Boundary condition effects on natural convection of Bingham fluids in a square enclosure with differentially heated horizontal walls

IF 1.3 Q3 THERMODYNAMICS
O. Turan, R. Poole, N. Chakraborty
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引用次数: 22

Abstract

Natural convection of Bingham fluids in square enclosures with differentially heated horizontal walls has been numerically analyzed for both constant wall temperature (CWT) and constant wall heat flux (CWHF) boundary conditions for different values of Bingham number Bn (i.e., nondimensional yield stress) for nominal Rayleigh and Prandtl numbers ranging from 10 to 10 and from 0.1 to 100, respectively. A semi-implicit pressure-based algorithm is used to solve the steady-state governing equations in the context of the finite-volume methodology in two dimensions. It has been found that the mean Nusselt number Nu increases with increasing Rayleigh number, but Nu is found to be smaller in Bingham fluids than in Newtonian fluids (for the same nominal values of Rayleigh and Prandtl numbers) due to augmented flow resistance in Bingham fluids. Moreover, Nu monotonically decreases with increasing Bingham number irrespective of the boundary condition. Bingham fluids exhibit nonmonotonic Prandtl number Pr dependence on Nu and a detailed physical explanation has been provided for this behavior. Although variation of Nu in response to changes in Rayleigh, Prandtl, and Bingham numbers remains qualitatively similar for both CWT and CWHF boundary conditions, Nu for the CWHF boundary condition for high values of Rayleigh number is found to be smaller than the value obtained for the corresponding CWT configuration for a given set of values of Prandtl and Bingham numbers. The physical reasons for the weaker convective effects in the CWHF boundary condition than in the CWT boundary condition, especially for high values of Rayleigh number, have been explained through a detailed scaling analysis. The scaling relations are used to propose correlations for Nu for both CWT and CWHF boundary conditions and the correlations are shown to capture Nu satisfactorily for the range of Rayleigh, Prandtl, and Bingham numbers considered in this analysis.
边界条件对水平壁面差热方形壁面中宾厄姆流体自然对流的影响
在Rayleigh数和Prandtl数分别为10 ~ 10和0.1 ~ 100的不同Bingham数Bn值(即无量纲屈服应力)条件下,采用定壁温度(CWT)和定壁热流密度(CWHF)边界条件,对具有差热水平壁面的方形壁面中Bingham流体的自然对流进行了数值分析。采用基于压力的半隐式算法求解二维有限体积方法下的稳态控制方程。发现平均努塞尔数Nu随着瑞利数的增加而增加,但由于宾厄姆流体中的流动阻力增大,宾厄姆流体中的Nu小于牛顿流体(在瑞利数和普朗特尔数的标称值相同的情况下)。而且,无论边界条件如何,Nu都随Bingham数的增加而单调减小。宾厄姆流体表现出非单调的普朗特数Pr依赖于Nu,并对此行为提供了详细的物理解释。尽管对于CWT和CWHF边界条件,Nu随Rayleigh、Prandtl和Bingham数变化的变化在性质上保持相似,但对于高Rayleigh数时,CWHF边界条件的Nu小于给定一组Prandtl和Bingham数时对应CWT构型的Nu。通过详细的标度分析,解释了CWHF边界条件对流效应弱于CWT边界条件的物理原因,特别是在高瑞利数边界条件下。缩放关系用于提出CWT和CWHF边界条件下Nu的相关性,并且在本分析中考虑的瑞利、普朗特和宾厄姆数范围内,相关性可以令人满意地捕获Nu。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
CiteScore
2.70
自引率
6.70%
发文量
36
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