TY - JOUR
T1 - Layer-by-layer assembly of inorganic nanosheets and polyelectrolytes for reverse osmosis composite membranes
AU - Choi, Jungkyu
AU - Sung, Hyemin
AU - Ko, Yongmin
AU - Lee, Seunghye
AU - Choi, Wanseok
AU - Bang, Joona
AU - Cho, Jinhan
PY - 2014
Y1 - 2014
N2 - 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 -25.5 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 -30 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 (-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 -7.5±0.5 L·m_2·h_1, comparable to commercial membranes, while the salt rejection ability is as high as - 75±2.5% and the stability against the chlorine attack is well preserved with - 74±5.0% ion rejection after the NaOCl treatment.
AB - 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 -25.5 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 -30 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 (-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 -7.5±0.5 L·m_2·h_1, comparable to commercial membranes, while the salt rejection ability is as high as - 75±2.5% and the stability against the chlorine attack is well preserved with - 74±5.0% ion rejection after the NaOCl treatment.
KW - Electrostatic interaction
KW - Layer-by-layer assembly
KW - Montmorillon-ite (MTM) nanosheet
KW - Polyelectrolyte layers
KW - RO membrane
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U2 - 10.1252/jcej.13we136
DO - 10.1252/jcej.13we136
M3 - Article
AN - SCOPUS:84894243188
SN - 0021-9592
VL - 47
SP - 180
EP - 186
JO - Journal of Chemical Engineering of Japan
JF - Journal of Chemical Engineering of Japan
IS - 2
ER -