Show simple item record

dc.contributor.authorReig i Amat, Mònica
dc.contributor.authorCasas Garriga, Sandra
dc.contributor.authorAladjem, Carlos
dc.contributor.authorValderrama Ángel, César Alberto
dc.contributor.authorGibert Agulló, Oriol
dc.contributor.authorValero Cervera, Fernando
dc.contributor.authorMiguel Centeno, Carlos
dc.contributor.authorLarrotcha, Enric
dc.contributor.authorCortina Pallás, José Luis
dc.contributor.otherUniversitat Politècnica de Catalunya. Departament d'Enginyeria Química
dc.date.accessioned2014-07-08T08:05:07Z
dc.date.created2014-06-02
dc.date.issued2014-06-02
dc.identifier.citationReig, M. [et al.]. Concentration of NaCl from seawater reverse osmosis brines for the chlor-alkali industry by electrodialysis. "Desalination", 02 Juny 2014, vol. 342, p. 107-117.
dc.identifier.issn0011-9164
dc.identifier.urihttp://hdl.handle.net/2117/23419
dc.description.abstractCurrently, numerous studies are focused on the valorisation of seawater desalination reverse osmosis brines. Electrodialysis can be used to concentrate one of the primary components (NaCI) and obtain a suitable raw material for industrial applications, such as the chlor-alkali industry. An electrodialysis pilot plant was used to evaluate the efficiency of concentrating a seawater reverse osmosis (SWRO) brine under representative full-scale operational conditions covering the temperature range of a semiarid climate. The results indicate that electrodialysis is a technology that can concentrate SVVRO brines from approximately 70 to 245 g/L NaCl, achieving an additional intrinsic purification of major multivalent ions (Ca2+, Mg2+, SO42-) due to the selectivity patterns of ion exchange membranes and the ion-complexation reactions in the concentrated brines. However, minor components, such as Ni and Cu, are concentrated due to the formation of Cu and Ni complexes with chloride ions to form monocharged species (e.g., NiCl+ and CuCl+). Energy consumption values of 0.12 kWh/kg NaCl for 185 g NaCl/l at 27 degrees C and 0.35 kA/m(2) or 0.19 kWh/kg NaCl for 203 g NaCl/l at 27 degrees C and 0.50 kA/m(2) were reached. These results were compared with the data obtained from the literature for salt production by electrodialysers. (C) 2013 Elsevier B.V. All rights reserved.
dc.format.extent11 p.
dc.language.isoeng
dc.rightsAttribution-NonCommercial-NoDerivs 3.0 Spain
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es/
dc.subjectÀrees temàtiques de la UPC::Enginyeria química
dc.subject.lcshSaline water conversion
dc.subject.otherIon exchange membranes
dc.subject.otherEnergy consumption
dc.subject.otherBrine reuse
dc.subject.otherChlor-alkali industry
dc.subject.otherEXCHANGE MEMBRANE ELECTRODIALYSIS
dc.subject.otherSALINE WATER DESALINATION
dc.subject.otherOF-THE-ART
dc.subject.otherCOMPUTER-SIMULATION
dc.subject.otherENVIRONMENTAL IMPACTS
dc.subject.otherSALT PRODUCTION
dc.subject.otherPLANT
dc.subject.otherEXTRACTION
dc.subject.otherDISPOSAL
dc.subject.otherEVAPORATION
dc.titleConcentration of NaCl from seawater reverse osmosis brines for the chlor-alkali industry by electrodialysis
dc.typeArticle
dc.subject.lemacAigua salada -- Dessalatge -- Osmosi inversa
dc.contributor.groupUniversitat Politècnica de Catalunya. SETRI - Grup de Tècniques de Separació i Tractament de Residus Industrials
dc.identifier.doi10.1016/j.desal.2013.12.021
dc.description.peerreviewedPeer Reviewed
dc.relation.publisherversionhttp://www.sciencedirect.com/science/article/pii/S0011916413006073
dc.rights.accessRestricted access - publisher's policy
local.identifier.drac14970720
dc.description.versionPostprint (published version)
dc.date.lift10000-01-01
local.citation.authorReig, M.; Casas, S.; Aladjem, C.; Valderrama, C.; Gibert, O.; Valero, F.; Miguel, C.; Larrotcha, E.; Cortina, J.
local.citation.publicationNameDesalination
local.citation.volume342
local.citation.startingPage107
local.citation.endingPage117


Files in this item

Thumbnail

This item appears in the following Collection(s)

Show simple item record