Calculation of heat exchangers in distillation towers
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This post was last edited by visavis on 2011-2-26 22:37. I want to perform calculations on the top condenser and the reboiler at the bottom of the distillation column; I’m not sure how to go about it A stream of fluid is led from the side of the tower into the heat exchanger, but there are always problems. May I ask everyone: is it correct to introduce a line from the side of the tower in this way?
I went to the company today to consult the expert, and the issue has been resolved. I’m sharing the solution: in virtual logistics, it’s sufficient to introduce a logistics flow that connects to the heat exchanger
Right~ Virtual logistics is very convenient to use here
Mm, right. Try exploring a bit more, hehe
Hello, original poster. I also need detailed information on the tower top condenser for my project. I’m not sure how to define what you mean by \"virtual logistics\"; could you please provide some guidance? Thank you. :)