Publication:
Effect of previous coagulation in direct ultrafiltration of primary settled municipal wastewater

dc.contributor.authorGonzález Cabrera, Enrique
dc.contributor.authorMartínez Soto, Marta
dc.contributor.authorVera Cabezas, Luisa Mayra
dc.contributor.authorBravo Sánchez, Luis Ramón
dc.contributor.authorDelgado Díaz, Sebastián Jesús
dc.contributor.authorVera Peña, Luisa
dc.date.accessioned2022-03-07T15:40:24Z
dc.date.available2022-03-07T15:40:24Z
dc.date.issued2012
dc.description.abstractDirect ultrafiltration of primary settled municipal wastewater can be a feasible option for water reuse in several applications by avoiding biological treatment. This paper discusses the effect of previous clarification by coagulation/sedimentation of raw wastewater on ultrafiltration performance and its relationship with the main operation parameters in dead-end mode (flux and backwashing duration). Reversible and residual membrane foulings in a hollow-fibre bench-scale unit were determined over a broad range of filtration parameters and coagulant doses used in the previous clarification of domestic wastewater. Moreover, results were also compared with those obtained by ultrafiltration of biologically treated effluent from a conventional WWTP. Reversible membrane fouling, which can be described by the cake formation model, seems mainly caused by the colloidal fraction of the wastewater. In fact, under optimal coagulant dosage, the cake resistance values (expressed by αω, in m− 2) were similar to those obtained with the secondary effluent. Direct observation of the membrane surface suggests a solid accumulation in the vicinity of the membrane after backwashing, which could justify the increase in cake resistance during the initial filtration/backwashing cycles until steady-state conditions are reached. Residual fouling resistance decreased exponentially with the duration of backwashing, obtaining a limit resistance value which was independent of the coagulant dose. Moreover, high efficiency of chemical oxygen demand (COD) removal was achieved by the tested treatment train, regardless of the coagulant dose and the initial quality of the primary effluent.
dc.identifier.doi10.1016/j.desal.2012.08.005
dc.identifier.issn0011-9164
dc.identifier.urihttp://dspace.ucuenca.edu.ec/handle/123456789/38387
dc.identifier.urihttps://www.scopus.com/record/display.uri?eid=2-s2.0-84865958368&origin=resultslist&sort=cp-f&src=s&st1=Effect+of+previous+coagulation+in+direct+ultrafiltration+of+primary+settled+municipal+wastewater&sid=4cbbb7757b37d6f553a825d9b132ec9d&sot=b&sdt=b&sl=101&s=ALL%28Effect+of+previous+coagulation+in+direct+ultrafiltration+of+primary+settled+municipal+wastewater%29&relpos=4&citeCnt=32&searchTerm=&featureToggles=FEATURE_NEW_DOC_DETAILS_EXPORT:1
dc.language.isoes_ES
dc.sourceDesalination
dc.subjectMembrane fouling
dc.subjectDead end ultrafiltration
dc.subjectHollow fibre
dc.titleEffect of previous coagulation in direct ultrafiltration of primary settled municipal wastewater
dc.typeARTÍCULO
dc.ucuenca.afiliacionDelgado, S., Universidad de la Laguna, San Cristobal de La Laguna, España
dc.ucuenca.afiliacionVera, L., Universidad de la Laguna, San Cristobal de La Laguna, España
dc.ucuenca.afiliacionGonzález, E., Universidad de la Laguna, San Cristobal de La Laguna, España
dc.ucuenca.afiliacionVera, L., Universidad de la Laguna, San Cristobal de La Laguna, España
dc.ucuenca.afiliacionMartínez, M., Universidad de la Laguna, San Cristobal de La Laguna, España
dc.ucuenca.afiliacionBravo, L., Universidad de la Laguna, San Cristobal de La Laguna, España
dc.ucuenca.areaconocimientofrascatiamplio2. Ingeniería y Tecnología
dc.ucuenca.areaconocimientofrascatidetallado2.4.2 Ingeniería de Procesos Químicos
dc.ucuenca.areaconocimientofrascatiespecifico2.4 Ingeniería Química
dc.ucuenca.areaconocimientounescoamplio07 - Ingeniería, Industria y Construcción
dc.ucuenca.areaconocimientounescodetallado0711 - Ingeniería y Procesos Químicos
dc.ucuenca.areaconocimientounescoespecifico071 - Ingeniería y Profesiones Afines
dc.ucuenca.correspondenciaVera Peña, Luisa, luvera@ull.edu.ec
dc.ucuenca.cuartilQ1
dc.ucuenca.factorimpacto1.79
dc.ucuenca.idautor0000-0001-9965-4407
dc.ucuenca.idautor0000-0001-5756-6628
dc.ucuenca.idautorXDA362792
dc.ucuenca.idautor0001-9589-1544
dc.ucuenca.idautor0000-0002-8435-5540
dc.ucuenca.idautor0000-0002-8851-5046
dc.ucuenca.indicebibliograficoSCOPUS
dc.ucuenca.numerocitaciones0
dc.ucuenca.urifuentehttps://www.sciencedirect.com/journal/desalination/vol/304/suppl/C
dc.ucuenca.versionVersión publicada
dc.ucuenca.volumenVolumen 304
dspace.entity.typePublication
dspace.entity.typePublication
relation.isAuthorOfPublication4b3dbc3a-c38c-4810-b1fd-6b54ad65b077
relation.isAuthorOfPublication.latestForDiscovery4b3dbc3a-c38c-4810-b1fd-6b54ad65b077

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