dc.contributor.author | Reig i Amat, Mònica |
dc.contributor.author | Casas Garriga, Sandra |
dc.contributor.author | Aladjem, Carlos |
dc.contributor.author | Valderrama Ángel, César Alberto |
dc.contributor.author | Gibert Agulló, Oriol |
dc.contributor.author | Valero Cervera, Fernando |
dc.contributor.author | Miguel Centeno, Carlos |
dc.contributor.author | Larrotcha, Enric |
dc.contributor.author | Cortina Pallás, José Luis |
dc.contributor.other | Universitat Politècnica de Catalunya. Departament d'Enginyeria Química |
dc.date.accessioned | 2014-07-08T08:05:07Z |
dc.date.created | 2014-06-02 |
dc.date.issued | 2014-06-02 |
dc.identifier.citation | Reig, 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.issn | 0011-9164 |
dc.identifier.uri | http://hdl.handle.net/2117/23419 |
dc.description.abstract | Currently, 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.extent | 11 p. |
dc.language.iso | eng |
dc.rights | Attribution-NonCommercial-NoDerivs 3.0 Spain |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/3.0/es/ |
dc.subject | Àrees temàtiques de la UPC::Enginyeria química |
dc.subject.lcsh | Saline water conversion |
dc.subject.other | Ion exchange membranes |
dc.subject.other | Energy consumption |
dc.subject.other | Brine reuse |
dc.subject.other | Chlor-alkali industry |
dc.subject.other | EXCHANGE MEMBRANE ELECTRODIALYSIS |
dc.subject.other | SALINE WATER DESALINATION |
dc.subject.other | OF-THE-ART |
dc.subject.other | COMPUTER-SIMULATION |
dc.subject.other | ENVIRONMENTAL IMPACTS |
dc.subject.other | SALT PRODUCTION |
dc.subject.other | PLANT |
dc.subject.other | EXTRACTION |
dc.subject.other | DISPOSAL |
dc.subject.other | EVAPORATION |
dc.title | Concentration of NaCl from seawater reverse osmosis brines for the chlor-alkali industry by electrodialysis |
dc.type | Article |
dc.subject.lemac | Aigua salada -- Dessalatge -- Osmosi inversa |
dc.contributor.group | Universitat Politècnica de Catalunya. SETRI - Grup de Tècniques de Separació i Tractament de Residus Industrials |
dc.identifier.doi | 10.1016/j.desal.2013.12.021 |
dc.description.peerreviewed | Peer Reviewed |
dc.relation.publisherversion | http://www.sciencedirect.com/science/article/pii/S0011916413006073 |
dc.rights.access | Restricted access - publisher's policy |
local.identifier.drac | 14970720 |
dc.description.version | Postprint (published version) |
dc.date.lift | 10000-01-01 |
local.citation.author | Reig, M.; Casas, S.; Aladjem, C.; Valderrama, C.; Gibert, O.; Valero, F.; Miguel, C.; Larrotcha, E.; Cortina, J. |
local.citation.publicationName | Desalination |
local.citation.volume | 342 |
local.citation.startingPage | 107 |
local.citation.endingPage | 117 |