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Interplay between physical cleaning, membrane pore size and fluid rheology during the evolution of fouling in membrane bioreactors

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Interplay between physical cleaning, membrane pore size and fluid rheology during the evolution of fouling in membrane bioreactors

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dc.contributor.author Martí Calatayud, Manuel César es_ES
dc.contributor.author Schneider, S. es_ES
dc.contributor.author Yüce, S. es_ES
dc.contributor.author Wessling, M. es_ES
dc.date.accessioned 2020-07-22T03:31:30Z
dc.date.available 2020-07-22T03:31:30Z
dc.date.issued 2018-12-15 es_ES
dc.identifier.issn 0043-1354 es_ES
dc.identifier.uri http://hdl.handle.net/10251/148455
dc.description.abstract [EN] Fouling is one of the most pressing limitations during operation of membrane bioreactors, as it increases operating costs and is the cause of short membrane lifespans. Conducting effective physical cleanings is thus essential for keeping membrane operation above viable performance limits. The nature of organic foulants present in the sludge and the membrane properties are among the most influential factors determining fouling development and thus, efficiency of fouling mitigation approaches. The role of other factors like sludge viscosity on fouling is still unclear, given that contradictory effects have been reported in the literature. In the present study we use a new research approach by which the complex interplay between fouling type, levels of permeate flux, membrane material and feed properties is analyzed, and the influence of these factors on critical flux and membrane permeability is evaluated. A variety of systems including activated sludge and model solutions with distinct rheological behavior has been investigated for two membranes differing in pore size distribution. We present a novel method for assessing the efficiency of fouling removal by backwash and compare it with the efficiency achieved by means of relaxation. Results obtained have proven that backwash delays development of critical fouling as compared with relaxation and reduces fouling irreversibility regardless of fluid rheology. It was shown that backwash is especially effective for membranes for which internal fouling is the main cause of loss in permeability. Nonetheless, we found out that for membranes with tight pores, both relaxation and backwash are equally effective. The critical flux decreases significantly for high-viscosity fluids, such as activated sludge. This effect is mainly caused by an intensified concentration polarization at the feed side rather than by internal fouling events. However, membrane permeability has been proven to rely more on the permeate viscosity than on the feed viscosity: poor rejection of organic fractions showcasing high viscosity causes an acute decline in membrane permeability as a consequence of increased shear stress inside the membrane pores. (C) 2018 Elsevier Ltd. All rights reserved. es_ES
dc.description.sponsorship M.W. acknowledges the support through an Alexander-von-Humboldt Professorship. M.C. Marti-Calatayud acknowledges the support to Generalitat Valenciana through the funding APOSTD2017. M.C. Marti-Calatayud thanks the contributions of Sybille Hanisch, Sanchita Khandelwal and Sara Vivanco. This work was supported by the German Federal Ministry of Education and Research (BMBF) through the project BRAMAR (02WCL1334A). We thank Synder Filtration for the supplied membranes es_ES
dc.language Inglés es_ES
dc.publisher Elsevier es_ES
dc.relation.ispartof Water Research es_ES
dc.rights Reserva de todos los derechos es_ES
dc.subject Backwash es_ES
dc.subject Membrane bioreactors es_ES
dc.subject Physical cleaning es_ES
dc.subject Fouling mitigation es_ES
dc.subject Relaxation es_ES
dc.subject Sludge rheology es_ES
dc.subject.classification INGENIERIA QUIMICA es_ES
dc.title Interplay between physical cleaning, membrane pore size and fluid rheology during the evolution of fouling in membrane bioreactors es_ES
dc.type Artículo es_ES
dc.identifier.doi 10.1016/j.watres.2018.10.017 es_ES
dc.relation.projectID info:eu-repo/grantAgreement/BMBF//02WCL1334A/ es_ES
dc.relation.projectID info:eu-repo/grantAgreement/GVA//APOSTD%2F2017%2F059/ 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 Martí Calatayud, MC.; Schneider, S.; Yüce, S.; Wessling, M. (2018). Interplay between physical cleaning, membrane pore size and fluid rheology during the evolution of fouling in membrane bioreactors. Water Research. 147:393-402. https://doi.org/10.1016/j.watres.2018.10.017 es_ES
dc.description.accrualMethod S es_ES
dc.relation.publisherversion https://doi.org/10.1016/j.watres.2018.10.017 es_ES
dc.description.upvformatpinicio 393 es_ES
dc.description.upvformatpfin 402 es_ES
dc.type.version info:eu-repo/semantics/publishedVersion es_ES
dc.description.volume 147 es_ES
dc.identifier.pmid 30336342 es_ES
dc.relation.pasarela S\384663 es_ES
dc.contributor.funder Generalitat Valenciana es_ES
dc.contributor.funder Alexander von Humboldt Foundation es_ES
dc.contributor.funder Bundesministerium für Bildung und Forschung, Alemania es_ES


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