Calculation problems for forced circulation evaporation
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I would like to ask the experts: in the calculation of forced circulation evaporation, how are the circulation rate and the flash vaporization temperature difference determined? Is iteration needed? How do we determine the convergence formula?
What I mean is a general approach – for example, should we start by specifying the flash temperature difference and then iterate? Should we still use the flow velocity inside the heat exchange tube to calculate the circulation rate? I’m not sure about the specific calculations; I’m still in the learning phase,,, I hope you can give me some guidance. Thank you!
Forced circulation heat exchange? Circulating water drum system?
External forced circulation process for heat exchangers,