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    FLEXICOKINGThe Flexible ResidUpgrading Technology 

     

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    Flexicoking Technology  at Hellenic

    Petroleum S.A. refinery in Elefsis, Greece.

    Commissioned in 2012. 

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    The Cost-Effective Coking Technology, without the Coke

    FLEXICOKING™ technology is a commercially proven, cost-effective, fluidized bed process that thermally converts

    heavy oils to lighter products and flexigas — “Coking without the Coke.” Low-cost feeds such as deep-cut vacuum resid;

    atmospheric resid; oil sands bitumen; heavy whole crudes; and DAU, FCC, and ebullated-bed bottoms are converted

    to high-value products. FLEXICOKING technology with integrated steam/air gasification offers greater flexibility thanconventional Delayed Coking, and does it economically. The FLEXICOKING technology not only produces clean liquids of

    equivalent quantities and similar quality to Delayed Coking, but also gasifies the low-value coke to produce a clean, high-

     value flexigas that can be used in place of natural gas and conventional fuel gas in refinery processes. Flexigas can also be

    used to generate electric power and to produce H2, N2, and CO2.

    Key Advantages

    • Proven: Commercially proven for more than38 years in ExxonMobil and in licensed third-partyunits. All FLEXICOKING units are operating todayat capacities greater than original design. Currentcombined operating capacity is 227 kbd/12 MTA.

    • FLEXible: A robust process, capable of handling a variety of feeds with a wide range of high ConradsonCarbon Residue (CCR), sulfur, and heavy metals, withoutthe need for a feed furnace.

    • Multi-Purpose: The high-sulfur, low-value coke isconverted to a clean, economical multi-purposeflexigas, which can be used in refinery furnaces,boilers, and gas turbines, or processed to recover H2,N2, and CO2. ExxonMobil’s FLEXSORB™ process isincorporated to reduce H2S in flexigas to 10 wppm,or as needed.

    • Optimizable: Coke gasification can be optimizedon the run, to debottleneck the unit, or to satisfyoperational requirements such as changes in feedformulations and variations in flexigas consumption.

    • Economic: Integrated “simple” steam/air gasification,carbon steel construction throughout, and theabsence of feed furnaces are key factors resulting insignificantly lower capital investment when comparedto Delayed Coking with “complex” oxygen gasification.Expect greater comparative savings in electric power-generation applications (steam or combined cycle).

    • Environmental: Continuous, non-batch operation andclosed coke handling system results in low-particulateand fugitive hydrocarbon emissions. Much lower SOxand NOx emissions are realized by burning the cleanflexigas, when compared to burning high sulfur coke.

    • Reliable: Continuous, steady state operation incombination with cold-wall carbon steel constructioncontributes to high reliability and service factors thatroutinely exceed 92 percent.

    These benefits come to you in a compact package. Thelayout of modern FLEXICOKING units offers reduced

    plot space — about 20 percent less than that of a basicDelayed Coking unit of similar capacity.

    FEED SELECTOR

    TOUGH FEED 1

    TOUGH FEED 2 TOUGH FEED 3

    COMBINATION

    FLEXIGAS USE

    FUEL GAS

    POWER GENERATION H2/N2/CO2 RECOVERY

    COMBINATION

    CONTROL PANEL

      GA S I FICAT I O N  

    C  O K E  MA K

      E

    Min.

    Max.

    0 1 2 3 4

    Power(Combined Cycle)

    Power(Steam Cycle)

    Flexigas forRefinery Fuel

    Coke for Sale     A     P     P     L     I     C     A     T     I     O     N     S

    CAPITAL INVESTMENT FACTOR

    2.53.1

    1.31.0

    2.94.0

    DELAYED COKING FLEXICOKING

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    How FLEXICOKING Technology WorksThe vacuum resid feed enters the scrubber for “direct-

    contact heat exchange” with the reactor overhead

    product vapors. The higher-boiling point hydrocarbons

    (~975°F+/525°C+) present in the reactor product vapors

    condense in the scrubber and return to the reactor, in

    mixture with the fresh feed. Lighter overhead product

     vapors in the scrubber go to conventional fractionation

    and light-ends recovery. The feed is thermally cracked inthe reactor fluidized bed to a full range of gas and liquid

    products, and coke. Coke inventory is maintained by

    circulating the bed coke from the reactor to the heater via

    the cold coke transfer line.

