xyz168,
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Is it possible to have a negative value on outlet dP calculation? If it's possible, does it apply to all kind of fluid? Or does it only apply to liquid? Thank you.
I hope you mean the static head gain is more than the frictional pressure and results in-situ pressure at pipe inlet end is lower than pipe outlet end.
For subcooled liquid relief and no flashing along PSV & discharge line (e.g. water), you may have the potential of pressure below atmospheric pressure in the event the PSV discharge line is long and vertically extended downward, small discharge line size result complete liquid sealing and liquid column form in the vertical piping. In this case, it is possible to have in-situ pressure at pipe inlet end is lower than pipe outlet end. This scenario invites a lot of problem like vibration, noise, surging, etc. You may consider to increase discharge line size to avoid formation of liquid column.
For flashing liquid or 2-phases flow, it is hard to experience "negative dP" as you mentioned.
For gas relief, there are several locations where possibly experience pressure recovery e.g. PSV discharge expander, small pipe expanded to large header, etc. In this area posible reverse pressure (e.g. inlet pressure smaller than outlet pressure). But per experience it is hardly to pressure lower than atmospheric.
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No...but what if we have a higher outlet point? Isn't there a potential energy aspect to it?
Not clear with this statement. Do you mean the PSV discharge is higher than the discharge pipe end or in opposite ?
For formal case, above explanation may helps.
For later case, the static head would properly sufficient to create positive pressure.
Hope above helps.