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    Opportunities andOpportunities andDevelo ments inDevelo ments in araara--X leneX lene

    ProductionProductionGuangdong Qu

    2014 China PX Development ForumApril 10-11, 2014

    2014 UOP LLC. All rights reserved. UOP 6123-1

    ,

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    Aromatics Technology Innovation

    Latest UOP technologies enable the lowestcost of production of aromatics

    UOP 6044P-2

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    Polyester chain drivers continue tobe strong

    ACT FRCST

    Key demand factors:

    Global economy Regional Middle Class Growth Substitut ion (container applications) Recycle & Renewable Raws

    PCI

    Fundamentals remain good

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    Global pX demand will increase by75% in 10 years

    Current View Q1 2014

    ~30 M~30 M

    ~ -

    ~~

    Source: UOP (SBA-CCI & PCI)

    New pX capacity needed to match demand growth

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    Chinas growing economydrives global pX demand

    35 M

    40 M

    -

    China

    Other Asia Pacific

    30 M

    India

    N AmericaME

    Europe 19 M

    20 M

    tric

    Tons

    10 M

    15 MM

    M

    5 M

    Almost 20 million tons of p-X demand growth in china alone

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    China will not be able to meet itspara-Xylene demand alone

    To

    ns

    Metri

    Deficit in China met via imports from Middle East andAsia Pacific regions

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    Para-Xylene margins have been atattractive levels

    PX naphtha marginshave begun to decline &expec e o con nue n

    2014 2015

    2011-2013 s reads haveexceeded most every prioryear average

    was a goo year ornaphtha based producers;mixed xylenes based

    roducers have been

    squeezed by MX suppliers

    Naphtha based

    advantage

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    p-Xylene Cost of Production impacted byregional utility costs

    $1,065 $1,044 $1,041$1,000 $988

    1,000

    1,200

    800

    PX

    Capital Charges

    Fixed COPCat & Chems

    Utilities

    $888 $870 $896$803

    $859

    400$/M

    NCOP

    CCOP

    0

    200

    East

    Basis Assumed:Energy Values, /mm btu: AP = $5.50 USGC = $3.9 China = $6.00 India = $4.20 ME = $1.25Location Factors: AP = 1.02 USGC = 1.00 China = 0.80 India = 0.77 ME = 1.08

    Reducing COP drives profitabil ity UOP 6044P-8

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    Latest technology advances drive COPreduction

    COP ContributorsCOP ContributorsAdvanced CatalystsAdvanced Catalysts

    and Adsorbentsand AdsorbentsEfficient Designs,Efficient Designs,

    World Class ServiceWorld Class Service

    FeedstockFeedstock Reduced byproduct formation,Reduced byproduct formation,enhanced recoveriesenhanced recoveriesMaximizing productMaximizing product

    recoveries drives feedstockrecoveries drives feedstockutilizationutilization

    Utilities

    High activity for reduced energyinput; High recoveries and

    maximum yields for reduced

    recycles

    Advanced processintegration maximizes

    energy efficiency

    Capital High activities and capacity forsmaller equipmentDesigns optimized for minimal

    capital overall

    Operations(Contributes to Fixed Costs)

    High activity and capacity extendintervals between turnarounds

    Designs reduce maintenanceneeds; high on-streamavailability

    UOP technology minimizes COP UOP 6044P-9

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    Latest Generation UOP AromaticsTechnologies Product Portfolio

    RaffinateBenzene

    EDSulfolane

    Unit

    EDSulfolane

    Unit

    PlatformingUnitPlatformingUnit

    B T

    ReformateSplitter Heavy

    AromaticsTA-32

    NHTNHTA10+

    UnitUnit

    ADS-47

    I-500

    Naphthap-Xylene

    Light EndsIsomarUnit

    IsomarUnit

    ParexUnit

    ParexUnit

    XyleneColumn Deheptanizer

    Column

    UOPs innovation delivers new products for key processes!

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    Continuous innovation at UOP drivestechnical leadership in aromatics

    Next Gen Aromatics Complex Design ImpX Rx System for Platforming Unit UOP I-600 Isomar EB Isom Catalyst

    - somar ea a a ys Low xy lenes losses 3 operating units

    UOP Tatoray PTD Process Low xylenes losses

    UOP R-284 Platforming Catalyst Improved aromatics yields

    UOP ADS-47 Parex Adsorbent Over 25% extra throughput 7 operating units

    Recently Commercialized

    UOP R-334 PlatformingTM

    Catalyst Maximizes aromatics yields

    UOP TA-32 Tatoray Catalyst Improved activity & yields

    rs un s u n rs un s u n

    Energy Efficient Aromatics Complex First unit s/u in 2014

    UOP TA-30 Tatoray Catalyst

    2004 2005 2006 2007 2008 2009 2010 2014+20122011

    3 operating units

    2013

    +22% ROI+15% ROIBase ROI +30% ROINet Energy Required

    Reduced by 1/3 vs.

