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Preparation of porous PMMA/Na+-montmorillonite cation-exchange membranes for cationic dye adsorption
Journal article   Peer reviewed

Preparation of porous PMMA/Na+-montmorillonite cation-exchange membranes for cationic dye adsorption

Ray-Yi Lin, Bang-Shuo Chen, Guan-Liang Chen, Jeng-Yue Wu, Hsin-Cheng Chiu and Shing-Yi Suen
Journal of Membrane Science, Vol.326(1), pp.117-129
05/01/2009

Abstract

Adsorption Cation-exchange membrane Cationic dye PMMA/Na+-MMT composite membrane
Porous PMMA/Na + -montmorillonite (MMT) cation-exchange membranes were successfully prepared by entrapment method in this study. One approach (simple mixing) was to mix commercial PMMA polymer with Na + -MMT clays in solvent for membrane preparation (Membrane A). The other approach (emulsion polymerization) was to synthesize the PMMA/Na + -MMT polymer composite via emulsion polymerization first, followed by membrane casting (Membrane B for Kunipia F clays and Membrane C for PK-802 clays). Membrane morphology and properties were characterized. The thermogravimetric analysis (TGA) verified the near complete incorporation of feed Na + -MMT clays in the PMMA/Na + -MMT composite membranes, while X-ray diffractograms (WXRD) exhibited the slightly enlarged interlayer spacing of Na + -MMT. The range of cation-exchange capacity (CEC) was 9-32 μequiv./47 mm disc. For batch cationic dye adsorption, the best performance was achieved by Membrane B with feed Na + -MMT/MMA (M/P) ratio (w/w) = 0.5 and Membrane C with feed M/P = 0.6, where about 95% Methyl violet adsorption was attained in 2 h. The optimal desorption solution was 1 M KSCN in 80% methanol and its related dye desorption efficiency was 92%. In the flow process using one piece of 47 mm disc of Membrane B (M/P = 0.5), dye solution was recirculated for 6 h and ≥85% dye could be removed. Higher than 94% of dye was desorbed at 1 or 4 mL/min, and the membrane regenerability was proved by successfully performing three consecutive cycles. © 2008 Elsevier B.V. All rights reserved.

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