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Refining & Petrochemicals Integration · 2017-04-24 · UOP 4585C-11 • Proven performance track...

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Raza Jawad Regional Director, Business Development UOP Middle East Company, Dubai Refining & Petrochemicals Integration Business Drivers & Enabling Technologies © 2006 UOP LLC. All rights reserved. UOP 4698-01 SAS-AIChE Meeting February 27, 2007 Al-Khobar, KSA
Transcript

Raza Jawad

Regional Director, Business Development

UOP Middle East Company, Dubai

Refining & Petrochemicals Integration

Business Drivers & Enabling Technologies

© 2006 UOP LLC. All rights reserved. UOP 4698-01

SAS-AIChE Meeting

February 27, 2007

Al-Khobar, KSA

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Refining & Petrochemicals Integration Business Drivers & Enabling Technologies

•Refining & petrochemicals markets

• Investment strategies

•Enabling technologies

•Concluding remarks

UOP 4698-02

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70%

75%

80%

85%

90%

1980

1985

1990

1995

2000

2005

Av

era

ge

Glo

ba

l U

tilis

ati

on

, %

Source: BP Statistical Review 2006

Refining Situation

Refining investments potentially attractive

• Refining utilisation significantly higher in 2004 - 06

• Margins currently above re-investment “threshold”

0

2

4

6

8

1990

1994

1998

2002

2006

Av

era

ge

Cra

ck

ing

Ma

rgin

, $

/ b

bl

Sources: BP Statistical Review 2006

IEA 2005 / 6

Investment “threshold”

UOP 4698-03

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Refining Investment Imperative

• ~ 1.5 Mb / d incremental refined fuels annually

- ~ 45% in M. East + China

- Clean transport fuel growth

• Refining investments essential

- Capacity

- Conversion

- Upgrading

Global Demand Growth

0

0.5

1

1.5

2

1996

- 20

01

2001

- 06

2006

- 11

Mb

/

da

y,

av

era

ge

0

0.5

1

1.5

2

2.5

% p

er

ye

ar,

av

era

ge

Source: IEA, July, 2006

$30 – 40 billion

per year

Substantial investments essential

UOP 4698-04

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Investment Remuneration

•Escalating fabrication and construction costs affecting investment returns

Investment Risk Remains Challenging

10% Internal Rate of Return

New 200 kb/d Cracking refinery

$4bn investment ~ $6+/bbl average margin

for 20+ years required

UOP 4698-05

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Risk Mitigation

•Feedstock and product flexibility

- “Opportunity” feedstocks

- Optimal upgrading & conversion

- Maximize value addition

- Prosper from cyclical markets

•Operational efficiency

- Economies of scale

- Energy

- Control & optimization

Flexibility, Efficiency, Integration

Leading-Edge Technology

UOP 4698-06

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Advantages Of Integration

UOP 4698-07

• Integrated refinery and petrochemical operations

minimize costs and optimize product distribution

• Optimized integration of hydrocarbon processes,

energy, hydrogen, and water

• Feedstock flexibility to capitalize on available low

cost crude oils and intermediates

• Supply chain optimization provides faster delivery

of products

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Adding Value to Crude $ p

er

To

n

0

100

200

300

400

500

600

700

800

Crude

900

1000

1200

Fuels

Gasoline

J / K Diesel

Fuel Oil

Petrochemicals

Benzene

Propylene PP

Styrene

Petrochemicals Can Add Significant Value

p-X

UOP 4698-08

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0

5

10

15

20

25

30

2000 2001 2002 2003 2004 2005 2006 2007 2008 2009

De

ma

nd

In

cre

as

e

ov

er

19

99

- M

M M

T

Other BZ BZ to Cyclohexane

BZ to Phenolics BZ to Styrenics

p-Xylene6.8%

3.6%

Sources: CMAI & UOP

Aromatics Markets

Annual

Growth

Strong Aromatics & Derivatives Growth

UOP 4698-09

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• Refineries are main

source of xylenes supply

• Future p-X demand

growth expected to

average 1.8M MTA/Yr

3 To 4 World Scale p-X Complexes Annually

p-Xylene Capacity & Demand (Committed Projects Only)

0

5

10

15

20

25

30

35

40

45

50

1992

1996

2000

2004

2008

2012

2016

p-X

yle

ne

, M

MT

A

Global Demand

ProductionCapacity

Future supply deficit

Sources: PCI & UOP

UOP 4698-10

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Propylene Market

MT Propylene / MT Ethylene

0.59

2004 2006 2008 2010 2012 2014

Supply from steam crackers

~ 1

8 M

MTA

0.40

0.35

0.45

Ste

am

Cra

cker P

rod

ucti

on

0.54

0.64

Dem

an

d

Source: CMAI 2005

Demand

0.62

0.36

Propylene

demand

increasing

faster than

supply from

conventional

sources

Growing Demand For “On-Purpose” Propylene

UOP 4698-11

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BTX & Olefins: Integration Potential

