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NexantThinking
The ICIS Asian Butadiene and Derivatives Conference
October 1, 2014
Issues Impacting U.S. In Olefins and Derivatives
Prepared for:
2nd Annual Petrochemical Seminar
Houston, Texas
By William L. Tittle, Principal
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1
Nexant Overview
Nexant is a leading advisor to the energy and chemicals industry
Through Nexant’s global footprint we will provide you with valuable market insight
Nexant has offices in the major fuels and chemicals producing and consuming regions of the world.
Our international presence allows us to provide insight through our consultants’ local market
knowledge and our vast network of sector specialists.
Our History
Nexant has been advising clients in the
chemicals industry for over 40 years.
The company has completed over 3000 client
assignments in more than 100 countries.
Our People
Over 150 consultants in Consulting Division
worldwide.
Our consultants blend strategic consulting,
operational and technical expertise with deep
chemicals sector knowledge.
Nexant’s consultants are typically Chemical
Engineers, Economists and MBA graduates.
Many of our consultants have also spent
several years working in industry for energy &
chemicals producers.
Our Services and Products
Nexant provides corporate and private equity
clients with advice in the following areas:
– Strategic Planning
– Commercial analysis
– Transaction support: Due Diligence
– Technology assessment
– Independent expert
In addition, Nexant has proprietary technology
and commercial analysis (NexantThinkingTM)
which includes market dynamics and pricing
forecasts, capacity developments and
production cost economics
San Francisco New York
Houston
London
Bahrain Shanghai
Bangkok
Frankfurt
Washington
Head office
Nexant’s main consulting offices
Other offices
Kuala Lumpur
Tokyo Seoul
Beijing
Singapore
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2
Nexant Overview
Nexant business model is geared to end to end service of the complete energy and chemicalsvalue chain
UPSTREAM MIDSTREAM CHEMICALS DOWNSTREAM
Oil & Gas Service
- Sector Planning
- Shale Gas & Oil
- Coal
GREEN CHEMICALS RENEWABLE ENERGY
OIL AND GAS
Biomass
Gasification
Solar (Thermal & PV)
Wind Power
Clean Coal
CO2 Capture and Sequestration
Fuel Cells & Hydrogen
Geothermal
Syngas
Biopolymers
Olefins
Alcohols
Aromatics
Sourced from Biomass, Algae, Wastes, and Agricultural Sources
CHEMICALS AND CLEANTECH
Processing
LNG Liquefaction
LNG Shipping & Regasification
Oil & Gas Pipelines
- Gas Processing
- Gas Distribution
Petroleum Refining
Product Market Assessment
- Coal to Liquids
- Gas to Liquids
Gas & Naphtha Based Petrochemicals
Olefins & Aromatics
Polymers
Fertilizers
Specialty Chemicals
Advanced Materials
NEXANT CAPABILITY
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Ethylene Capacity-So Many Projects, So Much Uncertainty
Propylene-PDH Plants Rebuilds Supply Base Trends
Impact on C4s Supply
Threat from Renewables?
3
Agenda
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5
The selection of new investments in commodity chemicals is driven by specific parameters
Commodity Chemicals Competitiveness Criteria
PARAMETER
Size Capture economies of scale
Location Access to low cost feedstocks /
Deficit markets / Market access
Technology Cost advantage /
Product differentiation
Integration Synergies with adjacent
facilities
KEY OBJECTIVES
Where is demand growth occurring? Where are the accessible low cost feedstocks?
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6
What are the Geographic and Feedstock trends ?
US Shale Gas / Oil Reserves
Increased oil & gas production, resulting in lower energy prices
Increased production of co-produced ethane and other NGLs
Improved competitive position, resulting in reinvestment in commodity products
Moderate demand growth, but export opportunities
Middle East Oil & Gas Reserves
Further utilization of ethane and other available NGLs, but likely higher feedstock prices for future plants
Investments in new refinery capacity with a focus on refinery / petchem integration
Declining competitive position off-set by mixed feeds, integration/scale and focus on higher value products
China Coal Reserves
High demand growth and desire to displace imports
Increase focus on coal to chemicals and PDH (via propane imports)
Investments in new refinery capacity with a focus on refinery/petchem integration
Variable competitive position depending on feedstock.
