Adsorptive removal of anionic dye by inorganic-organic hybrid anion-exchange membranes

被引:31
作者
Chiu, Hsin-Chieh [1 ]
Liu, Chia-Hung [1 ]
Chen, Shiow-Ching [2 ]
Suen, Shing-Yi [1 ]
机构
[1] Natl Chung Hsing Univ, Dept Chem Engn, Taichung 402, Taiwan
[2] Natl Chung Hsing Univ, Dept Environm Engn, Taichung 402, Taiwan
关键词
Inorganic-organic hybrid membrane; Anion-exchange membrane; Anionic dye; Adsorption; Dye removal; REACTIVE DYES; PLASMID DNA; NANOFILTRATION MEMBRANES; DIFFUSION DIALYSIS; CHARGED MEMBRANE; ACTIVATED CARBON; BOTTOM ASH; CONGO-RED; WASTE; WATER;
D O I
10.1016/j.memsci.2009.04.004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Anion-exchange membranes with quaternary ammonium groups were prepared by coating a precursor with secondary amino groups (the product of N-[3-(trimethoxysilyl)propyl] ethylene diamine and 3-(triethoxysjlyl)propyl isocyanate) on porous glass fiber membranes and further treated with bromoethane. The precursor coating and bromoethane treatment have been proved successful by membrane characterization such as Fourier-transform infrared (FTIR) spectrum, scanning electron microscopy (SEM) photo, contact angle, water content, and ion-exchange capacity. The optimal feed precursor/dimethyl formamide (DMF) ratio was found as 1: 3 (w/w) based on the batch adsorption results of anionic dye Cibacron blue 3GA. The membrane ion-exchange capacity for this condition was 6.8 mu mol/cm(2) (or 104.2 mu mol/cm(3)) and the maximum dye adsorption capacity was 2.12 mg/cm(3). Different desorption solutions were tested in batch desorption process, and the use of 1 N KSCN in 60% methanol attained a better performance (70% desorption). In the chromatography process with two pieces of 47 mm modified anion-exchange membrane discs (loading at 1 mL/min; washing and elution at 8 mL/min), more than 92% of dye molecules could be recovered from a 20 mL feed aqueous solution with an initial dye concentration of 0.05 g/L. Moreover, the membrane performance remained unaltered over 10 successive cycles of dye adsorption, washing, and elution. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:282 / 290
页数:9
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