Transport of organic solutes in ion-exchange membranes: Mechanisms and influence of solvent ionic composition.

Influence of salts Ion-exchange membranes Organic solutes Selective separation Transport mechanism

Journal

Water research
ISSN: 1879-2448
Titre abrégé: Water Res
Pays: England
ID NLM: 0105072

Informations de publication

Date de publication:
15 Feb 2021
Historique:
received: 18 08 2020
revised: 28 11 2020
accepted: 14 12 2020
pubmed: 3 1 2021
medline: 29 1 2021
entrez: 2 1 2021
Statut: ppublish

Résumé

Ion-exchange membrane (IEM)-based processes are used in the industry or in the drinking water production to achieve selective separation. The transport mechanisms of organic solutes/micropollutants (i.e., paracetamol, clofibric acid, and atenolol) at a single-membrane level in diffusion cells were similar to that of salts (i.e., diffusion, convection, and electromigration). The presence of an equal concentration of salts at both sides of the membrane slightly decreased the transport of organics due to lower diffusion coefficients of organics in salts and the increase of hindrance and/or decrease of partitioning in the membrane phase. In the presence of a salt gradient, diffusion was the main transport mechanism for non-charged organics, while the counter-transport of salts promoted the transport of charged organics through electromigration (electroneutrality). Conversely, the co-transport of salts hindered the transport of charged organics, where diffusion was the main transport mechanism of the latter. Although convection played a role in the transport of non-charged organics, its influence on the charged solutes was minimal due to the dominant electromigration. Positron annihilation lifetime spectroscopy showed a bimodal size distribution of free-volume elements of IEMs, with both classes of free-volume elements contributing to salt transport, while larger organics can only transport through the larger class.

Identifiants

pubmed: 33387949
pii: S0043-1354(20)31289-6
doi: 10.1016/j.watres.2020.116756
pii:
doi:

Substances chimiques

Drinking Water 0
Solutions 0
Solvents 0

Types de publication

Journal Article

Langues

eng

Sous-ensembles de citation

IM

Pagination

116756

Informations de copyright

Copyright © 2020. Published by Elsevier Ltd.

Déclaration de conflit d'intérêts

Declaration of Competing Interest The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Auteurs

Lingshan Ma (L)

Particle and Interfacial Technology Group, Ghent University, Belgium. Electronic address: lingshan.ma@ugent.be.

Leonardo Gutierrez (L)

Particle and Interfacial Technology Group, Ghent University, Belgium; Facultad del Mar y Medio Ambiente, Universidad del Pacifico, Ecuador.

Rhea Verbeke (R)

Membrane Technology Group, Centre for Membrane Separations, Adsorption, Catalysis and Spectroscopy for Sustainable Solutions, KU Leuven, Belgium.

Arnout D'Haese (A)

Particle and Interfacial Technology Group, Ghent University, Belgium.

Muhammad Waqas (M)

Particle and Interfacial Technology Group, Ghent University, Belgium.

Marcel Dickmann (M)

Institut für Angewandte Physik und Messtechnik, Universität der Bundeswehr München, Germany.

Ricardo Helm (R)

Institut für Angewandte Physik und Messtechnik, Universität der Bundeswehr München, Germany.

Ivo Vankelecom (I)

Membrane Technology Group, Centre for Membrane Separations, Adsorption, Catalysis and Spectroscopy for Sustainable Solutions, KU Leuven, Belgium.

Arne Verliefde (A)

Particle and Interfacial Technology Group, Ghent University, Belgium.

Emile Cornelissen (E)

Particle and Interfacial Technology Group, Ghent University, Belgium; KWR Water Research Institute, Netherlands. Electronic address: Emile.Cornelissen@UGent.be.

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Classifications MeSH