Layer-by-Layer Assembly of Inorganic Nanosheets and Polyelectrolytes for Reverse Osmosis Composite Membranes
- Authors
- Choi, Jungkyu; Sung, Hyemin; Ko, Yongmin; Lee, Seunghye; Choi, Wanseok; Bang, Joona; Cho, Jinhan
- Issue Date
- 2014
- Publisher
- SOC CHEMICAL ENG JAPAN
- Keywords
- RO Membrane; Layer-by-Layer Assembly; Electrostatic Interaction; Polyelectrolyte Layers; Montmorillonite (MTM) Nanosheet
- Citation
- JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, v.47, no.2, pp.180 - 186
- Indexed
- SCIE
SCOPUS
- Journal Title
- JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
- Volume
- 47
- Number
- 2
- Start Page
- 180
- End Page
- 186
- URI
- https://scholar.korea.ac.kr/handle/2021.sw.korea/101180
- DOI
- 10.1252/jcej.13we136
- ISSN
- 0021-9592
- Abstract
- In this study, we introduce a layer-by-layer (LbL) assembly method to prepare a reverse osmosis (RO) desalination membrane that consists of a hybrid combination of [polyelectrolyte (PE)/montmorillonite (MTM)](n) layers. First, adopting poly(allylamine hydrochloride) (PAH) for a PE layer, an RO test showed that the permeate flux of water through (PAH/MTM)(n) multilayer-coated membranes decreased from similar to 25.5 to similar to 8.3 L.m(-2).h(-1) with the increased bilayer number from n = 9 to n = 18. At the same time, the corresponding ion rejection with respect to NaCl is increased from similar to 30 to similar to 81%. Despite the increased ion rejection performance, (PAH/MTM)(n) membranes exhibit a poor chlorine resistance, as frequently observed in commercial polyamide-based RO membranes. In our previous study, it was noted that the RO membranes, prepared just from the PE multilayers (i.e., [PAH/poly(acrylic acid) (PAA)](n) layers), showed a marked chlorine tolerance, but concomitantly very low permeate flux (similar to 4-5 L.m(-2).h(-1)). Considering the significant drawback in each case (poor chlorine tolerance for (PAH/MTM)(n) layers and low permeate flux for (PAH/PAA)(n) layers), we proposed to combine the layer constituents primarily by inserting PAH/PAA layers between two adjacent PAH/MTM layers. Indeed, the flux is maintained at similar to 7.5 +/- 0.5 L.m(-2).h(-1), comparable to commercial membranes, while the salt rejection ability is as high as similar to 75 +/- 2.5% and the stability against the chlorine attack is well preserved with similar to 74 +/- 5.0% ion rejection after the NaOCl treatment.
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