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Interfacial Structure of Gas-Liquid Two-Phase Flow in Narrow Rectangular Channel

机译:窄矩形通道内气液两相流的界面结构

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The two-phase flow in mini/micro channels is becoming important in many industrial applications. To remove high heat flux from electric and power devices, the flow boiling in narrow rectangular channels is one of the most effective heat-dissipation methods, and several studies have been made on the two-phase flow characteristics confined to the narrow space. The present study addresses the effect of the flow orientation on the gas-liquid interfacial structure and the frictional pressure gradient in narrow rectangular channel. Simultaneous measurements of pressure gradients and spatio-temporal characteristics of gas-liquid interface are conducted for three different flow orientations; vertical upward flow (V flow), horizontal flow between horizontal plates (H-H flow) and horizontal flow between vertical plates (H-V flow). The velocity field in the liquid film with interfacial waves is also measured by PIV and LIF method. To investigate the contribution of the interfacial structure to the frictional pressure gradient, a hydrodynamic flow model of the liquid phase is presented for the narrow rectangular channel.
机译:微型/微型通道中的两相流在许多工业应用中变得越来越重要。为了消除电气和电力设备中的高热通量,在狭窄的矩形通道中沸腾的流动是最有效的散热方法之一,并且已经对局限于狭窄空间的两相流动特性进行了若干研究。本研究解决了流动方向对窄矩形通道内气液界面结构和摩擦压力梯度的影响。针对三种不同的流动方向,同时测量了压力梯度和气液界面的时空特性。垂直向上流动(V流),水平板之间的水平流(H-H流)和垂直板之间的水平流(H-V流)。带有界面波的液膜中的速度场也通过PIV和LIF方法测量。为了研究界面结构对摩擦压力梯度的贡献,提出了窄矩形通道的液相流体动力模型。

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