All
I am a Process Engineer working on the topsides design of a FPSO project. We have a Heating Medium (HM) system. This is a pressurised, closed loop system. The HM is a TEG / Fresh Water mixture. HM supply temperature (to consumers) = 140ºC, HM return temperature (from consumers) = 90ºC.
My previous project experience with such a system is that Gate valves should be selected for manual isolation valves in this service. However, I cannot recall the technical reason for avoiding other types, such as ball, for HM service. We also may have shutdown valves in this service and we have sown these as being gate types, but a query has been raised as to whether ball would be acceptable.
I would greatly appreciate any input to this, as I am sure Gate is the right selection and that ball should be avoided in this service - I just cannot remember why! Thanks.
M