    In the heater, the coke is heated by the gasifier products

    and circulated back to the reactor via the hot coke

    transfer line to supply the heat that sustains the thermal

    PRODUCT TO

    FRACTIONATOR

    CLEAN

    FLEXIGAS

    TO USERS

    SCRUBBER

    FEED MIX TO

    INJECTORS

    HOT

    COKE

    COLD

    COKE

    COKE PURGE

    HP STEAM

    GENERATION

    DRY COKE

    FINES

    WET COKE

    FINES

    SOUR

    WATER

    AIR + STEAM

    REACTOR

    FEED

    RICH FLEXSORB

    TO REGENERATION

    Flexicoking Process

    cracking reaction. The excess coke in the heater is

    transferred to the gasifier, where it reacts with air and

    steam to produce a gas. The gasifier products, consisting

    of a gas and coke mixture, return to the heater to heat up

    the coke. The gas exits the heater overhead and goes to

    steam generation, to dry/wet particulate removal, and to

    desulfurization in the integrated FLEXSORB™ process.

    The clean flexigas is then ready for use as fuel inrefinery boilers and furnaces and/or for steam and

    power generation.

     Approximately 95 percent of the coke generated in the

    reactor is converted in the process. Only a small amount

    of product coke is collected as fines from the flexigas and

    purged from the heater to extract feed metals.

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    Full-Range Products SlateFLEXICOKING technology produces a full range of

    products, from a C4- reactor gas to C5/975°F (525°C)

    liquid products, the multi-purpose flexigas, and lastly a

    small stream of low-sulfur coke that is purged to extract

    feed metals.

    Guaranteed Performance

    The first FLEXICOKING unit began operation in 1976, andsince then five others have come online, the most recent

    one in 2012. Since 2010, we have also licensed three new

    units with a combined capacity of 114kbd/6.3 MTA. These

    are currently in different stages of construction.

    COKER GASC2 Fuel Gas, C3/C4’S for Alkylation,

    Chemicals, LPG Sales

    LPG

    To Hydrotreating

    To FCC, Hydrocracker & Chemicals

    To Refinery Fuel, Power GenerationH2, N2, CO2 Production

    COKECoke Sales & Metals Reclamation

    H  In Operation

       Athens, Greece  Houston, Texas  Amuay, Venezuela  Kawasaki, Japan  Rotterdam, The Netherlands  Martinez, California

    H  In Construction

      Moscow, Russia  Tuapse, Russia  Talara, Peru  China

    ExxonMobil has licensed fluidized bed coking technology since the 1950s, including the largest fluid coker, which is

    located in Syncrude, Fort McMurray, Canada. Our experience ranges from 5 to 105 kbd (60 to 750 mtons/hr) unit

    capacities and a variety of difficult feeds with CCR values ranging between 17 and 37.

    ExxonMobil has equally extensive experience supporting its licensees, and this is particularly true of the FLEXICOKING

    technology, because ExxonMobil owns and operates FLEXICOKING units in two of its largest refineries: Rotterdam in the

    Netherlands and Baytown, Texas, in the United States.

    We see an increasing market interest in FLEXICOKING technology worldwide. We expect the trend to continue well into the

    future, particularly in parts of the world where natural gas is limited and/or expensive, and in environmentally sensitive areas.

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    FLEXICOKING™ Technology Highlights

    • Produces a clean and valuable flexigas fuel

    • Achieves superior environmental performance

    • Offers maximum flexibility in terms of processedfeeds, product utilization, and operating modes

    • Requires lower capital investment

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    FLEXICOKING Technology at ESSO Nederland refinery in Rotterdam,The Netherlands. Commissioned in 1986.

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    Printed in U.S.A.XXXX—XXXXXXXXXXXX—XX-XXXX

    www.exxonmobil.com/tsl

    © 2014 ExxonMobil. The user may forward, distribute, and/or photocopythis copyrighted document only if unaltered and complete, including all ofits headers, footers, disclaimers, and other information. The information inthis document relates only to the named product or materials when not incombination with any other product or materials. We based the informationon data believed to be reliable on the date compiled, but we do not represent,warrant, or otherwise guarantee, expressly or impliedly, the merchantability,fitness for a particular purpose, suitability, accuracy, reliability, or completenessof this information or the products, materials, or processes described. The useris solely responsible for all determinations regarding any use and any process.We expressly disclaim liability for any loss, damage, or injury directly or

    indirectly suffered or incurred as a result of or related to anyone using orrelying on any of the information in this document. There is no warrantyagainst patent infringement, nor any endorsement of any product or process,and we expressly disclaim any contrary implication. The terms, “we,” “our,”“ExxonMobil Chemical,” or “ExxonMobil” are used for convenience, and mayinclude any one or more of ExxonMobil Chemical Company, Exxon MobilCorporation, or any affiliates they directly or indirectly steward. TheExxonMobil Chemical Emblem, the “Interlocking X” Device, and Vistalon aretrademarks of Exxon Mobil Corporation.