Sep 28, 2011 #1 twoplates Petroleum Joined Sep 28, 2011 Messages 2 Location US If installing a RD below relief valve, does the pressure setting have to be below the PSV, or just below the MAWP of the vessel being protected? Or should it be slightly higher to prevent premature rupture and possible contamination/damage to PSV?
If installing a RD below relief valve, does the pressure setting have to be below the PSV, or just below the MAWP of the vessel being protected? Or should it be slightly higher to prevent premature rupture and possible contamination/damage to PSV?
Sep 28, 2011 1 #2 BenThayer Chemical Joined Jan 9, 2004 Messages 218 Location US check out Fike's info regarding the use of PSD and PSV combinations. EDIT: copy the entire address and paste it. the link doesn't work... http://www.fike.com/documents/presrel/adrd/technical_bulletins/TB8105 Best Practices for RD_PRV.pdf the excess flow valve to allow small leaks to escape or the use of a pressure switch between the PSD and PSV are not uncommon depending on the gas and service. Upvote 0 Downvote
check out Fike's info regarding the use of PSD and PSV combinations. EDIT: copy the entire address and paste it. the link doesn't work... http://www.fike.com/documents/presrel/adrd/technical_bulletins/TB8105 Best Practices for RD_PRV.pdf the excess flow valve to allow small leaks to escape or the use of a pressure switch between the PSD and PSV are not uncommon depending on the gas and service.