Removal of organic micro-pollutants (phenol, aniline and nitrobenzene) via forward osmosis (FO) process: Evaluation of FO as an alternative method to reverse osmosis (RO)

被引:110
作者
Cui, Yue [1 ,2 ]
Liu, Xiang-Yang [1 ,3 ]
Chung, Tai-Shung [2 ,4 ]
Weber, Martin [5 ]
Staudt, Claudia [5 ]
Maletzko, Christian [6 ]
机构
[1] Natl Univ Singapore, Dept Chem, Singapore 117542, Singapore
[2] Natl Univ Singapore, Dept Chem & Biomol Engn, Singapore 117542, Singapore
[3] Natl Univ Singapore, Dept Phys, Singapore 117542, Singapore
[4] King Abdullah Univ Sci & Technol, Water Desalinat & Reuse WDR Ctr, Thuwal 239556900, Saudi Arabia
[5] BASF SE, Adv Mat & Syst Res, GM-B001, D-67056 Ludwigshafen, Germany
[6] BASF SE, Performance Mat, G-PM PU-F206, D-67056 Ludwigshafen, Germany
基金
新加坡国家研究基金会;
关键词
Removal of organic micro-pollutants; Forward osmosis; Wastewater treatment; THIN-FILM COMPOSITE; HOLLOW-FIBER MEMBRANES; POSITRON-ANNIHILATION SPECTROSCOPY; OILY WASTE-WATER; FREE-VOLUME; NANOFILTRATION; FLUX; PERFORMANCE; ENERGY; LAYER;
D O I
10.1016/j.watres.2016.01.001
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this study, we have explored and compared the effectiveness of using (1) lab-fabricated forward osmosis (FO) membranes under both FO and reverse osmosis (RO) modes and (2) commercially available RO membranes under the RO mode for the removal of organic micro-pollutants. The lab-fabricated FO membranes are thin film composite (TFC) membranes consisting of a polyamide layer and a porous substrate cast from three different materials; namely, Matrimid, polyethersulfone (PESU) and sulfonated polyphenylene sulfone (sPPSU). The results show that the FO mode is superior to the RO mode in the removal of phenol, aniline and nitrobenzene from wastewater. The rejections of all three TFC membranes to all the three organic micro-pollutants under the FO processes are higher than 72% and can be even higher than 90% for aniline when a 1000 ppm aromatic aqueous solution and 1 M NaCl are employed as feeds. These performances outperform the results obtained from themselves and commercially available RO membranes under the RO mode. In addition, the rejection can be maintained even when treating a more concentrated feed solution (2000 ppm). The removal performance can be further enhanced by using a more concentrated draw solution (2 M). The water flux is almost doubled, and the rejection increment can reach up to 17%. Moreover, it was observed that annealing as a post-treatment would help compact the membrane selective layer and further enhance the separating efficiency. The obtained organic micro-pollutant rejections and water fluxes under various feasible operating conditions indicate that the FO process has potential to be a viable treatment for wastewater containing organic micro pollutants. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:104 / 114
页数:11
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