Access to markets is key
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7
41 million tons of ethylene consumption growth is inline with GDP, with 46% of additions in Asia
Projected Ethylene Consumption Change by 2020
Ethylene Capacity Additions
Million Tons
Global capacity additions
of 53 million tons per
annum of ethylene.
This equates to between
35-45 new world scale
steam crackers
Share of Ethylene Capacity
Additions
232 153
182 206
2013 2017 2020
+29 +24
133
0
20
40
60
80
100
120
140
160
180
200
2013 2020
Mill
ion T
ons
174 +41
Asia 46%
ME & AF 22%
Americas 22%
Europe 10%
Over the period 2013-
2020 all major regions
are expected to increase
net ethylene capacity.
What are the feedstock
trends for ethylene?
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8
Ethylene production processes will vary by region depending on feedstock
Ethylene
Heavy Liquids (Naphtha, Gas
Oil)
NGL (ethane, LPG) Steam
Crackers
Coal / Natural Gas / Petcoke SynGas Methanol
MTO
Ethanol
Dimethyl Ether
Bio-ethanol
Sucrose-based biomass (sugarcane,
sugarbeets, sorghum)
Start-based biomass (wheat, corn, barley)
Ligno-cellulosic biomass
(wood, straw, grasses)
Bio-
Renewable
Routes
Methane
OCM*
*Siluria Technologies is latest proponent of OCM (Oxidative Coupling of Methane)
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IA: Moderate/high
FS: Ethane/NGLs
New activity driven by shale gas
NORTH AMERICA
IA: Low/decline
FS: Naphtha/Ethane
Selective investments in FSU/EE
Further rationalisation in the EU
EUROPE
IA: Low/moderate
FS: Mixed
Potential for ethane, naphtha and
bio based projects
SOUTH AMERICA
IA: Moderate/high
FS: Ethane/NGLs
Further utilisation of ethane & NGLs
Selective Refinery integrated projects
MIDDLE EAST & AFRICA
IA: High
FS: Naphtha/Coal
Refinery integrated projects with
further expansions in CTO/MTO
CHINA
IA: Moderate
FS: Naphtha
Refinery integrated projects in
selected markets by NOCs
SEA/INDIA
IA = INVESTMENT ACTIVITY
FS = FEEDSTOCK SLATE
9
Each region has its own feedstock position in terms of cost, type and accessibility. These present a host of opportunities and challenges for the industry. Majority of the investments are expected in China and Middle East
Ethylene Net Capacity Additions 2013-2020 (Million tons)
9
3
6
11
15
9
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10
Naphtha grows as a feedstock, but cracking production share is forecast to decline by around 5% through 2020 as a result of consumption of light feedstock in U.S. and ME as well as MTO investment in China
2013 2015 2020
Gas Oil Coal
2013 2015 2020
Naphtha
2012 2015 2020
Ethane
2013 2015 2020
Butane Propane
50% 47% 45% 42%
0%
25%
50%
75%
100%
2005 2013 2015 2020
Naphtha AGO Butane Propane Ethane Other
Global Ethylene Production Development by Feedstock Unit: Million tons per year of ethylene
+8
+4
+11
+18
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11
China is continuing its investment drive into coal based chemicals
0
2
4
6
8
10
12
14
16
2012 2013 2014 2015 2016 2017
Mill
ion
Tons
Propylene Ethylene
CTO/CTP Operating Plants in China CTO/CTP Capacity
There could be up to 14 million tons of combined new coal-based ethylene and propylene capacity
by 2017 if current firm plants are completed on schedule
Key success factors relate to the mine mouth coal price and availability of water for the methanol
production
MTO based on imported methanol another option being pursued in China
Xinjiang
Qinghai
Tibet
Gansu
Sichuan
Yunnan
Hainan
Guangxi
Guizhou Fujian Hunan
Hubei
Henan
Jiangxi
Guangdong
Ningxia
Inner Mongolia
Heilongjiang
Jilin
Liaoyang
Hebei Tianjin
Zhejiang
Anhui
Jiangsu
Shandong Shanxi
Shaanxi
Beijing
