Mostrar el registro sencillo

dc.contributor.authorFernández González, Carolina 
dc.contributor.authorDomínguez Ramos, Antonio 
dc.contributor.authorIbáñez Mendizábal, Raquel 
dc.contributor.authorChen, Yongsheng
dc.contributor.authorIrabien Gulías, Ángel 
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2018-02-14T14:18:20Z
dc.date.available2019-03-31T02:45:12Z
dc.date.issued2017-03-16
dc.identifier.issn0011-9164
dc.identifier.other2014-57833-Res_ES
dc.identifier.otherCTQ2013-48280-C3-1-R-Des_ES
dc.identifier.urihttp://hdl.handle.net/10902/13038
dc.description.abstractElectrodialysis with bipolar membranes (EDBM) is a promising technology that simultaneously treats and valorizes desalination brines into acids and bases. An important techno-economic challenge of EDBM in this application is the purity of the products, related to the need for more selective ion exchange membranes with good stability working with acids and bases. This work presents the results of the treatment of model desalination brines by EDBM using nanocomposite anion exchange membranes in order to reduce the sulfate content as the main impurity in the acid stack. These membranes are composed by polyethylene, polypropylene, sulfonated poly (2,6-dimethyl-1,4-phenylene oxide) (sPPO) and different loads of Fe2O3-SO42 − nanoparticles. A reduction of the sulfate content in the acid stack was observed when using nanocomposite membranes. The stability of these membranes was evaluated measuring the Cl−/SO42 − selectivity after 31 h, 62 h and 93 h of operation. FTIR spectra before and after 93 h of operation also confirmed the stability of the membranes. The evolution of the main impurities in the acid and the base stacks versus time when applying different current densities is included and related to current efficiency. An estimation of the proton and hydroxyl ions leakages at the different current densities is also presented.es_ES
dc.description.sponsorshipFinancial support from MICINN under project 2014-57833-R and CTQ2013-48280-C3-1-R-D is gratefully acknowledged. The author thanks the Ministry of Education for FPI grant BES-2012-053461 and the scholarship EEBB-I-15-10268 for the stay at the Georgia Institute of Technology. In addition, this research was partially supported by the U.S. National Science Foundation CBET-1235166.es_ES
dc.format.extent23 p.es_ES
dc.language.isoenges_ES
dc.publisherElsevieres_ES
dc.rights© 2017, Elsevier. Licensed under the Creative Commons Reconocimiento-NoComercial-SinObraDerivadaes_ES
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es/*
dc.sourceDesalination, 2017, 406, 16-24es_ES
dc.subject.otherValorizationes_ES
dc.subject.otherRecoveryes_ES
dc.subject.otherBipolar membrane electrodialysises_ES
dc.subject.otherNanocomposite anion exchange membraneses_ES
dc.titleValorization of desalination brines by electrodialysis with bipolar membranes using nanocomposite anion exchange membraneses_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.relation.publisherVersionhttps://doi.org/10.1016/j.desal.2016.07.033es_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.1016/j.desal.2016.07.033
dc.type.versionacceptedVersiones_ES


Ficheros en el ítem

Thumbnail

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

Mostrar el registro sencillo

© 2017, Elsevier. Licensed under the Creative Commons Reconocimiento-NoComercial-SinObraDerivadaExcepto si se señala otra cosa, la licencia del ítem se describe como © 2017, Elsevier. Licensed under the Creative Commons Reconocimiento-NoComercial-SinObraDerivada