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Performance of negatively charged nanofiltration membranes prepared from mixtures of various dimethacrylates and methacrylic acid

Authors
Jeon, M. Y.Yoo, S. H.Kim, C. K.
Issue Date
10-Apr-2008
Publisher
ELSEVIER SCIENCE BV
Keywords
dimethacrylates; methacrylic acid; active layer; composite membrane; nanofiltration
Citation
JOURNAL OF MEMBRANE SCIENCE, v.313, no.1-2, pp 242 - 249
Pages
8
Journal Title
JOURNAL OF MEMBRANE SCIENCE
Volume
313
Number
1-2
Start Page
242
End Page
249
URI
https://scholarworks.bwise.kr/cau/handle/2019.sw.cau/23775
DOI
10.1016/j.memsci.2008.01.012
ISSN
0376-7388
1873-3123
Abstract
To produce composite membranes with desired salt rejection and water permeability properties for nanofiltration (NF), the negatively charged active layers were fabricated from monomer mixtures of various dimethacrylates and methacrylic acid (MAA), which contains a vinyl moiety and a carboxylic acid. Even though membranes prepared from various dimethacrylates such as 2,2-bis[4-(2-hydroxy-3-methacryloyloxy propoxy)phenyl]-propane (Bis-GMA) and diethylene glycol dimethacrylate (DEGDMA) do not exhibit performance advantages over commercially available NF membranes, the cross-over point of water permeability versus salt rejection shifted favorably for NF applications when the active layer of the composite membrane was prepared from monomer mixtures of dimethacrylate and MAA. MgSO4 rejection of the composite membranes prepared from Bis-GMA mixtures with MAA was higher than 99.5% when the monomer mixtures contained less than or equal to 20 wt% MAA, while water permeability rapidly increased when increasing the MAA content in the monomer mixture. MgSO4 rejection of the composite membranes prepared from DEGDMA and MAA mixtures initially increased with increasing MAA content in the monomer mixture passing through a maximum (98.5%) centered at about 20 wt% MAA before decreasing beyond this point, while the water permeability continuously increased with increasing MAA content. Some of composite membranes prepared here for the NF process exhibited superior performance compared to commercially available nanofiltration membranes such as NF-40. (C) 2008 Elsevier B.V. All rights reserved.
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