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Assisting and opposing mixed convection with conjugate heat transfer in a differentially heated cavity filled with coarse-grained porous media

机译:在填充有粗粒多孔介质的差热腔中,通过共轭传热辅助和对抗混合对流

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We report numerical simulations of assisting and opposing mixed convection in a side-heated, side-cooled cavity packed with relatively large solid spheres. The mixed convection is generated by imposing a movement on the isothermal vertical walls, either in or opposite to the direction of natural convection flow. For a fluid Prandtl number of 5.4 and fluid Rayleigh numbers of 10~6 and 10~7, we varied the modified Richardson number from 0.025 to 500. As in fluids-only mixed convection, we find that the mutual interaction between forced and natural convection, leading to a relative heat transfer enhancement in assisting - and a relative heat transfer suppression in opposing - mixed convection, is most prominent at a Richardson number of approximately one, when the Richardson number is modified with the Darcy number Da and the Forchheimer coefficient C_f = 0.1 as Ri_m = Ri × Da~(0.5)/C_f. We focus on local flow and heat transfer variations in order to explain differences in local and average heat transfer between a coarse grained and fine grained (Darcy-type) porous medium, at equal porosity and permeability. We found that the ratio between the thermal boundary layer thickness at the isothermal walls and the average pore size plays an important role in the effect that the grain and pore size have on the heat transfer. When this ratio is relatively large, the thermal boundary layer is locally disturbed by the solid objects and these objects cause local velocities and flow recirculation perpendicular to the walls, resulting in significant differences in the wall-averaged heat transfer. The local nature of the interactions between flow and solid objects cannot be captured by a volume averaged approach, such as a Darcy model.
机译:我们报告了在一个侧面加热,侧面冷却的腔体中,相对的混合对流的辅助和相对数值模拟,腔体中装有相对较大的实心球体。混合对流是通过在等温垂直壁上沿自然对流流动方向或相对于自然对流方向移动来生成的。对于5.4的流体Prandtl数和10〜6和10〜7的流体瑞利数,我们将修正的Richardson数从0.025更改为500。在仅流体混合对流中,我们发现强制对流与自然对流之间的相互作用当用达西数Da和Forchheimer系数C_f修改理查森数时,在辅助-对流混合对流中导致相对传热增强-在相对混合混合对流中相对传热抑制最为突出。当Ri_m = Ri×Da〜(0.5)/ C_f时= 0.1。为了说明在相同孔隙率和渗透率的情况下,粗粒和细粒(达西型)多孔介质之间局部和平均传热的差异,我们关注局部流动和传热的变化。我们发现等温壁处的热边界层厚度与平均孔径之间的比率在晶粒和孔径对传热的影响中起着重要作用。当此比率相对较大时,热边界层会受到固体物体的局部干扰,这些物体会导致局部速度和垂直于壁的气流再循环,从而导致壁平均传热的显着差异。流和固体对象之间相互作用的局部性质无法通过体积平均方法(例如Darcy模型)来捕获。

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