Shenhua Coal
Chemical Project
Datang Power Shenhua Baotou
Coal Chemical
Zhongyuan
Petrochemical
Ningbo
Heyuan
Wison
(Nanjing)
Chemical
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13
Even with a decline in gas rigs, the EIA Reference Case for both Tight Oil and Shale Gas Supply continues to be adjusted upward every year
EIA Shale Gas Production Forecast*
Last 3 Years (trillion cubic feet)
EIA Tight Oil Production Forecast*
Last 3 Years (million barrels per day)
Source: EIA, Nexant Analysis
* AEO (Annual Early Outlook) EIA Reference Case
Shale oil
peak in 2021
13
0
1
2
3
4
5
6
2009 2014 2019 2024P
rodu
ctio
n (m
illio
n ba
rrel
s pe
r da
y)
AEO 2012 AEO 2013 AEO 2014
0
2
4
6
8
10
12
14
16
18
2009 2014 2019 2024
Dry
Pro
duct
ion
(tril
lion
cubi
c fe
et)
AEO 2012 AEO 2013 AEO 2014
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200
400
600
800
1,000
1,200
1,400
1,600
2005.1 2007.1 2009.1 2011.1U
S D
olla
rs p
er T
on
Ethane E/P Naphtha
Many of the region’s existing crackers have undergone feedstock conversions and process optimization investments to maximize ethane cracking potential
Source: Nexant Source: Nexant
14
14
Ethylene cracking feedstock slate has shifted very quickly towards ethane, therefore improving product margins and production competitiveness versus heavier feedstock slates
U.S. Ethylene Feedstock Ratio
U.S. Ethylene Cash Cost of Production, $/ton
26%
45%
69% 76%
0%
20%
40%
60%
80%
100%
2005 2011 2015F 2020F
Wei
ght P
erce
nt
Ethane Propane Butanes Heavier than C4's
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1
5
Firm U.S. crackers match the low-end of ethane projections of 50 percent increase 2020 over 2012
0
5,000
10,000
15,000
20,000
25,000
New EthyleneCapacity
Low-endSupply
Forecast
High-endSupply
Forecast
Incr
emen
tal E
than
e V
olum
e,
Tho
usan
d To
ns p
er Y
ear
Company Location Capacity kt/yr
Chevron Phillips Cedar Bayou, TX 1,500
Dow Freeport, TX 1,500
ExxonMobil Baytown, TX 1,500
Formosa Plastics Point Comfort, TX 1,000
Ingleside Ethylene Ingleside, TX 544
Sasol Lake Charles, LA 1,500
Total 7,544
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1
6
There are enough crackers under study to occupy high-end ethane forecasts (Doubling by 2020)
0
5,000
10,000
15,000
20,000
25,000
NewEthyleneCapacity
Low-endSupply
Forecast
High-endSupply
Forecast
Incr
emen
tal E
than
e V
olum
e,
Tho
usan
d To
ns p
er Y
ear
Company Location Capacity kt/yr
Shell Pennsylvania 1,500
Braskem/
Odebrecht W Virginia 1,200
Axiall Lousiana 1,200
Indorama 1,300
Shin-Etsu USGC ~500
SABIC ~1,000
PTT Global Chemical ~1,000
Williams (Geismar II) Geismar, LA ~1,000
Others NA
Approximate Total 9,200
However, ethane exports may reach 6 million tons per year by 2020
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CP Chem, an early mover, saw estimated capital costs increase 20% from initial to final
estimates for its new ethane cracker and PE project
Shell cancelled its US GTL project when capital costs came in at twice the level of its
identical Pearl project
CHS suspended its North Dakota ammonia/urea project when capital costs came in at
twice its initial estimate
EPCs are currently unwilling to quote fixed price lump sum bids for major petrochemical
projects and creative approaches are being adopted to share risks between owners and
contractors
The result will likely be a slowing of project execution schedules in order to minimize capital
cost increases
Nexant estimates that with the anticipated rate of project implementation capital costs will
have increased 40-50% between 2012 and 2017
Capital costs are escalating rapidly due to the large number of U.S. petrochemical projects
