Heat transfer calculation problem
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Heat exchange calculation example: Here, acidic steam is being condensed for heat exchange; the acid content is very low and can be ignored. To completely condense the steam into condensed water, preliminary simulation calculations using horizontal shell-side condensation yielded the following approach: Why are the results so different despite the same structural design? I seek advice from experts; moreover, which approach is more reasonable?
This post was last edited by LZD420983 on 2020-11-27 at 08:00; it shows the results of a heat transfer calculation. I’m seeking guidance from experts