Hello Folks,
I am currently looking at the following plant design Issue:
I have been tasked to optimize buster compression design for a gas treating plant (300 MSCFD of wet gas), during the lifetime of the facility the pressure will drop from 1500 psia to 750 psia(at year 8) and then further...
Folks,
I am trying to collect some cost data to compare regular orifice plates to orifice plates with flow conditioning (single plate/multi holes).
I have estimates a reduction in straight pipe lengths of about from 20 diameter (upstream) to 2 d which is giving me considerable saving on large...
All,
In place of a pneumatic pressure test, my project is opting for a Hydro test be done no cryogenic piping. Can this be done? Are there reasons to stay away from the hydro test?
Thank you.
