albermarle catalysts

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    Strictly confidential - proprietary information of Albemarle Corporation

    Innovative Catalyst Solutions for (Ultra) Low Sulphur Diesel

    The Middle East Fuels Symposium 3rdAnnual Meeting

    Abu Dhabi, March 2009

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    1950 1960 1970 1980 1990 2000 2010

    YEAR

    RelVolActivity

    Catalyst Development for (Ultra) Low Sulphur

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    Contents

    STARS Catalyst

    Road to 50 / 10ppm sulphur

    Commercial experiences

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    STARS -- New catalyst manufacturing technology which

    maximizes the number ofSuperType IIActive Reaction Siteswith very high intrinsic activity for HDN and HDS

    What are Type II Sites? NiMoS (or CoMoS) with weak bond to the support -- more fully sulfided

    greater access to high activity edge and corner sites

    very high intrinsic activity per active site

    STARS can be sulphided using feed only (i.e without need

    for spiking agent) achieving maximum activity.

    STARS Technology

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    Performance and benefits demonstrated extensively in pilot

    plant tests and commercial units.

    First batches installed early 1998.

    Activity benefits of up to 20 C confirmed in commercialoperations with the latest generation of STARS catalysts.

    STARS Catalyst Technology

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    STARSTM Catalysts

    Ketjenfine KF 848, KF 860, KF 868

    NiMo STARSTM catalyst for deep HDN, applied

    in FCC pretreat, MHC and Hydrocracker

    pretreat service.

    Ketjenfine KF 757, KF 767, KF 770

    CoMo STARSTM catalyst for (Ultra) Deep Diesel

    HDS

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    HDS Performance of KF-757, CoMo STARS Catalyst

    80

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    120

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    160

    KF-752 KF-756 KF-757

    RVAH

    DS

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    Strictly confidential - proprietary information of Albemarle CorporationFigure 4

    Base

    +20

    +40

    +60

    0 500 1000 1500

    Time on stream (hrs)

    WABT(oC)

    KF 756

    KF 757

    LGO LGOHGO

    T= 8 T= 10oC

    HDS Performance of KF 757 vs KF 756,

    oC

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    STARSTM KF 757 has higher HDN activity

    RVA-HDN KF-756 KF-757

    LGO

    LGO/LCO 80/20

    LGO/LCO 50/50

    LCO 100

    100

    100

    100

    100

    130

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    127

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    The road to 50/10ppm

    Effects of 1000 50 10ppm sulfur diesel on:

    cycle length

    catalyst volume

    hydrogen consumption

    exotherm

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    Case Study Current case

    0.854kg/lFeed Specific Gravity

    1000ppmwtProduct Sulfur

    Feed Definition

    Operating Conditions

    37wt%Total Aromatics

    15% LCO / 85% SRGOFeed Blend

    C

    ppmwt

    wt-%

    monthsbarg

    184 / 285 / 360 / 374ASTM D86 IBP/50%/95%/FBP

    194Feed Nitrogen

    1.14Feed Sulfur

    > 60Cycle Length50Reactor Inlet Pressure

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    Effect of 50/10ppm on Cycle Length

    Decreasing Product Sulfur Specification

    Constant Catalyst VolumeUpgrading Catalyst Technology

    BaseBaseBaseBaseBasem3Catalyst Vol.

    T2T2-15T1+55=T2T1+20T1CWABT

    13

    Dense

    KF-757STARS

    50

    DenseSockSockSockLoading

    6636> 60MonthsCycle Length

    KF-767STARS

    KF-756KF-756KF-756Catalyst Type

    10503501000ppmwtProduct Sulfur

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    Effect of 50/10 ppm on Rx Vol

    Catalyst Volumes and Cycle length for 50/10pm

    2.5 * Base2.2 * Base1.6 * BaseBasem3Catalyst Volume

    36

    Dense

    KF 757

    STARS

    50

    242413MonthsCycle Length

    DenseDenseDenseLoading

    KF 767

    STARS

    KF 757

    STARS

    KF 757

    STARS

    Catalyst Type

    105050ppmwtProduct Sulfur

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    Effect of 50/10ppm on Hydrogen/Exotherm

    Base +10

    1.15 * Base

    KF 757

    STARS

    50

    1.3 * Base1.1 * Base

    Base +15Base + 5BaseCApprox.

