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First instability of the flow of shear-thinning and shear-thickening fluids past a circular cylinder

机译:剪切稀化和剪切稠化流体通过圆柱体的流动的第一不稳定

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摘要

The first bifurcation and the instability mechanisms of shear-thinning and shear-thickening fluids flowing past a circular cylinder are studied using linear theory and numerical simulations. Structural sensitivity analysis based on the idea of a wavemaker is performed to identify the core of the instability. The shear-dependent viscosity is modelled by the Carreau model where the rheological parameters, i.e. the power-index and the material time constant, are chosen in the range 0. 4≤ n≤ 1. 75 and 0. 1≤ λ ≤ 100. We show how shear-thinning/shear-thickening effects destabilize/stabilize the flow dramatically when scaling the problem with the reference zero-shear-rate viscosity. These variations are explained by modifications of the steady base flow due to the shear-dependent viscosity; the instability mechanisms are only slightly changed. The characteristics of the base flow, drag coefficient and size of recirculation bubble are presented to assess shear-thinning effects. We demonstrate that at critical conditions the local Reynolds number in the core of the instability is around 50 as for Newtonian fluids. The perturbation kinetic energy budget is also considered to examine the physical mechanism of the instability.
机译:利用线性理论和数值模拟研究了流过圆柱的剪切稀化和剪切稠化流体的第一次分叉和失稳机理。进行了基于造波器思想的结构敏感性分析,以识别不稳定的核心。剪切依赖性粘度由Carreau模型建模,流变参数(即功率指数和材料时间常数)在0.4≤n≤1. 75和0.1≤λ≤100的范围内选择。我们展示了当使用参考零剪切速率粘度解决问题时,剪切稀化/剪切增稠效果如何显着破坏流量/稳定流量。这些变化是由于剪切相关粘度对稳定基流的影响而解释的。不稳定机制只是略有变化。介绍了基本流量,阻力系数和再循环气泡大小的特征,以评估剪切变稀效应。我们证明,在临界条件下,不稳定性核心的局部雷诺数与牛顿流体一样约为50。扰动动能收支也被认为是检查不稳定性的物理机制。

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