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过程工程学报 ›› 2015, Vol. 15 ›› Issue (5): 881-891.DOI: 10.12034/j.issn.1009-606X.215160

• 综述 • 上一篇    下一篇

工业废水电渗析过程中膜污染研究进展

刘璐 赵志娟 李雅 石绍渊 吴新民 王丽英 李林1   

  1. 中国科学院过程工程研究所湿法冶金清洁生产技术国家工程实验室 中国科学院过程工程研究所湿法冶金清洁生产技术国家工程实验室 中国科学院过程工程研究所湿法冶金清洁生产技术国家工程实验室 中国科学院过程工程研究所 北京石油化工学院化学工程学院 鞍山钢铁集团公司 鞍山钢铁集团公司
  • 收稿日期:2015-03-13 修回日期:2015-07-27 出版日期:2015-10-20 发布日期:2015-10-20
  • 通讯作者: 刘璐

Research Progress in Fouling of Ion Exchange Membrane for Electrodialysis Desalination of Industrial Wastewater

LIU Lu ZHAO Zhi-juan LI Ya SHI SHAO-yuan WU Xin-min WANG Li-ying LI Lin   

  1. National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Institute of Process Engineering, Chinese Academy of Sciences National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Institute of Process Engineering, Chinese Academy of Sciences National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Institute of Process Engineering, Chinese Academy of Sciences Institute of Process Engineering, China Academy of Sciences Univ. CAS, Beijing 100049, China; 3. Sch. Chem. Eng., Beijing Institute of Petrochemical Technolog Anshan Iron and Steel Group Corporation Anshan Iron and Steel Group Corporation
  • Received:2015-03-13 Revised:2015-07-27 Online:2015-10-20 Published:2015-10-20
  • Contact: LIU Lu

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被引次数

2

摘要： 综述了工业废水电渗析体系膜污染类型、性质、影响因素等的研究进展. 无机污染主要是Ca2+, Mg2+或其他高价离子在离子膜表面或内部形成的结垢现象，原理是极化或溶液过饱和形成沉淀. 有机污染是由蛋白、腐植酸、表面活性剂及大分子有机物在离子膜表面沉积或渗透到膜内部而形成，原因主要是带负电荷的有机物与阴膜荷正电基团的静电作用及带苯环有机物与基膜的亲和作用，其次是有机物分子大小与膜的网络结构的作用. 膜污染形成及其性质与施加电流、共存组分、温度、pH值和运行时间等密切相关，可造成离子膜导电性、离子交换容量、水含量和极限电流密度等减小，且有机污染对电渗析性能的影响比无机污染更严重. 由有机物凝胶层形成的膜污染可用电渗析膜污染指数定量描述.

关键词: 工业废水, 电渗析, 离子交换膜, 污染

Abstract: The lasted research progresses related to types, properties, and influential factors of membrane fouling occurring in industrial wastewater desalination by electrodialysis are summarized. Inorganic fouling mainly results from the scaling of Ca2+, Mg2+ or other multivalent ions on the surface or inside of ion exchange membrane, in which the polarization or solution supersaturated precipitation leads to the membrane fouling. Organic fouling results from the deposition of proteins, humate, surfactant or other macromolecular organic matters on the surface or in inside of membrane. The main cause of anion membrane fouling by organic matters is related to the electrostatic interaction between negatively charged organic matters and anion exchange membrane with positively charged groups and the affinity interactions between the membrane matrix and aromatic compounds, and the membrane fouling is also related to the molecular size and network structure of organic compounds. The formation mechanisms and properties of membrane fouling are closely related to the applied electric current, coexisting components, temperature, pH value and running time, etc. The membrane fouling can result in the decrease of conductivity, ion exchange capacity, water content and limiting current density. Moreover, the effect of organic fouling on the electrodialysis performance is more obvious than that of inorganic fouling. The membrane fouling caused by the formation of organic compound gel layer can be quantitatively expressed by membrane fouling index for electrodialysis.

Key words: industrial wastewater, electrodialysis, ion exchange membrane, fouling

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