Department of Earth and Environmental Engineering, Columbia University, New York, New York 10027-6623, United States.
Department of Earth and Environmental Engineering, Columbia University, New York, New York 10027-6623, United States; Columbia Water Center, Columbia University, New York, New York 10027-6623, United States.
Water Res. 2021 Aug 1;201:117311. doi: 10.1016/j.watres.2021.117311. Epub 2021 May 28.
Fundamental understanding of the reverse osmosis (RO) transport phenomena is necessary for quantitative prediction of contaminant rejection and development of more selective membranes. The solution-diffusion (S-D) model predicts a tradeoff relationship between permeability and selectivity, and this tradeoff trend was recently reported for RO. But the first principles governing the relationship are not well understood for aqueous separation membranes. This study presents a framework to elucidate the underlying factors of the permeability-selectivity tradeoff relationship in thin-film composite polyamide (TFC-PA) membranes. Water and solute permeabilities of membranes with a range of selectivities are examined using six nonelectrolyte solutes of various sizes and dimensions. The permeability-selectivity tradeoff trend, as defined by S-D, was observed for all six solutes. Crucially, the slopes of the tradeoff lines, λ, are found to be related to the solute and solvent (i.e., water) diameters, d and d, respectively, by λ = (d/d) - 1, consistent with the S-D framework established for gas separation membranes. Additionally, the intercepts of the tradeoff lines are shown to be also influenced by d. These results highlight that solute molecular diameter is a primary influence on the permeability-selectivity tradeoff for the permeants investigated in this study. Furthermore, a transport regime where solute permeation is only very weakly coupled to water transport, in addition to the conventional S-D, is identified for the first time. We demonstrate that the boundary delineating the two transport regimes can be determined by the solute diameter. The relationship between characteristic features of the "additional regime" and solute dimensions are analyzed. The study shows that the general principles of the S-D framework are applicable to TFC-PA membranes and the analysis quantified the principal role of solute size in governing RO transport. The experimental and analytical evidence suggest that nonelectrolyte solute transport can, in principle, be a priori predicted using molecular diameter. Findings of this investigation provide new insights for understanding the transport mechanisms in osmotic membrane processes.
反渗透(RO)传输现象的基本理解对于定量预测污染物截留和开发更具选择性的膜是必要的。溶液扩散(S-D)模型预测了渗透性和选择性之间的权衡关系,这种权衡趋势最近在 RO 中得到了报道。但是,对于水分离膜,控制这种关系的基本原理还不是很清楚。本研究提出了一个框架来阐明薄复合聚酰胺(TFC-PA)膜中渗透性-选择性权衡关系的基本因素。使用六种不同大小和尺寸的非电解质溶质来检查具有一系列选择性的膜的水和溶质渗透性。观察到所有六种溶质的 S-D 定义的渗透性-选择性权衡趋势。至关重要的是,发现权衡线的斜率λ与溶质和溶剂(即水)直径 d 和 d 分别相关,λ=(d/d)-1,与为气体分离膜建立的 S-D 框架一致。此外,权衡线的截距也被证明受到 d 的影响。这些结果突出表明,对于本研究中研究的渗透物,溶质分子直径是对渗透性-选择性权衡的主要影响。此外,首次确定了除传统的 S-D 之外,溶质渗透与水传输仅非常弱耦合的传输状态。我们证明了可以通过溶质直径来确定区分两种传输状态的边界。分析了“附加状态”的特征与溶质尺寸之间的关系。该研究表明,S-D 框架的一般原则适用于 TFC-PA 膜,并且分析量化了溶质尺寸在控制 RO 传输中的主要作用。实验和分析证据表明,原则上可以使用分子直径来预先预测非电解质溶质的传输。本研究的结果为理解渗透膜过程中的传输机制提供了新的见解。