首页> 外文会议>AIChE annual meeting >An electrokinetic model for combined fouling during cross flow filtration of electrolyte solution and charged Colloids
【24h】

An electrokinetic model for combined fouling during cross flow filtration of electrolyte solution and charged Colloids

机译:电解质溶液和带电胶体错流过滤过程中复合污垢的电动模型

获取原文

摘要

Colloidal fouling, formation of a cake due to deposition of colloids on to a membrane, is commonlyencountered in pressure driven filtration processes, such as nanofiltration and reverse osmosis.The influence of these deposited charged colloids on the ion concentration polarization,ion rejection and the overall permeate flux is the focus of the present work. A common situationencountered during membrane filtration is the combined influence of charged colloids and the associatedelectrolyte on the flux decline and rejection. In this context, coupled model of concentrationpolarization (CP), cake layer formation by charged colloidal particles and ion transport through theinterstitial spaces of the cake layer has been developed to predict the permeate flux decline andobserved salt rejection during cross flow filtration of an electrolyte and colloidal mixture. The suspensionstructure of the cake layer is considered as a swarm of colloidal particles, represented usingthe Kuwabara cell model. For this system, the electroosmotic flow is calculated analytically usingthe Levine-Neale model. The analysis is then combined with the standard film theory of cross flowmembrane filtration to predict the flux decline, observed rejection, cake layer thickness and resistance,and osmotic pressure difference. The model illustrates the combined influence of electricaland physical properties of colloids and electrolytes, mass transfer coefficient or crossflow conditionand membrane resistance on the separation process. This approach provides a comprehensiveinsight into the mechanism of cake enhanced concentration polarization for charged colloids.
机译:胶体结垢是由于胶体沉积在膜上而形成的滤饼 在压力驱动的过滤过程(例如纳滤和反渗透)中会遇到。 这些沉积的带电胶体对离子浓度极化的影响, 离子排斥和总的渗透通量是当前工作的重点。常见情况 膜过滤过程中遇到的是带电胶体和相关胶体的综合影响 电解液对通量的下降和抑制。在这种情况下,集中度耦合模型 极化(CP),带电胶体颗粒形成滤饼层以及离子通过 滤饼层的间隙空间已被开发出来,以预测渗透通量的下降和 在电解质和胶体混合物的错流过滤过程中观察到了脱盐现象。悬架 滤饼层的结构被认为是一大堆胶体颗粒,用 Kuwabara细胞模型。对于该系统,使用以下方法解析地计算电渗流 Levine-Neale模型。然后将分析与标准膜理论相结合 膜过滤以预测通量下降,观察到的截留率,滤饼层厚度和电阻, 和渗透压差。该模型说明了电气的综合影响 和电解质的物理性质,传质系数或错流条件 和膜电阻对分离过程的影响。这种方法提供了全面的 深入了解蛋糕提高带电胶体浓度极化的机理。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号