Transport in reverse osmosis membranes: observations and comments on the pore flow model versus the solution‒diffusion model

Sixty-four years have passed since the announcement of the cellulose acetate membrane for seawater desalination by Loeb and Sourirajan at UCLA on 23 Aug 1960. Reverse osmosis (RO) is now well established as a process for desalination of seawater, brackish water, as well as for wastewater treatment....

Full description

Saved in:
Bibliographic Details
Main Authors: Takeshi Matsuura, Michael D. Guiver, Woei Jye Lau, Ahmad Fauzi Ismail
Format: Article
Language:English
Published: Frontiers Media S.A. 2025-02-01
Series:Frontiers in Membrane Science and Technology
Subjects:
Online Access:https://www.frontiersin.org/articles/10.3389/frmst.2025.1513591/full
Tags: Add Tag
No Tags, Be the first to tag this record!
_version_ 1832542330643546112
author Takeshi Matsuura
Michael D. Guiver
Woei Jye Lau
Ahmad Fauzi Ismail
author_facet Takeshi Matsuura
Michael D. Guiver
Woei Jye Lau
Ahmad Fauzi Ismail
author_sort Takeshi Matsuura
collection DOAJ
description Sixty-four years have passed since the announcement of the cellulose acetate membrane for seawater desalination by Loeb and Sourirajan at UCLA on 23 Aug 1960. Reverse osmosis (RO) is now well established as a process for desalination of seawater, brackish water, as well as for wastewater treatment. The number of research papers on RO is growing. In contrast to the numerous publications on RO membrane preparation and applications, studies on transport mechanisms have been largely neglected. However, this changed recently when M. Elimelech’s research group from Yale University published several papers challenging the applicability of the solution‒diffusion (S‒D) model. Especially, in the most recent paper published in 2024, they have shown seven reasons why the well-accepted S‒D model appears to be wrong. It is interesting to note that, according to Srinivasa Sourirajan, one of the co-inventors of cellulose acetate RO membrane, their work was guided by the Preferential Sorption‒Capillary Flow model. Moreover, he wrote that this pore model was based on the presence of a pure water layer at the salt solution‒air interface, which could be predicted by the Gibbs Adsorption Isotherm. The purpose of this short communication is to present some observations and discussion in response to the 2024 paper published by Elimelech’s group in Desalination journal. In addition, the Gibbs Adsorption Isotherm was revisited to examine if there is a pure water layer at the sodium chloride‒cellulose acetate membrane interface.
format Article
id doaj-art-bbe946a01eb741b7ad6c60775c7c011b
institution Kabale University
issn 2813-1010
language English
publishDate 2025-02-01
publisher Frontiers Media S.A.
record_format Article
series Frontiers in Membrane Science and Technology
spelling doaj-art-bbe946a01eb741b7ad6c60775c7c011b2025-02-04T06:31:50ZengFrontiers Media S.A.Frontiers in Membrane Science and Technology2813-10102025-02-01410.3389/frmst.2025.15135911513591Transport in reverse osmosis membranes: observations and comments on the pore flow model versus the solution‒diffusion modelTakeshi Matsuura0Michael D. Guiver1Woei Jye Lau2Ahmad Fauzi Ismail3Department of Chemical and Biological Engineering, University of Ottawa, Ottawa, ON, CanadaState Key Laboratory of Engines, School of Mechanical Engineering, Tianjin University, Tianjin, ChinaAdvanced Membrane Technology Research Centre, Universiti Teknologi Malaysia, Johor Bahru, Johor, MalaysiaAdvanced Membrane Technology Research Centre, Universiti Teknologi Malaysia, Johor Bahru, Johor, MalaysiaSixty-four years have passed since the announcement of the cellulose acetate membrane for seawater desalination by Loeb and Sourirajan at UCLA on 23 Aug 1960. Reverse osmosis (RO) is now well established as a process for desalination of seawater, brackish water, as well as for wastewater treatment. The number of research papers on RO is growing. In contrast to the numerous publications on RO membrane preparation and applications, studies on transport mechanisms have been largely neglected. However, this changed recently when M. Elimelech’s research group from Yale University published several papers challenging the applicability of the solution‒diffusion (S‒D) model. Especially, in the most recent paper published in 2024, they have shown seven reasons why the well-accepted S‒D model appears to be wrong. It is interesting to note that, according to Srinivasa Sourirajan, one of the co-inventors of cellulose acetate RO membrane, their work was guided by the Preferential Sorption‒Capillary Flow model. Moreover, he wrote that this pore model was based on the presence of a pure water layer at the salt solution‒air interface, which could be predicted by the Gibbs Adsorption Isotherm. The purpose of this short communication is to present some observations and discussion in response to the 2024 paper published by Elimelech’s group in Desalination journal. In addition, the Gibbs Adsorption Isotherm was revisited to examine if there is a pure water layer at the sodium chloride‒cellulose acetate membrane interface.https://www.frontiersin.org/articles/10.3389/frmst.2025.1513591/fullreverse osmosissolution-diffusion modelGibbs Adsorption Isothermpreferential sorption-capillary flow modelmembrane desalination
spellingShingle Takeshi Matsuura
Michael D. Guiver
Woei Jye Lau
Ahmad Fauzi Ismail
Transport in reverse osmosis membranes: observations and comments on the pore flow model versus the solution‒diffusion model
Frontiers in Membrane Science and Technology
reverse osmosis
solution-diffusion model
Gibbs Adsorption Isotherm
preferential sorption-capillary flow model
membrane desalination
title Transport in reverse osmosis membranes: observations and comments on the pore flow model versus the solution‒diffusion model
title_full Transport in reverse osmosis membranes: observations and comments on the pore flow model versus the solution‒diffusion model
title_fullStr Transport in reverse osmosis membranes: observations and comments on the pore flow model versus the solution‒diffusion model
title_full_unstemmed Transport in reverse osmosis membranes: observations and comments on the pore flow model versus the solution‒diffusion model
title_short Transport in reverse osmosis membranes: observations and comments on the pore flow model versus the solution‒diffusion model
title_sort transport in reverse osmosis membranes observations and comments on the pore flow model versus the solution diffusion model
topic reverse osmosis
solution-diffusion model
Gibbs Adsorption Isotherm
preferential sorption-capillary flow model
membrane desalination
url https://www.frontiersin.org/articles/10.3389/frmst.2025.1513591/full
work_keys_str_mv AT takeshimatsuura transportinreverseosmosismembranesobservationsandcommentsontheporeflowmodelversusthesolutiondiffusionmodel
AT michaeldguiver transportinreverseosmosismembranesobservationsandcommentsontheporeflowmodelversusthesolutiondiffusionmodel
AT woeijyelau transportinreverseosmosismembranesobservationsandcommentsontheporeflowmodelversusthesolutiondiffusionmodel
AT ahmadfauziismail transportinreverseosmosismembranesobservationsandcommentsontheporeflowmodelversusthesolutiondiffusionmodel