I am trying to size the nitrogen blanketing inbreathing and outbreathing valve (open to atmosphere) for Amine sump drum in LNG plant.
This is underground sump pressure vessel with a PSV installed.
It also has the submerged intermittent service pump.
The PSV on the vessel is designed for the blocked vapor outlet scenario. In the event the nitrogen outbreathing valve remains closed or fails closed during the fire event or does not have enough capacity during the event overpressure will occur.
I do not have a firm flow rate for the material coming in to the sump. The pump is sized for the intermittent service.
My concern is, should I size the outbreathing valve for the overpressure event (as the PSV sizing is in the event the control valve fails close) or assume the incoming flowrate under normal circumstances.
Please explain the best design for the case.
Thank you for all the help.