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Pulsating flow and convective heat transfer in a cavity with inlet and outlet sections

机译:带有入口和出口部分的腔体中的脉动流和对流传热

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摘要

This paper deals with the study of 2-D, laminar, pulsating flow inside a heated rectangular cavity with different aspect ratios. The cooling liquid (water with temperature dependent viscosity and thermal conductivity) comes and leaves the cavity via inlet and outlet ports. The flow topology is characterised by the large recirculation regions that exist at inner corners of the cavity. These low velocity regions cause the heat transfer to be small when compared, for instance, to that of a straight channel. We study the effect that a prescribed pulsation at the inlet port has on the cavity heat transfer. This pulsating boundary condition, of the unsteady Poiseuille type, is described by its frequency and the amplitude of the pressure gradient. The time averaged Reynolds number of the flow, based on the hydraulic diameter of the inlet channel, is 100 and we consider that the dimensionless pulsation frequency (Strouhal number) varies in the range from 0.0 to 0.4. We show that the prescribed pulsation enhances heat transfer in the cavity and that the mechanism that causes this enhancement appears to be the periodic change in the recirculation flow pattern generated by the pulsation. Regarding the quantitative extent of heat transfer recovery, we find that appropriate selection of the pulsation parameters allows for the cavity to behave like a straight channel that is the configuration with the highest Nusselt number.
机译:本文研究了不同纵横比的加热矩形腔体内的二维层流脉动流。冷却液(具有与温度相关的粘度和导热系数的水)通过入口和出口进入和离开腔体。流动拓扑的特征在于在腔体的内角处存在较大的再循环区域。当与例如直通道相比时,这些低速区域导致热传递较小。我们研究了入口处的规定脉动对腔体传热的影响。这种不稳定的Poiseuille型脉动边界条件由其频率和压力梯度的幅度来描述。基于入口通道的水力直径,流的时间平均雷诺数为100,我们认为无因次脉动频率(斯特劳哈尔数)在0.0到0.4的范围内变化。我们表明,规定的脉动增强了腔体中的热传递,导致这种增强的机制似乎是由脉动产生的再循环流型的周期性变化。关于传热回收的定量范围,我们发现适当选择脉动参数可以使腔体表现得像直通道,这是具有最高努塞尔数的配置。

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