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首页> 外文期刊>Frontiers in Heat and Mass Transfer >SLIP EFFECTS ON BOUNDARY LAYER FLOW AND MASS TRANSFER WITH CHEMICAL REACTION OVER A PERMEABLE FLAT PLATE IN A POROUS MEDIUM
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SLIP EFFECTS ON BOUNDARY LAYER FLOW AND MASS TRANSFER WITH CHEMICAL REACTION OVER A PERMEABLE FLAT PLATE IN A POROUS MEDIUM

机译:多孔介质中渗透性平板对化学反应边界层流动和传质的滑移效应

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A mathematical model is presented to analyse the steady boundary layer slip flow and mass transfer with nth order chemical reaction past a porous plate embedded in a Darcy porous medium. Velocity as well as mass slips are considered at the boundary. The governing PDEs are transformed into self-similar nonlinear ODEs by similarity transformations. The reduced nonlinear equations are solved numerically. The momentum boundary layer thickness is reduced for increase of permeability and suction parameters, whereas it increases with blowing parameter. The increase of velocity slip parameter reduces the momentum boundary layer thickness and also enhances the mass transfer from the plate. Importantly, due to increase of mass slip the concentration and mass transfer decrease.
机译:提出了一个数学模型,以分析通过嵌入达西多孔介质中的多孔板的n阶化学反应的稳定边界层滑流和传质。在边界处考虑了速度以及质量滑移。通过相似性转换将控制PDE转换为自相似的非线性ODE。简化的非线性方程是数值求解的。动量边界层厚度减小,以增加渗透率和吸力参数,而动量边界层厚度随吹塑参数而增加。速度滑移参数的增加减小了动量边界层的厚度,也增强了从板的传质。重要的是,由于传质的增加,浓度和传质降低。

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