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Etude rheologique des composites charges de fibres de verre courtes (French text).

机译:短玻璃纤维复合填料的流变学研究(法文)。

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The rheological behavior of short-fiber polypropylene has been studied in shear flow. Because of some restrictions in the measurement and the complex behavior of the matrix, we chose to use model fiber suspensions in two different types of matrix, a Newtonian polybutene and a Boger fluid. The steady-state viscosity of the Newtonian polybutene increased by adding fibers and the behavior of the fiber suspensions essentially remained Newtonian. The Boger fluid was obtained by adding a high molecular weight polyisobutylene to the Newtonian polybutene.; The transient behavior of all types of fiber suspensions (with the viscoelastic, the Newtonian and the Boger fluid matrices) in shear flow has been investigated.; Following a first deformation, the sample has been sheared in the reverse direction and a viscosity overshoot called the "reverse overshoot" was measured at a larger strain in comparison with the primary viscosity overshoot. The reverse overshoot has been attributed to tumbling of fibers that are not totally aligned with the flow direction even after a very long time. When the flow was reversed, the normal stress difference took initially minimum values and depicted a smaller positive overshoot before reaching the steady-state plateau.; Two models have been used to simulate the rheological behavior of fiber suspensions. The first model is based on the Folgar and Tucker equation for fiber motion and Lipscomb constitutive equation. This model describes qualitatively well the transient behavior of fiber suspensions in both forward and reverse direction flows. However, the fiber motions predicted by the model are faster than deducted from the experiments. This was tentatively explained by non-affined deformation and direct contacts with neighboring fibers, reducing fiber rotation.; The second model investigated was the extended Jeffery model developed by Grmela et al. (2003) who generalized the Jeffery model, to include fiber-fiber interactions via angular momentum and effective inertia of fibers. With a correct choice for the free energy, the model can describe, in principle, the rheological behavior of fiber suspensions. (Abstract shortened by UMI.)
机译:在剪切流中已经研究了短纤维聚丙烯的流变行为。由于测量的限制和基质的复杂行为,我们选择在两种不同类型的基质(牛顿聚丁烯和Boger流体)中使用模型纤维悬浮液。牛顿聚丁烯的稳态粘度通过添加纤维而增加,并且纤维悬浮液的行为基本上保持牛顿性。博格流体是通过向牛顿聚丁烯中添加高分子量聚异丁烯而获得的。研究了所有类型的纤维悬浮液(粘弹性,牛顿和Boger流体矩阵)在剪切流中的瞬态行为。第一次变形后,样品已沿反方向剪切,与初始粘度超调相比,在更大的应变下测量了称为“反向超调”的粘度超调。反向过冲归因于即使经过很长时间仍未完全与流动方向对齐的纤维翻滚。当流动反向时,法向应力差最初取最小值,并在达到稳态平台之前表现出较小的正过冲。已经使用两个模型来模拟纤维悬浮液的流变行为。第一个模型基于纤维运动的Folgar和Tucker方程以及Lipscomb本构方程。该模型定性地很好地描述了纤维悬浮液在正向和反向流动中的瞬态行为。但是,由模型预测的纤维运动比从实验中推断的运动要快。初步解释是通过非固定变形和与相邻纤维的直接接触,减少了纤维的旋转。研究的第二个模型是Grmela等人开发的扩展Jeffery模型。 (2003年)推广了Jeffery模型,以包括通过角动量和纤维的有效惯性进行的纤维-纤维相互作用。通过正确选择自由能,该模型原则上可以描述纤维悬浮液的流变行为。 (摘要由UMI缩短。)

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