ProjectEng
Chemical
- Nov 6, 2002
- 55
We have 3 reverse osmosis units, each fed by a 200hp centrifugal pump capable of approx 1600gpm @280' head and 150psi. The actual vertical run between the pump and the inlet to the RO units is about 30'. I have verified the head/flow requirements and we're ok there.
There is a 6" V-ball flow control valve on the inlet to each RO unit. As soon as the flow control valve comes off the seat, the pressure spikes up from 0 to ~130psi.
How can I economically modify this system to allow slow ramp-up in pressure, say 10psi at a time?
My thought is to put a 1 1/2" bypass w/ control valve around the existing 6" control valve. This way, I can use the bypass on start-up and slowly transition over to the 6" valve when the system was at operating pressure.
ProjectEng
There is a 6" V-ball flow control valve on the inlet to each RO unit. As soon as the flow control valve comes off the seat, the pressure spikes up from 0 to ~130psi.
How can I economically modify this system to allow slow ramp-up in pressure, say 10psi at a time?
My thought is to put a 1 1/2" bypass w/ control valve around the existing 6" control valve. This way, I can use the bypass on start-up and slowly transition over to the 6" valve when the system was at operating pressure.
ProjectEng