Identificador persistente para citar o vincular este elemento:
http://hdl.handle.net/10553/132738
Campo DC | Valor | idioma |
---|---|---|
dc.contributor.author | Roo Filgueira, Francisco Javier | en_US |
dc.contributor.author | Arenas Urrea, Sigrid Yurena | en_US |
dc.contributor.author | Pordomingo Bañó, Jorge | en_US |
dc.contributor.author | Ramos Marrero, Cristofer | en_US |
dc.contributor.author | Mesa de León, Rubén | en_US |
dc.contributor.author | de la Fuente Bencomo, Juan Antonio | en_US |
dc.contributor.author | León Zerpa, Federico Antonio | en_US |
dc.date.accessioned | 2024-08-26T10:49:45Z | - |
dc.date.available | 2024-08-26T10:49:45Z | - |
dc.date.issued | 2022 | en_US |
dc.identifier.issn | 0012-7361 | en_US |
dc.identifier.uri | http://hdl.handle.net/10553/132738 | - |
dc.description.abstract | The reverse osmosis seawater desalination plants open-intake requires different strategies of pre-treatment to reduce the biofouling and scaling. The UltraFiltration (UF) technology is a recent application to this process. In this work, some alternatives to chemical products reducing in chemically enhanced backwash (CEB) and clean in place (CIP) of a UF rack have been studied. Mainly the sodium hypochlorite consumption, due to its biofouling precursor effect over reverse osmosis membranes. For this purpose, the optimal filtration time has been studied, to get the highest water production prior to the CIP, as well as some modifications in the conventional CIP's, modifying the duration of the stages of the same. The results were compared with the current mode of daily operation of the CEB. The results show that a reduction of up to 60% in the amount of sodium hypochlorite per cubic meter of water produced employed in UF CEB's, mini CIP's and CIP's can be achieved. However, the consumption of the rest of chemical dosing increased notably, and therefore the operating cost of UF also increased. In addition, there was an increase of desalted water consumption to the chemical products removed, up to almost 95,84 %, in comparison with the currently operational mode of CEB. On the other hand, operating the UF plant in the manner proposed requires a automatization of the process and expert staff to programme the control. Therefore, based on the results obtained, the alternatives proposed could reduce the chemical products in use, but it is not conclusive in terms of exploitation operational costs. Key Words: Ultrafiltration, Reverse osmosis, Open-intake, Clean in place, Chemically Enhanced Backwash, chemical products reduction, biofouling, pre-treatment. | en_US |
dc.language | eng | en_US |
dc.relation | Plataforma Macaronésica para el incremento de la excelencia en materia de I+D en desalación de agua y del conocimiento del nexo agua desalada-energía | en_US |
dc.relation.ispartof | Dyna (Bilbao) | en_US |
dc.source | DYNA [ISSN 0012-7361], v. 97 (6), p. 658-664. | en_US |
dc.subject | 3308 Ingeniería y tecnología del medio ambiente | en_US |
dc.subject | 330806 Regeneración del agua | en_US |
dc.subject.other | Ultrafiltration | en_US |
dc.subject.other | Reverse osmosis | en_US |
dc.subject.other | Open-intake | en_US |
dc.subject.other | Clean in place | en_US |
dc.subject.other | Chemically Enhanced Backwash | en_US |
dc.subject.other | Chemical products reduction | en_US |
dc.subject.other | Biofouling | en_US |
dc.subject.other | Pre-treatmen | en_US |
dc.title | Análisis y viabilidad de la reducción de productos químicos en los lavados de la ultrafiltración como tecnología de pretratamiento de la desalación por osmosis inversa | en_US |
dc.type | info:eu-repo/semantics/article | en_US |
dc.type | Article | en_US |
dc.identifier.doi | https://doi.org/10.6036/10454 | en_US |
dc.description.lastpage | 664 | en_US |
dc.description.firstpage | 658 | en_US |
dc.relation.volume | 97 | en_US |
dc.investigacion | Ingeniería y Arquitectura | en_US |
dc.type2 | Artículo | en_US |
dc.utils.revision | Sí | en_US |
dc.date.coverdate | November 2022 | en_US |
dc.identifier.ulpgc | Sí | en_US |
dc.contributor.buulpgc | BU-ING | en_US |
dc.description.sjr | 0,158 | |
dc.description.jcr | 1,0 | |
dc.description.sjrq | Q4 | |
dc.description.jcrq | Q4 | |
dc.description.sellofecyt | Sello FECYT | |
dc.description.scie | SCIE | |
dc.description.miaricds | 11,0 | |
item.grantfulltext | open | - |
item.fulltext | Con texto completo | - |
crisitem.project.principalinvestigator | Schallenberg Rodríguez, Julieta Cristina | - |
crisitem.author.dept | GIR Grupo de Investigación en Acuicultura | - |
crisitem.author.dept | IU de Investigación en Acuicultura Sostenible y Ec | - |
crisitem.author.dept | Departamento de Biología | - |
crisitem.author.dept | GIR IUNAT: Control analítico de fuentes medioambientales | - |
crisitem.author.dept | IU de Estudios Ambientales y Recursos Naturales | - |
crisitem.author.dept | Departamento de Ingeniería de Procesos | - |
crisitem.author.orcid | 0000-0002-9660-230X | - |
crisitem.author.orcid | 0000-0003-2284-8400 | - |
crisitem.author.parentorg | IU de Investigación en Acuicultura Sostenible y Ec | - |
crisitem.author.parentorg | IU de Estudios Ambientales y Recursos Naturales | - |
crisitem.author.fullName | Roo Filgueira, Francisco Javier | - |
crisitem.author.fullName | Arenas Urrea, Sigrid Yurena | - |
crisitem.author.fullName | León Zerpa, Federico Antonio | - |
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