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Visualisation and analysis of polyethylene coextrusion melt flow

机译:聚乙烯共挤熔体流动的可视化和分析

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摘要

Polymer melts experience complex, time variant, stress and deformation fields on their passage through fixed geometries in many conversion operations. Flow complexity is further increased in operations involving the co-joining of two or more melt streams where one confining boundary is moving and viscoelastic. Such a complex situation arises in coextrusion processes. This work covers experimental studies on polyethylene melt flows in complex coextrusion geometries with a view to understanding the stress fields involved and their effects on flow stability. A 30°1coextrusion geometry is studied using two extrusion arrangements. In one arrangement a single extruder is used to feed a 'bifurcated' die design wherein the melt stream is split prior to, and rejoined after, a divider plate in the die. In the other design melt streams are delivered to, and converged at 30°, using two independent extruders. In a second die melt streams are brought together at 90°. In each die arrangement melt flow in the confluent region and die land to the die exit was observed through side windows of a visualisation cell. Velocity ratios of the two melt streams were varied and layer thickness ratios producing instability are determined for each melt for a variety of flow conditions. Stress and velocity fields in the coextrusion arrangements were quantified using stress birefringence and particle image velocimetry techniques. The study demonstrates conclusively that wave type interfacial instability occurred in the coextrusion geometries when the same low density polyethylene melt is used in each stream. This observation occurred at specific, repeatable, stream layer ratios in each die arrangement. The complex flows were numerical modelled using a modified Leonov model and Flow 2000P software. There was reasonable agreement between modelled at experimentally determined stress fields. Modelling however provided far more detailed stress gradient information than could be resolved from the optical techniques. A total normal stress difference (TNSD) sign criterion was used to predict the critical layer ratio for the onset of the interfacial instability in one die arrangement and good agreement between theory and experiment has been obtained. The study conclusively demonstrates wave type interfacial instability in the coextrusion process is not caused by process perturbations potentially introduced by extruder screw rotation but is associated with process-history dependant differences in melt elasticity. © 2009 American Institute of Physics.
机译:在许多转换操作中,聚合物熔体通过固定的几何形状时会经历复杂的,时变的,应力和变形场。在涉及两个或两个以上熔体流的合并操作的情况下,流程的复杂性进一步增加,其中一个限制边界正在移动并且是粘弹性的。这样的复杂情况在共挤出过程中出现。这项工作涵盖了对复杂共挤几何形状的聚乙烯熔体流动的实验研究,旨在了解所涉及的应力场及其对流动稳定性的影响。使用两个挤压装置研究了30°1共挤压几何形状。在一种布置中,使用单个挤出机进料“分叉”的模具设计,其中熔体流在模具中的分隔板之前分开,然后在模具中重新接合。在另一种设计中,使用两个独立的挤出机将熔体流输送至30°并会聚。在第二模具中,将熔体流以90°聚集在一起。在每个模具布置中,通过可视化单元的侧窗观察熔体在汇合区域中的流动以及模具到达模具出口的状态。改变两种熔体流的速度比,并确定在各种流动条件下每种熔体产生不稳定性的层厚比。使用应力双折射和颗粒图像测速技术对共挤出装置中的应力和速度场进行了量化。该研究结论性地表明,当在每个流中使用相同的低密度聚乙烯熔体时,在共挤出几何形状中会发生波型界面不稳定性。该观察在每个模具布置中以特定的,可重复的流层比率发生。使用改良的Leonov模型和Flow 2000P软件对复杂的流进行数值建模。在通过实验确定的应力场进行建模之间存在合理的一致性。然而,建模提供的应力梯度信息比光学技术所能解决的更为详细。使用总法向应力差(TNSD)符号准则来预测在一个模具布置中界面不稳定性发生的临界层比率,并且在理论和实验之间取得了良好的一致性。该研究结论性地表明,共挤出过程中的波型界面不稳定性不是由挤出机螺杆旋转可能引起的过程扰动引起的,而是与取决于过程历史的熔体弹性差异有关。 ©2009美国物理研究所。

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