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Technip Ethylene

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     A FULL-SERVICE ETHYLENE PRODUCT LINE

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    TECHNIP-COFLEXIP

    ETHYLENE TECHNOLOGY 

    TECHNIP-COFLEXIP offers the ethylene manufacturing industry SINGLE-

    SOURCE PROJECT RESPONSIBILITY throughout all phases of a new

    grassroots ethylene plant or revamp project, from basic design phase

    up to project implementation, start-up and operational services.

    THE TECHNOLOGY CORNERSTONES

    TECHNIP-COFLEXIP applies unique technology features:

    • SPYRO ® FURNACE DESIGN AND OPTIMIZATION SOFTWARE

    • TECHNIP-COFLEXIP CRACKING FURNACE TECHNOLOGY

    • PROGRESSIVE SEPARATION TECHNOLOGY

    • THE T-PAR® PROCESS

    • OPERATIONS SUPPORT SERVICES: e -OSS ®

    - CLX ® anti-coking services developed jointly with ATOFINA of France,

    - Unattended operations concepts.

     And for capacity expansion of existing plants :

    • THE SYSTEMATIC APPROACH TO MODERNIZATION

    • THE CAPACITY AND PERFORMANCE IMPROVEMENTS OF EXISTING

    FURNACES.

    The application of these proven proprietary technologies in the design of

    modern large-scale grassroots ethylene plants and in the revamp of existing

    ethylene crackers offers the plant operator a SAFE, RELIABLE ethylene

    plant, easy to operate and maintain, resulting in a very efficient cost saving

    olefin production unit for the Owner.

    SPYRO ®, e-OSS ® and T-PAR ® are registered trademarks of TECHNIP-

    COFLEXIP.

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    Simulation of a largecapacity furnace

    THE SPYRO ® FURNACE DESIGN AND

    OPTIMIZATION SOFTWARE

    SPYRO® is now used by the vast majority

    of ethylene producers and is applied for

    feedstock selection, process scheduling

    and production optimization. A large

    number of plants run on-line control and

    optimization systems having a dedicated

    SPYRO ® program embedded in the sys-

    tem software. The application of the proven

    SPYRO® program provides detailed infor-

    mation on yields and furnace availability

    which can also be used to set up revamp

    scenarios for the furnace and downstreamsections of the plant.

    For optimum design of large- capacity

    GK®, and SMK®, cracking furnaces, TECH-

    NIP-COFLEXIP applies SPYRO ® linked

    with CFD (computational fluid dynamics),

    enabling the best design of burner arran-

    gement, cracking coil layout and flue gas

    ducting.

    Hydrocarbons are thermally cracked in a

    tubular fired reactor, the cracking furnace.

    The thermal cracking process requires

    high temperatures and to be selective to

    the desired light olefins, optimal residence

    times and pressure profile have to be se-

    lected. Due to the complex nature of the

    cracking process, accurate predictive

    design and simulation tools are needed

    to arrive at the best reactor coil and fire-

    box design.

    TECHNIP-COFLEXIP ETHYLENE TECH-

    NOLOGY makes use of TECHNIP’s pro-prietary SPYRO® yield prediction program.

    The heart of SPYRO® is a rigorous kinetic

    model describing in detail the thousands

    of elementary reactions occurring during

    pyrolysis of hydrocarbons, ranging from

    light gases such as ethane to heavy oils

    such as hydrocracked VGO (Hydrowax).

    SPYRO ® is the result of more than 30

    years of joint development and continuing

    improvements in close cooperation with

    the original authors of the program, theteam of Professor Dente in Milan.

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    THE TECHNIP-COFLEXIP

    CRACKING FURNACE

    TECHNIP-COFLEXIP CRACKING FUR-

    NACES use the proven high selective,

    short residence time coils of the GK ® and

    SMK® types (originally developed by KTI ® ).

    The Cracking Coils of GK®

    and SMK®

    fur-naces are tailored to the specific needs

    of the ethylene plant. Normally these are

    geared towards the maximum production

    of the light olefins, ethylene and propylene.

     Additionally, for liquid crackers integrated

    with downstream production units,

    requirements such as maximum BTX

    co-production and feed/products flexi-

    bility are also important parameters for

    an optimal coil design.

