The operating cost of an anaerobic membrane bioreactor (AnMBR) treating sulphate-rich urban wastewater
| dc.contributor.author | Pretel Jolis, Ruth | es_ES |
| dc.contributor.author | Robles Martínez, Ángel | es_ES |
| dc.contributor.author | Ruano García, María Victoria | es_ES |
| dc.contributor.author | Seco Torrecillas, Aurora | es_ES |
| dc.contributor.author | FERRER, J. | |
| dc.contributor.funder | Centro para el Desarrollo Tecnológico Industrial | es_ES |
| dc.contributor.funder | Ministerio de Economía y Competitividad | es_ES |
| dc.date.accessioned | 2015-10-07T11:11:42Z | |
| dc.date.available | 2015-10-07T11:11:42Z | |
| dc.date.issued | 2014-04 | |
| dc.description.abstract | The 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 UWW | es_ES |
| dc.description.accrualMethod | S | es_ES |
| dc.description.bibliographicCitation | Pretel 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.2014.02.013 | es_ES |
| dc.description.issue | 15 | es_ES |
| dc.description.sponsorship | This 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.upvformatpfin | 38 | es_ES |
| dc.description.upvformatpinicio | 30 | es_ES |
| dc.description.volume | 126 | es_ES |
| dc.identifier.doi | 10.1016/j.seppur.2014.02.013 | |
| dc.identifier.issn | 1383-5866 | |
| dc.identifier.uri | https://riunet.upv.es/handle/10251/55699 | |
| dc.language | Inglés | es_ES |
| dc.publisher | Elsevier | es_ES |
| dc.relation.ispartof | Separation and Purification Technology | es_ES |
| dc.relation.publisherversion | http://dx.doi.org/10.1016/j.seppur.2014.02.013 | es_ES |
| dc.relation.senia | 269357 | es_ES |
| dc.rights | Reserva de todos los derechos | es_ES |
| dc.rights.accessRights | Abierto | es_ES |
| dc.subject | Industrial-scale hollow-fibre membranes | es_ES |
| dc.subject | Operating cost | es_ES |
| dc.subject | Anaerobic membrane bioreactor (AnMBR) | es_ES |
| dc.subject | Sulphate-rich urban wastewater | es_ES |
| dc.subject | Energy consumption | es_ES |
| dc.subject.classification | INGENIERIA HIDRAULICA | es_ES |
| dc.subject.classification | TECNOLOGIA DEL MEDIO AMBIENTE | es_ES |
| dc.title | The operating cost of an anaerobic membrane bioreactor (AnMBR) treating sulphate-rich urban wastewater | es_ES |
| dc.type | Artículo | es_ES |
| dc.type.version | info:eu-repo/semantics/publishedVersion | es_ES |
| dspace.entity.type | Publication | |
| upv.uuid | 89c8c0af-bcda-48d6-b9fe-d963898c655a | es_ES |
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