Yang Qian, Wang Kai Yu, Chung Tai-Shung
Department of Chemical and Biomolecular Engineering, National University of Singapore, Singapore.
Environ Sci Technol. 2009 Apr 15;43(8):2800-5. doi: 10.1021/es803360t.
We have demonstrated in this work the prospect of dual-layer polybenzimidazole-polyethersulfone (PBI-PES) nanofiltration (NF) hollow fiber membranes in the forward osmosis (FO) process for water production: The state-of-the-art for dual-layer membrane fabrication via coextrusion technology could produce the resultant membrane consisting of an ultrathin selective skin, fully porous water channels underneath, and a microporous sponge-like support structure. Together with its sharp pore size distribution and self-charged PBI selective membrane surface, the dual-layer hollow fiber forward osmosis membrane can achieve a water flux as high as 33.8 L x m(-2) x hr(-1) and a salt flux less than 1.0 g x m(-2) x hr(-1) at room temperature of 23 degrees C using 5 M MgCl2 as the draw solution. A comprehensive literature review of previous efforts on identifying suitable membranes and appropriate draw solutions in the FO process for water production and seawater desalination have also been conducted. It shows that the water fluxes of the dual-layer hollow fiber FO membrane developed in this work utilizing MgCl2 as the draw solutions generally surpasses those FO processes utilizing RO membranes and is comparable to most FO processes using commercial FO membrane and employing other salts or sugar instead of MgCl2 as the draw solutions.
在这项工作中,我们展示了双层聚苯并咪唑-聚醚砜(PBI-PES)纳滤(NF)中空纤维膜在正向渗透(FO)制水过程中的应用前景:通过共挤出技术制造双层膜的最新技术能够制备出具有超薄选择性皮层、下方完全多孔的水通道以及微孔海绵状支撑结构的复合膜。双层中空纤维正向渗透膜具有尖锐的孔径分布和带正电荷的PBI选择性膜表面,在23℃室温下,以5M MgCl₂作为汲取溶液时,水通量可达33.8L·m⁻²·h⁻¹,盐通量小于1.0g·m⁻²·h⁻¹。我们还对以往在正向渗透制水和海水淡化过程中寻找合适的膜及适当汲取溶液的研究进行了全面的文献综述。结果表明,本工作中以MgCl₂为汲取溶液制备的双层中空纤维正向渗透膜的水通量普遍超过使用反渗透膜的正向渗透过程,并且与大多数使用商业正向渗透膜、采用其他盐类或糖类而非MgCl₂作为汲取溶液的正向渗透过程相当。