Tube side flow velocity issues in shell and tube heat exchangers
Thread Content
For the calculated heat exchanger, the flow velocity in the tube side is less than 1, approaching 0.5 m/s – but is this solution feasible? Due to practical constraints on the length of the heat exchangers, as well as the issue of temperature cross-talk, when using heat exchangers with pure counterflow arranged in series, it is not possible to increase the flow rate within the tube side. . What should I do?
Condensate-heating return water heat exchanger: hot fluid condensate, heating return water flows through the shell side
The poster should still consult specialized heat exchanger design experts for the design, as there are too many factors to consider that cannot be explained in just a few words