I'm a process engineer working for the design of a unit processing LPG. The unit includes columns, heat exchangers pumps etc.
In P&ID under development I noticed that several LOCAL drain and vent, with simple valve and cap, have been added for example between control valve isolation valves, heat exchangers isolation valves etc. Being LPG a flammable and hazardous fluid is this correct? One should not connect all vent and drain to flare/closed drain system? Is it acceptable to have local drain and vent when processing hazardous fluid?
Thanks for your help
Edited by Priolo, Today, 02:03 PM.

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