    TECHNIP-COFLEXIP CRACKING FUR-NACES are equipped with a combination

    of low NOx bottom and up-shot side wall

    burners. The specific GK ® or SMK ® coil

    arrangement, burner lay-out and the box

    dimensions allow for a very large capacity

    per furnace cell, while maintaining high

    radiant fuel efficiency. In most cases the

    application of low NOx burners will meet

    emission specifications imposed by coun-

    try or state legislation. For stringent NOx

    specifications, the application of flue gas

    NOx removal using low temperature SCR

    (selective catalytic NOx removal) can also

    be applied.

    TECHNIP-COFLEXIP CRACKING FUR-

    NACES feature shell-and-tube TLE’s

    (transfer line exchangers) as well as dou-

    ble pipe direct quench coolers. High on-

    stream time is achieved by minimizingmechanical decoke cycles of the TLE’s.

    In 1999 TECHNIP introduced the GK6 fur-

    nace. The GK6 furnace features an 8-8

    cracking coil configuration. The GK6 fur-

    nace can be equipped with all available

    types of quench coolers.

    The GK6 cracking furnace is a large capa-

    city furnace with high selectivity and large

    on-stream time characteristics at the

    lowest possible capital costs. The applieddesign tools and expertise contained in

    TECHNIP-COFLEXIP ETHYLENE TECH-

    NOLOGY enables TECHNIP-COFLEXIP

    to offer its customers an optimized,

    tailor-made cracking furnace design

    at the LOWEST COST OF

    OWNERSHIP for their

    specific need.

    GK ® and SMK ® are

    registered trademarks

    of TECHNIP-COFLEXIP.

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    THE T-PAR PROCESS

    The ethylene recovery and purification

    process is energy and investment cost

    intensive. For large capacity gas or liquid

    feed crackers TECHNIP-COFLEXIP has

    developed a unique processing sequence

    centered on the efficient acetylene removal

    by either hydrogenation or liquid absorp-

    tion. The main features of this process are:

    • Controlled acetylene hydrogenation

    avoiding runaway reaction and poisoning

    • Reduced equipment dimensions andpiece count

    • Reduced compression machine size

    and power

    • Excellent control stability by

    process-to-process

    heat integration

    • Very competitive

    investment cost.

    PROGRESSIVE

    SEPARATION

    PROGRESSIVE SEPARATION technology

    is a stepwise separation of the lightest

    and the heaviest components in a multi-

    component hydrocarbon mixture. It uses

    a series of condensate strippers that haveonly bottom product purity specifications.

    Hence, easy controllability and operability

    make multivariable optimizers redundant.

    The tailgas from the strippers is proces-

    sed for recovery of valuable ethylene by

    self-contained cryogenic technology. This

    concept lends itself well to revamp pro-

     jects where the standard package can be

    implemented without extensively modi-

    fying the existing equipment. PROGRES-

    SIVE SEPARATION can be applied for the

    revamping of existing back-end and front-

    end hydrogenation schemes in relation to

    either high pressure or low pressure deme-

    thanizers.

    Due to the intrinsic autostability of new

    and revamped ethylene plants equipped

    with PROGRESSIVE SEPARATION, start-

    up is extremely smooth and easy. New

    and revamped ethylene plants based on

    PROGRESSIVE SEPARATION have a track

    record of short start-up times, typically 24

    hours from first feed intake to full opera-

    tions.

     As one operator put it: “You start it up and

    you experience a new feeling of comfort

    and ease”.

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    ETHYLENE PLANT

    MODERNIZATION,

    CAPACITY EXPANSION

     AND REVAMP PROJECTS

    Ethylene plant modernization projects vary

    in scope and size. Existing cracking fur-

    naces, even if they originate from a recent

    generation, may be redesigned to increase

    their ethylene capacity by some 20% to

    100% of original capacity. At the same

    time, specific feed consumption is dras-

    tically reduced, thereby contributing to an

    attractive low cost of production per ton

    of incremental ethylene. For complete

    modernization of existing ethylene plants,

    including revamp of the cracking section,

    compression and separation sections,

    TECHNIP-COFLEXIP offers a unique pro-

    ven approach, applied successfully inseveral recent revamp projects.

