首页> 外文会议>International Conference on Computational Methods and Experimental Measurements(CMEM XII); 2005; Malta(MT) >Modelling of a LPM filling process with special consideration of viscosity characteristics and its influence on the microstructure of a non-crimp fabric fiber bed
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Modelling of a LPM filling process with special consideration of viscosity characteristics and its influence on the microstructure of a non-crimp fabric fiber bed

机译:LPM填充过程的建模,特别考虑了粘度特性及其对非卷曲织物纤维床微观结构的影响

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Recently, in RTM process techniques, in-situ polymerizing thermoplastics are a promising alternative for conventional thermoset matrix systems. The advantages of these systems are given by a low initial injection viscosity in combination with a polymerization process during injection. This means that a fast mold filling is possible even for high fiber volume fractions. Additionally, the process steps of injection and curing are combined to one single step, which leads to a significant reduction in cycle time. From these advantages several problems arise for the simulation of a filling process, which is mainly based on Darcy's Law. The low initial viscosity causes high and inertia affected fluid velocities, violating the Darcy's Law restriction of a sufficient slow flow. With proceeding polymerization the viscosity characteristic is changing from an initial Newtonian to a visco-elastic flow behavior. The shear rate dependency of the fluid is additionally violating the restriction of a constant viscosity. The intention of this paper is to investigate high velocity and therefore inertia affected fluid flow in a non-crimp fabric fiber bed. Several fluids have been characterized by their rehological behavior. Based on these characterizations, flow experiments were executed to investigate the deviations between Darcy flow and fluid flow, which does not fulfill the restrictions. Additionally, the influence of visco-elastic fluid characteristic on the fiber bed microstructure was analyzed.
机译:最近,在RTM工艺技术中,原位聚合热塑性塑料是常规热固性基体系统的有希望的替代方法。这些系统的优势是由于低的初始注入粘度以及注入过程中的聚合过程而产生的。这意味着即使纤维体积分数较高,也可以快速填充模具。另外,将注射和固化的工艺步骤组合为一个步骤,从而大大缩短了循环时间。由于这些优点,主要基于达西定律的填充过程模拟出现了一些问题。低的初始粘度会导致较高的流体速度和受惯性影响的流体速度,这违反了达西定律对充分缓慢流动的限制。随着聚合的进行,粘度特性从最初的牛顿流变为粘弹性流动行为。流体的剪切速率依赖性还违反了恒定粘度的限制。本文的目的是研究非卷曲织物纤维床中的高速流动并因此影响惯性影响的流体流动。几种流体的流变行为已被表征。基于这些特征,进行了流动实验以研究达西流和流体流之间的偏差,这没有满足限制条件。另外,分析了粘弹性流体特性对纤维床微观结构的影响。

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