首页> 外文会议>ASME Fluids Engineering Division Meeting >SIMULATION OF FORWARD OSMOSIS FLOW IN A TWO-DIMENSIONAL ASYMMETRIC MEMBRANE CHANNEL WITH DRAW CHANNEL CIRCULAR BAFFLE IMPLEMENTATION
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SIMULATION OF FORWARD OSMOSIS FLOW IN A TWO-DIMENSIONAL ASYMMETRIC MEMBRANE CHANNEL WITH DRAW CHANNEL CIRCULAR BAFFLE IMPLEMENTATION

机译:三维非对称膜通道前渗透流的模拟与拉伸通道圆形挡板实现

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Forward Osmosis (FO) driven asymmetric membrane filtration is a developing technology which shows promise for seawater desalination and wastewater treatment. Due to the fact that asymmetric membranes are widely used in conjunction with this technology, internal concentration polarization (ICP), a flow-entrainment effect occurring within such membranes, is a significant if not dominant source of overall osmotic pressure loss across the membrane. Accurate modeling of ICP effects is therefore very critical for accurate Computational Fluid Dynamic (CFD) modeling of asymmetric membranes. A related, dilutive effect known as external concentration polarization (ECP) also develops on both the rejection and draw sides of the membrane, further contributing to osmotic pressure loss. In order to increase the overall water flux, circular spacers can be implemented within the draw channel of FO cross-flow membrane exchange units to decrease the effects of ICP and draw ECP. The drawback of spacer inclusions is an increased pressure loss across the length of the feed channel. The system efficiency gained by the decrease in ECP must therefore be weighed against the energy cost of hydraulically making up lost channel pressure. To model the geometry of a FO cross-flow channel, the open source CFD package OpenFOAM is used. A compressible flow model with explicit boundary conditions is developed to simulate the flux transfer and ICP effects present within an asymmetric membrane when exposed to a NaCl solution. Results are validated by comparison with the numerical data generated by earlier models of asymmetric membranes implemented by other investigators using similar simulation conditions.
机译:前渗透(Fo)驱动的不对称膜过滤是一种显影技术,其显示海水淡化和废水处理的承诺。由于不对称膜广泛与该技术结合使用,内部浓度极化(ICP),在这种膜内发生的流动夹带效果是显着的,如果在膜上穿过膜上的整体渗透压损失的显着源。因此,ICP效果的精确建模对于不对称膜的准确计算流体动态(CFD)建模非常关键。称为外部浓度偏振(ECP)的相关的稀释效果也在膜的排斥和侧面上发育,进一步有助于渗透压力损失。为了增加整个水通量,圆形间隔物可以在横流膜交换单元的拉伸通道内实现,以降低ICP的效果并绘制ECP。间隔物夹杂物的缺点是进料通道长度的压力损失增加。因此,通过ECP降低获得的系统效率可以根据液压构成频道压力的能量成本来称量。为了模拟FO横流通道的几何形状,使用开源CFD封装OpenFoam。开发了一种具有明确边界条件的可压缩流模型,以模拟在暴露于NaCl溶液时显示在非对称膜内的磁通量传递和ICP效果。通过使用类似的模拟条件的其他研究人员实现的不对称膜的早期模型产生的数值数据来验证结果。

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