     

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    Main steps involvedin the Systematic Approachto Modernization

    THE SYSTEMATIC

     APPROACH

    TO MODERNIZATION

    The SYSTEMATIC APPROACH TO MO-

    DERNIZATION developed and applied by

    TECHNIP-COFLEXIP is a project oriented

    methodology which enables an indepth

    evaluation of the technology options and

    project implementation scenarios, leading

    to the most economical capacity expan-

    sion of the existing ethylene plant. With the

    application of the Systematic Approach to

    Modernization, bottlenecks in an existing

    plant are identified and prioritized such

    that a maximum return on a given invest-ment is obtained.

    The SYSTEMATIC APPROACH TO MO-

    DERNIZATION concept considers the

    ethylene plant to consist of a series of

    interrelated functional blocks.

    To determine the best capacity increase

    option versus energy demand and invest-

    ment cost, to yield lowest cost of pro-

    duction per ton of incremental ethylene,

    each functional block can be evaluatedseparately on those three targets that are

    related to particular technical and econo-

    mic aspects. The final result of the eva-

    luation is an insight into the relationship

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    Interrelated functionalblocks of an ethylene plant

    between required investment cost and

    target capacity increase. This enables the

    choice of the best revamp scenario lea-

    ding to incremental ethylene production

    at lowest cost.

    IMPROVEMENT OF

    EXISTING CRACKING

    FURNACES

    When extra capacity is needed in an

    existing ethylene plant, to consider one

    or more additional furnaces seems to be

    the obvious choice. The recoiling or even

    complete modernization of existing fur-

    naces however can be a more attractive

    option.

    Capital cost per ton of incremental ethy-

    lene can be significantly reduced, and

    furnace fuel consumption, as well as

    emissions (noise, NOx), can be brought

    into line with today’s standards.

    Many existing furnace designs of different

    origins have a large potential for extra ethy-

    lene output when a redesign is applied.

    This extra ethylene can be more than

    double, as is proven by recent real life

    revamp references.

    TECHNIP-COFLEXIP has the tools and

    expertise to quantify this potential and to

    study the available revamp options in com-

    parison with newly built furnace capacity.

    TECHNIP-COFLEXIP has executed many

    furnace conversion projects, resulting in

    minimum downtime requirements and

    minimum impact on existing plant opera-

    tions.

    Insight into the relation betweenrequired investment costand target capacity increase

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    OPERATIONS SUPPORT

    SERVICES: e- OSS ®

    e-OSS ®: advanced technology for optimal

    operations of ethylene plants.

    Under e-OSS ®, TECHNIP-COFLEXIP is

    offering services based on recent advan-

    ces in automation, control and information

    technologies that are dramatically impac-

    ting the economics of ethylene plants:

    Process observability• Use of Near Infrared Spectroscopy with

    the TOPNIR ® technology to measure at

    high frequency the naphtha feed proper-

    ties, including the PIONA distribution per

    number of carbon atoms which is used

    by SPYRO ®.

    • Real time data reconciliation using the

    DATREC technology to close mass and

    heat balances and detect abnormal beha-

    viour of instruments.

    Unattended operations

    • Use of field-bus, wireless equipment,

    smart sensors to automate most sequen-

    tial operations.

    •  Abnormal situation management to

    detect potentially hazardous situations

    before they escalate into incidents.

    • Equipment health management to remo-

    tely perform diagnosis of critical hardware.

    Optimal operations

    • Optimized scheduling of operationsusing the FORWARD technology: Feeds

    sequencing, de-coking schedule, modes

    of operations.

    • Overall plant accounting and losses

    monitoring using the GERA technology.

    CLX Anti-coking Services

    CLX®: On-line pretreatment of radiant coil

    to improve cracking furnace performance.

    TECHNIP-COFLEXIP and ATOFINA, a sub-

    sidiary of TotalFinaElf, have developed a

    system to pretreat radiant coils of gas-

    cracking furnaces. When applied, the fur-

    nace run-length is dramatically improvedand doubling of the run-length is proven

    to be achievable.

    The CLX ® system is based upon a pro-

    prietary sulphur-silica organic component

    mixture and is well tested both on lab

    and pilot scales and on an industrial scale

    in ATOFINA's commercial installations.

    The CLX® system is easy to apply. The CLX®

    ingredients are injected during a very short

    period in the dilution steam directly after

    the decoke cycle of a running furnace

    before next feed is taken in. The system

    works optimally when followed by conti-

    nuous DMDS dosing with the feed.

