Hi there
this seems an unusual application for a (Valtek?) ShearStream valve as you are dropping all your pressure at one point and flashing. You will get less noise and vibration either by going to a multiport valve such as MegaStream, Tigertooth or Channelstream, but at considerable cost.Some of these styles are suitable for flashing service. If the flow is fairly constant, you could look at a Megastream plate diffuser to take out some of the sting.I have never used one in flashing service,however. Note that all the above have small passages. If your liquid is dirty, blockages may be a problem. In this case you will probably have to use a choke tube, but this is only effective at constant flow, and the valve will have to do the work at reduced flows. The alternative is a series of series staged valves - very expensive and may be difficult to design for flashing service. I assume you have checked that the vibration is not a resonance problem. If it is, a large lump of concrete or steel will quiet things down. Finally, you may need to check that you are not getting gas pockets upstream of the valve. It may be causing slugging. If you can eliminate the gas, things may settle down.
Cheers
Steve McKenzie
-----Original Message-----
From: Paul Bowers [mailto:pbowers@pipingdesign.com]
Sent: Thursday, June 27, 2002 3:17 PM
To: PipingDesign@yahoogroups.com
Subject: [PipingDesign] Fwd:Vibration from flashing valve
Importance: High
____________________Forward Header_____________________Subject: Vibration from flashing valve Author: KV Ravichandran
Hi,
Can any one give guidelines for quelling vibrations from flashing control
valve.
This is my problem
There is in one 8" Zirconium line carrying acetic acid/ catalyst from
reactor
to flash tank. At the flash tank side the line has one flashing control
valve ,
gate valve and a conical expander section of about 4.6m long where the pipe
dia
increases from 10" to 26" and connects to the flash tank eccentrically.The
source of vibration is the flashing control valve (shear stream ball
valve)which
throttles from 26 bars to 2 bars. The liquid flow velocity is about 8.5m/s
at
the valve.Operating temperature of the line is 193 deg C.
During the original design two phase flow and vibration was considered and
the
line is supported with TICO Vibration isolation pads and U bolt clamps.
Now the platform from the flash tank as well as the structure supporting the piping near the flashing valve is vibrating.
To have an idea about the magnitude of the vibration following is the latest measurements at the flashing valve.
Fcy Velocity Hz mm/sec 4.405 1.418 8.811 1.049 13.22 .6426 22.03 .6278 48.46 1.876
Thanks in advance
Regards,
K.V.RaviChandran
Senior Piping Engineer
Foster Wheeler Eastern Pte. Ltd.
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Received on Wed Jun 26 21:02:00 2002
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