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Excellent video prof Hugo!! Process engineer here who uses this theory to size steam heat exchangers! Is it worth the precision for wavy and turbulent film? Or are the films generally so slow that laminar is a good worst case approximation?
Excellent video prof Hugo!! Process engineer here who uses this theory to size steam heat exchangers! Is it worth the precision for wavy and turbulent film? Or are the films generally so slow that laminar is a good worst case approximation?