Overbudget
Civil/Environmental
- Aug 21, 2006
- 12
I have a vertical turbine pump delivering 800 gpm @ 420 psi at the pump discharge. I want to divert some flow from that stream to spray nozzles to clean an intake screen. No other water supply is available. The screen needs 30 gpm at 40 psi. I was looking at adding a tap in the piping and using a globe valve or needle valve to reduce the pressure. To get that flow with that pressure loss, the required Cv works out to about 1.5. I can get a 1" Class 300, bronze globe valve that will produce that Cv in a partially closed position, for about $200. I could go to a 1/2" globe valve and get the Cv I need with the valve full open. The alternative would be stainless steel needle valves made out of bar stock with a similar Cv values. It looks like these go for about $50.
Even though the math and the Cv calculation comes out "right" it still seems like a lot of flow and a lot of loss to create for a relatively small and simple valve. Are either of these valves going to have a life expectency of more than about a week in that service? For the price, I can put two or three of these valves in series, and either take the pressure down in steps or do it all in one valve and switch to the second or third valve when the first one starts to lose effeciveness.
Can anyone offer any thoughts?
Even though the math and the Cv calculation comes out "right" it still seems like a lot of flow and a lot of loss to create for a relatively small and simple valve. Are either of these valves going to have a life expectency of more than about a week in that service? For the price, I can put two or three of these valves in series, and either take the pressure down in steps or do it all in one valve and switch to the second or third valve when the first one starts to lose effeciveness.
Can anyone offer any thoughts?