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Propylene production from steam cracking is declining due to the preference for lighter feeds, leading to need for On-Purpose Propylene
19
Propylene Feedstocks and Value Chain
Steam cracker
Polymer / Chemical Grade
Propylene Refinery Grade Propylene Splitter
Refinery FCCU
Oxo -
alcohols Acrylonitrile Polypropylene Acrylic Acid
Propylene
Oxide Isopropanol Cumene
Propane
Dehydrogenation Metathesis MTO/MTP
On - Purpose Propylene (OPP) By - Product Propylene
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Source: Nexant
Available propylene is increasing in the Middle East, due to increased LPG cracking and propane dehydrogenation projects
In the US, the impact of shale gas has resulted in a move towards using lighter feedstocks in steam crackers, reducing propylene availability
0%
50%
100%
NorthAmerica
WesternEurope
Middle East Asia Pacific
Steam Cracker Refinery PDH MTO/MTP Others
0
25
50
NorthAmerica
WesternEurope
Middle East Asia Pacific
Mill
ion
Tons
Steam Cracker Refinery PDH MTO/MTP Others
20
Steam cracking and refinery sources currently account for the majority of propylene supply. On-purpose production on a global absolute volume basis is still relatively modest
Relative Capacity By Source – Propylene
(Percentage Volume Basis, 2013)
Capacity by Source – Propylene
(Absolute Volume Basis, 2012)
Source: Nexant
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Global Propylene Capacity Development by Feedstock
Source: Nexant
Global Propylene Capacity
Development:
(million tons per year):
PDH (in N America, China, E Europe and Middle East) and MTO/MTP (in China) impacting recent global propylene market tightness
62% 58% 55% 50%
33% 34%
33%
30%
0%
25%
50%
75%
100%
2007 2010 2013 2016
Cracker Refinery Metathesis PDH Other
Incremental supply from co-product sources continuing to be
insufficient to balance propylene demand growth…
2010 2013 2016
Cracker:
2010 2013 2016
Refinery:
2010 2013 2016
On-Purpose: PDH, MTP/MTO & Other:
+3.1
+1.6
+11
Significant amount of OPP
capacity being added
Going forward, a greater need for on-purpose production (OPP) capacity is emerging to meet future propylene demand requirements
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30 percent of global propylene supply will be produced from on-purpose sources by 2025
Global Propylene Production by Process
(thousand tons)
Overview
Propylene production from
steam cracking is declining in
some areas due to the
preference for lighter feeds.
PDH has been through a
phase of major expansion in
the Middle East, but the focus
is now moving to China and
the United States.
Methanol-based
developments are so far all in
China, and mainly based on
coal/methanol. Projects are
now being developed in gas-
advantaged regions such as
Central Asia and the United
States (BASF).
0
20,000
40,000
60,000
80,000
100,000
120,000
140,000
160,000
2000 2005 2010 2015 2020 2025
Steam Cracking Refinery FCC/DCC Metathesis
PDH Methanol Conversion
22
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23
MTO and PDH will constitute 45 percent of Chinese propylene capacity by 2018
China Propylene Capacity, (thousand tons)
Source: Nexant Analysis, OICA
0
5,000
10,000
15,000
20,000
25,000
30,000
35,000
40,000
2010 2011 2012 2013 2014 2015 2016 2017 2018 2019 2020
Steam Cracking Refinery PDH Methanol Conversion
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2.0
0.7
3.8
3.0
4.7
4.7
1.8
3.9
4
4.1
4.8
5
0 2 4 6
Others
Acrylonitrile
Propylene Oxide
Cumene
Polypropylene
Acrylic Acid
2013-2020 2000-2013
24
Global propylene consumption is forecast to grow at an average annual growth rate of 4.8% to 2020
