工业水处理 ›› 2006, Vol. 26 ›› Issue (1): 55-58. doi: 10.11894/1005-829x.2006年.26(01).55

• 试验研究 • 上一篇    下一篇

聚偏氟乙烯膜生物反应器处理城市污水的膜污染分析

伍海辉1, 高乃云1, 万金保2   

  1. 1. 同济大学环境科学与工程学院, 上海 200092;
    2. 南昌大学环境与科学工程学院, 江西, 南昌 330029
  • 收稿日期:2005-04-07 出版日期:2006-01-20 发布日期:2010-10-01
  • 作者简介:伍海辉(1978- ),2000 年毕业于南昌大学,博士研究 生,E-mail: whh_2003@eyou.com。

Membrane fouling analysis of the polyvinylidene difluoride membrane bioreactor treating the sewage

Wu Haihui1, Gao Naiyun1, Wan Jinbao2   

  1. 1. Environmental Science and Engineering College, Tongji University, Shanghai 200092, China;
    2. Environmental Science and Engineering College, Nanchang University, Nanchang 330029, China
  • Received:2005-04-07 Online:2006-01-20 Published:2010-10-01

摘要:

膜污染是制约膜生物反应器应用的关键因素,通过实验分析了聚偏氟乙烯膜生物反应器运行操作压力的变化。膜通量为10L/(h.m2)时,操作压力在3.73×104Pa以下,比较了降低膜污染的不同方法:水力清洗能恢复操作压力77%;倾斜50°放置,压力增长缓慢;膜组件离容器底部最佳位置为20cm。计算了膜总阻力的组成。

关键词: 膜生物反应器, 聚偏氟乙烯, 膜污染, 膜位置

Abstract:

Membrane fouling is the key factor of restricting the application of membrane bioreactor (MBR). Running pressure was paid attention on. When the membrane flux is 10 L/(h·m2), the running pressure is lower than 3.73×104 Pa, compared with the different reducing membrane fouling measures: water washing could resume 70% pressure, the running pressure ascended slower when the membrane is inclination at 50 degree, and the best position is 20 cm on the base of the container. In the end, analysis and calculation of the composition of total membrane resistance are given.

Key words: membrane bioreactor, polyvinylidene difluoride, membrane fouling, position of membrane

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