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dc.contributor.authorPardo Pardo, Fernando 
dc.contributor.authorGutiérrez Hernández, Sergio Valentín 
dc.contributor.authorRodríguez San Miguel, Paula 
dc.contributor.authorZarca Lago, Gabriel 
dc.contributor.authorUrtiaga Mendia, Ana María 
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2023-05-31T16:34:04Z
dc.date.available2023-05-31T16:34:04Z
dc.date.issued2023-09-01
dc.identifier.issn1383-5866
dc.identifier.issn1873-3794
dc.identifier.otherPID2019-105827RB-I00es_ES
dc.identifier.urihttps://hdl.handle.net/10902/29174
dc.description.abstractDifluoromethane (R-32) is a hydrofluorocarbon (HFC) that has been massively used over the last 30 years in refrigeration and air conditioning as a primary component of azeotropic or close boiling refrigerant mixtures. Despite environmental directives commanded to drastically reduce the use of HFCs, R-32 has excellent thermodynamic properties and moderate GWP, thus its recovery from depleted mixtures collected from end-of-life equipment is sought to synthesize alternative low-GWP refrigerant blends. Membrane separation using composite polymer/ionic liquid membranes based on poly-ether-block-amide have shown potential to separate R-32 from other fluorinated hydrocarbons, yet the development of this type of composite membranes still remains at laboratory scale. In this work, a spray coating technique was successfully applied to create defect-free thin selective layers of neat Pebax®1657, Pebax®1657/40 wt% [C2C1im][BF4] and Pebax®1657/40 wt% [C2C1im][SCN] coated on porous PVDF substrates. This methodology was transferred from the lab-scale tests (12.6 cm2) to a custom pilot set-up (300 cm2). The pilot results confirmed the superior performance and stability of [C2C1im][SCN]-based membranes, which allowed the recovery of up to 64.3% and 67.1% R-32 from the refrigerant mixtures R-410A (69.8 mol % R-32 and 30.2 mol % R-125) and R-454B (82.1 mol % R-32 and 17.9 mol % R-1234yf) at 6 bar, increasing the R-32 permeate concentration up to 89.6 and 95.9 mol %, respectively. These results highlight the need to expand the knowledge of this type of gas separation membranes towards thinner and defect-free selective dense layers with the purpose of approaching their real applications.es_ES
dc.description.sponsorshipThis research is supported by Project KET4F-Gas – SOE2/P1/P0823, Project PID2019-105827RB-I00 funded by MCIN/AEI/10.1039/501100011033 (Spain), and project LIFE4F-Gases (LIFE20CCM/ES/001748) co-funded by the European Union LIFE programme. F.P. acknowledges the post-doctoral fellowship (IJC2020-043134-I, ‘Juan de la Cierva Incorporación’) funded by the Spanish Ministry of Science and Innovation MCIN/AEI/10.13039/501100011033 and the European Union NextGenerationEU/PRTR. S. V. G. acknowledges the pre-doctoral fellowship FPI PRE2020-093568, funded by the Spanish Ministry of Science and Innovation MCIN/AEI/10.13039/501100011033 and by “ESF Investing in your future”.es_ES
dc.format.extent11 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, 2023, 320, 124115es_ES
dc.subject.otherThin film compositees_ES
dc.subject.otherSpray coatinges_ES
dc.subject.otherFluorinated hydrocarbones_ES
dc.subject.otherGas separationes_ES
dc.subject.otherScale-upes_ES
dc.subject.otherPebax membranees_ES
dc.titlePolymer/ionic liquid pilot scale membrane prototype for the recovery of difluoromethane (R-32) from refrigerant mixtureses_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.relation.publisherVersionhttps://doi.org/10.1016/j.seppur.2023.124115es_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.1016/j.seppur.2023.124115
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