Hi All,
Please i need assistance again on the subject of blowdown system on pressure vessel. I am involved in an LPG plant project where we have a pressure vessel (cold pressure separator) operating at a pressure greater than 300 psig. The detailed designer has omitted blowdown line/valve on...
Hello,
Please i need to be advised on draining the cold separator Vessel downstream of the a turbo expander in an LPG plant. I have been told that this is not a safe practice to drain into the closed drain system. What is proposed by design is to drain this vessel to the atmosphere. Please i...