    The CLX ® system contains chemicals,

    which fall in the category of normal pa-

    raffins on the aspects of toxicity, safety

    and environment.

    The CLX® system is exclusively available

    through TECHNIP-COFLEXIP for new fur-

    nace installations and through ATOFINA for existing installations.

    The service which is provided by ATO-

    FINA consists of a dosing kit lease, CLX ®

    inhibitor, maintenance, training and hot

    line support.

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    ETHYLENE PLANT

    PROJECT EXECUTION

    TECHNIP-COFLEXIP is active in many

    areas of the petrochemical industry. For

    the ethylene production units, which form

    the heart of the petrochemical industry,

    TECHNIP-COFLEXIP executes grass-

    roots and modernization projects world-

    wide. TECHNIP-COFLEXIP offers the full

    scope of engineering, procurement andconstruction services ranging from the

    execution of feasibility studies, FEED

    ( front end engineering and design) pack-

    ages, EPC (engineering, procurement and

    construction) projects up to full LSTK

    (lump sum turn key) project responsibility.

    This also includes the supply of proprie-

    tary technology, the start-up capabilities

    for the olefins plant, its ancillary units and

    the associated off-sites and utility sec-

    tions. TECHNIP-COFLEXIP has the pro-

    cess capabilities and resources to serve

    the industry through TECHNIP’s multiple

    offices in all parts of the world.

    Project services offered by TECHNIP to

    satisfy the need of the customer are:

    • TECHNIP-COFLEXIP applies high stan-

    dard safety related procedures in a cons-

    tant dialog with the client to arrive at an

    intrinsically safe plant throughout all pha-

    ses of the project, from basic design stage

    to start-up and plant hand-over.

    • TECHNIP-COFLEXIP’s recognized ex-

    pertise in quality assurance and quality

    control procedures ensures the future

    plant operator is able to run a trouble-

    free plant which is safe and reliable and

    which meets its production objectives

    from day one.

    TECHNIP-COFLEXIP is a world leader in

    executing projects under the LSTK ( lump

    sum turn key) contract type with or with-

    out financing constraints. TECHNIP-

    COFLEXIP’s global presence and access

    to international resources enable TECHNIP

    to include local knowledge and domestic

    capabilities in its projects teams, thus en-

    suring a smooth interface with the client.

    • Financing support

    • Project management

    • Feasibility study

    • Conceptual design

    • Cost estimating

    • Project planning and scheduling• Front end engineering and design

    (FEED)

    • Detailed engineering of equipment,

    piping, civil, instrumentation, electrical

    and automation

    • Procurement including purchasing,

    expediting and inspection

    • Construction

    • Start-up services

    • Environmental permitting

    • HAZOP & HAZAN

    • Safety studies• Support in authority approval and

    permit procedures

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    Photographs:Technip-Coflexip photo library, Synchro Copyright ®, X.

    Cover photo:GK6 furnace.

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    Did you know

    that apples

    produce

    ethylene?

    So does TECHNIP-COFLEXIP with its in-house technology

       U   L   T   I   M   U   M   -

       R   C   S   N  a  n   t  e  r  r  e   B   4   0   2   9   6   1   3   2   0

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    TECHNIP-COFLEXIP

    Tour Technip - La Défense 692973 Paris La Défense cedexPhone: + 33 1 47 78 21 21

    Fax: + 33 1 47 78 33 40

    TECHNIP FRANCE

    Phone: + 33 1 47 78 21 21Fax: + 33 1 47 78 33 40

    TECHNIP ITALY 

    Phone: + 39 06 65981Fax: + 39 06 655 1402

    TECHNIP BENELUX BV 

    Phone: + 31 79 329 36 00Fax: + 31 79 351 35 61

    TECHNIP GERMANY 

    Phone: + 49 211 659-1

    Fax: + 49 211 659-3264

    TECHNIP MALAYSIA 

    Phone: + 60 3 21 16 78 88Fax: + 60 3 21 16 79 99

    TECHNIP USA CORP.

    Phone: + 1 713 548 4000Fax: + 1 713 548 4013

    Phone: + 1 909 592 4455Fax: + 1 909 592 3399

    www.technip-coflexip.com


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