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Thread: Crude or Gas Header (manifold) Design [Request]

  1. #1

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    Crude or Gas Header (manifold) Design [Request]

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    Dear friends

    Does anybody have a document or standard to design crude or gas header (manifold)?



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  3. #2
    I guess the only one that may help is Nabilia.

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  5. #3
    Please share.

  6. #4

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    in fact, I want to know which parameters should be considered in manifold design? As mentioned in IPS-E-PR-440 one of them is Ro*V^2 that should be less than 14800 (SI Units).

    EVR=v/(c/Ro^0.5)

    EVR must below 1.0 and c=100 and 122 for English and SI unit respectively then:

    c < Ro^0.5 *v ....... Ro*v^2 > 10,000 or 14800


    Do you know another parameter?


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    Last edited by motaleby; 10-24-2011 at 11:30 AM.

  7. #5
    This is what I was able to send to motaleby
    It is just a couple of docs related to manifolds and headers

    headers, manifolds.zip 5.8 MB

    [link Point to another website Only the registered members can access]


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  9. #6
    Quote Originally Posted by Nabilia View Post
    This is what I was able to send to motaleby
    It is just a couple of docs related to manifolds and headers

    headers, manifolds.zip 5.8 MB

    [link Point to another website Only the registered members can access]

    Nabilia, thanks a lot.

  10. Dear orbawy,

    Hi there!...please could you send me the archive or upload again please!. Additionally if you have some information about manifolds design (eg. in treatment plants, please tell me)

    Luiz.

  11. #8
    Quote Originally Posted by lserpach View Post
    Dear orbawy,

    Hi there!...please could you send me the archive or upload again please!. Additionally if you have some information about manifolds design (eg. in treatment plants, please tell me)

    Luiz.
    Iserpach, the link is still active

  12. #9
    Thanks for sharing

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