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dc.contributor.author | García Fayos, Beatriz | es_ES |
dc.contributor.author | Arnal Arnal, José Miguel | es_ES |
dc.contributor.author | Gimenez Anton, Adria Carles | es_ES |
dc.contributor.author | Alvarez Blanco, Silvia | es_ES |
dc.contributor.author | Sancho Fernández, María Pino | es_ES |
dc.date.accessioned | 2016-10-04T08:44:35Z | |
dc.date.available | 2016-10-04T08:44:35Z | |
dc.date.issued | 2015-09-19 | |
dc.identifier.issn | 1944-3986 | |
dc.identifier.uri | http://hdl.handle.net/10251/71086 | |
dc.description.abstract | Research in cleaning procedures of reverse osmosis membranes used in seawater desalination to minimize costs and achieve high efficiency is necessary. Multi-step cleaning can represent a useful tool, since the cleaning efficiency can be improved by means of utilization of different chemicals with complementary cleaning mechanisms. The objective of this work was the optimization of a two-step cleaning procedure to recover the membrane properties and reduce power costs. Spent Hydranautics SWC3 membranes (USA) were supplied by a desalination plant. Cleaning tests were performed in three stages: one-step static cleaning, two-step static cleaning and characterization of the membrane surface after the cleaning process. Four cleaning agents at two different concentrations were used. All possible combinations of them were considered, including sequence effect. After the cleaning process, membrane surface was characterized by field emission scanning electron microscopy coupled with energy dispersive X-ray spectroscopy and atomic force microscopy. One-step static cleaning test indicated that sodium dodecyl sulphate 1% w/v was the most efficient cleaning solution, followed by NaOH 2% w/v. Two-step cleaning tests showed that the procedure that maximized permeate flux recovery was surfactant-alkaline cleaning, whereas the one that maximized the recovery of the salt rejection index was alkaline-acid sequence. Characterization of the membrane surface after the cleaning steps confirmed that fouling deposits were significantly removed. | es_ES |
dc.description.sponsorship | The authors wish to thank Abengoa Water, S.L. for the financial support given to this research through the project "Cleaning and re-use of reverse osmosis membranes in desalination plants", which belongs to the CENIT-Tecoagua research project, funded by the Spanish Ministry of Science and Innovation. The authors would like to gratefully acknowledge Vicente Fornes and Rosa Torrero from the CSIC-I.T.Q research centre from the Universitat Politecnica de Valencia for their support given in the ATR-FTIR analysis. | en_EN |
dc.language | Inglés | es_ES |
dc.publisher | Taylor & Francis | es_ES |
dc.relation.ispartof | Desalination and Water Treatment | es_ES |
dc.rights | Reserva de todos los derechos | es_ES |
dc.subject | Chemical agent | es_ES |
dc.subject | Multi-step cleaning | es_ES |
dc.subject | RO | es_ES |
dc.subject | Static test | es_ES |
dc.subject.classification | INGENIERIA QUIMICA | es_ES |
dc.title | Optimization of chemical cleaning of a reverse osmosis membrane from a desalination plant by means of two step static tests | es_ES |
dc.type | Artículo | es_ES |
dc.identifier.doi | 10.1080/19443994.2014.959738 | |
dc.relation.projectID | info:eu-repo/grantAgreement/CDTI/CENIT/CEN-20091028/ES/Desarrollo de tecnologías sostenibles para el ciclo del agua/TECOAGUA | |
dc.rights.accessRights | Cerrado | es_ES |
dc.contributor.affiliation | Universitat Politècnica de València. Departamento de Ingeniería Química y Nuclear - Departament d'Enginyeria Química i Nuclear | es_ES |
dc.contributor.affiliation | Universitat Politècnica de València. Instituto de Seguridad Industrial, Radiofísica y Medioambiental - Institut de Seguretat Industrial, Radiofísica i Mediambiental | es_ES |
dc.description.bibliographicCitation | García Fayos, B.; Arnal Arnal, JM.; Gimenez Anton, AC.; Alvarez Blanco, S.; Sancho Fernández, MP. (2015). Optimization of chemical cleaning of a reverse osmosis membrane from a desalination plant by means of two step static tests. Desalination and Water Treatment. 55(12):3367-3379. doi:10.1080/19443994.2014.959738 | es_ES |
dc.description.accrualMethod | S | es_ES |
dc.relation.publisherversion | http://dx.doi.org/10.1080/19443994.2014.959738 | es_ES |
dc.description.upvformatpinicio | 3367 | es_ES |
dc.description.upvformatpfin | 3379 | es_ES |
dc.type.version | info:eu-repo/semantics/publishedVersion | es_ES |
dc.description.volume | 55 | es_ES |
dc.description.issue | 12 | es_ES |
dc.relation.senia | 286047 | es_ES |
dc.identifier.eissn | 1944-3986 | |
dc.contributor.funder | Ministerio de Ciencia e Innovación | es_ES |
dc.contributor.funder | Abengoa | es_ES |
dc.contributor.funder | Centro para el Desarrollo Tecnológico Industrial |