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Enhanced flux performance of polyamide composite membranes prepared via interfacial polymerization assisted with ethyl formate
Author(s) -
Liu Zhao-feng,
Guiru Zhu,
Yulin Wei,
Dapeng Zhang,
Lei Jiang,
Haizeng Wang,
Congjie Gao
Publication year - 2017
Publication title -
water science and technology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.406
H-Index - 137
eISSN - 1996-9732
pISSN - 0273-1223
DOI - 10.2166/wst.2017.349
Subject(s) - interfacial polymerization , polyamide , membrane , chemical engineering , formate , chemistry , polymer chemistry , thin film composite membrane , ethyl formate , aqueous solution , ultrafiltration (renal) , nanofiltration , materials science , reverse osmosis , chromatography , polymer , organic chemistry , biochemistry , monomer , engineering , catalysis
A novel thin film composite (TFC) polyamide reverse osmosis membrane was prepared via the interfacial polymerization of m-phenylene diamine (MPD) in aqueous phase and 1,3,5-trimesoyl chloride (TMC) in organic phase on a polysulfone ultrafiltration support by assisting with ethyl formate as a co-solvent added in the organic phase. The ethyl formate added in the organic phase is intended to form a narrow miscibility zone, which leads to the thicker reaction zone. The multi-layered loose polyamide structure with larger pore size was formed due to the thicker reaction zone and lower content of MPD. The enhanced hydrophilicity of the membrane was proved by the decreased water contact angle. Water flux was measured at 1.6 MPa with 2,000 ppm NaCl aqueous solution. Compared to the TFC membrane prepared without ethyl formate, the water flux across the TFC membrane with ethyl formate in the organic phase increased with the increased ethyl formate content (from 23 to 45 L/(m 2 h)) and the salt rejection remained at a high level (>90%). The ethyl formate can be used as a co-solvent to effectively enhance the performance of the TFC membrane.

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