas to valuable product such as H2, Methane, Ethylene, Ethane.

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GENERAL PROCESS DESCRIPTIONCOLD SECTION (cont’d)

Deethanizer

DepropanizerNo. 2

DepropanizerNo. 1

Debutanizer

C4/C5Reactor

PyGasReactor

PropyleneDryer

MAPDConverter

PropyleneFractionator No. 2

PropyleneFractionator No. 1

Depentanizer BTX TowerHeavy Gasoline

From Quench Tower

To Acetylene ConverterPropylene

C3 LPG &C3 Recycled

Crude C4

C4 Recycled

C5 mix with Naphtha

PyGas

C9+

Hot Distillation: -Depropanizer, Propylene Fractionator, Debutanizer, Depentanizer, BTX Tower-Operating T > ambient T-Separate the remaining valuable product such as Propylene, C3LPG, CC4, C5, Pygas & C9

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General DescriptionDesigned to produce polymer grade ethylene by thermal cracking of:

Naphthas C3 LPG Heavy NGL Ethane Recycle Propane recycle Hydrotreated C4/C5

Also designed to produce the following y-products:

High Pressure Hydrogen Methane Offgas Polymer Grade

Propylene Hydrotreated Pyrolysis

Gasoline Pyrolisys Fuel Oil Heavy Tail End (from H-

NGL)