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  • Re: phast model

    by
    safetyuser
    Published on 03-09-2012 10:09 AM
    0 Comments Comments
    Quote Originally Posted by macvin View Post
    Hi,

    I have to run a model in which LPG is transferred from Refinery to storage terminal through LPG pipeline. Which scenarios I can consider for model input??
    I was trying for long pipeline scenario, however the model says long pipeline scenario cannot be considered for mixtures. Please help.

    Regards,
    -Macvin
    with small size holes I would use the vessel leak model, it should not make much difference.

    If you have large holes or ruptures the dynamics in pipeline is complicated: you cannot leave the pipeline model out of consideration.
    Furthermore since you have LPG the flash is important at release. In these cases in the past I used to model the release with hysys.
    This article was originally published in forum thread: phast model started by macvin View original post

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