Research of Flow Boiling Bubble Dynamics in Vertical Rectangular Mini-channel

Lei Guo, Shu-Sheng Zhang, Yaqun Chen, Lin Cheng
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引用次数: 5

Abstract

Flow boiling in vertical rectangular mini-channel with width of 2mm and length of 390mm is studied in this paper. In single-side heating situation, the narrow channel is divided into three zones, bubbles generating zone, growth zone and annihilation zone. The motion characteristics of bubbles in various stages are accompanied by the changes of three zones. The courses of bubbles generation, growth and departure are numerically simulated. All the calculation conducted takes the gravity, surface tension and wall adhesion into account. Found that surface tension is much more important than gravity in the process of boiling heat transfer. As the overheating increases, the departure diameter D of bubbles increases significantly. When the bubble diameter D is larger than 1.5mm, it will be influenced by the incoming flow. The existence of bubble bottom micro-layer accelerates the flow convection on the wall and increases the coefficient of heat transfer. The results of simulation have a good coherence with experimental datum.
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垂直矩形小通道内流动沸腾泡动力学研究
本文研究了宽度为2mm、长度为390mm的垂直矩形微通道内的流动沸腾。在单面加热情况下,窄通道分为气泡产生区、生长区和湮灭区三个区域。气泡在各个阶段的运动特性都伴随着三个区域的变化。数值模拟了气泡的产生、生长和离开过程。所有的计算都考虑了重力、表面张力和壁面附着力。发现在沸腾传热过程中,表面张力比重力更重要。随着过热程度的增加,气泡的偏离直径D显著增大。当气泡直径D大于1.5mm时,会受到来流的影响。气泡底微层的存在加速了壁面上的流动对流,增大了换热系数。仿真结果与实验数据有较好的一致性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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