pathways to profit uop dehydrogenation...
TRANSCRIPT
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1914 - 2014 A Century of Innovation in the Oil and Gas Industry
2014 UOP LLC. All rights reserved.
Pathways to Profit UOP Dehydrogenation Technology
Anish Paunwala
UOP 6570H_R_1
16th INDIAN Petrochem Conference Mumbai, India October 30-31, 2014
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Agenda
Propane
Butane
Propylene
Isobutylene
UOP OleflexTM Process
UOP 6570H_R_2
Light Olefin Demand Outlook
Light Olefin Supply Routes and Market Shift
On-Purpose Propylene Production Technology
UOP Oleflex Process
Why Customers Choose Oleflex Process?
Conclusion
PP
Acrylonitrile
PO
MTBE
Cumene
Etc..
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Tremendous Opportunities in Petrochemicals
0
50
100
150
200
250
300
350
2000 2005 2010 2015 2020 2025
Millio
n M
TA
Light Olefin Demand
Propylene
Ethylene
World demand for ethylene and propylene growing (about 4%/yr)
More than 100 MMTA of additional capacity will be needed by 2025
Consumption being driven by growing middle class in developing regions
The world market continues to drive demand for products derived from light olefins
Source: IHS Chemical UOP 6570H_R_3
http://www.google.com/aclk?sa=l&ai=CJ_mBofm2TpmmNcmziAL4noDPDb-hkIQBv5y__RCZ7uPQLwgAEAEgk6z7BVCogYu4-_____8BYMm-yYbEo8gXoAH71b3_A8gBAaoEGU_Qg8I1jSBVB2I9crzp0-11jJNT4GayaF8&sig=AOD64_2YbSUQ8gcSc5xdqV7LO98QmQAGAg&ved=0CAUQ1xI&adurl=http://www.dultmeier.com/prod-search.asp?source=google&searchstring=HDPE&rct=j&q=high density polyethylene pipe&ctbm=ischhttp://en.wikipedia.org/wiki/File:Bonduelle.frozen.JPG
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Cracker Feed Slate Swings Past Propylene
Shift to lower cost, lighter feeds results in decrease in propylene
Ethane
E/P Mix
LPG
Light Naphtha
FBR
Naphtha
Gas Oil
Ethylene
Propylene
Butadiene
Other C4 By-products
Pygas
Cracker Feeds Cracker Products
Steam Cracker
UOP 6570H_R_4
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Refinery Objective
By Products
Shift towards heavier diesel reduces byproduct light olefins
Refinery Shifts Balance Away from Light Olefins
Refinery economics favor diesel production over gasoline in many regions
Less severe catalytic cracking, more mild hydrocracking produce less gasoline and less light byproducts
Diesel Ethylene
Propylene
UOP 6570H_R_5
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Tremendous Opportunities in Light Olefins
0
50
100
150
200
250
300
350
2000 2005 2010 2015 2020 2025
Millio
n M
TA
Light Olefin Supply
Propylene - Other
Propylene - FCC
Propylene - Steam Cracking
Ethylene - Steam Cracking
UOP technologies to meet your light olefin market demands
Growing share from other sources besides steam cracking and refineries
Propylene gap developing
Several options for on-purpose propylene production
Source: IHS Chemical UOP 6570H_R_6
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UOP 6570H_R_7
Get into the Action with Oleflex Process
Propane
Isobutane
Propylene
Isobutylene
High performance plastic
Fiber
Packaging
Gasoline Blending Components
MTBE
Iso-Octane
ETBE
Synthetic Rubbers & Acrylics
Propane
Isobutane +
Propylene +
Isobutylene
H2
UOP Oleflex Process
Feedstocks Products Uses
Economic
Feasibility-
Low CoP,
Low Investment
High IRR or
NPV
Simple
Process
and Easy
to Operate
Proven &
Strong
Technical
Support
Safe and
Environment
Friendly
Selection of Process
Technology
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Capacity
650 KMTA
500 KMTA
350 KMTA
PDH Project Economics Example
Profitability is attractive over wide range of price differentials
PDH P-P Spread is Main Economic Driver
PDH economics primarily driven by the price differentials between propylene and propane
Data Source: IHS Chemical
PG Propylene Propane Price Spread, $/MT
Propylene to Propane differentials support investment in PDH
1,500
1,300
1,100
900
700
500
300
100
00 01 02 03 04 05 06 07 08 09 10 11 12 13 14 15 16
W. Europe
SE Asia
NE Asia
North America
Saudi Arabia
$/M
T
Year
UOP 6570H_R_8
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Oleflex
Unit
C3 Oleflex Complex Simple Perfection
C3 LPG
C4+
Byproduct H2
C2-
Propylene
SHP
P-P Splitter
Deethanizer
Depropanizer
Selective Hydrogenation Process converts methyl acetylene & propadiene to valuable propylene
Elegant & simple solution!
