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I have16" gasoil line for transportation along 3.5 km our temp rang 25 50 degree C class 150,sch 30 19.2 bar design presser WP 12 bar
my question how to design the reliefe valve for :
1\ thermal exp.
2\ over pressure
3\ MAIP
4\ surge
If you can give me all guide and help
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Overpressuer Protection
Started by Guest_mohamed_*, Apr 21 2004 05:47 AM
1 reply to this topic
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#2
pleckner
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Posted 03 May 2004 - 04:35 PM
The reason you haven't gotten any response is because the Internet community is not going to size the PSV for you. This is a reliability (and legal) issue and you or some other, and hopefully more qualified, engineer are the only ones who can be responsible
I strongly suggest you get a copy of API RP520 and RP521 immediately. Also, I strongly recommend you get the book, "Guidlines for Pressure Relief and Effluent Handling Systems", Center for Chemical Process Safety of the American Institute of Chemical Engineers.
I strongly suggest you get a copy of API RP520 and RP521 immediately. Also, I strongly recommend you get the book, "Guidlines for Pressure Relief and Effluent Handling Systems", Center for Chemical Process Safety of the American Institute of Chemical Engineers.
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