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dc.contributor.author | Vincent Vela, Maria Cinta | es_ES |
dc.contributor.author | Cuartas Uribe, Beatriz Elena | es_ES |
dc.contributor.author | Alvarez Blanco, Silvia | es_ES |
dc.contributor.author | Lora García, Jaime | es_ES |
dc.date.accessioned | 2015-06-08T09:26:11Z | |
dc.date.available | 2015-06-08T09:26:11Z | |
dc.date.issued | 2011-04 | |
dc.identifier.issn | 0255-2701 | |
dc.identifier.uri | http://hdl.handle.net/10251/51379 | |
dc.description.abstract | The mechanisms of fouling in the ultrafiltration of polyethylene glycol (PEG) are analysed using the complete blocking and the intermediate blocking Hermia's models adapted to crossflow filtration. The parameters of these models were theoretically estimated. The predicted results were compared with experimental data. Ultrafiltration experiments were performed with Carbosep M2 monotubular ceramic (Orelis, S.A. (France)). The fouling ultrafiltration experiments were carried out at a constant temperature and feed concentration and different feed flow rates and transmembrane pressures. The precision in the predictions is very high. The results showed that the phenomenon controlling fouling was intermediate blocking for high fouling conditions. © 2011 Elsevier B.V. | es_ES |
dc.description.sponsorship | The authors of this work wish to gratefully acknowledge the financial support of the Spanish Ministry of Science and Technology (MCYT) through its project no. CTQ2005-03398. | en_EN |
dc.language | Inglés | es_ES |
dc.publisher | Elsevier | es_ES |
dc.relation.ispartof | Chemical Engineering and Processing: Process Intensification | es_ES |
dc.rights | Reserva de todos los derechos | es_ES |
dc.subject | Crossflow ultrafiltration | es_ES |
dc.subject | Fouling | es_ES |
dc.subject | Modelling | es_ES |
dc.subject | Polyethylene glycol | es_ES |
dc.subject | Constant temperature | es_ES |
dc.subject | Cross flow filtration | es_ES |
dc.subject | Cross-flow ultrafiltration | es_ES |
dc.subject | Dynamic membranes | es_ES |
dc.subject | Experimental data | es_ES |
dc.subject | Feed concentration | es_ES |
dc.subject | Feed flow rate | es_ES |
dc.subject | Fouling resistance | es_ES |
dc.subject | Transmembrane pressures | es_ES |
dc.subject | Experiments | es_ES |
dc.subject | Microfiltration | es_ES |
dc.subject | Polyethylene oxides | es_ES |
dc.subject | Polyethylenes | es_ES |
dc.subject | Thermoplastics | es_ES |
dc.subject | Ultrafiltration | es_ES |
dc.subject | Polyethylene glycols | es_ES |
dc.subject.classification | INGENIERIA QUIMICA | es_ES |
dc.title | Analysis of fouling resistances under dynamic membrane filtration | es_ES |
dc.type | Artículo | es_ES |
dc.identifier.doi | 10.1016/j.cep.2011.02.010 | |
dc.relation.projectID | info:eu-repo/grantAgreement/MEC//CTQ2005-03398/ES/TECNICAS COMBINADAS DE SEPARACION PARA LA GESTION DE SALMUERAS PROCEDENTES DE PROCESOS DE MEMBRANA PARA LA DESALACION DE AGUAS SALOBRES./ | es_ES |
dc.rights.accessRights | Abierto | es_ES |
dc.contributor.affiliation | Universitat Politècnica de València. Departamento de Ingeniería Química y Nuclear - Departament d'Enginyeria Química i Nuclear | es_ES |
dc.description.bibliographicCitation | Vincent Vela, MC.; Cuartas Uribe, BE.; Alvarez Blanco, S.; Lora García, J. (2011). Analysis of fouling resistances under dynamic membrane filtration. Chemical Engineering and Processing: Process Intensification. 50(4):404-408. https://doi.org/10.1016/j.cep.2011.02.010 | es_ES |
dc.description.accrualMethod | S | es_ES |
dc.relation.publisherversion | http://dx.doi.org/10.1016/j.cep.2011.02.010 | es_ES |
dc.description.upvformatpinicio | 404 | es_ES |
dc.description.upvformatpfin | 408 | es_ES |
dc.type.version | info:eu-repo/semantics/publishedVersion | es_ES |
dc.description.volume | 50 | es_ES |
dc.description.issue | 4 | es_ES |
dc.relation.senia | 206008 | |
dc.contributor.funder | Ministerio de Educación y Ciencia | es_ES |