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Using Structured Surfaces to Enhance Heat Transfer in Falling Film Flow

机译:利用结构化表面增强降膜流动中的传热

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The heat transfer performance of an ordinary roughened (sand-blasted) surface and four commercially available structured surfaces were tested with falling film flow arrangement. The commercial surfaces were: High Flux (Union Carbide), Gewa-T (Wieland) and Thermoexcel-E and -EC (Hitachi). The test evaporator consisted of a jacket and a single, vertical 2 m long test tube. The evaporating liquid flowed down on the outside of the test tube. The tests were conducted with refrigerant R114 at evaporation temperature of 23 deg C. In the fully developed region (x>0.4-1.0 m) the flow was distorted due to strong nucleation and droplet entrainment. At higher evaporation rates (>35-45%) the bottom parts of the test tube were not properly wetted and the heat transfer coefficient decreased although no permanent dry patches were yet seen. Nucleate boiling was dominant at all het fluxes tested with the commercial surfaces. No boiling hysteresis was observed. They all showed excellent performance, the best one (Thermoexcel-E) having 12 times better heat transfer than smooth tube. When heat flux was increased they all showed similar trend: the obtained enchancement compared to smooth tube was reduced. The sand-blasted tube could not compete with the structured surfaces. Its behaviour was more like smooth tube. During surface evaporation its performance was 1.4 to 1.8 times and during nucleation 1.7 times higher than smooth tube values. (ERA citation 11:037834)

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