Petroleum Community Forum - Re: phast model

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Re: phast model
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Published on 03-09-2012 10:09 AM

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Originally Posted by macvin

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
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