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The Global Petrochemical Industry:
Understanding the Complex Interactions Between Technology, Economics and Markets
Online Training
Manuel Asali
Vice President
Copyright © by Nexant Inc. 2019
All rights reserved
Propylene and derivatives
Section 3
Propylene
Section 3 Module 1
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Like ethylene, propylene’s double bond enables
polymerization, hydroformylation, epoxidation
CH3 CH2 CH
Polypropylene
Oxo alcohols
Cumene
MMA
Propylene oxide
Epichlorohydrin
Acetone/IPA
Acrylonitrile
Acrylic acid
Acrolein
Acrylamide
Allyl Chloride
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Propylene and ethylene price differential
P/E Contract Price Ratio Evolution
Source: Nexant
0.0
0.2
0.4
0.6
0.8
1.0
1.2
1.4
1.6
1995 1997 1999 2001 2003 2005 2007 2009 2011 2013 2015
P/E
Pric
e R
atio
NW Europe US Gulf Coast
0.4
0.6
0.8
1.0
1.2
1.4
1.6
1.8
2.0
2.2
1995 1997 1999 2001 2003 2005 2007 2009 2011 2013 2015 2017
P/E
Pric
e R
atio
NW Europe US Gulf Coast
C2= prices collapse in the US
while C3= still expensive
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What about the other regions of the world?
Regional Propylene Supply Sources, 2018
0
10
20
30
40
50
60
70
North America South America Western Europe Middle East Asia Pacific
Mill
ion
tons
Steam Crackers Refinery OPP
Source: Nexant
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On-purpose propylene technologies
Propane Dehydrogenation (PDH)
Olefin Metathesis
Olefin Interconversion (Olefin Cracking)
Enhanced Catalytic Cracking
Methanol to Olefins (MTO/MTP)
“Green” Propylene
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Propane dehydrogenation is simple in concept but
difficult to carry out
High Temperatures
Low Pressures
Endothermic
Fairly capital intensive
CH3CH2CH3 CH3CH=CH2 + H2
Catalyst
Propane Dehydro Plants in the World represent
5% of Global Propylene Capacity
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Olefin metathesis is as a way to increase propylene output from
crackers
CH2=CH2 + CH3CH=CHCH3
2 CH3CH=CH2
Ethylene Ethylene Butene
Propylene
Lyondell has operated such a plant since 1985, now Lummus
is the leading licensor of metathesis technology
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Ways to increase propylene output in a naphtha
cracker
Metathesis Olefin Interconversion
Steam
cracker
Naphtha
Metathesis
C2=
C3=
C4S
C3=
Naphtha
Olefin
Interconversion
C2=
C3=
C4S C3=
BTX
Pygas
Steam
cracker
Aromatic
Extraction
C5S
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MTO – new paradigm for olefins production?
Catalyst – Zeolite
SAPO-34 model
Source: UOP and DOI: 10.1021/acscatal.5b00007
Methanol (CH3OH) Olefins + water + side products
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Major Chinese coal to olefins (CTO) projects
up to 2015
Location of Coal to Olefin Plant Hainan
Xinjiang
Qinghai
Tibet
Gansu
Sichuan
Yunnan Guangxi
Fujian
Henan
Guangdong
Ningxia
Inner Mongolia
Heilongjiang
Jilin
Liaoning
Hebei
Tianjin
Zhejiang
Anhui
Jiangsu
Shandong
Shanxi
Beijing
Shanghai
Hunan
Hubei
Guizhou
World’s first:
Shenhua Group – Baotou
(2010),
300kta PE & 300kta PP
6. Baofeng Energy
(2014), Yinchuan,
300kta PE & 300kta PP
7. Shenda Chemicals
(2014), Tengzhou,
200kta PP, 100kta EVA, 120 EO
5. ChinaCoal
(2014), Yulin,
300kta PE & 300kta PP
3. Wison Clean Energy
(2013), Nanjing,
300kta PE/PP
4. Yanchang Group
(2014) – Jingbian,
300kta PE & 300kta PP
8. Pucheng Clean Energy
(2014), Pucheng,
320kta PE & 350kta PP
9. Zhejiang Xingxing
(2015), Jiaxing,
300kta PE & 390kta PP
Chongqing
Jiangxi
2. Fund Energy
(2013), Ningbo,
300kta EG & 400kta PP
Shaanxi
Source: C&EN
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New propylene capacity by region (2018-2020)
By region
By technology
New propylene capacity = 13.7 million metric tons
MTO/MTP 20%
PDH 25% Steam
Cracker 39%
FCC 16%
Metathesis 0%
Asia Pacific 79%
Middle East 9%
Africa 8%
Eastern Europe
3%
Central Europe
1%
Source: Nexant
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Leading global propylene producers, 2018
(chemical and polymer grade)
Top 10 represents 28 percent of global capacity
0
1000
2000
3000
4000
5000
6000S
inop
ec
Pet
roC
hina
Dow
DuP
ont
Exx
onM
obil
She
ll
Tot
alP
etro
chem
ical
s
Ent
erpr
ise
Rel
ianc
e
For
mos
aP
etro
chem
ical
SA
BIC
Tho
usan
d to
ns p
er y
ear
Steam Cracking Refinery Metathesis PDH MTOSource: Nexant
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Propylene net trade (thousand metric tons)
Eastern Europe
North America
South America
Western Europe
Middle East
Asia Pacific
Source: Nexant
(564)
(140)
(689) 233
367
102
179
(86) (280)
131 41
304
164
399
836
(304)
(44) (119)
2008 2013 2018
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Global propylene consumption, 2018
Source: Nexant
Global Demand = 107.3 Million Tons
Polypropylene 66%
Propylene Oxide
7%
Acrylonitrile 6%
Acrylic Acid 4%
Cumene 4%
2-Ethylhexanol 3%
Butanols 3%
Isopropanol 1%
EPDM 1% Others
5%
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