Chemical cleaning of reverse osmosis membranes used for treating wastewater from a rolling mill process

被引:24
|
作者
Jung, YJ
Kiso, Y [1 ]
Yamada, T
Shibata, T
Lee, TG
机构
[1] Toyohashi Univ Technol, Dept Ecol Engn, Toyohashi, Aichi 4418580, Japan
[2] Toyohashi Univ Technol, Dept Architecture & Civil Engn, Toyohashi, Aichi 4418580, Japan
[3] Nippon Steel Co, Energy Facil, Civil Engn & Marine Construct Div, Chiyoda Ku, Tokyo 1008071, Japan
[4] Keimyung Univ, Dept Environm Sci, Taegu 704701, South Korea
基金
日本学术振兴会;
关键词
reverse osmosis membrane; wastewater treatment; fouling; membrane cleaning; atomic force microscopy;
D O I
10.1016/j.desal.2005.08.009
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An analysis of fouling material and the effects of chemical cleaning were examined for a reverse osmosis (RO) membrane, which was used for the treatment of wastewater from a rolling mill process in the steel industry. The bulk foulant accumulated in the membrane module consisted mainly of CaSO(4)(.)2H(2)O, and the organic contaminants were contained at a very low level. The test pieces obtained from the exhausted RO membrane module (spiral-wound type) were used to examine chemical cleaning with the following solutions: acid and alkaline solutions with EDTA added, 50% methanol, and 10% ethyleneglycol monobutyrate (EGMB). Although a major component of the fouling material was calcium salt, the acid or alkaline solution containing EDTA did not promote the effective recovery of the water flux. On the other hand, cleaning with 50% methanol or 10% EGME solution increased the water flux significantly. The atomic force microscopy images of the membrane surface indicated that relatively large particles accumulated at the surface of the fouled membranes, and the large particles remained even after acid or alkaline cleaning. In the case of EGMB cleaning after alkaline cleaning, large particles did not remain, and uniform and fine particles were observed. The results that calcium salt, a major fouling material, was not removed effectively with the acid and alkaline solution may be due to trace organic materials in the fouling layer that act as a binder for inorganic fouling materials.
引用
收藏
页码:181 / 188
页数:8
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