Global Propylene Consumption by Derivative,
2013-e
Global Propylene Consumption Growth by
Derivative (percent Volume Growth, 2000-2013)
Poly-propylene
63%
Propylene Oxide
8%
Acrylonitrile 7%
Cumene 5%
Acrylic Acid 4%
Isopropanol 1%
Others 12%
Source: Nexant Analysis
As the predominant propylene derivative, polypropylene dictates the global growth outlook
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The import requirement of propylene derivatives tripled between 2000-12
Massive new capacity has been started up / is under construction / is in planning in China
Source: Nexant Source: Nexant
25
In China, a rising deficit in propylene derivatives over the past decade has spurred massive new investments in production capacity
Imports of Propylene Derivatives In China,
(ton of each product)
Incremental Propylene Derivatives Capacity in
China, (base year = 2012, ton of each product)
0
10
20
30
2016 2020
Mill
ion
Tons
per
Yea
r
PP PO Acrylonitrile
Phenol Acrylic acid Isopropanol
0
4
8
2000 2006 2012
Mill
ion
Tons
per
Yea
r
PP PO Acrylonitrile
Phenol Acrylic acid Isopropanol
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26
One of the key factors determining profitability of U.S. PDH investments will be competitiveness versus MTP in China
Propylene Cost Plus Return, $ per MT, 2017
<Insert date using ‘Insert – Header & Footer’> <Insert job number using 'Insert - Header & Footer'>
However, equally important will be the competitiveness of U.S. PDH with the many coastal China PDH plants being built
0
500
1,000
1,500
2,000
US PDH China MTP Imported MeOH at COP
Cos
t + 1
0% R
OC
E
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Despite relatively weak performance in recent years, Nexant’s forecast assumes propylene
consumption will return to growth rates well above GDP, before again descending towards GDP rates
– The majority of new demand is in Asia, with polypropylene and China the primary drivers
– Short of a severe demand downturn, China is likely to remain an importer of propylene and
derivatives
Propylene feedstock slates are set to transform, as a greater need for on-purpose capacity is required
to meet future demand requirements
– Despite projected higher global operating rates, relative propylene output from steam cracking will
decrease further as a result of the ongoing shift towards lighter feeds.
– The U.S. is set to fill its propylene supply gap through several PDH plants in the US, and at least one
in Canada; in addition BASF announced a methane to propylene unit
– In Western Europe, increased imports of ethane and LPG, and the closure of some older steam
crackers, will reduce propylene supply
– Chinese propylene capacity is set to surge as a result of numerous MTO/MTP and PDH
developments; yet China is projected to continue to import both propylene and most derivatives
A large propylene price premium over ethylene is not sustainable in the long term, due both to inter-
polymer competition in PP as well as rising on-purpose production
27
Summary: On-Purpose Propylene will be increasingly required
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Butane/butene dehydrogenation is an alternative route for butadiene production
C4 Stream
Refinery FCCU Dehydrogenation
Butane / Butene
Dehydrogenation
Styrene Butadiene Rubber,
Polybutadiene Rubber,
Styrene Butadiene Latex ,
ABS, HMDA, SBCs,
Nitrile Rubber,
Etc.
Butadiene Derivatives Mixed Butanes Mixed Butenes Butene-1
N-butane
Derivatives,
Acetic Acid,
gasoline,
Etc.
Butan-2-ol,
Higher Oxo-
Alcohols,
Etc.
LLDPE
comononer.
HDPE
comonomer,
Etc.
High Purity:
Butyl
rubber
etc.
Contained:
MTBE
ETBE
Etc.
