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dc.contributor.authorVadillo Abascal, José Manuel 
dc.contributor.authorGómez Coma, Lucía 
dc.contributor.authorGarea Vázquez, Aurora 
dc.contributor.authorIrabien Gulías, Ángel 
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2020-09-28T15:11:57Z
dc.date.available2020-09-28T15:11:57Z
dc.date.issued2020-09-14
dc.identifier.issn2077-0375
dc.identifier.otherCTQ2016-76231-C2es_ES
dc.identifier.otherPID2019-108136RB-C31es_ES
dc.identifier.urihttp://hdl.handle.net/10902/19209
dc.description.abstractIn this work, the membrane vacuum regeneration (MVR) process was considered as a promising technology for solvent regeneration in post-combustion CO2 capture and utilization (CCU) since high purity CO2 is needed for a technical valorization approach. First, a desorption test by MVR using polypropylene hollow fiber membrane contactor (PP-HFMC) was carried out in order to evaluate the behavior of physical and physico-chemical absorbents in terms of CO2 solubility and regeneration efficiency. The ionic liquid 1-ethyl-3-methylimidazolium acetate, [emim][Ac], was presented as a suitable alternative to conventional amine-based absorbents. Then, a rigorous two-dimensional mathematical model of the MVR process in a HFMC was developed based on a pseudo-steady-state to understand the influence of the solvent regeneration process in the absorption–desorption process. CO2 absorption–desorption experiments in PP-HFMC at different operating conditions for desorption, varying vacuum pressure and temperature, were used for model validation. Results showed that MVR efficiency increased from 3% at room temperature and 500 mbar to 95% at 310K and 40 mbar vacuum. Moreover, model deviation studies were carried out using sensitivity analysis of Henry’s constant and pre-exponential factor of chemical interaction, thus as to contribute to the knowledge in further works.es_ES
dc.description.sponsorshipThis work was funded by the Spanish Ministry of Economy, Industry and Competitiveness (MINECO), project CTQ2016-76231-C2-(AEI/FEDER, UE) and project PID2019-108136RB-C31).es_ES
dc.format.extent25 p.es_ES
dc.language.isoenges_ES
dc.publisherMDPIes_ES
dc.rights© 2020 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, 2020, 10(9), 234es_ES
dc.subject.otherCO2 desorptiones_ES
dc.subject.otherMembrane vacuum regenerationes_ES
dc.subject.otherHollow fiber membrane contactores_ES
dc.subject.otherIonic liquid [emim][Ac]es_ES
dc.subject.otherModelinges_ES
dc.titleCO2 desorption performance from imidazolium ionic liquids by membrane vacuum regeneration technologyes_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.3390/membranes10090234
dc.type.versionpublishedVersiones_ES


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© 2020 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 © 2020 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.