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Phase-field modeling of mixing/demixing of regular binary mixtures with a composition-dependent viscosity

机译:具有粘度依赖性的常规二元混合物混合/脱脂的相场建模

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摘要

We simulate the mixing (demixing) process of a quiescent binary liquid mixture with a composition-dependent viscosity which is instantaneously brought from the two-phase (one-phase) to the one-phase (two-phase) region of its phase diagram. Our theoretical approach follows a standard diffuse-interface model of partially miscible regular binary mixtures wherein convection and diffusion are coupled via a nonequilibrium capillary force, expressing the tendency of the phase-separating system to minimize its free energy. Based on 2D simulation results, we discuss the influence of viscosity ratio on basic statistics of the mixing (segregation) process triggered by a rapid heating (quench), assuming that the ratio of capillary to viscous forces (a.k.a. the fluidity coefficient) is large. We show that, for a phase-separating system, at a fixed value of the fluidity coefficient (with the continuous phase viscosity taken as a reference), the separation depth and the characteristic length of single-phase microdomains decrease monotonically for increasing values of the viscosity of the dispersed phase. This variation, however, is quite small, in agreement with experimental results. On the other hand, as one might expect, at a fixed viscosity of the dispersed phase both of the above statistics increase monotonically as the viscosity of the continuous phase decreases. Finally, we show that for a mixing system the attainment of a single-phase equilibrium state by coalescence and diffusion is retarded by an increase in the viscosity ratio at a fixed fluidity for the dispersed phase. In fact, for large enough values of the viscosity ratio, a thin film of the continuous phase becomes apparent when two drops of the minority phase approach each other, which further retards coalescence.
机译:我们模拟了具有静态粘度的静态二元液体混合物的混合(脱胶)过程,其粘度随成分的变化而立即从其相图的两相(一相)区域变为一相(两相)区域。我们的理论方法遵循部分可混溶规则二元混合物的标准扩散界面模型,其中对流和扩散通过非平衡毛细管力耦合,表达了相分离系统将其自由能最小化的趋势。基于2D模拟结果,我们假设毛细管​​与粘性力之比(又称为流动系数)大时,我们讨论了粘度比对由快速加热(淬火)触发的混合(偏析)过程基本统计的影响。我们表明,对于一个相分离系统,在固定的流动性系数值(以连续相粘度为参考)下,单相微区的分离深度和特征长度随该值的增加而单调减小。分散相的粘度。然而,这种变化很小,与实验结果一致。另一方面,正如人们所预期的,在固定相的分散相下,上述两种统计量都随着连续相的粘度降低而单调增加。最后,我们表明对于混合系统,由于分散相在固定流动性下的粘度比增加,通过聚结和扩散达到的单相平衡态受到阻碍。实际上,对于足够大的粘度比值,当两滴少数相彼此接近时,连续相的薄膜变得明显,这进一步阻碍了聚结。

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  • 来源
    《Journal of Applied Physics 》 |2017年第13期| 134302.1-134302.8| 共8页
  • 作者

    A. Lamorgese; R. Mauri;

  • 作者单位

    DICI, Laboratory of Multiphase Reactive Flows, University of Pisa, Largo Lazzarino 1,56122 Pisa, Italy;

    DICI, Laboratory of Multiphase Reactive Flows, University of Pisa, Largo Lazzarino 1,56122 Pisa, Italy;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
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