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高性能薄膜复合正向渗透中空纤维膜,具有无大孔和高多孔结构,用于可持续水生产。

High performance thin-film composite forward osmosis hollow fiber membranes with macrovoid-free and highly porous structure for sustainable water production.

机构信息

Department of Chemical and Biomolecular Engineering, National University of Singapore, 10 Kent Ridge Crescent 4 Engineering Drive 4, Singapore 117576, Singapore.

出版信息

Environ Sci Technol. 2012 Jul 3;46(13):7358-65. doi: 10.1021/es301559z. Epub 2012 Jun 15.

Abstract

The development of high-performance and well-constructed thin-film composite (TFC) hollow fiber membranes for forward osmosis (FO) applications is presented in this study. The newly developed membranes consist of a functional selective polyamide layer formed by highly reproducible interfacial polymerization on a polyethersulfone (PES) hollow fiber support. Using dual-layer coextrusion technology to design and effectively control the phase inversion during membrane formation, the support was designed to possess desirable macrovoid-free and fully sponge-like morphology. Such morphology not only provides excellent membrane strength, but it has been proven to minimize internal concentration polarization in a FO process, thus leading to the water flux enhancement. The fabricated membranes exhibited relatively high water fluxes of 32-34 LMH and up to 57-65 LMH against a pure water feed using 2 M NaCl as the draw solution tested under the FO and pressure retarded osmosis (PRO) modes, respectively, while consistently maintaining relatively low salt leakages below 13 gMH for all cases. With model seawater solution as the feed, the membranes could display a high water flux up to 15-18 LMH, which is comparable to the best value reported for seawater desalination applications.

摘要

本研究提出了一种用于正向渗透(FO)应用的高性能、结构良好的薄膜复合(TFC)中空纤维膜的开发。新开发的膜由聚醚砜(PES)中空纤维支撑上通过高度可重复的界面聚合形成的功能选择性聚酰胺层组成。通过使用双层共挤出技术来设计和有效控制膜形成过程中的相转化,支撑体被设计为具有理想的无大孔和全海绵状形态。这种形态不仅提供了优异的膜强度,而且已被证明可以最大程度地减少 FO 过程中的内部浓差极化,从而提高水通量。所制备的膜在 FO 和压力延迟渗透(PRO)模式下分别使用 2 M NaCl 作为汲取液进行测试时,表现出相对较高的水通量,分别为 32-34 LMH 和高达 57-65 LMH,而所有情况下的盐泄漏率均保持在 13 gMH 以下。对于模型海水溶液作为进料,膜可以显示高达 15-18 LMH 的高水通量,这与海水淡化应用的最佳值相当。

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