When determining the overall compression required for natural Gas across a compressor or compressor station. What Delta P drop should I used for the suction and discharge of the compressor station assuming. Is there a rule of thumb of 5psig or something of the like for each side ( suction and discharge). Or is there a pressure drop rule for each componene like scrubbers valves, coolers and Ts etc. Any help will really assist me. Also is there a user friendly software out there that could simulate my velocities and pressure drop in my compressor station yard piping. Thanks
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