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首页> 外文期刊>Communications in Nonlinear Science and Numerical Simulation >Forced convective heat transfer of nonlinear viscoelastic flows over a circular cylinder at low Reynolds inertia regime
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Forced convective heat transfer of nonlinear viscoelastic flows over a circular cylinder at low Reynolds inertia regime

机译:低雷诺惯性条件下圆柱上非线性粘弹性流的强迫对流换热

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摘要

In this paper, the forced convective heat transfer of viscoelastic fluid flow around a circular cylinder at a low Reynolds number is studied numerically. The effect of viscous dissipation on the problem is modeld which is the main innovative aspect of present study. The Phan-Thien-Tanner (PTT) model is used as the nonlinear constitutive equation. To avoid divergence and stabilize the numerical process in high elastic cases, the log-conformation approach is used. The results indicated that the Nusselt number (Nu) monotonically increases with increasing elasticity number (El), retardation ratio (beta), Prandtl number (Pr), and Brinkman number (Br) in a wide range. Both drag reduction (for El < 0.025) and drag enhancement (for El > 0.025) were seen in the numerical results. In high elastic flow regime (El > 10), due to the increased storing nature of viscoelastic fluid compared to the dissipative nature, drag coefficient (C-D) and Nu become constant, which causes the fluid to behave like a Newtonian fluid. The temperature-dependent properties were also investigated for all of fluid property, and the large effects of viscosity, and relaxation time were seen in hydrodynamic and thermal parameters. The contribution of normal stresses in viscous dissipation (VD) is much lower than shear stress, due to the lower values of corresponding components in deformation tensor. The elasticity influences the heat transfer by two mchanisms of convection empowering as an indirect way and viscous dissipation as a direct way. Increasing El, beta, and xi increases Nu via the convection mechanism (even at Br = 0), while Nu is decreased with epsilon. However, Nu increases with the variations of all the parameters, in presence of viscous dissipation. It was also seen that the heat transfer direction changes for Br > 90. Finally, the effects of El, beta, epsilon, xi, Pr, and Br on the distribution of stress components, velocity, temperature, Nu, and C-D were investigated. Two accurate correlations were proposed for the variations of C-D and Nu against El, which were validated for a wide range of El. (C) 2019 Elsevier B.V. All rights reserved.
机译:本文以低雷诺数数值研究了绕圆柱体的粘弹性流体的强迫对流换热。对粘性耗散对问题的影响进行了建模,这是本研究的主要创新方面。 Phan-Thien-Tanner(PTT)模型用作非线性本构方程。为了避免发散并稳定高弹性情况下的数值过程,使用了对数构造方法。结果表明,在宽范围内,随着弹性数(El),延迟比(β),普朗特数(Pr)和布林克曼数(Br)的增加,努塞尔数(Nu)单调增加。在数值结果中可以看到减阻作用(对于El <0.025)和减阻增强作用(对于El> 0.025)。在高弹性流态(El> 10)中,由于粘弹性流体的存储特性与耗散特性相比有所增加,因此阻力系数(C-D)和Nu变得恒定,这导致流体的行为类似于牛顿流体。还研究了所有流体性质的温度依赖性性质,并且在流体力学和热学参数中看到了粘度和松弛时间的较大影响。由于变形张量中相应分量的值较低,因此正应力在粘滞耗散(VD)中的贡献远低于剪切应力。弹性通过对流授权的两种机制影响传热,间接对流授权的机理对流传热,而粘滞耗散则直接影响两种方式。通过对流机制(即使在Br = 0时),增加El,β和xi也会增加Nu,而ε会减少Nu。但是,在存在粘性耗散的情况下,Nu随着所有参数的变化而增加。还可以看出,当Br> 90时,传热方向会发生变化。最后,研究了El,β,ε,xi,Pr和Br对应力分量,速度,温度,Nu和C-D分布的影响。针对C-D和Nu对El的变化,提出了两个准确的相关性,并针对广泛的El进行了验证。 (C)2019 Elsevier B.V.保留所有权利。

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