pengolahan minyak bumi nelson saksono & yuliusman ref

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Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref : 1. Speight, James G. The Chemistry and Technology of Petroleum 2nd edition. Marcel Dekker Inc. New York. 1991. 2. James H . Gary. “ Petroleum Refining, Technology and Economic”, Marcel Dekker,Inc, New York, 1975

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Page 1: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

Pengolahan Minyak Bumi

Nelson Saksono & Yuliusman

Ref :1. Speight, James G. The Chemistry and Technology of Petroleum 2nd edition. Marcel Dekker Inc. New York. 1991.

2. James H . Gary. “ Petroleum Refining, Technology and Economic”, Marcel Dekker,Inc, New York, 1975

Page 2: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

World Proven Reserves of Crude Oil

63.7

89.5

20.6

74.9

65.4

44.0675.7

Billion barrels

Page 3: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

World Proven Crude Oil Reserves

as percent of 1296 billion barrel total

Page 4: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

Composition of Crude Oil

CRUDE OIL

HYDROCARBONS NON-HYDROCARBONS

ALIPHATICS AROMATICS NAPHTHENES SULFURS NITROGENS OXYGENS METALLICS

25% 17% 50% <8% <1% <3% <100PPM

C1 - C60 (C6H5)n CYCLOALKANES SH

S

NH

O

COOH

Page 5: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

Crude Oil Classification

PETROLEUMSaturates

AromaticsAsphaltics

n-alkanes C5 - C44branched alkanescycloalkanes (napthenes) single ring

condensed ring

nitrogenoxygensulfur

containing compounds

API Gravity = 35o

Page 6: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

The Uses of Crude Oil

Page 7: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

The Xylenes

Boiling Point 144oC 139.3oC 137-138oC Melting Point -25oC -47.4oC 13-14oC

ortho meta para

CH3

CH3

CH3

CH3

CH3

CH3

Page 8: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref
Page 9: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

CRUDE

DESALTING

REFINING

REFORMING

BLENDING

Distillation to separate by boiling point ranges

Water washing to remove impurities

Conversion reactions to alter molecular structures

Mixing to obtain maximum commercial characteristics

Petroleum delivered from well field

Page 10: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

Petroleum Refining

GAS

LIGHT NAPHTHA

HEAVY NAPHTHA

KEROSENE

ATM. GAS OIL

RESIDUUM

CRUDE DESALTER FURNACE

C1-C4

bp < 50 oF

C5 - C?

bp 50-200oF

C? - C12

bp 200-400oF

C12 - C16

bp 400-500oF

C15 - C18

bp 500-650oC

> C20

bp >650oF

TOWER

Distillation – separation by boiling point

Page 11: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

Petroleum ReformingGAS

LIGHT NAPHTHA

HEAVY NAPHTHA

KEROSENE

ATM. GAS OIL

RESIDUUM

TOWER

FUEL GAS

TREATER

HYDROTREATER

HYDROTREATER

HYDROTREATER

REFORMER AROMATIC EXTRACTION

CATALYTICCRACKER

JET FUELS/KEROSENE

DIESEL & FUEL OILS

GASOLINE

AROMATICS

VacuumDistillation

VACUUM GAS OIL

LUBRICATING OIL

COKER COKE

ASPHALT

CATALYTICCRACKER

Page 12: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

Conversion Reactions

gasoline gasoline additive recycle

C7H15.C15H30.C7H15 C7H16 + C7H14 + C15H30CRACK

COMBINE

REARRANGE

THERMAL

CATALYTIC

ALKYLATION

POLYMERIZATION

REFORMIING

ISOMERIZATION

CH3CH2CH3 CH2 CH CH2 CH3CH3CH2CH2 CH2CH2CH2CH3

C H3C

CH3

CH2C H3C

CH3

CH2C H3C

CH3

CH3

C CH2

CH3

H

CH2C CHCH3

CH3CH3

CH3

H3CC

82% 18%

Dehydrogenation

Dehydroisomerization

Isomerization

Dehydrocyclization

Hydrocracking

Page 13: Pengolahan Minyak Bumi Nelson Saksono & Yuliusman Ref

Catalytic Reforming – Conversion ReactionsDehydrogenation of cycloalkanes to aromatics

Dehydroisomerization of cyclopentanes to aromatics

Isomerization of alkanes

Dehdrocyclization of alkanes

Hydrocracking of alkanes

CH3 CH3

3H2

CH3

3H2

CH3CH2CH2CH2CH3 CHH3C

CH3

CH2 CH3

CH3CH2CH2CH2CH2CH2CH3

CH3

4 H2

CH3CH2CH2CH2CH2CH2CH3 CH3CH2CH3 CH3CH2CH2CH3