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Heat and Mass Transfer in 3D Inclined Lid-Driven Solar Distiller

机译:3D倾斜盖驱动太阳能蒸馏器的传热传质

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This work is dedicated to study numerically an inclined solar distiller subject of a moving cold wall. The cavity is heated from left side and cooled from the right one. Constant and different concentrations are imposed in the two vertical sides of the cavity, while the other walls are adiabatic and impermeable. The flow is considered laminar and caused by the interaction of the thermal energy and the chemical species diffusions. Equations of concentration, energy and momentum are formulated using vector potential-vorticity formulations in its three-dimensional form, then discretized by the finite volumes method. The Rayleigh, Prandtl, Lewis numbers and buoyancy ratio are respectively fixed at Ra=10~5, Pr=0.7, Le=0.85 and N=0.85. Reynolds number (Re) is varied along the study from 0 to 150. The angles for the cavity inclination under this investigation are considered to be 0°, 30°, 45°, 60° and 90°. A particular interest to the flow structure and evolution of the heat and transfer i highlight in this paper.
机译:这项工作致力于从数值上研究移动的冷壁的倾斜太阳蒸馏器。从左侧加热型腔,从右侧冷却型腔。在空腔的两个垂直侧面施加恒定且不同的浓度,而其他壁是绝热且不可渗透的。该流动被认为是层流的,是由热能和化学物质扩散的相互作用引起的。浓度,能量和动量方程式是使用矢量势-涡度公式以其三维形式公式化的,然后通过有限体积法离散化。瑞利,普朗特,路易斯数和浮力比分别固定为Ra = 10〜5,Pr = 0.7,Le = 0.85和N = 0.85。雷诺数(Re)在研究中从0到150变化。在此研究中,腔倾斜角度被认为是0°,30°,45°,60°和90°。在本文中,我特别关注流动结构以及热量和传递的演化。

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