29
Butadiene Isobutylene
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30
Why naphtha supplies are important for the butadiene industry
Co-Products from Ethylene Plants
(per ton ethylene)
Butadiene Yield per Ton Ethylene
(by feedstock)
Butadiene supply is highly dependent on feedslate type. Majority of butadiene supply is from heavy feed cracker (e.g., naphtha, gas oil)
Except for the USA, where C4s are aggregated and processed, butadiene component from light feed cracker is typically co-crack recycled as the quantity is small and insufficient for commercial scale butadiene
Methanol-to-olefins plant does not produce butadiene but butylenes
0.0
0.5
1.0
1.5
2.0
2.5
MTO Ethane Propane n-Butane Naphtha
Pro
duct
per
Ton
Eth
ylen
e
Ethylene Propylene Butadiene BTX
0%
5%
10%
15%
20%
MTO Ethane Propane n-Butane Naphtha
BD
Pro
duct
ion
per
Ton
Eth
ylen
e
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31
Global butadiene consumption is forecast to grow at an average annual growth rate of 3.2% to 2020 driven mainly by automotive sector
Global Butadiene Demand by Application (2013) Global Butadiene Demand Growth by
Application (%AAGR)
Total Demand = 10.5 Million tons
Butadiene industry is driven by demand growth from BR, SBR (for tires) and ABS
Demand into HMDA (hexamethylene diamine) for nylon 6,6 production is driven by use of nylon tyre cord and resin for injection molded components
Other demand includes nitrile rubber and styrene block co-polymers (SBCs)
AAGR (%)
'13-'20
2.0
7.4
0.6
3.9
4.1
3.0
3.2
-5 0 5 10
Global
BR
SBR
ABS
SBL
HMDA
Others
2013-2020 2000-2013
Butadiene Rubber
SB Rubber ABS
SB Latex
HMDA
Others
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In North America, after a decade of plant closures, new tire factories may lead to additional domestic rubber demand
Source: Michelin / LMC
North American PC Replacement Tire Capacity, (Millions of tires)
However, existing plants may also shut-down; but worst case, it appears that rubber demand decline
(especially for premium grades) may finally flatten
277
194
226
0
50
100
150
200
250
300
2002 2012 2018
2012-2018 Projections:
+16% PC tire units
PC
Announcements:
Michelin
Bridgestone
Continental
Kumho
Toyo
Pirelli
~30%
Units
~12%
tonnage
14 plant closures
The Story of North American
Industrial Capacity
After a rational phase,
North American
manufacturers are actively
investing in premium and
growing segments
Other Announcements:
Michelin (TB & OTR)
Bridgestone (TB & OTR)
Continental (TB)
Yokohama (TB)
Mitas (AG)
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33
Asia will continue to be the focus of global development for butadiene, as well as derivatives
Asia Pacific
Europe
North America
South America
ME / AF
Total Demand = 10.5 Million tons
Global Butadiene Demand Growth by Region
0 5 10 15
Global
Asia Pacific
Europe
North America
South America
ME / AF 2013 2020
AAGR (%)
'13-'20
10.7
5.8
-0.1
1.3
4.5
3.2
Global Butadiene Demand by Region (2013)
+2.6
million
Additional annual butadiene demand growth over the next 7 years is around 2.6 million tons per year of which around 80 percent will be in Asia, especially China
Is butadiene supply from steam crackers sufficient for incremental butadiene demand ?
Con
sum
ptio
n (M
illio
n To
ns)
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Nexant’s Global Butadiene Supply – Demand – Trade - Pricing Model
Shale gas
availability and
pricing
Naphtha
availability and
pricing
Ethylene Demand
growth – New &
Refurbished
Crackers C4s Supply
Butadiene
C2-C4
Hydrogenation
Ethylene
Feedstock Model
Cracker C4 Analysis
Coal to Olefins
CTO/MTO
Butadiene Supply
On-
purpose
Butadiene
C4
On-Purpose BD
Analysis
BD
Demand &
Substitution
Analysis
Butadiene
Derivatives
Demand
Substitutes for
BD Derivatives
Demand
BD
Butadiene
Exports/Imports
Demand Drivers
Regional GDP
Growth
Oil Price Scenario
Vehicle Sales
Tire Chemistry
Replacement tire
cycle
Miles driven
Recession Echo
Effect
Appliances
Electronics
Trade Dynamics
Echo recovery
BD Price
Butadiene Demand
C4
C4?
