the future of the gulf coast petrochemical industry
TRANSCRIPT
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The Role of Innovation in US GulfCoast Competitiveness
The Future of the Gulf CoastPetrochemical Industry
Global Energy Management Institute
University of Houston
Aril !"# !$$%
James H. DAuriaUOP C
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A!en"a
The cometitiveness ga
Potential for technology innovations toimrove cometitiveness
&ey technology innovations
E'amles of otions for the U(GC
The integration conundrum
Final thoughts
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The USGC Cost of Pro"u#tion Gap$%th&lene %'ample
)orth American Ethane Crac*ers
Have +ecome the High Cost Producers
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Ho( Can Te#hnolo!& Innovation Help)
Technology can be develoed to, Ma*e use of lo-er cost and.or uni/ue
feedstoc*s
Create feedstoc* or roduct fle'ibility
Hedge0educe volatility
0educe re/uired caital investment
Ma*e e'isting assets more efficient
Integrate e'isting assets to increaseefficiency
Imrove roduct /uality
Cometitive advantage is gained
-hen technology innovations arelin*ed -ith the right mar*et or
business circumstances
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Alternative *ee"sto#+s to Consi"er
1o- 2alue 0efinery.Crac*er (treams 1ight Gases
+y Product 3lefins
Pentanes
1ight Cycle 3il
0esid
0emote Gas
Coal 4 +iomass 444
+asis for U( Industry Advantage,
GC 0efining Concentration
Atlantic +asin (tranded Gas
Coal 0eserves
+iomass otential
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,e& Te#hnolo!& Innovations Use of Alternative feedstoc*s
(tranded Gas to 3lefins.Polymers5Mega6Methanol7 PlantsMethanol to 3lefins
Clean Coal
0efinery6 Petrochemical integration Petrochemicals from FCC
3lefins Conversion
1C3 Conversion
)ahtha otimi8ation
1onger term +rea*through Technologies
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-ethanol-TO %#onomies of S#aleConstant IRR
Mega Methanol Plants Enable Gas to 3lefins Pro9ects
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-TO on the USGC
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-TO on the USGC
/ 0ase" on 123-T methanol from Atlanti# 0asin Stran"e" Gas
// 0ase" on 1455-T methanol
U(GC MT3 +ecomes Attractive At High 3il Prices
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Clean Coal Te#hnolo!&CoalCoal
Gasification (ynthesis Gas
Methanol
Po-erF6T 1i/uids(team# H!
Chemicals
Alternative GasificationFeedstoc*s,
Petroleum co*e0esidbio6residue
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Coal to Olefins in the US67 18500 Cru"e9
* Based on correlation
of 97-05 CMAI data:
weighted avg. feedstoc
** Ass!"es #$%5&M'
"ethanol fro" coal
High 3il Prices Imrove Attractiveness of Coal To 3lefins
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,e& Te#hnolo!& Innovations
Use of Alternative feedstoc*s (tranded Gas to 3lefins.Polymers
5Mega6Methanol7 Plants
Methanol to 3lefins
Clean Coal 0efinery6 Petrochemical integration
Petrochemicals from FCC
3lefins Conversion
1C3 Conversion
)ahtha otimi8ation
1onger term +rea*through Technologies
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Prop&lene from Refineries
2G3
Crude
3il
Cru"eCru"eColumnColumn
C:and 1ighter
(traight 0un Gasoline
&erosene
AG3
:a#uum:a#uumColumnColumn
2acuum 0esidue2acuum 0esidue
FCCFCC
ProyleneProylene
Fuel GasFuel Gas
1PG1PG
GasolineGasoline
;iesel;iesel
HeavyHeavy
Fuel 3ilFuel 3il
P0UP0U
;o-nstreamProcessing
UOP 4288K-40efinery FCC is an Imortant (ource of Proylene
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Petro#hemi#als from *CC
Proylene 6 % -t?
GasolineGasoline
EnhancedEnhancedProyleneProylene% @ -t?% @ -t?
CC>>BB
GasolineGasoline
High6(everityHigh6(everityFCCFCC
$ 6D -t?$ 6D -t?
CC!!BB
CC>>BB
GasolineGasoline
PetroFCCPetroFCC!$ -t?!$ -t?
CC!!BB
CC>>BB
AromaticsAromatics
UOP 4399A-7
In#reas
in!Petr
o#hemi
#alPro"u#t
ion
Challenge, Manage Across Traditional +oundaries
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RefineriesRefineries
FCC
3lefin
3lefin0ecovery
GasGas
3ils3ils FCCGasolineGasoline
Cycle 3ilsCycle 3ils
1ight1ight
3lefins3lefins
CC::6C6C
1PG1PG
CC!!BBCC>>BB
3lefin
Crac*ing
Olefins Conversion Te#hnolo!&
;aphtha Cra#+ers;aphtha Cra#+ers
Furnace Product0ecovery
CC%%.C.CDDParaffin60ichParaffin60ich
CC
::.C.C
%%
3lefins3lefins
CC!!BB
CC>>BB
3lefin
Crac*ing
)ahtha)ahtha
UOP 4399A-22
Metathesis, Converts ethylene C: olefins to roylene
3lefin Crac*ing, Converts C: @ C olefin streams to roylene ethylene
Utili8e U(GC refinery li/uid crac*er caacity
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U1(;U1(;
)e- catalysis selectivelyoens rings to ugrade 1ightCycle 3il to roduce,
Clean fuels
+T Aromatics
Environmental +enefits,
0educes H(F3 roduction
U1( ;iesel co6roduct
U1( Gasoline co6roduct
Rin! Openin! to Up!ra"e CO
1C31C3
1C3 0ing3ening
High 3ctaneHigh 3ctaneGasolineGasoline
PetrochemicalsPetrochemicals
UOP 4288A-18
U(GC 3ortunity, Pool 1C3 (treams
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;aphtha Optimi$?higher than -ithconventional nahtha
(ame roylene yield
Increased octane6barrel roduction
Economic value of J>$ MM.year
0e/uires close integration of olefins gasoline roduction
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Concentration of refining caacity in U(GC
rovides basis for cometitive advantage Technology innovations that cross traditional
boundaries can create economic value andcost advantage 6 53n Paer7
+arriers to integration are many, Increasing comle'ity.1imiting fle'ibility
Conflicting ob9ectives
Mi'ing disarate cultures
;ifficult technical issues
;iffusing business focus KLhat businessare -e in4
The Inte!ration Conun"rum
)eed to develo integration enablers
+usiness management ractices
Advanced rocess technology
Information technology
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on!er Term Te#hnolo!& Outloo+
Continuing investments are needed to develone- chemistries
E'amle areas of focus, Catalytic )ahtha Crac*ing
Paraffin ActivationEthane +en8ene to E+;irect Proane to P3# CA)# Acrylic AcidPentanes to Higher 2alue Chemicals
;irect Methane to Methanol 0ene-ables as Feedstoc*s Kcarbohydrates#
biomass
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The Role of Te#hnolo!&$*inal Thou!hts
Technologies are available today to ta*e advantage oflo-er cost feeds
0emote gas# coal# refinery by6roducts
Future technology advances -ill continue to come viarocess engineering catalysis innovations
)e- technology needs to be matched -ith the rightsituations to rovide a cometitive advantage= ForU(GC,
Integration -ith refining# o-er Ability to increase roylene roduction Pooling of by6roduct streams
Access to Atlantic basis remote gas# U( coal Can -e imrove the ris*6re-ard balance4
Cost to develo commerciali8e ne- technology First user ris*s re-ards Government regulations incentives
Mar*et uncertainties
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THA;, =OU