Dear All
We are supposed to design a " Flare Gas Recovery and Utilization" unit for a gas refinery. The capacity of FGRU is 11.5 MMSCFD.
The existing flare system consists of three lines: HP, MP and LP.
Could we use a " Liquid Seal Drum" for sealing the HP path. the total back pressure of the HP flare header is 4 barg.
Some of standards such as API 521 recommend the seal drum while Total: GS EP SAP 262 didn't say anything about seal drum and recommended the " FOV" (Fast opening Valve) instead of the seal drum.
Furthermore, is there any design procedure for seal drum except API 521?