Refinery and Bio
C4 Source
34
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35
A gradual feedstock slate transition in the ethylene sector will be driving down the portion of butadiene supply from steam crackers
Global Butadiene: Ethylene Production Ratio
5%
6%
7%
8%
9%
10%
0
2,000
4,000
6,000
8,000
10,000
12,000
14,000
2000 2005 2010 2015 2020
% B
D/E
thyl
ene
Pro
duct
ion
Tho
usan
d To
ns o
f But
adie
ne p
er Y
ear
Butadiene Production from Extraction % BD/E
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36
Over the period 2013-2020, additional around 2.6 million tons per year of butadiene production is required to meet global demand
Ethylene Demand Growth
Butadiene Demand Growth
Additional 2.6 mmta of butadiene demand is equivalent to almost 20 mmta of liquid cracker feed, while ethylene production of naphtha feed crackers are expected to increase by only 11 mmta
The remainder of ethylene growth is from ethane (18 mmta); coal (8 mmta); propane & butane (4 mmta) which yield little (or no) butadiene
0
50
100
150
200
2013 2020
Mill
ion
Tons
per
Yea
r
41 Million
3.9% AAGR
0
5
10
15
2013 2020M
illio
n To
ns p
er Y
ear
2.6 Million
3.2% AAGR
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37
Where can missing butadiene supply come from?
Butadiene
Mixed C4s Extraction Process
Butane
Butenes
Dehydrogenation
Process
Dehydrogenation
Process
Bio-mass
Bio-ethanol
Bio-butanol
Butanediol
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Asia added 1 million tons of new capacity in 2014, of which a large share is dehydrogenation
38
Asia Butadiene Capacity Addition, Thousand tons
0
200
400
600
800
1,000
1,200
2011 2012 2013 2014 2015 2016 2017
Dehydrogenation Extractive Distillation
Several new steam crackers in Asia with 1.6 million tons of new butadiene capacity by 2015
Butene dehydrogenation technology is being developed at twelve new plants in China with total capacity of around 1.2 million tons per year. Two plants are already operational
On-purpose capacity is likely to be used as ‘top up’ capacity during periods of tight supply/demand
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39
On-purpose butadiene production will be required to fulfill total butadiene demand
Global Butadiene Capacity, (by process)
China Butadiene Capacity, (by process)
China will represent 40% of global butadiene capacity in 2020
On-purpose butadiene production will concentrate in China, where demand growth is outpacing butadiene supply growth and (eventually) in the U.S., where butadiene supply is also short
0%
2%
4%
6%
8%
10%
12%
0
2,000
4,000
6,000
8,000
10,000
12,000
14,000
2000 2003 2006 2009 2012 2015 2018D
ehyd
roge
natio
n P
ortio
n
Tho
usan
d To
ns p
er Y
ear
ExtractionDehydrogenation
0
1,000
2,000
3,000
4,000
5,000
6,000
2005 2010 2013 2020 Est.
Tho
usan
d To
ns p
er Y
ear
Dehydrogenation Extractive Distillation
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0
500
1,000
1,500
2,000
2,500
0
500
1,000
1,500
2,000
2,500
3,000
3,500
2000 2004 2008 2012
But
adie
ne a
nd N
apht
ha P
rice
Gap
US
Dol
lars
per
Ton
Naphtha Butadiene BD-N Gap
40
Value of ethylene has been in line with naphtha price while butadiene has been increasing with extreme volatility to a higher value
Asia Butadiene and Ethylene Prices Asia Butadiene and Naphtha Prices
Butadiene/Ethylene
Price Trend
Historically, butadiene cost a small premium over ethylene price
As a result of heavy capacity addition of ethylene crackers in Middle East since 2008 and the effect of shale gas, butadiene supplies have tightened, the price level has increased, and the ratio of butadiene to ethylene prices stepped up with the record high in 2011
0.0
0.5
1.0
1.5
2.0
2.5
3.0
0
500
1,000
1,500
2,000
2,500
3,000
3,500
2000 2004 2008 2012
BD
/Eth
ylen
e P
rice
US
Dol
lars
per
Ton
Ethylene Butadiene BD/Ethylene
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Butadiene is difficult to store and degrades with time, so normally it is converted to a derivative, sold
and converted, or destroyed. As a result, butadiene prices have become increasingly volatile as the
supply demand balance for mixed C4 has tightened
Echo Recession for tires: Synthetic rubber demand is extremely volatile, as today’s demand for rubber
depends on sale of both new vehicles and sales of replacement tires for vehicles that were sold during
the recession and earlier. Consequently, 2012 was a poor year for rubber demand and 2013 was even
worse
Echo Recovery: It is likely that synthetic rubber demand for replacement tire will improve in the short-
term, as 2014 will be four years after a large increase in new vehicle sales (post recession in 2010) in
America and Western Europe and five years after a 45 percent increase in new vehicle production in
China (2009)
Butadiene consumption: Expected to grow by 2.6 million tons per year by 2020 with specific focus in
China, which will account for 60 percent of incremental demand
Butadiene supply: Naphtha crackers should supply around 2 mmta by 2020 based on 11 mmta
additional naphtha-based ethylene production. Therefore, naphtha will remain the primary source of
butadiene production
Butadiene’s intrinsic properties and position as a by-product of ethylene production creates a lot of interesting market dynamics
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New byproduct BD supplies postpones the necessity for OPBD (until the next price spike!)
