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EXPERIMENTAL ANALYSIS OF OPPOSING FLOW IN MIXED CONVECTION IN A CHANNEL WITH AN OPEN CAVITY BELOW

机译:下面具有开放腔的沟道中混合对流相对流的实验分析

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In this paper mixed convection in an open cavity with a heated wall bounded by a horizontal unheated plate is investigated experimentally. The cavity has the heated wall on the opposite side of the forced inflow. The results are reported in terms of wall temperature profiles of the heated wall and flow visualization for Reynolds number (Re) from 100 to 2000 and Richardson number (Ri) in the range 4.3 - 6400; the ratio between the length and the height of cavity (L/D) is in the range 0.5-2.0 and the ratio between the channel and cavity height (H/D) is equal to 1.0. The present results show that at the lowest investigated Reynolds number the surface temperatures are lower than the corresponding surface temperature for Re=2000, at same the ohmic heat flux. The flow visualization points out that for Re=1000 there are two nearly distinct fluid motions: a parallel forced flow in the channel and a recirculation flow inside the cavity. For Re=100 the effect of a stronger buoyancy determines a penetration of thermal plume from the heated plate wall into the upper channel. Moreover, the flow visualization points out that for lower Reynolds numbers the forced motion penetrates inside the cavity and a vortex structure is adjacent to the unheated vertical plate. At higher Reynolds number the vortex structure has a larger extension at same L/D value.
机译:在实验上研究了由由水平未加热板界定的加热壁的开孔中的混合对流。腔在强制流入的相对侧具有加热壁。结果是在4.3 - 6400范围内的加热壁的壁温和雷诺数(RE)的流量可视化和Reynolds Number(RE)的流量可视化而言。长度和腔高度之间的比率(L / D)的比率在0.5-2.0的范围内,并且通道和腔高度(H / d)之间的比率等于1.0。本结果表明,在最低调查的雷诺数,表面温度低于RE = 2000的相应表面温度,在相同的欧姆热通量。流量可视化指出,对于Re = 1000,存在两个几乎不同的流体运动:通道中的平行强制流动和腔内的再循环流动。对于RE = 100,较强的浮力的效果决定了从加热的板壁到上通道中的热羽流的渗透。此外,流量可视化指向用于下雷诺的数字,强制运动穿过腔内,涡流结构与未加热的垂直板相邻。在较高的Reynolds编号,涡流结构具有相同L / D值的较大延伸。

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