Influence of monomer concentrations on the performance of polyamide-based thin film composite forward osmosis membranes

薄膜复合膜 正渗透 浓差极化 聚酰胺 界面聚合 磁导率 化学工程 材料科学 反渗透 色谱法 扩散 聚合物 高分子化学 单体 化学 有机化学 工程类 热力学 生物化学 物理
作者
Jing Wei,Xin Liu,Changquan Qiu,Rong Wang,Chuyang Y. Tang
出处
期刊:Journal of Membrane Science [Elsevier]
卷期号:381 (1-2): 110-117 被引量:185
标识
DOI:10.1016/j.memsci.2011.07.034
摘要

Abstract Polyamide thin film composite (TFC) membranes with tailored porous substrate and rejection layer are promising for forward osmosis (FO) applications. The current study investigates the effect of rejection layer synthesis conditions on the performance of the resulting TFC polyamide FO membranes. The influence of monomer concentrations (i.e., m-phenylenediamine (MPD) and trimesoyl chloride (TMC) concentrations) on the membrane separation properties as well as FO performance was systematically studied. A strong trade-off between the water permeability and salt rejection was observed, where increasing the TMC concentration or reducing the MPD concentration resulted in higher membrane permeability but lower salt rejection. In FO tests, membranes with poor salt rejection had severe solute reverse diffusion, which enhanced the internal concentration polarization (ICP). It was found that the FO water flux was governed by both the membrane water permeability and its solute rejection. For a membrane with higher water permeability but lower solute rejection, the reduced membrane frictional resistance was compensated by the simultaneously more severe solute-reverse-diffusion-induced ICP. The net effect on the FO water flux depends on the competition of these two opposing mechanisms. Under conditions where solute reverse diffusion may cause severe ICP (e.g., high draw solution concentration and high water flux level), membranes need be optimized to achieve a high salt rejection even if this is at the expense of lower water permeability.
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