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R.‘FTR = £ R^ = (tute resistance) R = l/lnJL,. (refrigerant-side convec -LX A.£ tive resistance) The above relationships are valid for heat transfer between air and dry surfaces of the heat exchanger. For the wetted surface and for the flow arrangements shown in Fig. 10 additional information is needed. WATER FILM Figure 10. Flow Parameters of the Wetted Modules The water film is assumed to flow laminarly downward under the influence of gravity. The air passage between the fin is smaller duetothepresenceofwateronbothchannelwalls. Thepassageis smallest where the water flows around the tube. Obviously the water flow must be selected such that the smallest cross-section is never blocked. (38) Water flow by gravity on inclined or vertical walls has been studied extensively [^,5,6,7]• It was shown that the flow is laminar forRe^_<250. Underthoseconditionsthewaterflowratethrough the elemental channel of the module can be given as C-23PDF Image | Development of the Zinc-Chlorine Battery for Utility
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