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dc.contributor.authorUlloa Guntiñas, Laura 
dc.contributor.authorMartínez Minchero, Marina 
dc.contributor.authorBringas Elizalde, Eugenio 
dc.contributor.authorCobo García, Adolfo 
dc.contributor.authorSan Román San Emeterio, María Fresnedo 
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2020-09-21T11:02:56Z
dc.date.available2022-12-31T00:13:24Z
dc.date.issued2020-12-15
dc.identifier.issn1383-5866
dc.identifier.issn1873-3794
dc.identifier.otherCTM2017-87740-Res_ES
dc.identifier.otherRTI2018-093310-B-Ies_ES
dc.identifier.otherTEC2016-76021-C2-2-Res_ES
dc.identifier.urihttp://hdl.handle.net/10902/19139
dc.description.abstractThe management of spent acids containing heavy metals has been traditionally carried out by neutralization-precipitation technologies that often fail to provide the required selectivity for metal recovery. This work proposed a split elution process using H2SO4 and NH4OH solutions to regenerate bispicolylamine-based chelating resins (Puromet™ MTS9600) employed in a previous work to separate nickel and copper from spent sulfuric acid effluents. Operation variables namely S/L ratio, concentration of the regeneration agents and process configuration were analysed to select the best conditions to optimize the metal unloading and their selective recovery in independent solutions. It was found that 43% of nickel was eluted from the resin by H2SO4 2.0 M and recovered with purities of 98% while 47% of copper was desorbed with NH4OH 2.0 M and recovered with purities of 97%. The long-term assessment evidenced that copper removal and metal recovery were not affected after 10 adsorption-regeneration cycles, while the nickel adsorption efficacy decreased about 10%.es_ES
dc.description.sponsorshipThis research was developed in the framework of the projects CTM2017-87740-R (Spanish Ministry of Science, Innovation and Universities), RTI2018-093310-B-I00 (Spanish Ministry of Science, Innovation and Universities), TEC2016-76021-C2-2-R) (AEI/FEDER, UE & PID2019-107270RB-C21/AEI/10.13039/501100011033), and grant BES-2017-080076.es_ES
dc.format.extent39 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, 253, 117516es_ES
dc.subject.otherIndustrial spent acidses_ES
dc.subject.otherHeavy metalses_ES
dc.subject.otherAdsorptiones_ES
dc.subject.otherChelating resinses_ES
dc.subject.otherRegenerationes_ES
dc.titleSplit regeneration of chelating resins for the selective recovery of nickel and copperes_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.relation.publisherVersionhttps://doi.org/10.1016/j.seppur.2020.117516es_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.1016/j.seppur.2020.117516
dc.type.versionacceptedVersiones_ES


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© 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