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首页> 外文期刊>International Journal of Heat and Mass Transfer >A comparative study of permeable and semipermeable membranes constructed multiple layer water filters by non-dimensional lattice Boltzmann simulations
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A comparative study of permeable and semipermeable membranes constructed multiple layer water filters by non-dimensional lattice Boltzmann simulations

机译:基于无量纲格子玻尔兹曼模拟的渗透膜和半渗透膜构造多层滤水器的比较研究

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HighlightsFluid flow and mass transfer in multiple layer filters are modeled and simulated.Two types of permeable and semipermeable membranes have been compared.Streamlines and isoconcentrations in fluid and solid phases are shown.Effects of porosities, Schmidt, Sherwood, and Reynolds numbers are illustrated.AbstractA Non-Dimensional Lattice Boltzmann Method (NDLBM) based on a multiple zone porous medium model is extended to simulate fluid flow and mass transfer inside multiple layer water filters. Comparative studies based on two basic design models (permeable and semipermeable membrane model) are carried out to investigate the flow and mass transport inside cylindrical multiple layer water filters. In the permeable membrane design model, the water is purified by passing multiple units with sandwich like structures. In the semipermeable membrane model, macromolecules such as suspended particulates cannot pass the semipermeable membranes, while micromolecules can pass the porous semipermeable membranes. The quasi-steady state velocity distributions are obtained. The transient concentrations of suspended particulates captured by porous solid structures and left in water are compared for the two design models. Different dimensionless governing parameters and the porosities for the membranes are studied to understand the underlying mechanism of the purification procedure and to compare performance of the two models.
机译: 突出显示 对多层过滤器中的流体流动和传质进行建模和仿真。 已比较了两种类型的渗透膜和半渗透膜。 显示了液相和固相的流线和等浓度。 孔隙率,施密特(Schmidt),舍伍德(Sherwood)和雷诺数的影响均无效 摘要 < ce:simple-para id =“ sp010” view =“ all”>基于多区域多孔介质模型的无量纲格子玻尔兹曼方法(NDLBM)得以扩展,以模拟多层滤水器内部的流体流动和传质。基于两个基本设计模型(渗透膜和半渗透膜模型)进行了比较研究,以研究圆柱形多层滤水器内部的流量和质量传输。在渗透膜设计模型中,通过使具有三明治状结构的多个单元通过来净化水。在半透膜模型中,大分子(如悬浮颗粒)不能通过半透膜,而小分子可以通过多孔半透膜。得到准稳态速度分布。比较了两种设计模型中被多孔固体结构捕获并留在水中的悬浮颗粒的瞬态浓度。研究了不同的无量纲控制参数和膜的孔隙率,以了解纯化程序的基本机理并比较两种模型的性能。

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