    Exotherm

    BaseNm3/m3

    Chem.

    HydrogenConsumption

    KF 767

    STARS

    KF 756KF 756Catalyst Type103501000ppmwtProduct Sulfur

    Higher chemical hydrogen consumption and exotherm caused by

    higher aromatics saturation at lower product sulphur

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    Commercial Experience

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    Commercial Experience (1) KF 757 in LSD operation

    Installed in May 1998, replacing KF-756, 20,000 BPSD

    Blocked operation LGO and HGO

    30 bars ppH2

    Reports 8C better activity with KF-756, as expected from laboratory test

    Cycle length from 1 year with KF 756 to 2 years with KF-757

    Deactivation Rate = 0.7 C/month

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    0 50 100 150 200 250 300 350

    Days on stream (Days)

    KF-757

    KF-756

    WABT(C)

    Deactivation Rate = 0.7 C/month

    340

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    400

    0 50 100 150 200 250 300 350

    Days on stream (Days)

    KF-757

    KF-756

    WABT(C)

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    Commercial Experience (2) KF-757

    Total pressure 42 bar

    Treat gas H2 purity 85%

    LHSV 3

    H2/oil 300 Nm3/m3

    Feed Sulphur 0.2 0.8%wt

    Product Sulphur 35ppm

    Cycle length 3 years

    WABT, Normalised to 35ppm

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    0 5 10 15 20 25 30 35 40

    TOS, Months

    WABT,C

    0 - 16 months on stream

    Deactivation 0.3C/month

    16 - 34 months on stream

    Deactivation 1.1C/month

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    About 30 % CGO in feed

    Inlet pressure 65 bar

    LHSV 1.2 1.8

    5 Years cycle, 1st year 50 -10 ppm S, last four years 10 ppm S)

    Commercial Experience (3) KF-848 in ULSD

    0.0000

    0.0001

    0.0010

    0.0100

    0.1000

    1.0000

    1-Aug-01 1-Aug-02 1-Aug-03 31-Jul-04 31-Jul-05 31-Jul-06

    Date

    Sulfur,wt%

    Sulfur Feed wt%

    Sulfur Product wt%

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    Commercial Experience (3) KF-848 in ULSD

    WABT, Normalised to 10 ppm

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    0 10 20 30 40 50 60

    TOS, Months

    WABT,

    C

    0 - 30 months on strea m

    Deactivation 0.5C/month

    30 - 60 months on strea m

    Deactivation 1.4C/month

    Cycle 60 months

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    Commercial Experience STARS Catalysts

    To date we have sold more

    than 90,000 tons of STARSTMcatalysts world wide

    Of this 54,000 tons is KF 757

    STARSTM

    Of the 54,000 tons KF 757,

    42,000 tons are for (U)LSDproduction

    KF 757 60%

    Other STARS

    catalysts

    77% KF 757 in

    (U)LSD

    KF 757 other

    applications

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    Commercial Experience STARS Catalysts

    Via the UOP-Albemarle HPC Alliance, we have designed a large

    number of grassroots/revamped HDS units for ultra low sulphurunits on STARS (KF 757)

    Among these a number of units in Takreer and 2 other large projects

    in the Middle East

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    Summary

    STARSTM is a new concept in catalyst design, maximizing the number of

    SuperType IIActive Reactions Sites.

    STARSTM catalyst have significantly higher HDS activity (up to 160%) thannon-STARS for ultra deep desulfurization of diesels down to 10 ppm.

    STARSTM catalysts can be sulphided with feed only without the need for aspiking agent for maximum activity

    Decreasing product sulfur specifications reduces cycle length dramatically

    STARSTM catalysts can make (ultra) low sulphur diesel in existing units with

    acceptable cycle length. No CAPEX may be required

    Excellent commercial experience ofSTARSTM catalysts with respect toactivity and stability

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    Innovative Catalyst Solutions for (Ultra) Low Sulphur Diesel

    The Middle East Fuels Symposium 3rdAnnual Meeting

    Abu Dhabi, March 2009