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Cooperating Double Diffusion Natural Convection in a Square Enclosure with Partially Active Vertical Wall

机译:具有部分主动垂直墙的方形外壳中的双重扩散自然对流

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Steady, laminar, double diffusion natural convection flow in a square enclosure with partially active vertical wall is considered. The enclosure is filled with a binary fluid and subjected to horizontal temperature and concentration gradients. The flow is driven by cooperating thermal and solutal buoyancies. Finite volume method is used to solve the dimensionless governing equations. The physical problem depends on five parameters: thermal Rayleigh number (Ra_t = 10~3-10~6), Prandtl number (Pr = 7), Schmidt number (Sc = 240), buoyancy forces ratio (N = 1) and the aspect ratio of the enclosure (A = 1). The active location takes three positions in the left wall: top (T), middle (M) and bottom (B). The main focus of the study is on examining the effect of Rayleigh number on fluid flow and heat and mass transfer rates. The results including the streamlines, isotherm and iso-concentration patterns, flow velocity and the average Nusselt and Sherwood numbers for different values of Ra_t. The obtained results show that the increase of Ra_t leads to enhance heat and mass transfer rates. The fluid particles move with greater velocity for higher thermal Rayleigh number. Also by moving the active location from the top to the bottom on the left vertical wall, convection and heat and mass transfer rates are more important in case (B). Furthermore for high Rayleigh number (Ra_t = 10~6), Convection mechanism in (T) case is principally in the top of the enclosure, whereas in the remaining cases it covers the entire enclosure.
机译:考虑了具有部分有源垂直壁的方形外壳中的稳定,层状,双扩散自然对流流量。外壳填充有二元流体并进行水平温度和浓度梯度。该流动是通过合作热和溶型浮力的驱动。有限体积法用于解决无量纲的控制方程。物理问题取决于五个参数:热瑞利数(RA_T = 10〜3-10〜6),PRANDTL编号(PR = 7),施密特数(SC = 240),浮力力比(n = 1)和方面外壳的比率(a = 1)。活动位置在左侧墙中取出三个位置:顶部(t),中间(m)和底部(b)。该研究的主要重点是在检查Rayleigh数量对流体流量和热量和传质速率的影响。结果包括流线,等温线和异浓度图案,流速和用于不同RA_T值的平均NUSERET和SHERWOOD编号。所得结果表明,RA_T的增加导致增强热量和传质速率。流体颗粒具有更高的热瑞利数的速度。另外,通过从左侧垂直墙壁上的顶部到底部的活动位置,对流和热量和传质速率更为重要,在这种情况下(b)更重要。此外,对于高瑞利数(RA_T = 10〜6),(T)壳体的对流机构主要在外壳的顶部,而在其余情况下,它覆盖整个外壳。

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