共 50 条
A novel membrane reactor for ozone water treatment
被引:60
|作者:
Heng, Samuel
Yeung, King Lun
Djafer, Malik
Schrotter, Jean-Christophe
机构:
[1] Hong Kong Univ Sci & Technol, Dept Chem Engn, Kowloon, Hong Kong, Peoples R China
[2] Hong Kong Univ Sci & Technol, Environm Engn Program, Kowloon, Hong Kong, Peoples R China
[3] Veolia Water Asia 22F, Hong Kong, Hong Kong, Peoples R China
[4] Water Res Ctr Veolia, Anjou Rech, F-78603 Maisons Laffitte, France
关键词:
membrane reactor;
membrane pervaporation;
ozonation;
ZSM-5;
wastewater;
D O I:
10.1016/j.memsci.2006.11.039
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
A novel membrane reactor was designed for the ozonolysis of refractory organic pollutants in water. The reactor employed a membrane contactor and a membrane separator in a concentric arrangement to affect a uniform ozone distribution along the reactor length, while allowing the simultaneous membrane separation and production of clean water. An alumina capillary membrane contactor and a ZSM-5 zeolite pervaporation membrane were used in this study. Using potassium hydrogen phthalate as model pollutant, the performance of the novel membrane reactor was tested and compared to ozone reaction carried out using the capillary membrane contactor and membrane pervaporation using the ZSM-5 membrane. The novel membrane reactor consistently outperformed both membrane processes. Forty-seven percent higher TOC degradation was observed compared to ozone reaction using a capillary membrane contactor. This enhancement is due to the increase in the organic pollutant concentration in the reaction zone as a result of water withdrawal by membrane pervaporation. As in the case of membrane pervaporation, clean water was produced at the permeate outlet of the novel membrane reactor. Clean water with less than 0.5 +/- 10.1 ppm was collected from the membrane permeate outlet at a rate of 11-15 kg(-1) h(-1) m(-2). (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:67 / 75
页数:9
相关论文