大连理工大学  登录  English 
杨凤林
点赞:

教授   博士生导师   硕士生导师

性别: 男

毕业院校: 大连工学院

学位: 硕士

所在单位: 环境学院

电子邮箱: yangfl@dlut.edu.cn

手机版

访问量:

开通时间: ..

最后更新时间: ..

当前位置: 中文主页 >> 科学研究 >> 论文成果
Rotating a helical membrane for turbulence enhancement and fouling reduction

点击次数:

论文类型: 期刊论文

发表时间: 2012-02-01

发表刊物: CHEMICAL ENGINEERING JOURNAL

收录刊物: SCIE、EI

卷号: 181

页面范围: 486-493

ISSN号: 1385-8947

关键字: Rotating helical membrane; Turbulence enhancement; Membrane fouling

摘要: To reduce fouling, enhance turbulence and permeate flux in membrane filtrations, similar to the rotating disk membrane modules, in this paper, a new helical membrane was rotated and its features in filtrating different particle suspensions such as yeast, kaolin and CaCO3 in a cylindrical container were studied. About 27% enhancement of stable flux can be maintained by rotating a 360 degrees helical membrane, comparing with rotating a same sized flat membrane, at a rotating speed of 160 rpm. The flux enhancement and fouling reduction were affected by the helical angles (best at 360 degrees) of the membrane module, the enhancement in turbulence intensity and the hydraulic flow regime and dimensions, such as the ratio of the membrane width to the diameter of the separation unit. The stable permeate flux of rotating a 360 degrees helical membrane were higher than that of rotating a flat membrane both at 5.3 kPa or 6.5 kPa, a higher flux enhancement at 6.5 kPa was observed. The order of membrane fouling was yeast > kaolin > nano-CaCO3 when the particles concentrations were all at 5.0 g l(-1). Fouling is less severe when the diameter of separation units is smaller, and vice versa. Rotating a helical membrane is specifically useful for stirring separations without aeration. (C) 2011 Elsevier B.V. All rights reserved.

辽ICP备05001357号 地址:中国·辽宁省大连市甘井子区凌工路2号 邮编:116024
版权所有:大连理工大学