I have to size the PSV on discharge of recip-compressor for blocked outlet case.
I believe, it should be sized for 110% of comp. rated capacity, as the segment has to be protected with margin, when compressor is running at it's rated capacity.
Others feel it should be at rated capacity only.
I...
Hi All,
I am not clear about following information:
I am working on control valve process datasheet, and find kerosene having vapor pressure of 34.3 bara and critical pressure of 27 bara.
I was expecting it otherway around i.e. vapor pressure < critical pressure.
I would appreciate if you can...
Thanks in advance for your help.
It's about distillation column design. I need to seperate multicomponent mixture of hydrocarbons. I just have feed, expected products (Top & bottom).I would like to kow how to start the design.
First, we need to have vapor liquid equilibrium, this is to be...
Hi All,
I am looking for some information about wash water mixing in Refinery catalytic reactor (say Hydrotreater / hydrocracker) effluent, to dissolve and remove chlorides/Ammonium bisulfides, before cooling below water dewpoint.
What I need information about is,
1)philosophy about method of...
