What is the empirical range for the gas flow velocity at the evaporation interface during atmospheric or reduced-pressure distillation? It’s best to have a source
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Now, let’s calculate the size of the vessel for a flash tank. Given the amount of vaporization that occurs, the liquid flow rate, and the liquid residence time, it is possible to determine the volume occupied by the liquid. But how should the size of the gas phase space be calculated? Are there any standards that can be used as a reference? Are there any requirements or empirical values regarding the gas flow velocity at the evaporation cross-section? It would be great if there are sources available. I hope fellow experts can help; thank you
No one is browsing it. Where are you all, experts?
It seems to be a problem related to the process design; could it be due to considerations in the process design?
It should be, but right now the experience value can’t be found; not to mention what standard it’s based on – it simply can’t be located