Correlations of mixed convection in a double lid-driven shallow rectangular cavity: The case of non-Newtonian power-law fluids

IF 2.8 Q2 THERMODYNAMICS Heat Transfer Pub Date : 2024-08-05 DOI:10.1002/htj.23138
A. Louaraychi, M. Lamsaadi
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Abstract

This work provides an analytical and numerical assessment, complete with correlations, of mixed convection in a double lid-driven shallow rectangular enclosure, which confines non-Newtonian fluids of the Ostwald–de Waele type and which a uniform thermal flux heats. The finite volume method with the SIMPLER algorithm is the numerical method used to solve the governing partial differential equations along with the boundary conditions, where the parallel flow concept is the analytical approach. In the limits of the explored values of the governing parameters of this study, which are the Rayleigh number, the Peclet number, and the behavior index, the results obtained by these approaches appear to be in good harmony. On the basis of the results obtained by these approaches, we established helpful correlating relations between the governing parameters to realize the contribution of mixed convection to heat transfer. This leads to the finding that the ratio Ra/Pe2+n is the mixed convection parameter, which is the key to distinguishing the three convective flow modes. On the basis of this parameter, which allows the transition from one regime to another, it is possible to identify the zones that designate the predominance of natural, forced, and mixed convection. The limits of these latter depend on the behavior index, n, which is diversified from 0.6 to 1.4 to account for shear thinning (0 < n < 1, low apparent viscosity, high fluid flow, and high heat transfer rate), Newtonian (n = 1), and shear thickening (n > 1, high apparent viscosity, slow fluid flow, and low heat transfer rate) fluids. On the other hand, the study presents and interprets the influences of the steering factors on heat transfer and fluid flow.

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双盖驱动浅矩形腔中混合对流的相关性:非牛顿幂律流体的情况
这项研究对双盖驱动浅矩形围壳中的混合对流进行了分析和数值评估,并提供了相关数据。该围壳内是奥斯特瓦尔德-德韦勒型非牛顿流体,由均匀热流加热。采用 SIMPLER 算法的有限体积法是一种数值方法,用于求解与边界条件相关的偏微分方程,平行流概念是一种分析方法。在雷利数、佩克莱特数和行为指数等本研究的控制参数的探究值范围内,这些方法得出的结果似乎非常一致。在这些方法得出的结果基础上,我们建立了控制参数之间的相关关系,以实现混合对流对传热的贡献。由此发现,混合对流参数 Ra/Pe2+n 是区分三种对流模式的关键。该参数允许从一种状态过渡到另一种状态,根据该参数可以确定自然对流、强制对流和混合对流占主导地位的区域。后者的界限取决于行为指数 n,该指数从 0.6 到 1.4 不等,可用于剪切稀化流体(0 < n < 1,低表观粘度、高流动性和高传热率)、牛顿流体(n = 1)和剪切增稠流体(n > 1,高表观粘度、低流动性和低传热率)。另一方面,研究还介绍并解释了转向因素对传热和流体流动的影响。
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来源期刊
Heat Transfer
Heat Transfer THERMODYNAMICS-
CiteScore
6.30
自引率
19.40%
发文量
342
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