UOP Oleflex Process used in 12 of the 19 operating PDH Units today
UOP 6570H_R_9
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Heater Cells
Net Hydrogen
To Frac Section
Dryer
Cold Box
Fresh & Recycle
Feed
H2 Recycle
CCR
Rx Effluent Compressor
Regeneration Section
Reactor Section
Product Recovery Section
Catalyst Flow
C3 Oleflex Unit = 4 Rxs C4 Oleflex Unit = 3 Rxs
Leverage UOP CCR Experience in PDH/BDH
Positive Pressure / Pt Catalyst
Lowest Energy Usage & Emissions
Fewest & Smallest Reactors
Catalyst Change-Out without Shutdown
>250 UOP CCRs in Operation Today
UOP 6570H_R_10
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Six Operating C4 Oleflex Complexes World-Wide
Fresh Methanol
MTBE
C4 LPG
C5+
DIB Column
DeC3 Column
C3-
nC4 iC4
iC4 iC4=
H2 By-product
Alternate End-Product processing options:
ETBE from Ethanol, Tert-Butyl Alcohol from Water
Alkylation (Indirect or Direct)
High Purity Isobutylene (HPIB) via MTBE Decomposition
Others (Methyl MethAcrylate, Isoprene, etc.)
Oleflex Unit
ButamerTM Unit
EthermaxTM Unit
Raffinate Treatment
UOP 6570H_R_11
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Ethermax Unit
Fresh Methanol
MTBE
LPG
Butamer Unit
C3= Oleflex
Unit
C3/C4 Separation Section
C2-
C5+
C3/C4 Oleflex MTBE Complex
UOP has 20 years of experience for C3/C4 dehydrogenation
DIB Column
Raffinate Treatment
Net Hydrogen
UOP 6570H_R_12
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0
2,000
4,000
6,000
8,000
10,000
12,000
Ole
fin
Ca
pa
cit
y, k
MT
A
Award, Design or Construction
Commissioned
iC4 Dehydro C3 Dehydro
5 units 11 units
5 units
C3/iC4 Dehydro
UOP Leads the Way in C3 and iC4 Dehydro
9 units
1 unit
13 units
UOP has been awarded 28 of the last 33 dehydro projects world-wide since 2011
Worlds Largest PDH at 1000 kmta and 2 PDH Projects at 750 kmta propylene capacity
Highest ROI and Highly Reliable Technology keeps Oleflex
Process as the choice of the industry UOP 6570H_R_13
+3
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Location of Operating UOP C3 Oleflex Units
14
Russia and China (x2) join the Oleflex Family
UOP 6520-14
14
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UOP Proven Track Record of Innovation
1990-1992 - 1st Commercial Oleflex Units with DeH-6 Catalyst
1992-1993 DeH-8 and DeH-10 Catalysts (2nd and 3rd Generations)
1996 DeH-12 Catalyst (4th Generation)
2001 DeH-14 Catalyst (5th Generation)
2007 DeH-16 Catalyst (6th Generation)
1995 250 kMTA propylene designed
1998 300 & 350 kMTA propylene designed
2003 400 kMTA propylene designed
2004 460 kMTA propylene designed
2008 510 kMTA propylene designed
2011 750 kMTA propylene designed
2013 1000 kMTA propylene design
2012 UOP/HPS Oleflex Automation Package
2012 UOP/HPS Training Simulator
Continuous Innovation Driven by Customer Needs
30th licensed Oleflex Unit (>12.0 MMTA)
15th licensed Oleflex Unit (>5.0 MMTA )
10th licensed Oleflex Unit (>3.0 MMTA)
UOP 5809K_RP-15
2014 DeH-18 (7th Generation)
UOP - CONFIDENTIAL
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UOPs Modular and Equipment Commitment
UOP Enhanced Tubes
Modular supply by UOP
UOP Column Internals
Advance your schedule and improve your bottom line with UOP Equipment & Modular Supply
UOP 6005K_RP-16
MD / ECMD Trays
Smaller tower diameter
Close tray spacing
Lower column pressure drop
High Flux / High Cond Tubes
Highest heat transfer performance
Closer Approach
Fewer / smaller bundles
Modular Supply
Highest quality
Delivered on time & on budget
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Lowest Overall Cost of Production:
Low feed consumption design available
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High Reliability / On-Stream Availability
Constant process conditions
Robust design incorporates largest operating base
CCR technology well proven across the industry
Smallest Environmental Footprint:
Lowest energy leads to lowest CO2
Low NOx & VOC emissions
Non-toxic catalyst system
Why Customers Choose UOP Oleflex (Cont..)
UOP 6570H_R_18
The safest & most environmentally friendly technology also leads in reliability
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In Conclusion
UOPs Oleflex Process: Best dehydrogenation technology
Lowest CAPEX + lowest CCOP = Best Bottom Line
Largest experience base & most reliable technology
UOP as Your Technology Provider: The best keeps getting better
Continuous innovation for new & existing customers
Extensive capabilities with regional support
Drive Your Profitability to new heights with UOP
as your Technology Provider
UOP 6570H_R_19
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Thank You
UOP 6570H_R_20
Pathways to Profit - UOP Dehydrogenation Technology
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UOP 6570H_R_21