Influence of feed concentration and transmembrane pressure on membrane fouling and effect of hydraulic flushing on the performance of ultrafiltration

被引:54
作者
Huang, Jinhui [1 ,2 ]
Liu, Liuxia [1 ,2 ]
Zeng, Guangming [1 ,2 ]
Li, Xue [3 ]
Peng, Lei [1 ,2 ]
Li, Fei [1 ,2 ]
Jiang, Yongbing [1 ,2 ]
Zhao, Yong [1 ,2 ]
Huang, Xiaolong [1 ,2 ]
机构
[1] Hunan Univ, Coll Environm Sci & Engn, Changsha 410082, Hunan, Peoples R China
[2] Hunan Univ, Minist Educ, Key Lab Environm Biol & Pollut Control, Changsha 410082, Hunan, Peoples R China
[3] Changsha Univ, Dept Bioengn & Environm Sci, Changsha 410003, Hunan, Peoples R China
基金
高等学校博士学科点专项科研基金; 中国国家自然科学基金;
关键词
Micellar-enhanced ultrafiltration; Membrane fouling; Sodium dodecyl sulfate; Hydraulic flushing; MICELLAR-ENHANCED ULTRAFILTRATION; HOLLOW-FIBER MEMBRANE; SODIUM DODECYL-SULFATE; WASTE-WATER; CADMIUM IONS; BACKFLUSHING CONDITIONS; NONIONIC SURFACTANT; CERAMIC MEMBRANES; AQUEOUS STREAMS; METHYLENE-BLUE;
D O I
10.1016/j.desal.2013.11.038
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Micellar-enhanced ultrafiltration (MEUF) is a promising technology developed for treating the wastewater containing metal ions or organic pollutants. One of the greatest problems in MEUF is membrane fouling which is mainly caused by concentration polarization, gel layer or cake formation caused by the deposition of surfactant micelles on the membrane surface and surfactant adsorption in the membrane interior. In this study, surfactant sodium dodecyl sulfate (SDS), which was used in membrane separation as colloidal particles, caused the flux decline. The transmembrane pressure (TMP) and feed concentration of SDS had significant influences on the flux. This paper presented that the lower TMP had a smaller effect on membrane fouling, and when SDS concentration was around the critical micelle concentration (CMC), lower permeate flux and higher additional membrane fouling resistance were obtained. The effects of three kinds of hydraulic flushing methods on membrane permeate flux were investigated, including periodic forward flushing, periodic backwashing and forward flushing followed by backwashing. It was found that when the periodic combined flushing interval was 10 min, forward flushing and backwashing phase times were 150 s and 90 s, respectively, and that combined flushing was more conductive to permeate flux recovery in this study. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:1 / 8
页数:8
相关论文
共 35 条
[31]   Removal of Cd2+ from synthetic wastewater using micellar-enhanced ultrafiltration with hollow fiber membrane [J].
Xu Ke ;
Zeng Guang-ming ;
Huang Jin-hui ;
Wu Jiao-yi ;
Fang Yao-yao ;
Huang Guohe ;
Li Hanbing ;
Xi Beidou ;
Liu Hongliang .
COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS, 2007, 294 (1-3) :140-146
[32]   Micellar enhanced ultrafiltration of phenol in synthetic wastewater using polysulfone spiral membrane [J].
Zeng, Guang-Ming ;
Xu, Ke ;
Huang, Jin-Hui ;
Li, Xue ;
Fang, Yao-Yao ;
Qu, Yun-Huan .
JOURNAL OF MEMBRANE SCIENCE, 2008, 310 (1-2) :149-160
[33]   Micellar-enhanced ultrafiltration of cadmium and methylene blue in synthetic wastewater using SDS [J].
Zeng, Guang-Ming ;
Li, Xue ;
Huang, Jin-Hui ;
Zhang, Chang ;
Zhou, Chun-Fei ;
Niu, Jing ;
Shi, Liang-Jing ;
He, Song-Bao ;
Li, Fei .
JOURNAL OF HAZARDOUS MATERIALS, 2011, 185 (2-3) :1304-1310
[34]   Chemical cleaning of fouled PVC membrane during ultrafiltration of algal-rich water [J].
Zhang, Yan ;
Tian, Jiayu ;
Liang, Heng ;
Nan, Jun ;
Chen, Zhonglin ;
Li, Guibai .
JOURNAL OF ENVIRONMENTAL SCIENCES, 2011, 23 (04) :529-536
[35]   Efficacy of relaxation, backflushing, chemical cleaning and clogging removal for an immersed hollow fibre membrane bioreactor [J].
Zsirai, T. ;
Buzatu, P. ;
Aerts, P. ;
Judd, S. .
WATER RESEARCH, 2012, 46 (14) :4499-4507