Local overall heat transfer coefficient. In Problem 14A.1 the thermal resistances of the condensed steam film and
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Local overall heat transfer coefficient. In Problem 14A.1 the thermal resistances of the condensed steam film and wall were neglected. Justify this neglect by calculating the actual inner-surface temperature of the tubes at that cross section in the exchanger at which the oil temperature is 150°F. You may assume that for the oil hloc is constant throughout the exchanger at 190 Btu/hr ∙ ft2 ∙ F. The tubes are horizontal.
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Local overall heat transfer coefficient Let 0 and 1 denote the inner and outer surfaces of the tube ...View the full answer
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