化工进展

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旋转流三管微滤膜强化分离过程

杨宗伟,王志斌,邢晓林,申 静,高朝祥,周 文   

  1. 四川化工职业技术学院
  • 出版日期:2010-06-05 发布日期:2010-06-05

Enhanced separation process of 3-tube microfiltration membrane
with rotating flow

YANG Zongwei,WANG Zhibin,XING Xiaolin,SHEN Jing,GAO Zhaoxiang,ZHOU Wen   

  1. Sichuan Chemical Vocational and Technical College
  • Online:2010-06-05 Published:2010-06-05

摘要: 利用聚乙烯三管微滤膜在不同浓度、不同操作压力下,分别以切向进料和径向错流进料进行了分离实验对比研究,结果表明:在浓度为0.25%时三管膜切向进料具有通量大、能耗低的特征;切向进料的渗透通量是径向错流进料的2倍,且在浓度为0.5%时切向进料有一最佳操作压力,为深入研究多管膜过滤提供了依据。

Abstract: Separation process was investigated with 3-tube polyethylene microfiltration membrane based on the difference in concentration,operation pressure and inlet arrangement. Results indicated that the 3-tube membrane showed characteristics of higher permeation flux and less energy consumption when the concentration was 0.25%. The permeation flux with tangential inlet was 2 times of that with radial inlet. An optimum operation pressure was observed for the rotating flow of tangential inlet when the concentration was 0.5%.

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