Mostrar el registro sencillo

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.accessioned2020-06-16T07:36:13Z
dc.date.available2022-10-15T23:11:28Z
dc.date.issued2020-10-15
dc.identifier.issn1383-5866
dc.identifier.issn1873-3794
dc.identifier.urihttp://hdl.handle.net/10902/18693
dc.description.abstractThe separation of hydrofluorocarbons (HFCs) and hydrofluoroolefins (HFOs) from novel refrigerant blends will become essential to boost the recycling of these compounds and drastically reduce the emission of HFCs, which are powerful greenhouse gases. In this work, the use of ionic liquids (ILs) as solvent media is explored to perform the selective separation of HFC/HFO refrigerant mixtures composed of the HFCs R32 (difluoromethane) and R134a (1,1,1,2-tetrafluoroethane) and the HFO R1234yf (2,3,3,3-tetrafluoropropene). The low-viscosity IL 1-ethyl-3-methylimidazolium thiocyanate, [C2mim][SCN], is selected as separation agent to prove that small and non-fluorinated ILs, with lower hydrogen bonding capability than other ILs, can provide enhanced solubility selectivity and mass transport properties for the selective separation of HFC/HFO refrigerant blends. The phase behavior of IL-refrigerant systems is determined at temperatures between 283.15 and 313.15 K and pressures up to 0.7 MPa. Results are parametrized according to the NRTL activity model and the separation selectivity is assessed in terms of Henry?s law constants, solvation enthalpies and entropies, infinite dilution coefficients, Gibbs free energy of mixing, and ideal and noncompetitive selectivity. Results show superior HFC/HFO solubility selectivity in [C2mim][SCN] compared to other ILs due to unfavorable entropic effects that difficult the solvation of large molecules such as R1234yf.es_ES
dc.description.sponsorshipThis research is supported by Project KET4F-Gas – SOE2/P1/P0823, which is co-financed by the European Regional Development Fund within the framework of Interreg Sudoe Programme. S. A-D. and F.P acknowledge the FPU grant (18/03939) and the post-doctoral fellowship (FJCI-2017-32884 Juan de la Cierva Formación), respectively, awarded by the Spanish Ministry of Science, Innovation and Universities.es_ES
dc.format.extent30 p.es_ES
dc.language.isoenges_ES
dc.publisherElsevieres_ES
dc.rights© 2020 This manuscript version is made available under the CC-BY-NC-ND 4.0 licensees_ES
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.sourceSeparation and Purification Technology, 2020, 249, 117136es_ES
dc.subject.otherDifluoromethanees_ES
dc.subject.otherIonic liquides_ES
dc.subject.otherNRTL modeles_ES
dc.subject.otherSolubility selectivityes_ES
dc.subject.other1,1,1,2-tetrafluoroethanees_ES
dc.subject.other2,3,3,3-tetrafluoropropenees_ES
dc.titleEnhanced absorption separation of hydrofluorocarbon/hydrofluoroolefin refrigerant blends using ionic liquidses_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.relation.publisherVersionhttps://doi.org/10.1016/j.seppur.2020.117136es_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.1016/j.seppur.2020.117136
dc.type.versionacceptedVersiones_ES


Ficheros en el ítem

Thumbnail

Este ítem aparece en la(s) siguiente(s) colección(ones)

Mostrar el registro sencillo

© 2020 This manuscript version is made available under the CC-BY-NC-ND 4.0 licenseExcepto si se señala otra cosa, la licencia del ítem se describe como © 2020 This manuscript version is made available under the CC-BY-NC-ND 4.0 license