Abstract

A previous study presented a design method for compact plate-fin heat exchangers having flow passages with frequent interruptions. The local assumption was applied whereby the local boiling heat transfer coefficient was assumed to be fixed by the local metal-to-liquid ΔT. The present study extends the local assumption to include the effect of velocity on the local heat transfer coefficient. Confirmation of the new method is provided by a comparison of prediction and data for Freon-113 in an actual heat exchanger.

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