Authors | آرش یونس نیالهی,احمد اکبری,حسنا سلیمانی |
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Journal | membrane water treatment |
Page number | 173 |
Volume number | 6 |
IF | 0.625 |
Paper Type | Full Paper |
Published At | 2015-01-11 |
Journal Grade | Scientific - research |
Journal Type | Electronic |
Journal Country | Iran, Islamic Republic Of |
Journal Index | ISI |
Abstract
The goal of present work is the preparation of a novel positively charged nanofiltration (NF) membrane and its development for the cation removal of aqueous solutions. This NF membrane was fabricated by the surface modification of polysulfone (PSf) ultrafiltration support. The active top-layer was formed by interfacial cross-linking polymerization of poly(ethyleneimine) (PEI) with p-xylylene dichloride (XDC) and then quaternized with methyl iodide to form a perpetually positively charged layer. In order to improve the efficiency of nanofiltration membrane, the concentration of PEI, XDC and methyl iodide solutions, PEI coating and cross-linking time have been optimized. As a result, a high water flux and high 2 rejection (1,000 ppm) was obtained for the composite membrane with values of 18.29 L/m .h and CaCl 2 93.62% at 4 bar and 25°C, respectively. The rejections of NF membrane for different salt solutions followed SO < MgSO < NaCl < CaCl . Molecular weight of cut off (MWCO) was calculated via the order of Na 2 4 4 2 retaining of PEG solutions with different molecular weights that finally, it revealed the Stokes and hydrodynamic radius of 1.457 and 2.507 nm on the membrane selective layer, respectively. The most 2+ rejection of 96.26% for industrial efficient positively charged nanofiltration membrane exhibited a Ni wastewater from Shamse Hadaf Co. (Kashan, Iran).
tags: cross-linking; nanofiltration; poly (ethyleneimine); polysulfone; positively charged membrane