nctexan22
Mechanical
- Apr 14, 2008
- 26
I am designing a 1", quarter-turn ball control valve and in need of some overall guidance.
The inlet and outlet seat trims are modified with a pattern of holes intended to help reduce flow. The valve is required to pass water at a flow rate of 19 gpm, with inlet pressures ranging from 750 psig to 350 psig, while maintaining an outlet pressure of at least 150 psig.
Plugging this data into Cv = q (SG / dp)1/2, tells me that my valve must have a Cv ranging from .77 to 1.34.
My unknown is obviously pressure drop, as unless a prototype is produced and tested, the resultant p.out from the inlet pressure range is unknown.
How do I go about determining what the pressure drop will be at differing degrees of valve travel without a flow test/ CFD software?
I have been studying ANSI/ISA-75.01.01 and it seems as if these equations are geared towards globe and butterfly valves.
Any help would be greatly appreciated.
The inlet and outlet seat trims are modified with a pattern of holes intended to help reduce flow. The valve is required to pass water at a flow rate of 19 gpm, with inlet pressures ranging from 750 psig to 350 psig, while maintaining an outlet pressure of at least 150 psig.
Plugging this data into Cv = q (SG / dp)1/2, tells me that my valve must have a Cv ranging from .77 to 1.34.
My unknown is obviously pressure drop, as unless a prototype is produced and tested, the resultant p.out from the inlet pressure range is unknown.
How do I go about determining what the pressure drop will be at differing degrees of valve travel without a flow test/ CFD software?
I have been studying ANSI/ISA-75.01.01 and it seems as if these equations are geared towards globe and butterfly valves.
Any help would be greatly appreciated.