How to calculate a falling film evaporator?
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This post was last edited by beileim1 on 2009-5-2 09:44. I would like to ask if anyone has calculated for falling-film evaporators? Could you tell me what model was used for the calculation? Is it the same as the falling-film type?
The calculation principle for all devices is basically the same; it’s just that the empirical values differ (empirical data is very important). Everything is calculated based on the generation capacity; design work is generally done in a conservative manner, with a certain margin added on top of the calculated values.
Got it; I’ll pay special attention to the margin when doing the calculations
The general calculation principles are similar to those used for heat exchangers; however, certain empirical data need to be taken into consideration, such as the heat transfer coefficient and the arrangement of the tubes.
Oh, I’m facing such a problem
No matter what type of evaporator it is, the design remains the same; you just need to look at the design of chemical processing equipment
Is the calculation for the condenser consistent with that for the evaporator? I would appreciate the advice from those who are more experienced