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Direct numerical simulation of solid-liquid flow of Newtonian and viscoelastic fluids.

机译:牛顿流体和粘弹性流体固液流动的直接数值模拟。

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The main theme of this work is to enhance the understanding on the behavior of solid particles in flows of Newtonian or viscoelastic fluids by using both two-dimensional and three-dimensional direct numerical simulations (DNS). A large-scale state-of-the-art software package PARTMOVER3D is developed based on an Arbitrary Lagrangian-Eulerian (ALE) technique and an Elastic-Viscous-Stress-Split (EVSS) scheme. Our numerical results are extensively compared with analytical, experimental and numerical ones in the literature.; We studied the motion of spheres sedimenting in a cylindrical tube filled with a Newtonian fluid. The hydrodynamic drag and lift on the particle are investigated under various conditions. The effects of the tube wall, in terms of the blockage ratio and the eccentricity ratio, on the particle terminal velocity, migration and rotation are studied. We also investigated the interaction between pair particles released in tandem or side by side at different Reynolds numbers.; The migration of particles in a pressure driven flow is the heart of vast number of industrial applications. Using 3-D direct numerical simulations, we systematically investigated the independent parameters controlling the particle migration, which are the blockage ratio, the flow Reynolds number, and the solid-liquid density ratio. During the particle migration, the mechanisms of the fluid inertia, the wall confinement, the local flow shear rate, the particle slip velocity, the particle size, and the particle rotation were extensively examined through the stress distribution on the particle surface under different flow conditions.; In the presence of a shear flow, an initially deposited bed of heavy particles will be entrained into the bulk fluid and convected away with the flow. We investigated the mechanism of this particle resuspension by using 2-D direct numerical simulations. Various effects on the lift force on the particle was analyzed by examining the distribution of the stress on the particle surface. We also studied the orientation of an elliptic particle during its resuspension, analyzed the interaction between a pair of particles, and presented the results of the resuspension of a layer of particles.; There are striking differences of particle motions in viscoelastic and Newtonian fluids. We explained the mechanism of the anomalous particle behavior due to the elasticity of the viscoelastic fluid. The effects of the Deborah number, the Reynolds number, the retardation-relaxation time ratio, the blockage ratio, and the eccentricity rate on the behavior of the particles were also systemically investigated.
机译:这项工作的主要主题是通过使用二维和三维直接数值模拟(DNS)来增强对牛顿或粘弹性流体流动中固体颗粒行为的理解。基于任意拉格朗日-欧拉(ALE)技术和弹性-粘性-应力-分裂(EVSS)方案,开发了大规模的最新软件包PARTMOVER3D。我们的数值结果与文献中的分析,实验和数值结果进行了广泛的比较。我们研究了在充满牛顿流体的圆柱管中球体沉降的运动。在各种条件下研究了颗粒上的流体动力阻力和升力。研究了管壁在堵塞率和偏心率方面对颗粒末端速度,迁移和旋转的影响。我们还研究了在不同雷诺数下串联或并排释放的成对颗粒之间的相互作用。颗粒在压力驱动流中的迁移是众多工业应用的核心。使用3-D直接数值模拟,我们系统地研究了控制颗粒迁移的独立参数,包括阻塞率,流雷诺数和固液密度比。在颗粒迁移过程中,通过不同流动条件下颗粒表面的应力分布,广泛研究了流体惯性,壁约束,局部流动剪切速率,颗粒滑移速度,颗粒大小和颗粒旋转的机制。 。;在存在剪切流的情况下,最初沉积的重颗粒床将被带入本体流体中,并与流对流。我们通过使用二维直接数值模拟研究了这种颗粒重悬浮的机理。通过检查颗粒表面应力的分布,分析了对颗粒上提升力的各种影响。我们还研究了椭圆颗粒在重悬期间的方向,分析了一对颗粒之间的相互作用,并给出了重悬颗粒层的结果。在粘弹性和牛顿流体中,粒子运动存在显着差异。我们解释了由于粘弹性流体的弹性导致的异常颗粒行为的机理。还系统地研究了Deborah数,雷诺数,延迟-松弛时间比,阻滞比和偏心率对颗粒行为的影响。

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