WHEN regulating the level in a scrubber(control valve after the pump) should we use PI or PID?
NB
scrubber--> pumps(export condensate)--> control valve
WHEN SIZING A SCRUBBER I FOUND A 'MOMENTUM CRITERION' TO SIZE THE INTERNAL NOZZLE DIAMETER IT WAS/
mean density of the mixturein the feed pipe*(velocity of the mixture)^2
it's value must be < 6000
can u explain for what is this criterion and if i have a momentum > 6000 what shall i do
thx
i have a cavitation problem in my centrifugal pumps.
in the bigining, i thought that it was a problem of NPSHA which was in fact bearly lower than the NPSHr but our pump supplier told me that the problem of cavitation could have many rasons not only NPSHA and proposed an expensive pump.
can...