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反渗透膜中的盐和水传输:超越溶液扩散模型。

Salt and Water Transport in Reverse Osmosis Membranes: Beyond the Solution-Diffusion Model.

机构信息

Department of Chemical and Environmental Engineering, Yale University, New Haven, Connecticut 06520-8286, United States.

Environmental Technology, Wageningen University, Bornse Weilanden 9, 6708 WG Wageningen, The Netherlands.

出版信息

Environ Sci Technol. 2021 Dec 21;55(24):16665-16675. doi: 10.1021/acs.est.1c05649. Epub 2021 Dec 8.

Abstract

Understanding the salt-water separation mechanisms of reverse osmosis (RO) membranes is critical for the further development and optimization of RO technology. The solution-diffusion (SD) model is widely used to describe water and salt transport in RO, but it does not describe the intricate transport mechanisms of water molecules and ions through the membrane. In this study, we develop an ion transport model for RO, referred to as the solution-friction model, by rigorously considering the mechanisms of partitioning and the interactions among water, salt ions, and the membrane. Ion transport through the membrane is described by the extended Nernst-Planck equation, with the consideration of frictions between the species (i.e., ion, water, and membrane matrix). Water flow through the membrane is governed by the hydraulic pressure gradient and the friction between the water and membrane matrix as well as the friction between water and ions. The model is validated using experimental measurements of salt rejection and permeate water flux in a lab-scale, cross-flow RO setup. We then investigate the effects of feed salt concentration and hydraulic pressure on salt permeability, demonstrating strong dependence of salt permeability on feed salt concentration and applied pressure, starkly disparate from the SD model. Lastly, we develop a framework to analyze the pressure drop distribution across the membrane, demonstrating that cross-membrane transport dominates the overall pressure drop in RO, in marked contrast to the SD model that assumes no pressure drop across the membrane.

摘要

理解反渗透(RO)膜的盐水分离机制对于 RO 技术的进一步发展和优化至关重要。溶液扩散(SD)模型广泛用于描述 RO 中的水和盐传输,但它无法描述水分子和离子通过膜的复杂传输机制。在本研究中,我们通过严格考虑分配机制以及水、盐离子和膜之间的相互作用,为 RO 开发了一种离子传输模型,称为溶液摩擦模型。通过扩展的能斯特-普朗克方程描述离子通过膜的传输,其中考虑了物种(即离子、水和膜基质)之间的摩擦力。膜中水的流动由液压梯度以及水和膜基质之间以及水和离子之间的摩擦力控制。该模型通过在实验室规模的错流 RO 装置中进行的盐截留和渗透水通量的实验测量进行了验证。然后,我们研究了进料盐浓度和液压对盐渗透性的影响,结果表明盐渗透性强烈依赖于进料盐浓度和施加的压力,这与 SD 模型形成鲜明对比,后者假设膜内没有压力降。最后,我们开发了一个分析膜内压力降分布的框架,结果表明 RO 中的跨膜传输主导了总压力降,与 SD 模型假设膜内没有压力降形成鲜明对比。

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