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Instability of Newtonian and non-Newtonian free shear flows.

机译:牛顿和非牛顿自由剪切流的不稳定性。

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The effects of viscoelasticity on the stability of the two-dimensional mixing layer are examined through linear stability analysis and direct numerical simulations using four rheological models to describe the polymer.; The linear stability analysis of the inviscid flow described by the Oldroyd-B model shows that in the special limit of a fluid with a relaxation time comparable in magnitude to viscous diffusion time, the effect of increasing viscoelasticity is to reduce the instability of the flow resulting in smaller growth rates and a narrower spectrum of unstable wavenumbers. On the other hand, the effects of viscoelasticity on the viscous modes are model dependent and in general remain weak for moderate Reynolds number, Re, and Weissenberg number, We.; Direct numerical simulations of the temporally evolving mixing layer have been performed using a spectral method based on the Hartley transform. The code has been validated by reproducing the main structures of roll-up and pairing of the Newtonian fluid. Using the FENE-P model, simulations of the roll-up and pairing of the viscoelastic fluid have been conducted for various values of the Reynolds number, and sufficiently high Weissenberg numbers. These simulations did not show important changes in the roll-up and pairing times or in the global structure of the vortex. They have however, revealed that viscoelasticity tends to produce an intensification of vorticity in some regions of the flow namely the braids and that this intensification is spatially correlated with regions of build-up of the first normal stress difference. In agreement with previous experimental studies of the viscoelastic mixing layer, we observed a trend for smaller values of the minimal (negative) vorticity as well as the tendency for the vortex structures to be more compact and to have longer life times than in the Newtonian case.; The examination of the evolution of the first normal stresses revealed that the stresses are initially entrained by the roll-up of the flow and then reach a steady state characterized by the absence of any extensional forces and a balance between shearing forces and the polymer relaxation stresses.
机译:通过线性稳定性分析和使用四个流变模型描述聚合物的直接数值模拟,研究了粘弹性对二维混合层稳定性的影响。由Oldroyd-B模型描述的无粘性流的线性稳定性分析表明,在流体的特殊极限中,弛豫时间的大小可与粘性扩散时间相媲美,增加粘弹性的作用是减少流动的不稳定性较小的增长率和较窄的不稳定波数频谱。另一方面,粘弹性对粘滞模态的影响取决于模型,通常对于中等的雷诺数Re和魏森伯格数We仍然很弱。已经使用基于Hartley变换的频谱方法对时间演化混合层进行了直接数值模拟。该代码已通过再现牛顿流体的卷起和配对的主要结构进行了验证。使用FENE-P模型,对各种雷诺数值和足够高的魏森伯格数进行了粘弹性流体的卷起和配对模拟。这些模拟并未显示出累积时间,配对时间或漩涡整体结构的重要变化。然而,他们发现,粘弹性倾向于在流体的某些区域即辫子上产生涡度的增强,并且这种增强在空间上与第一法向应力差的累积区域相关。与以前对粘弹性混合层的实验研究相一致,我们观察到最小(负)涡旋值较小的趋势,以及与牛顿情况相比,涡旋结构更紧凑,寿命更长的趋势。 。;对第一个法向应力的演变的检查表明,应力最初是由流体的卷起夹带的,然后达到一种稳定状态,其特征在于没有任何拉伸力以及剪切力和聚合物松弛应力之间的平衡。

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