Issues with the temperature curve of the shell and tube sides in EDR simulation results
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When simulating a heat exchanger, a drop in the temperature curve of the tube side occurs. How should this be interpreted? Is it caused by the physical properties? Figure: The length of the pipe in the pipe train is 6000 mm.
The setting is incorrect, right? The temperatures at the hot ends are the same, but there is a crossover at the cold end
A temperature drop is also possible; the tube side should be a pure component. Are these two pipelines?
The shell side is where steam condenses into condensed water, while the tube side contains an oil-water mixture; there are two tube sides in total.