Integrating seawater desalination and wastewater reclamation forward osmosis process using thin-film composite mixed matrix membrane with functionalized carbon nanotube blended polyethersulfone support layer

被引:56
|
作者
Choi, Hyeon-gyu [1 ,2 ]
Son, Moon [2 ,3 ]
Choi, Heechul [1 ,2 ]
机构
[1] KRICT, Ctr Membranes, Adv Mat Div, Daejeon 34114, South Korea
[2] GIST, Sch Earth Sci & Environm Engn, Gwangju 61005, South Korea
[3] Penn State Univ, Dept Civil & Environm Engn, University Pk, PA 16802 USA
基金
新加坡国家研究基金会;
关键词
Thin-film composite membrane; Carbon nanotube; Forward osmosis; Seawater desalination and wastewater reclamation; Effluent organic matter fouling; Electrostatic repulsion; ENHANCED PERFORMANCE; SUBSTRATE MEMBRANE; CELLULOSE-ACETATE; REVERSE-OSMOSIS; FOULING CONTROL; FABRICATION; NANOFILTRATION; PRESSURE; TFC;
D O I
10.1016/j.chemosphere.2017.06.136
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Thin-film composite mixed matrix membrane (TFC MMM) with functionalized carbon nanotube (fCNT) blended in polyethersulfone (PES) support layer was synthesized via interfacial polymerization and phase inversion. This membrane was firstly tested in lab-scale integrating seawater desalination and wastewater reclamation forward osmosis (FO) process. Water flux of TFC MMM was increased by 72% compared to that of TFC membrane due to enhanced hydrophilicity. Although TFC MMM showed lower water flux than TFC commercial membrane, enhanced reverse salt flux selectivity (RSFS) of TFC MMM was observed compared to TFC membrane (15% higher) and TFC commercial membrane (4% higher), representing membrane permselectivity. Under effluent organic matter (EfOM) fouling test, 16% less normalized flux decline of TFC MMM was observed compared to TFC membrane. There was 8% less decline of TFC MMM compared to TFC commercial membrane due to fCNT effect on repulsive foulant membrane interaction enhancement, caused by negatively charged membrane surface. After 10 min physical cleaning, TFC MMM displayed higher recovered normalized flux than TFC membrane (6%) and TFC commercial membrane (4%); this was also supported by visualized characterization of fouling layer. This study presents application of TFC MMM to integrated seawater desalination and wastewater reclamation FO process for the first time. It can be concluded that EfOM fouling of TFC MMM was suppressed due to repulsive foulant membrane interaction. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1181 / 1188
页数:8
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