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Influence of Chemical Reaction on Mixed Convection of Non-Newtonian Fluids Along Non-isothermal Horizontal Surface in Porous Media

机译:化学反应对多孔介质中非等温水平表面的非牛顿液混合对流的影响

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The effect of chemical reaction on mixed convection heat and mass transfer in non-Newtonian fluid a long non-isothermal horizontal surface embedded in a saturated porous medium has been studied. The mixed convection regime is divided into two regions, namely, the forced convection dominated regime and the free convection dominated regime. The two solutions are matched. Numerical calculations are carried out for various values of dimensionless parameters and an analysis of the results obtained shows that the flow field is influenced appreciably by the chemical reaction, the buoyancy ratio, the viscosity index and the power-law of the wall temperature parameter. Effects of these parameters on the transport behaviors are investigated methodically and typically results are illustrated to reveal the tendency of the solutions. The results are presented graphically and the conclusion is drawn that the flow field and other quantities of physical interest are significantly influenced by these parameters.
机译:研究了化学反应对非牛顿流体中混合对流热和传质的影响,已经研究了嵌入在饱和多孔介质中的长非等温水平表面。混合对流制度分为两个地区,即强迫对流主导地位和免费对比主导地位。这两个解决方案匹配。为各种无量纲参数的数值进行数值计算,并获得所得结果的分析表明,通过化学反应,浮力比,壁温参数的浮力指数和动力定律,流场的影响是明显的影响。这些参数对有条不紊地研究了这些参数对运输行为的影响,并且通常进行结果以揭示溶液的趋势。结果以图形方式提出,结论被绘制的是,流场和其他数量的物理兴趣受到这些参数的显着影响。

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