共 50 条
Fluoride removal from brackish groundwater by direct contact membrane distillation
被引:6
|作者:
Hou, D. Y.
[1
]
Wang, J.
[1
]
Wang, B. Q.
[2
]
Luan, Z. K.
[1
]
Sun, X. C.
[1
]
Ren, X. J.
[1
]
机构:
[1] Chinese Acad Sci, State Key Lab Environm Aquat Chem, Ecoenvironm Sci Res Ctr, Beijing 100085, Peoples R China
[2] China Univ Min & Technol, Sch Chem & Environm Engn, Beijing 100083, Peoples R China
关键词:
brackish groundwater;
fluoride removal;
membrane distillation;
REVERSE-OSMOSIS;
WATER;
PERFORMANCE;
ADSORPTION;
ELECTRODIALYSIS;
NANOFILTRATION;
DEFLUORIDATION;
D O I:
10.2166/wst.2010.878
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
The direct contact membrane distillation (DCMD) applied for fluoride removal from brackish groundwater is presented. The self-prepared polyvinylidene fluoride membrane exhibited high rejection of inorganic salt solutes and a maximum permeate flux 35.6 kgm(-2)h(-1) was obtained. The feed concentration had no marked impact on the permeate flux and the rejection of fluoride. The precipitation of CaCO3 would clog the hollow fiber inlets and foul the membrane surface with the increase of concentration factor when natural groundwater was used directly as the feed, which resulted in a rapid decline of the module efficiency. This phenomenon was diminished by acidification of the feed. The experimental results showed that the permeate flux and the quality of obtained distillate kept stable before concentration factor reached 5.0 with the acidified groundwater as feed. The membrane module efficiency began to decline gradually when the feed continued to be concentrated, which can be mainly attributed to the formation of CaF2 deposits on the membrane surface. Finally, a 300 h continuous fluoride removal experiment on acidified groundwater was carried out with concentration factor at 4.0, the permeate flux kept stable and the permeate fluoride was not detected.
引用
收藏
页码:3178 / 3187
页数:10
相关论文