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    “The Cooldown Gap”

    Session 15, Supplemental Gas

    LNG

    LNG

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    · n erna onaPresenter: Jeff Beale

    Coauthor: Osifo Akhuemonkhan

     May 20, 2009

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    Presentation Outline

    Introduction

    Explanation of “The Gap”

     

    • Preparation

    • ryogen c p ng ryou Cooldown / Start-Up Gaps

    • LNG Tank Cooldown

     

    SummaryH

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    – ·www.CH-IV.com

     

    Offices near Baltimore & in Houston

     

    • Conceptual Design / Pre-FEED

     

    • Front End Engineering Design (FEED)

    • ’ ,

    • Commissioning / Start-Up Support

    • Trainin

    • Operations Support

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    Introduction – CH·IV International

    Recent LNG Terminal Commissioning Experience

    • Multiple LNG terminals in Europe

    • World’s first GBS LNG import terminal – on going• Dom n on Cove Po nt LNG Expans on

    • Energía Costa Azul (Mexico)

    ecent ront n ng neer ng es gn• Oregon LNG

    •   parrows o n

    • Downeast LNG• co ec r ca

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    Introduction – CH·IV International

    Owners Engineering

    • EcoElectrica

    • Cove Point Reactivation• Lake Charles Expansion

    • Energía Costa Azul (Mexico)

    • ameron• Piedmont Natural Gas (Peakshaver on hold)

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    LNG Terminal Phases

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    “ ” ga ons o e ng neer ng, rocuremen an

    Construction (EPC) contractor are set early. Typically, limited clarification on the particulars of

    commissioning & start-up.

    Owner / operator does not recognize what is neededuntil well into the construction.

    EPC’s definitions of “needs” does not always agree

    with owner.

    There in lies the “Gap.”

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    “ ” 

    ng neer ng vs. pera ons

    (Too bad it’s not Engineering & Operations)• Engineering – Project Control

    • Time & Mone

    • Responsibility last 3 – 5 years

    •  

    • Safety & Reliability

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      pe ean ness er ons ruc on

    • Debris and/or standing water usually presentupon completion of construction.

    • This can find its wa into valve seats and

    compromise the valve integrity.

    •  

     pump bearings and cooling paths.

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     ere w a ways e some e r s an poss y

    standing water, but how do we minimize theamounts??

    • Store i in com onents with end ca s in lace. 

    • Delay insulation (particularly foam glass) until as

    .

    • Use valve operating management system, avoidunnecessary open ng an c os ng.

    • Keeping inspection covers on when not in use.H

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    ’  . wner pera or s ou se e s an ar or

     pipe cleanliness well in advance ofcompletion of construction (ideally in

    contract .

    EPC Contractor should provide records

    .

    Owner/Operator should conduct independentchecks and reviews of piping.

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    “ ” 

    “ ”  .

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    “ ” 

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    “ ” 

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    • At cryogenic temperatures any water (vapor) will.

    • Ice can – • Foul strainers

    • Scratch “Tight Shut Off” valve seats• Gaul bearings

    • Plug pump cooling paths

    • Reduce insulation effectiveness

      , positive pressure – piping “breathes.”

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    Dr out cont’d

    LNG Tank Dryout• Typically the responsibility of tank contractor 

    • Review purging / sparging design• Annular space as well as inner tank 

    • Must assure systems are completely dried • ax mum - ew po n

    • Design review needs to assure adequate testing pointswill be available

    • Media

    • Nitrogen• Dry Air 

     – Will require total N2 purge prior to LNG cooldown

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    Dr out cont’d

    Cryogenic System Dry-Out

    • vo one ryout

    • If Contractor responsible:• How is dry media provided?

    • Assure / Review detailed procedures with logs

    • Provide independent confirmation – Acquire “Company” hygrometer 

    • Areas of concern

     – Dead legs

     – ow pa o s ruc ons c ec va ves, e c.

     – Free water - Low points

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    Dr out cont’d

    Cr o enic S stem Dr -Out

    • If Owner / Operator Responsible:

     – Heat?

     – Pressure cycle

     – Low pressure Sweep – Sweep & Soak 

    • Choice of media

     – Nitrogen

     –

     – Rental dry air units

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    Wh C ld ?

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    Why Cooldown?

    i erentia emperatures  

    • LNG is “sneaky” fast

    “ ”• g eren a empera ure prov es g e pa

    • Controlled pipe movement

    • 3" shrinkage per 100 feet

    • Large diameter pipe bowing

    • Can lift pipe off supports

    • What’s not “large” diameter?• Pipe anchor / support damage

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    rec e y an con rac or  

    Duration of 24 to 72 hours

    Substantial temperature monitoring necessary

    oo own contro e y spray contro va ve

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    -

    Was this planned for?

    Use LNG Transfer Line

    •  • Geysering in cooldown line, need to release the

    .

    • Choking at spray nozzles

    se rec rcu a on ne ava a e

    • Smaller pipe, less heat gain• Provide isolation valves in design

    • Temporary crossovers / connectionsH

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    If you are going to flare your cooldown gas,

    consider the neighborhood -

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    All piping over 10" (8"?) should be pre-cooled.

    • What does the EPC say?

     . . .Early design

     

    • Once through

    • Recirculate using vapor return blowers

    • Use cold vapor from tank • Vaporized LIN/BOG/Trickle Cool

    • Local in ectionH

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    o om on y op on y o

    Permanent vs. Tem orar 

    Local vs. Remote? Or combination?

    nsta at on• Dry, continuous contact

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    nce co , ry o eep p p ng a way

    Avoid thermal c cles and look out for:• Pipe movement

     

    • Insulation breakdown

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    Thank youThank you

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    Thank youThank you

    CH·IV International

    -. .

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