reda08
Mechanical
- Jan 24, 2012
- 7
Please advice regarding the behaviour of a suction pressure control valve (during turbo compressor start up)which is located upstream the suction scrubber for a centrifugal gas compressor the valve is designed on upstream pressure 60 bar with pressure drop of 14.5 bar,but now the condition of the plant pressure is 48 bar and pressure drop varing between 8 to 12 barg (set point between 40 and 36 barg), in that case the valve is not stable (playing in 2-3 barg) around the set point.Please advisce is this due to varing between the design conditions and the site conditions or may be there is a problem in the valve itself