用CEF模型处理非牛顿流体介质中的颗粒沉降

Ş. Celasun
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引用次数: 0

摘要

在本研究中,考虑了小颗粒在非牛顿流体介质中的沉降。根据流体力学原理对这一问题的模拟可以用非牛顿流体沿圆柱形管的中心线绕球体运动来实现。在实际操作中,粒子沉降速率的知识对于确定诸如食品、清洁材料和许多其他材料的保质期尤为重要。因此,这个问题在许多自然和物理过程中以及在化学、遗传和生物医学工程操作等大量工业应用中具有重要意义。文献中可用的大多数理论、实验和数值研究都涉及牛顿流体。相反,对于非牛顿流体,问题要复杂得多。众所周知,非牛顿流体中的拉伸行为在复杂流动中起着重要作用。大多数非牛顿流体,如聚合物溶液和熔体,都表现出剪切变薄的行为。在这项研究中,旨在确定控制这一过程的方程,并得出一些关于聚合物液体的性质与其粘弹性结构有关的重要结论。有效地发现,对于聚合物液体,以法向应力系数为特征的弹性行为意味着相对于广义牛顿流体的法向应力相对增加,而剪切应力趋于减少,从而在一定程度上以较小的速率将流动类别从剪切流动转变为拉伸流动。因此,聚合物液体的粘弹性必须通过其本构方程的选择来强调,这导致了CEF模型的产生。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Particle Settling in a Non-Newtonian Fluid Medium Processed by Using the CEF Model
In this study, the settling of small particles in a non-Newtonian fluid medium is consid- ered. The simulation of this problem according to the fluid mechanics principles may be realized by the flow of a non-Newtonian fluid around a sphere falling along the centerline of a cylindrical tube. The knowledge of the rate of settling of particles in practice is particularly significant in determining the shelf life of materials such as foodstuffs, cleaning materials and many others. Thus, this problem has great importance in many natural and physical processes and in a large number of industrial applications such as chemical, genetic and biomedical engineering operations. The majority of the theoretical, experimental and numerical studies available in the literature deal with Newtonian fluids. Conversely, for non-Newtonian fluids the problem is considerably more complex. It is well-recognized that extensional behaviour in non-Newtonian fluids plays a major role in complex flows. Most non-Newtonian fluids such as polymeric solutions and melts exhibit shear-thinning behaviour. In this study it is aimed to determine the equations governing this process and some important conclusions about the properties of polymeric liquids related to their viscoelastic constitution are drawn. Effectively, it is found that for poly- meric liquids, the elastic behaviour characterized by the normal stress coefficients, implies relatively increased normal stresses with respect to the generalized Newtonian fluids, whereas the shear stresses tend to decrease, thus changing somewhat the category of the flow from shear-flow into extensional flow in a small rate. Hence, the viscoelastic property of the polymeric liquids must be stressed by their constitutive equation choice, which led us to the CEF model.
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