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dc.contributor.authorAsensio Delgado, Salvador 
dc.contributor.authorPardo Pardo, Fernando 
dc.contributor.authorZarca Lago, Gabriel 
dc.contributor.authorUrtiaga Mendia, Ana María 
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2021-09-30T11:14:00Z
dc.date.available2021-09-30T11:14:00Z
dc.date.issued2021-12-01
dc.identifier.issn1383-5866
dc.identifier.issn1873-3794
dc.identifier.otherPID2019-105827RB-I00es_ES
dc.identifier.urihttp://hdl.handle.net/10902/22608
dc.description.abstractInterest in recovering and reclaiming refrigerant gases is growing as a consequence of increasing concern about the high global warming potential of some hydrofluorocarbons (HFCs). However, advanced separation processes, like extractive distillation, are required to selectively separate azeotropic and close-boiling refrigerant mixtures. In this regard, ionic liquids (ILs) arise as promising entrainers because of their favorable properties, including nonvolatility and good HFC solubility selectivity. The aim of this review is to become a reference text for the research and design of novel separation processes for mixtures of fluorinated gases based on the use of ILs. We include an extensive compilation of publications on equilibrium, mass transport, and absorption and membrane separation related to the use of ILs to selectively separate, not only the most relevant refrigerants employed nowadays, namely, HFCs, hydrofluoroolefins, and hydrochlorofluoroolefins, but also other relevant refrigerant families, such as chlorofluorocarbons, hydrochlorofluorocarbons, and perfluorocarbons. The UC-RAIL database provided as Supplementary Information compiles more than 5000 data points that are comprehensively analyzed in the review focusing on process design. Finally, we provide a set of directions that lead to the recovery of fluorinated refrigerant gases, to shift the refrigeration and air conditioning sector towards a more circular economy.es_ES
dc.description.sponsorshipThe authors fully acknowledge the financial support received from Project KET4F-Gas-SOE2/P1/P0823, which is co-financed by the European Regional Development Fund within the framework of Interreg Sudoe Programme, and project PID2019-105827RB-I00 – Agencia Estatal de Investigacion, Spain. S. A.-D. and F. P. acknowledge the FPU grant (18/03939) and the post-doctoral fellowship (FJCI-2017-32884 Juan de la Cierva Formacion), respectively, awarded by the Spanish Ministry of Science and Innovation. Marta Romay’s graphical abstract is gratefully acknowledged.es_ES
dc.format.extent28 p.es_ES
dc.language.isoenges_ES
dc.publisherElsevieres_ES
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internationales_ES
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.sourceSeparation and Purification Technology, 2021, 276, 119363es_ES
dc.subject.otherHydrofluorocarbonses_ES
dc.subject.otherHydrofluoroolefinses_ES
dc.subject.otherIonic liquidses_ES
dc.subject.otherSolubilityes_ES
dc.subject.otherDiffusivityes_ES
dc.subject.otherMembrane separationes_ES
dc.titleAbsorption separation of fluorinated refrigerant gases with ionic liquids: Equilibrium, mass transport, and process designes_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.relation.publisherVersionhttps://doi.org/10.1016/j.seppur.2021.119363es_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.1016/j.seppur.2021.119363
dc.type.versionpublishedVersiones_ES


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Attribution-NonCommercial-NoDerivatives 4.0 InternationalExcepto si se señala otra cosa, la licencia del ítem se describe como Attribution-NonCommercial-NoDerivatives 4.0 International