The Numerical Prediction of Flow of Branched Polymer Melts Through Planar Contraction Channel by Finite Element Method

H. Khalaf
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Abstract

In this work we present an investigation of a complex viscoelastic flow through an abrupt expansion with expansion ratio D/d = 4, where the Oldroyd-B model was consider as a constitutive equation. The governing equations are solved using the Finite Element Method. The polymer is modeled as a monodisperse suspension of “Oldroyd-B” molecules, which provides a direct link the molecular topology and the flow properties of the melt. The branching produces an enhancement in the size of upstream vortex in creeping flows. Also was found that including inertia forces will give the intensity of lip vortex increases, while the size of corner vortex will initially decreased with growth of Weissenberg number but with more increase (We>4), the size of corner vortex will begin to increase in size.  The effect arises from the differing responses in shear and extensional flows of polymer melts.
支化聚合物熔体通过平面收缩通道流动的有限元数值预测
在这项工作中,我们提出了通过膨胀比D/ D = 4的复杂粘弹性流动的研究,其中Oldroyd-B模型被认为是一个本构方程。采用有限元法求解控制方程。该聚合物被建模为“Oldroyd-B”分子的单分散悬浮液,这为分子拓扑结构和熔体的流动特性提供了直接联系。在蠕变流中,分支的存在使上游涡的大小增大。同时发现,加入惯性力会使唇涡强度增大,而转角涡的大小会随着Weissenberg数的增加而开始减小,但随着Weissenberg数的增加(We>4),转角涡的大小开始增大。这种效应是由聚合物熔体在剪切和拉伸流动中的不同响应引起的。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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