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dc.contributor.authorHerrero González, Marta 
dc.contributor.authorDíaz Guridi, Pedro 
dc.contributor.authorDomínguez Ramos, Antonio 
dc.contributor.authorIrabien Gulías, Ángel 
dc.contributor.authorIbáñez Mendizábal, Raquel 
dc.contributor.otherUniversidad de Cantabriaes_ES
dc.date.accessioned2020-06-08T09:18:14Z
dc.date.available2022-07-01T23:19:37Z
dc.date.issued2020-07-01
dc.identifier.issn1383-5866
dc.identifier.issn1873-3794
dc.identifier.otherCTM2017-87850-Res_ES
dc.identifier.urihttp://hdl.handle.net/10902/18632
dc.description.abstractElectromembrane technologies, such as electrodialysis with bipolar membranes (EDBM) have been widely proposed for the treatment and valorization of seawater reverse osmosis (SWRO) concentrated streams. The EDBM technology applied to brines produces acids (HCl) and bases (NaOH) with just two inputs: electric energy and brine. Thus, the reagents self-supply to the SWRO plant could be achieved, which definitively fits the principles of the Circular Economy. However, previous works have shown low concentration values of the produced acids and bases by EDBM, which undoubtedly hampers the possibility of its use in the SWRO plant. Therefore, the aim of the present work is to demonstrate the viability of a new strategy to valorise SWRO brine producing commercial HCl at 35 wt.% by means of the integration of EDBM technology under constant (galvanostatic, equivalent to the use of electrical energy from the grid mix) and variable current intensity (equivalent to the use of PV solar energy) and azeotropic distillation. Concentrations of HCl and NaOH up to ~3.3 mol·L-1 and ~3.6 mol·L-1 are obtained respectively, which are almost 50% higher than any other reported in the literature so far using this technology. The specific energy consumption of the EDBM unit was in the range of 21.8 kWh·kg-1 of HCl and 43.5 kWh·kg-1 of HCl, being dependant on the average applied current density. These HCl concentrations, although being acceptable for internal use in the SWRO plant, did not reach commercial levels (35 wt.% of HCl), so a further concentration stage using distillation has been evaluated through simulation. Minimum values of the overall EDBM plus distillation process specific energy consumption (SECOV) was between ~40 kWh·kg-1 and ~60 kWh·kg-1 of HCl. Moreover, the environmental burdens associated with the energy consumption are quantified in terms of the carbon footprint (CF). Although the SECOV is slightly higher, the use of PV solar energy instead of the grid mix let the process to provide a better environmental performance. The renewable alternative provides values between 1.61 kg CO2-eq.·kg-1 of HCl (full PV solar energy) and 6.97 kg CO2-eq.·kg-1 of HCl (PV solar energy and steam).es_ES
dc.description.sponsorshipFinancial support from the Spanish Ministry of Science, Innovation and Universities under project CTM2017-87850-R is gratefully acknowledged. Marta Herrero-Gonzalez thanks the Spanish Ministry of Economy and Competitiveness for FPI grant BES-2015-07350.es_ES
dc.format.extent28 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, 242, 116785es_ES
dc.subject.otherConcentrates valorizationes_ES
dc.subject.otherBipolar membrane electrodialysises_ES
dc.subject.otherPhotovoltaic solar energyes_ES
dc.subject.otherAcid productiones_ES
dc.subject.otherCircular economyes_ES
dc.titleHighly concentrated HCl and NaOH from brines using electrodialysis with bipolar membraneses_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.relation.publisherVersionhttps://doi.org/10.1016/j.seppur.2020.116785es_ES
dc.rights.accessRightsopenAccesses_ES
dc.identifier.DOI10.1016/j.seppur.2020.116785
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