Good Afternoon,
I have some questions in regards to vortex breakers to prevent vortexing when the vessel is dumping; when it is requirement to install them into a Vertical / Horizontal process vessels? Is it a function of L/D, retention time, inlet velocity, inlet pressure and / or the diameter of the inlet and the dump connections on the bottom of the vessel? Do we have to consider this when we are sizing the vessel? I was able to find any lecture, calculations and or design criteria in my searcher. I was wondering someone could shed / or provide some clarification on this manner would be appreciated!