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Highly Permeable Double-Skinned Forward Osmosis Membranes for Anti-Fouling in the Emulsified Oil-Water Separation Process
被引:138
作者:
Duong, Phuoc H. H.
[1
]
Chung, Tai-Shung
[1
,2
]
Wei, Shawn
[3
]
Irish, Lana
[3
]
机构:
[1] Natl Univ Singapore, Dept Chem & Biomol Engn, Singapore 117585, Singapore
[2] King Abdullah Univ Sci & Technol, Water Desalinat & Reuse WDR Ctr, Thuwal 239556900, Saudi Arabia
[3] Kraton Polymers LLC, Houston, TX 77032 USA
基金:
新加坡国家研究基金会;
关键词:
THIN-FILM COMPOSITE;
PRESSURE RETARDED OSMOSIS;
INTERNAL CONCENTRATION POLARIZATION;
HOLLOW-FIBER MEMBRANES;
SULFONATED POLYPHENYLENESULFONE SPPSU;
WASTE-WATER;
FO MEMBRANES;
PENTABLOCK COPOLYMERS;
FLUX BEHAVIOR;
PERFORMANCE;
D O I:
10.1021/es405644u
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
Forward osmosis (FO) has attracted wide attention in recent years. However, the FO performance may be restricted due to internal concentration polarization (ICP) and fast fouling propensity that occurs in the membrane sublayer. Particularly, these problems significantly affect the membrane performance when treating highly contaminated oily wastewater. Recently, double-skinned flat sheet cellulose acetate (CA) membranes consisting of two selective skins via the phase inversion method have demonstrated less ICP and fouling propensity over typical single-skinned membranes. However, these membranes exhibit low water fluxes of <12 LMH under 2 M NaCl draw solution. Therefore, a novel double-skinned FO membrane with a high water flux has been aimed for in this study for emulsified oil-water treatment. The double-skinned FO membrane comprises a fully porous sublayer sandwiched between (i) a truly dense skin for salt rejection and (ii) a fairly loose dense skin for emulsified oil particle rejection. The former dense skin is a polyamide synthesized via interfacial polymerization, while the latter one is a self-assembled sulfonated pentablock copolymer (Nexar copolymer) layer. The resultant double-skinned membrane exhibits a high water flux of 17.2 LMH and a low reverse salt transport of 4.85 gMH using 0.5 M NaCl as the draw solution and DI water as the feed. The double-skinned membrane outperforms the single-skinned membrane with much lower fouling propensity for emulsified oil-water separation.
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页码:4537 / 4545
页数:9
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