HTRI simulation of velocity problems in falling film evaporators
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In HTRI simulations of falling film evaporators, the flow velocity inside the tubes as shown in the TEMA table and in the Tubeside Incremental Monitor is calculated using what method? Is it related to the flow velocity of the liquid film controlled by gravity? After all, in the Tubeside Incremental Monitor, the flow velocity remains the same for different distances from the tube inlet when no vaporization occurs. This is really confusing; what exactly is the meaning of this flow rate? Thank you in advance to all the experts!
Give it a push – does no one know? I’ll keep asking for help!
Give it a push; I have the same question – is it possible to design falling film condensation in HTRI?