Please use this identifier to cite or link to this item: http://dspace.utpl.edu.ec/handle/123456789/69535
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dc.contributor.authorArroyo, Fátimaes_ES
dc.contributor.authorMorillo, Josées_ES
dc.contributor.authorUsero, Josées_ES
dc.contributor.authorRosado, Danieles_ES
dc.contributor.authorEl Bakouri, Hichames_ES
dc.date.accessioned2024-10-25T22:33:35Z-
dc.date.available2024-10-25T22:33:35Z-
dc.date.issued2019es_ES
dc.identifier.issn00119164es_ES
dc.identifier.other10.1016/j.desal.2019.114073es_ES
dc.identifier.otherhttps://www.scopus.com/inward/record.uri?eid=2-s2.0-85069544497&doi=10.1016%2fj.desal.2019.114073&partnerID=40&md5=7b5b94c3e8d3a792366c8f9fb9b69432es_ES
dc.identifier.otherCODEN: DSLNAes_ES
dc.identifier.urihttps://dspace.utpl.edu.ec/bitstreams/2-s2.0-85069544497.pdfes_ES
dc.identifier.urihttp://dspace.utpl.edu.ec/handle/123456789/69535-
dc.description.abstractThis study evaluated the possibility of recovering lithium from brines by ion-exchange procedures. Three commercial ion-exchange resins were studied: K2629, TP207 and TP208. Different tests have been carried out with artificial solutions and real brines. In addition, tests were carried out for Li elution, regeneration of the resins and reuse of the regenerated resins. Sorption kinetics of lithium retention onto the three resins were studied and experimental data fit to the pseudo-second order kinetics model. Equilibrium sorption data were analysed by the Langmuir, Freundlich, Temkin and Dubinin-Radushkevic approaches. Langmuir isotherm model best described the process. The order of retention capacity of the amendments was TP207 > K2629 > TP208. Recovering Li from brines was possible with ion exchange resins. In solutions containing only Li, the three resins studied had high retention yields (>95%). The presence of other ions in solution negatively affects the behavior of the three resins studied. Regarding desorption, yields obtained ranged 73.8% - 89.8%, reaching the highest (>80%) using 4 M HCl as eluting solution. Regenerated resins showed similar yields to those obtained when the resin is used for the first time. © 2019 Elsevier B.V.es_ES
dc.language.isoenges_ES
dc.sourceVolume: 468es_ES
dc.sourceScopuses_ES
dc.sourceDesalination, Volume: 468es_ES
dc.subjectBrineses_ES
dc.subjectChlorine compoundses_ES
dc.subjectDesalinationes_ES
dc.subjectIon exchange resinses_ES
dc.subjectIonses_ES
dc.subjectIsothermses_ES
dc.subjectLithiumes_ES
dc.subjectRecoveryes_ES
dc.subjectData fitses_ES
dc.subjectEquilibrium sorptiones_ES
dc.subjectFreundliches_ES
dc.subjectLangmuir isotherm modelses_ES
dc.subjectLithium recoverieses_ES
dc.subjectPseudo second order kineticses_ES
dc.subjectRetention capacityes_ES
dc.subjectSorption kineticses_ES
dc.subjectbrinees_ES
dc.subjectdesalinationes_ES
dc.subjection exchangees_ES
dc.subjectlithiumes_ES
dc.subjectresines_ES
dc.subjectIon exchangees_ES
dc.titleLithium recovery from desalination brines using specific ion-exchange resinses_ES
dc.typeArticlees_ES
dc.publisherElsevier B.V.es_ES
Appears in Collections:Artículos de revistas Científicas

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