多孔支撑层在正向渗透膜中的作用:计算流体动力学模拟

Ahmed M. Alshwairekh, Abdullah A. Alghafis, M. Usta, Anas M. Alwatban, Robert Krysko, A. Oztekin
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引用次数: 5

摘要

采用计算流体力学(CFD)模拟研究了正向渗透(FO)模块内螺旋缠绕膜(SWM)内的输运现象。考察了多孔层对膜性能的影响。通过使多孔层面向绘制通道,模拟了三种不同的多孔层厚度,这种模式称为AL-FS(主动层面向馈电溶液)。本研究考虑的雷诺数范围为2 ~ 500。利用Navier-Stokes方程和质量输运方程得到了流道内的速度场、压力场和浓度场。用局部渗透压和膜的性质来计算膜表面的渗透率。该膜被认为是零厚度的半透功能表面。通量模型中考虑了多孔层的影响,但未解析多孔层内的流动场和浓度场。结果表明,随着流速的增加,膜两侧的外浓度极化水平降低,从而导致通过膜的水通量增加。同时,多孔层的存在降低了膜的性能。在相同的孔隙层厚度下,随着流速的增加,水通量没有明显的提高。膜上的吸力速度在抽吸通道入口处开始处于一个较高的值,直到到达抽吸通道出口时,由于进料溶液入口的影响,膜上的吸力速度开始略有增加。随着净渗透压差的增大,水通量呈非线性增长。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
The Effect of Porous Support Layer in Forward Osmosis Membranes: A Computational Fluid Dynamics Simulation
Computational fluid dynamics (CFD) simulations are conducted to study the transport phenomena in spiral wound membranes (SWM) within a Forward Osmosis (FO) module. The effect of the porous layer on the membrane performance is examined. Simulations are prepared for three different porous layer thicknesses by having the porous layer facing the draw channel, a mode known as AL-FS (active layer facing feed solution). In the current study, a Reynolds number range from 2 to 500 is considered. The Navier-Stokes and the mass transport equations are used to obtain the velocity, pressure and concentration fields in the flow channels. The local osmotic pressure and the membrane properties are used to calculate the water permeation over the membrane surface. The membrane is considered as a semipermeable functional surface of zero thickness. The effect of the porous layer is included in the flux model, but the flow and concentration fields in the porous layer are not resolved. The results suggest that increasing the streamwise velocity decreases the level of the external concentration polarization on both sides of the membrane which in turn leads to higher water flux through the membrane. Also, the existence of the porous layer reduced the membrane performance. The water flux didn’t improve much with increasing streamwise velocity at the same porous layer thickness. The suction velocity over the membrane starts at a high value at the inlet of the draw channel and decreases until reaching the outlet of the draw channel then it starts to increase slightly from the effect of the inlet of feed solution. Moreover, by increasing the net osmotic pressure difference, the water flux exhibited a non-linear increase.
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