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Recent content by Petroprocess

  1. Petroprocess

    location for 10% back pressure on convenstaion PSV tail pipe

    Similarly while modeling flare systems in Aspen Flare system Analyzer, putting in the correct PSV outlet flange is required. I have noticed that it does change the back pressure on PSV. So yes, uptill the PSV outlet flange.
  2. Petroprocess

    Steam - fire case allowable overpressure

    For fire scenarios the overpressure is always 21% even if it is a steam relief.
  3. Petroprocess

    Open discharge system: Pressure value at point of discharge??

    There was a similar discussion in our company. The situation was that there was a scenario where a single valve was relieving gas to an atmospheric vent. A couple guys argued that the pressure "available" at the tip of vent is basically pressure at the inlet of relieving valve (not PSV, consider...
  4. Petroprocess

    velocity criteria for PSV suction line

    I would agree with joerd. There is just the "3%" rule for the grass root design as per API guideline. Although I have seen engineers take slightly higher pressure drop acceptabe in older/existing facilities. So when you design for 3% od set pressure of PSV as pressure drop (inlet line)the...

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