New European BD Supplies: Several European steam cracker operators that until recently exported
mixed C4, or destroyed their C4/butadiene through hydrogenation, have announced plans for almost
500 000 tons of butadiene extraction capacity by 2016
– New Asian BD Supplies: In addition, there are several new steam crackers in Asia with 1.6 million
tons of new butadiene capacity by 2015
– BD from C4 supplies will be insufficient: In the long-term, butadiene demand is growing at slightly
less than GDP, which is faster than supplies of mixed C4 from steam crackers
New Price setting mechanism for BD: Consequently, the market will develop new sources of
marginally cost effective butadiene supply - for instance, on-purpose butadiene (OPBD) from
dehydrogenation or bio-based butadiene. The marginal cost of this OPBD will be the new price setting
mechanism for butadiene
Chinese OPBD Supply: China producers have announced plans for 12 plants producing 1.25 million
tons per year of OPBD, of which 2 plants are already operational. This OPBD capacity is likely to be
used as swing capacity during periods of tight supply/demand
The long-term shortage of mixed C4 has led to rapid development of additional BD extraction and OPBD in China
Butadiene prices are likely to remain volatile until additional (on-purpose) supplies balance the market
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Renewable Chemicals Value Chain
Feedstocks
Corn
Sugar
Switchgrass
Hybrid Poplar
Corn Stover
MSW
Conversion
Technologies
Cellulosic
Hydrolysis
Genetically Modified
Fermentations
Biomass
Gasification
Thermochemical
and Catalytic
Transformation
Chemicals/
Plastics
C1
C2
C3
C4
Aromatics
Vegetable Oils
Others
Fabrication
Technologies
Injection molding
Blow molding
Thermoforming
End Products
Packaging
Automotive
Electronics
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Renewable Chemicals Value Chain and Cost Competitiveness
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Renewable Bio-Adipic Acid Cost Competitiveness, 2014
0
200
400
600
800
1,000
1,200
1,400
1,600
1,800
2,000
BoricAcid
Rennovia20 kta
Rennovia135 kta
Boric Acid
Dol
lars
per
Ton
Net Raw Materials Net Utilities Fixed Costs Depreciation
Stand-Alone Adipic Acid Plant Plant Integrated Upstream
with Benzene
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pX Price
Anellotech Gevo Micromidas Virent Petro
Aromatic Renewable Chemicals Cost Competitiveness: para-Xylene
para-Xylene Competitive Costs, 1Q2014
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Special Report: U.S. Ethane Utilization : Domestic Use Versus Exports
Special Report : On-purpose Propylene : Is Propane the Best Feedstock?
Petroleum & Petrochemicals Economic (PPE) : 2014 Butadiene & Derivatives
Petroleum & Petrochemicals Economic (PPE) : 2014 Propylene & Derivatives
Petroleum & Petrochemicals Economic (PPE) : 2014 Olefins
Process Evaluation/Research Planning (PERP) program : Propylene
Process Evaluation/Research Planning (PERP) program : Bio-Butadiene
Process Evaluation/Research Planning (PERP) program : On-purpose Butadiene
Process Evaluation/Research Planning (PERP) program : Butadiene/Butylenes
Special Report: Biorenewable Insights
Please visit http://thinking.nexant.com/ for more information.
49
Latest NexantThinking’s Related Reports
William L. Tittle Principal Nexant, Inc. 44 South Broadway White Plains, NY 10601 USA tel +1 914 609-0303 email [email protected]
www.nexant.com