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Computational fluid dynamics modelling of flow and permeation for pressure-driven membrane processes

机译:压力驱动膜工艺流动和渗透的计算流体动力学建模

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While models of membrane systems with varying degrees of complexity have been developed since the early 1960s, reports of the use of computational fluid dynamics to provide in-depth insights into the separation phenomenon have only recently appeared in the literature. This paper describes the validation and application of a computational fluid dynamics model of pressure-driven membrane processes involving selective removal of components in the feed channel and their transfer to the permeate channel. The effects of changes in rejection, wall permeation rates and solution properties on velocity and concentration profiles are presented for empty channels and channels with eddy promoters. For high polarisation applications typically encountered in conventional ultrafiltration applications, the results demonstrate the need for very fine meshes near the membrane wall, together with high order numerical schemes and accurate modelling of rejection and physical property variations in order to obtain accurate and reliable predictions of the polarisation and flow phenomenon.
机译:虽然有不同程度的复杂的膜系统的模型已经从60年代初期开发,利用计算流体动力学的报告,提供深入分析上市公司分离现象直到最近才在文献中出现。本文描述了涉及供给通道选择性去除组件和它们转移到渗透通道压力驱动的膜过程的计算流体动力学模型的验证和应用。上的速度和浓度分布在排斥变化,壁的渗透速率和溶液性质的效果呈现为空信道和信道与涡启动子。对于典型地在常规的超滤应用中遇到的高极化的应用,其结果与高阶数值格式和排斥反应和物理性质的变化的精确建模表明需要靠近膜壁非常细的网格,一起以获得的精确和可靠的预测极化和流动现象。

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