    Best 2009 Designs

    Addit ional 14%+Energy

    Reduction vs.

    +45% ROI

    CAPEX and OPEXReductions vs.

    Best 2012 Design

    Best 2010 Design

    Substantial CAPEX/OPEX reductions over last 4 years

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    ADS-47 Adsorbent Developmentand Commercialization

    Drop-in replacement for existingadsorbent resulting in low capital costsfor ca acit additions

    -ADSADS--47 Adsorbent47 Adsorbent is theis theresult ofresult of improvingimproving massmass

    transfer and capacitytransfer and capacity

    Up to 50% capacity increase in existingunits

    -

    same proven chemistrysame proven chemistry

    (~ $2-5 / ton of pX benefit over ADS-37)

    Significantly lower capital per ton of pX(less adsorbent, smaller chambers) -

    -

    Fast revamp execution; implementacross a standard turnaround

    Seven commercial units successfull

    1990 ADS-27

    loaded with ADS-47 Adsorbent since2011

    Five new unit designs have been based1971 ADS-3

    1980 ADS-7

    on ADS-47 Adsorbent

    UOPs Parex technology leads innovation and value

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    UOP TA-32 Tatoray catalyst setsnew standard for activity & stability

    Twice the catalyst li fe Hi her activit b 30C

    TA-32 BenefitsNovel & proprietaryNovel & proprietaryzeolitezeolite structure atstructure at

    --

    Novel & proprietaryNovel & proprietaryzeolitezeolite structure atstructure at

    -- Lower heater firing: $1/MT pX IRR Improvement by +1 to 3%

    Higher xylenes yield-

    More than 1% higher xylene selectivity Value improved by > $3/MT pX

    Lower feed requirementerature,

    C

    Up to 50% lower ring loss

    Broad range of operating parameters Designs optimized to maximize value

    Temp

    TA-32

    More Stable

    Commercially Proven Nearing two year of stable performanceCatalyst L ife

    Improved profitabili ty through selectivity and catalyst life

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    UOP I-500 Isomar catalyst sets newstandard for isomerization

    Improved Xylene Selectivity ~0.5 % better Xylene Retention

    High Paraxylene Selectivi ty ~24% pX/X at high WHSV

    Higher EB Conversion Activity 8 10C better than I-300

    High Benzene Selectivity > 98% compared to 90% Bz Sel

    High Benzene Purity > 99.8% Benzene Purity

    I-500 catalyst improves COP by ~ $3-9 / ton pX

    UOP 5892B-14

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    Latest products improve yields andcapital investment effectiveness

    BaseBase LatestLatest COP ReductionCOP Reduction

    For new aromatics complex designed with the latest products:

    CCR Platforming R-264 R-284 $3+ /MT pXIsomar I-300/350 I-500 $1-8* / MT pX

    - -

    Parex ADS-37 ADS-47 $3 / MT pX

    Total COP Reduction Over $10 / MTOver $10 / MT ppXX

    * For complexes without transalkylation

    d Cos

    ts

    Latest products substantiallyreduce production costs

    Re

    du

    c

    Pro

    duction

    UOP 6044P-15

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    Integrated process design reduces energycosts by over 53%

    Total EnergyRequirement(MMBtu/hr)

    Energy Savings(MMBtu/hr)

    Energy Savings@ $6 / mm Btu

    (MM$/year)*

    UOP Design 2009 1150 Base Base

    UOP Design 2011 455 (40%) $22.9

    Energy Benefit / MT pX 4.2 MMBtu / MT pX $26/ MT pX

    ADS-47 Energy Benefit /MT pX $5 / MT pX

    TA-32 Energy Benefit / MT pX $1 / MT pX

    I-500 Energy Benefit / MT pX $3 / MT pX

    Addit ional Energy Benefitfrom Upgraded Products

    1.2+ MMBtu / MT pX $9 / MT pX

    *Aromatics Complex pX Capacity = 900,000 tonne pX / year

    Total Energy Benefit / MT pX 5.6+ MMBTU / MT pX $35 / MT pX

    UOP 5625E-16

    Latest products and integrated design substantially improveenergy efficiency

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    UOP technology advances enablelarger scale plants

    Parex Adsorbent Train Size Increases Over Time

    1800

    1200

    1400

    KMTA

    600

    800

    1000

    -Xylene,

    0

    200

    400

    1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 2020

    Commissioned In Design / Construction

    UOP continues to lead the market in all size pX complexes

    Source: UOP licensed uni t data

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    Summary

    Since 2009, UOP has achieved $45+ per ton reductionin COP of pX

    Catalyst and adsorbent advancements have improved yields

    and selectivities, but also improve energy efficiency

    Latest technolo develo ments have enabled sin le traincomplex designs in excess of 1.5 MM TPA pX

    Our development pipeline is loaded with projects that

    UOPs Parex/Isomar/Tatoray portfolio is the clearleader in highest margin pX in the market

    OFITABILIT

    P

    to address diverse challenges

    UOP 6044P-18

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    UOP 6123-19