The operating cost of an anaerobic membrane bioreactor (AnMBR) treating sulphate-rich urban wastewater

dc.contributor.authorPretel Jolis, Ruthes_ES
dc.contributor.authorRobles Martínez, Ángeles_ES
dc.contributor.authorRuano García, María Victoriaes_ES
dc.contributor.authorSeco Torrecillas, Auroraes_ES
dc.contributor.authorFERRER, J.
dc.contributor.funderCentro para el Desarrollo Tecnológico Industriales_ES
dc.contributor.funderMinisterio de Economía y Competitividades_ES
dc.date.accessioned2015-10-07T11:11:42Z
dc.date.available2015-10-07T11:11:42Z
dc.date.issued2014-04
dc.description.abstractThe objective of this study was to evaluate the operating cost of an anaerobic membrane bioreactor (AnMBR) treating sulphate-rich urban wastewater (UWW) at ambient temperature (ranging from 17 to 33 degrees C). To this aim, energy consumption, methane production, and sludge handling and recycling to land were evaluated. The results revealed that optimising specific gas demand with respect to permeate volume (SGDp) and sludge retention time (for given ambient temperature conditions) is essential to maximise energy savings (minimum energy demand: 0.07 kW h m(-3)). Moreover, low/moderate sludge productions were obtained (minimum value: 0.16 kg TSS kg(-1) CODRemoved), which further enhanced the overall operating cost of the plant (minimum value: is an element of 0.011 per m(3) of treated water). The sulphate content in the influent UWW significantly affected the final production of methane and thereby the overall operating cost. Indeed, the evaluated AnMBR system presented energy surplus potential when treating low-sulphate UWWes_ES
dc.description.accrualMethodSes_ES
dc.description.bibliographicCitationPretel Jolis, R.; Robles Martínez, Á.; Ruano García, MV.; Seco Torrecillas, A.; Ferrer, J. (2014). The operating cost of an anaerobic membrane bioreactor (AnMBR) treating sulphate-rich urban wastewater. Separation and Purification Technology. 126(15):30-38. doi:10.1016/j.seppur.2014.02.013es_ES
dc.description.issue15es_ES
dc.description.sponsorshipThis research work was possible thanks to projects CTM2011-28595-C0-01/02 (funded by the Spanish Ministry of Economy and Competitiveness jointly with the European Regional Development Fund) and aqualia INNPRONTA IISIS IPT-20111023 (partially funded by the Centre for Industrial Technological Development (CDTI) and supported by the Spanish Ministry of Economy and Competitiveness).en_EN
dc.description.upvformatpfin38es_ES
dc.description.upvformatpinicio30es_ES
dc.description.volume126es_ES
dc.identifier.doi10.1016/j.seppur.2014.02.013
dc.identifier.issn1383-5866
dc.identifier.urihttps://riunet.upv.es/handle/10251/55699
dc.languageIngléses_ES
dc.publisherElsevieres_ES
dc.relation.ispartofSeparation and Purification Technologyes_ES
dc.relation.publisherversionhttp://dx.doi.org/10.1016/j.seppur.2014.02.013es_ES
dc.relation.senia269357es_ES
dc.rightsReserva de todos los derechoses_ES
dc.rights.accessRightsAbiertoes_ES
dc.subjectIndustrial-scale hollow-fibre membraneses_ES
dc.subjectOperating costes_ES
dc.subjectAnaerobic membrane bioreactor (AnMBR)es_ES
dc.subjectSulphate-rich urban wastewateres_ES
dc.subjectEnergy consumptiones_ES
dc.subject.classificationINGENIERIA HIDRAULICAes_ES
dc.subject.classificationTECNOLOGIA DEL MEDIO AMBIENTEes_ES
dc.titleThe operating cost of an anaerobic membrane bioreactor (AnMBR) treating sulphate-rich urban wastewateres_ES
dc.typeArtículoes_ES
dc.type.versioninfo:eu-repo/semantics/publishedVersiones_ES
dspace.entity.typePublication
upv.uuid89c8c0af-bcda-48d6-b9fe-d963898c655aes_ES

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