• Strong growth potential

• Attractive value addition

• Assured feedstock supply

- Potential for low cost & “distressed” refinery

intermediates

• High value return streams to refinery, e.g.,

hydrogen, high octane gasoline

Potential To Raise Returns & Mitigate Risk

+ Petrochemicals Refining

UOP 4698-12

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Integration Strategies

Light

Olefins

BTX

Detergents

Chemicals

Hydrogen

Power

Technology Provides Link

Crude

Oil

Naphtha

Reformate

FCC Intermediates

• LPG

• Cracked Naphtha

• Light Cycle Oil

Residues

Kerosene

Refinery

UOP 4698-13

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Crude

Oil

Naphtha

Reformate

FCC Intermediates

• LPG

• Cracked Naphtha

• Light Cycle Oil

Residues

Kerosene

Refinery

Integration Strategies

Light

Olefins

BTX

Detergents

Chemicals

Hydrogen

Power

Technology Provides Link

UOP 4698-14

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AGO / VGO

Refinery – Light Olefins Integration

Gasoline

Fuel oil

C3=

FCC

Propylene Recovery

Olefin Cracking

UOP 4698-15

Olefin Cracking: Developed by Total Petrochemicals & UOP Doubles Propylene Production & Reduces C4/C5 Olefins

LPG

AGO / VGO

Fuel oil

Gasoline

C3=

Lt. Olefin Recovery

FCC

C2=

Lt. Olefin Recovery

FCC

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Olefin Cracking Enhances Gas To Olefins

Ethylene & Propylene

Gas UOP / Hydro MTO Process

Methanol Synthesis

Olefin Cracking

•20% increase in light olefin yields

•Nearly 80% reduction in C4+ by-products

•2:1 propylene/ethylene production ratio

UOP 4698-16

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PetroFCCTM Process: BTX + Olefins

Naphtha

Distillate

Fuel Oil Coke

53.5

14

7 5

28

9.5

5.5 5

C4’s

11

19 14

C4=

Traditional FCC PetroFCC Process Light Olefins

C3’s 6.5

24

22 C3=

C2-

9

6 C2

=

3

18

Aromatics

BTX

The “Petrochemicals Refinery” Enabler

UOP 4698-17

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Tatoray™

process

Aromatics Processing

p-Xylene

Xylene Fractionation

Parex™

process

Benzene

CCR

Platforming™

process

Naphtha

Conversion Ring Adjustment Separation

UOP 4585C-11

• Proven performance track record

• State of the art technology – continuous innovation

• Cost effective designs; high on-stream efficiency

90% of p-X capacity since 1970 uses Parex process

BT Fractionation

Sulfolane™

process

Isomar™

process

UOP 4698-18

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BTX Innovation: LCO-XTM Process

• FCC light cycle oil (LCO)

- Distillate range intermediate product

- High sulfur, high density, highly aromatic

- Difficult to blend to clean transport fuel

• High content of multi-ring aromatics

- Unlock benzene and xylenes

Low value as fuel blendstock

Low cost, high

value BTX feedstock

$0.75/Bbl crude increase in operating margin

• LCO-X process for converting LCO to BTX recently announced

UOP 4698-19

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Refining

Gasification

Syn Gas Production

Hydrogen

Carbon monoxide

Fertilizer

SNG

Olefins

Methanol/Ethanol

Acetic acid

Naphtha

Diesel

Jet fuel

Wax

Electricity

Separation

O2, N2, CO2, S, sulfuric acid

Transportation Fuels

Resid

Natural Gas Reforming

Electricity

Hydrogen

A Future Scenario

Chemicals

Gas Conversion

Power

Crude Oil

Resid

Technology Developments Key To Deeper Integration

UOP 4698-20

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Innovation, Research, Development

Broaden the knowledge base

Leverage academic and industrial experts

Keys to success:

− Collaboration / alliances

− Commercialize

Technology Imperative – A Key Enabler

UOP Awarded National Medal of Technology in 2005 “…over 85 years of sustained technical leadership and innovation

for the worldwide petroleum refining and petrochemical

industries……benefited quality of life throughout the world.”

Universities

Government Labs

Startups

Technology Leaders

Customers

Suppliers

uop A Honeywell Company

UOP 4698-21

Ref: National Medal of Technology Award to UOP, 2005

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Summary

•Strong growth of refining and petrochemicals markets, healthy margins

- Investment in additional capacity essential

• Integrating petrochemicals with refining can mitigate investment risk

•Continuing technology innovation key enabler for successful integration

UOP 4698-22

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Thank You

UOP 4698-23

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