notnats
Mechanical
- Apr 25, 2003
- 179
I am using a modified globe valve to regulate flow from a filtering plant. A relief valve is fitted upstream from the globe valve. This valve cracks at 2.5 bar and at full flow of about 5000l/h has a back pressure of 8 bar. The medium is light oil about 15 cSt.
To get good flow control we have replaced the normal poppet in the 25mm globe valve with a tapered plug topped with a 45 deg face to match the valve seat when fully closed.
The system works well except that as the valve is closed, at about 2000l/h and about 5 bar the valve starts to vibrate and howl.
As the valve is re opened, at the point where the howling stops the pressure suddenly rises by about 0.5 bar.
I suspect that I am going from laminar flow to turbulent and the howling vibration could be cured by machining slots or grooves to create more turbulence.
Has anybody any suggestions?
Jeff Stanton
To get good flow control we have replaced the normal poppet in the 25mm globe valve with a tapered plug topped with a 45 deg face to match the valve seat when fully closed.
The system works well except that as the valve is closed, at about 2000l/h and about 5 bar the valve starts to vibrate and howl.
As the valve is re opened, at the point where the howling stops the pressure suddenly rises by about 0.5 bar.
I suspect that I am going from laminar flow to turbulent and the howling vibration could be cured by machining slots or grooves to create more turbulence.
Has anybody any suggestions?
Jeff Stanton