Dear all,
I am involved in design of vortex breaker for crude oil storage tank liquid side outlet. Tank height - 22 mtrs & Diameter - 110 mtrs, Outlet nozzle size is 48". Being no enough liquid submergence,I have to do alternate design to avoid vortex formation. Can anybody having more experience & exposure in this design can forward their suggestion,calculation,excel sheets & post their replies ASAP Email ID - viswa7109a@yahoo.co.in. * How to relate froude number & reynolds number what are values & range to be followed?
Thanks in advance.
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Vortex Breaker Design
Started by viswanathan, Nov 01 2009 04:38 AM
3 replies to this topic
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#1
Posted 01 November 2009 - 04:38 AM
#2
Posted 01 November 2009 - 05:03 AM
#3
Posted 01 November 2009 - 05:09 AM
Hi
Let you try this link:
http://cr4.globalspe.../Vortex-Breaker
Hope it helps
Breizh
Hai Thanks
I already refered this thread, I want to prove the client with calculation that vortex will not form,Please forward if you have any calculations
#4
Posted 04 November 2009 - 06:12 AM
I do not know any empirical relation to calculate this (and how to account for geometry) - the only way I can see to accomplish the task is running CFD simulation and applying VOF (volume of fluid) multiphase model, which is suitable for free surface flows (in past I applied this to obtain vortex surface in an unbaffled stirred tank).
Hope this helps.
Hope this helps.
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