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Numerical study on the effect of rheological parameters on the droplet deformation process in Newtonian and non-Newtonian two-phase systems using extended finite element method

机译:利用延长有限元法研究流变参数对牛顿和非牛顿两相系统液滴变形过程的影响

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In the present study, attempts were made to study the effect of rheological parameters on the drop deformation process. For this purpose, both Newtonian and non-Newtonian (Carreau-Yasuda model) were considered and extended finite element method (XFEM) along with level-set method (LSM) were used to simulate the process. The result showed that in Newtonian-Newtonian systems, there was no shear stress overshoot (maximum) during the deformation process and the shear stress increased monotonically until it reached a steady-state, whereas, it exhibited an overshoot (maximum) for non-Newtonian systems. Results also showed that the increase of the wall confinement parameter (R/H) would increase the droplet deformation monotonically for studied viscosity ratios. It was further observed that the steady-state deformation parameter (Dss) was increased as Ca increased from 0.2 to 0.8 for viscosity ratio (λ) between 0.5 and 2.5.
机译:在本研究中,尝试研究流变参数对下落变形过程的影响。为此,考虑了牛顿和非牛顿模型(Carreau-Yasuda模型)和扩展有限元方法(XFEM)以及Level-Set方法(LSM)用于模拟该过程。结果表明,在牛顿 - 牛顿系统中,在变形过程中没有剪切应力过冲(最大值),并且剪切应力单调增加,直到它达到稳态,而它表现出非牛顿的过冲(最大值)系统。结果还表明,壁限制参数(R / H)的增加将单调地增加液滴变形,用于研究粘度比。进一步观察到,随着Ca从0.5至2.5之间的粘度比(λ)增加0.2至0.8,增加了稳态变形参数(DSS)。

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