Flow condensation in parallel micro-channels - Part 2: Heat transfer results and correlation technique

被引:140
作者
Kim, Sung-Min
Mudawar, Issam [1 ]
机构
[1] BTPFL, W Lafayette, IN 47907 USA
关键词
Condensation; Micro-channel; High-flux; FALLING LIQUID-FILMS; PRESSURE-DROP; TRANSFER COEFFICIENT; MOMENTUM TRANSPORT; DIFFUSION-MODELS; SMOOTH TUBES; 2-PHASE FLOW; FLUID-FLOW; SINKS; TEMPERATURE;
D O I
10.1016/j.ijheatmasstransfer.2011.10.012
中图分类号
O414.1 [热力学];
学科分类号
摘要
This second part of a two-part study concerns heat transfer characteristics for FC-72 condensing along parallel, square micro-channels with a hydraulic diameter of 1 mm, which were formed in the top surface of a solid copper plate. Heat from the condensing flow was rejected to a counter flow of water through channels brazed to the underside of the copper plate. The FC-72 condensation heat transfer coefficient was highest near the channel inlet, where the annual liquid film is thinnest. The heat transfer coefficient decreased along the micro-channel because of the film thickening and eventual collapse of the annular regime. Notable heat transfer enhancement was observed for annular flow regions of the micro-channel associated with interfacial waves. Comparing the present data to predictions of previous annular condensation heat transfer correlations shows correlations intended for macro-channels generally provide better predictions than correlations intended specifically for mini/micro-channels. A new condensation heat transfer coefficient correlation is proposed for annular condensation heat transfer in mini/micro-channels. The new correlation shows excellent predictive capability based on both the present FC-72 data and a large database for mini/micro-channel flows amassed from eight previous sources. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:984 / 994
页数:11
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