dc.contributor.author | Vadillo Abascal, José Manuel | |
dc.contributor.author | Gómez Coma, Lucía | |
dc.contributor.author | Garea Vázquez, Aurora | |
dc.contributor.author | Irabien Gulías, Ángel | |
dc.contributor.other | Universidad de Cantabria | es_ES |
dc.date.accessioned | 2020-09-28T15:11:57Z | |
dc.date.available | 2020-09-28T15:11:57Z | |
dc.date.issued | 2020-09-14 | |
dc.identifier.issn | 2077-0375 | |
dc.identifier.other | CTQ2016-76231-C2 | es_ES |
dc.identifier.other | PID2019-108136RB-C31 | es_ES |
dc.identifier.uri | http://hdl.handle.net/10902/19209 | |
dc.description.abstract | In 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.sponsorship | This 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.extent | 25 p. | es_ES |
dc.language.iso | eng | es_ES |
dc.publisher | MDPI | es_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.uri | http://creativecommons.org/licenses/by/4.0/ | * |
dc.source | Membranes, 2020, 10(9), 234 | es_ES |
dc.subject.other | CO2 desorption | es_ES |
dc.subject.other | Membrane vacuum regeneration | es_ES |
dc.subject.other | Hollow fiber membrane contactor | es_ES |
dc.subject.other | Ionic liquid [emim][Ac] | es_ES |
dc.subject.other | Modeling | es_ES |
dc.title | CO2 desorption performance from imidazolium ionic liquids by membrane vacuum regeneration technology | es_ES |
dc.type | info:eu-repo/semantics/article | es_ES |
dc.rights.accessRights | openAccess | es_ES |
dc.identifier.DOI | 10.3390/membranes10090234 | |
dc.type.version | publishedVersion | es_ES |