Thank for your comments. SeanB the gas doesn't have any liquid.
JoeWong88, you are right, Design Pressure of compressor suction Drum normally is based on settle-out pressure with some margin, but in my case its design pressure is based on compressor discharge pressure with some margin. The...
Hi, I want to size a PSV based on fire case scenario on a vessel. The vessel is used as compressor knocks out drum. Sizing information is as following:
Operating Temperature: 47 .C (Tn)
Operating Pressure: 9.4 barg (Pn)
Design Temperature: 165 .C
Design Pressure: 69.4 barg
Vessel Size: ID=2.0...