hello hope you are doing well
about the margin between NPSH disponible and NPSH required in centrifugal pump ,
with
design pressure 11 barg
design temperature 90
RPM 1200
process fluid water with traces of co2 and condensate
discharge pressure 4 barg
NPSH margin is 0.5 m , is it enough ?
Hope you are doing well
About horizontal pressure vessel installed 13m on a rack, upon installation and in order to achieve levelness the sliding plate was removed.
Is removing the sliding plate acceptable and can the vessel slide freely without it on the rack?