More fouling resistant modified PVDF ultrafiltration membranes for water treatment

被引:48
|
作者
Pezeshk, Niloufar [1 ]
Narbaitz, Roberto M. [1 ]
机构
[1] Univ Ottawa, Dept Civil Engn, Ottawa, ON K1N 6N5, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Ultrafiltration; Fouling; NOM; Surface-modified membranes; PVDF; NATURAL ORGANIC-MATTER; ASSISTED GRAFT-POLYMERIZATION; DEAD-END MICROFILTRATION; FLUX DECLINE; CROSS-FLOW; SURFACE-WATER; FILTRATION; PERFORMANCE; MECHANISMS; APPARATUS;
D O I
10.1016/j.desal.2011.11.048
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Polyvinylidene fluoride (PVDF) membranes were modified using L2MM, a new type of hydrophilic polyurethane additive, to improve membrane performance. Membranes were prepared using 15 and 18%PVDF and small weight percentages (i.e., 1.5 and 3%) of L2MM. Their fouling resistance was evaluated by filtration/ fouling tests with Ottawa River Water (ORW) using membranes incorporating two different types of L2MMs (L2MM(PEG-200) and L2MM(PEG-600)). For comparisons a commercial membrane (HFM-180) was also tested. A PVDF membrane prepared with 3% L2MM(PEG-200) which produced the highest cumulative permeate volume, had a lower flux reduction and its TOC removal was 24% higher than the HEM-180 membrane. L2MM produced more hydrophilic PVDF membranes which had pure water permeation (PWP) rates up to 128% greater than the control PVDF membranes. Many of the L2MM blended membranes had significantly higher total organic carbon (TOC) removals than the HEM-180 membrane tested (64-67% versus 46%). Modeling of the flux decline suggested the membranes fouled via a combination of pore blocking and cake filtration: scanning electron microscopy (SEM) of the fouled membrane surface confirmed the existence of a cake layer. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:247 / 254
页数:8
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