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dc.contributor.authorAbejón Elías, Ricardo 
dc.contributor.authorSaidani, Hafedh
dc.contributor.authorDeratani, André
dc.contributor.authorRichard, Christophe
dc.contributor.authorSánchez Marcano, José
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2019-12-11T17:08:38Z
dc.date.available2019-12-11T17:08:38Z
dc.date.issued2019-11-26
dc.identifier.issn2077-0375
dc.identifier.otherCTQ2014-56820-JINes_ES
dc.identifier.urihttp://hdl.handle.net/10902/17480
dc.description.abstractSweeping gas membrane distillation (SGMD) is a useful option for dehydration of aqueous solvent solutions. This study investigated the technical viability and competitiveness of the use of SGMD to concentrate aqueous solutions of 1,3-dimethyl-2-imidazolidinone (DMI), a dipolar aprotic solvent. The concentration from 30% to 50% of aqueous DMI solutions was attained in a bench installation with Liqui-Cel SuperPhobic® hollow-fiber membranes. The selected membranes resulted in low vapor flux (below 0.15 kg/h·m2) but were also effective for minimization of DMI losses through the membranes, since these losses were maintained below 1% of the evaporated water flux. This fact implied that more than 99.2% of the DMI fed to the system was recovered in the produced concentrated solution. The influence of temperature and flowrate of the feed and sweep gas streams was analyzed to develop simple empirical models that represented the vapor permeation and DMI losses through the hollow-fiber membranes. The proposed models were successfully applied to the scaling-up of the process with a preliminary multi-objective optimization of the process based on the simultaneous minimization of the total membrane area, the heat requirement and the air consumption. Maximal feed temperature and air flowrate (and the corresponding high operation costs) were optimal conditions, but the excessive membrane area required implied an uncompetitive alternative for direct industrial application.es_ES
dc.description.sponsorshipR. Abejón acknowledges the financial support from the Spanish Ministry of Economy and Competitiveness (MINECO) through CTQ2014-56820-JIN Project, co-financed by FEDER funds. KERMEL is acknowledged for the financial support of this research.es_ES
dc.format.extent16 p.es_ES
dc.language.isoenges_ES
dc.publisherMDPIes_ES
dc.rights© 2019 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license.es_ES
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/*
dc.sourceMembranes, 2019, 9(12), 158es_ES
dc.subject.otherSweeping gas membrane distillationes_ES
dc.subject.other1,3-dimethyl-2-imidazolidinonees_ES
dc.subject.otherSolvent dehydrationes_ES
dc.subject.otherHollow-fiber membranees_ES
dc.subject.otherMulti-objective optimizationes_ES
dc.titleConcentration of 1,3-dimethyl-2-imidazolidinone in aqueous solutions by sweeping gas membrane distillation: from bench to industrial scalees_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.3390/membranes9120158
dc.type.versionpublishedVersiones_ES


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© 2019 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license.Excepto si se señala otra cosa, la licencia del ítem se describe como © 2019 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license.