Hi everybody,
I'd like to know if anybody has ever considered in its design the possibility of installing a set of two choke valves in series on a XT, namely a non-regulating choke valve, whose opening should be sized to reduce the well pressure to a desired value, followed downstream by a traditional flow control choke valve.
Which are the advantages of such a configuration? Does it help in some way with hydrate formation control in very high pressure wells?
API 14E quotes that the number and location of chokes depend on the amount of pressure drop, well fluid, flow rate and possible solids presence. Furthermore in Chapter 5 of "Lease Pumper's Handbook" it is reported that "Permitting this pressure reduction to occur in two steps instead of one can reduce the possibility of the line freezing", but since the cooling of the fluid across the choke is due to the Joule-Thomson cooling effect, I think that no matter in how many steps I reduce the pressure from P1 to P2, the final T2 should be the same (give or take, we are moving along the same isoenthalpic curve).
Thank you in advance for your help..



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