- -

A study of the osmotic membrane bioreactor process using a sodium chloride solution and an industrial effluent as draw solutions

RiuNet: Repositorio Institucional de la Universidad Politécnica de Valencia

Compartir/Enviar a

Citas

Estadísticas

  • Estadisticas de Uso

A study of the osmotic membrane bioreactor process using a sodium chloride solution and an industrial effluent as draw solutions

Mostrar el registro sencillo del ítem

Ficheros en el ítem

dc.contributor.author Luján Facundo, María José es_ES
dc.contributor.author Soler Cabezas, José Luis es_ES
dc.contributor.author Mendoza Roca, José Antonio es_ES
dc.contributor.author Vincent Vela, Maria Cinta es_ES
dc.contributor.author Bes-Piá, M.A. es_ES
dc.contributor.author Doñate Hernández, Silvia es_ES
dc.date.accessioned 2018-07-07T04:26:47Z
dc.date.available 2018-07-07T04:26:47Z
dc.date.issued 2017 es_ES
dc.identifier.issn 1385-8947 es_ES
dc.identifier.uri http://hdl.handle.net/10251/105472
dc.description.abstract [EN] Osmotic membrane bioreactor (OMBR) is an emerging membrane process which has gained interest in the recent years because of the low energy consumption and the high effluent quality. The osmotic membrane bioreactor combines a forward osmosis (FO) membrane and a biological treatment. However, salt reverse flux is the main problem because of the negative effect of the salt concentration increase in the reactor on the microbial activity. This is the reason why the study of a suitable draw solution (DS) is very important in the overall performance of the reactor. This study compares the process performance using two draw solutions: a 53 g L-1 NaCI solution and a real waste water solution (waste water from an absorption column consisting mainly of SO42- and NH4-N with concentrations of 153 g L-1 and 19 g L-1, respectively). The comparison is focused on the salt reverse flux during the reactor operation, the mixed liquor characteristics, the membrane fouling and the overall performance. The results indicated that the industrial wastewater showed a higher salt reverse flux, but also a less severe fouling and a higher the osmotic pressure difference in comparison with the NaCl solution. In terms of chemical oxygen demand (COD) removal efficiencies, both draw solutions attained values higher than 80%, though the efficiency was slightly lower when the industrial effluent was used as DS. This was related to the higher conductivity reached in the bioreactor when the industrial effluent was used as draw solution. In spite of it, the use of this industrial effluent as draw solution is strongly recommended because of the high permeate fluxes yielded, the low membrane fouling and the lack of necessity of regenerating the draw solution. (C) 2017 Elsevier B.V. All rights reserved. es_ES
dc.description.sponsorship This study was supported by the Spanish Ministry of Economy and Competitiveness (Spain) through the project RTC-2015-3582-5-AR.
dc.language Inglés es_ES
dc.publisher Elsevier es_ES
dc.relation.ispartof Chemical Engineering Journal es_ES
dc.rights Reconocimiento - No comercial - Sin obra derivada (by-nc-nd) es_ES
dc.subject Forward osmosis es_ES
dc.subject Osmotic membrane bioreactor es_ES
dc.subject Membrane fouling es_ES
dc.subject Wastewater treatment es_ES
dc.subject Draw solution es_ES
dc.subject.classification INGENIERIA QUIMICA es_ES
dc.title A study of the osmotic membrane bioreactor process using a sodium chloride solution and an industrial effluent as draw solutions es_ES
dc.type Artículo es_ES
dc.identifier.doi 10.1016/j.cej.2017.04.062 es_ES
dc.relation.projectID info:eu-repo/grantAgreement/MINECO//RTC-2015-3582-5Q4618002BC.VALENCIANA/ES/Desarrollo de un proceso de biorreactor de membranas para gestión de efluentes salinos. Proyecto ODEON/ es_ES
dc.rights.accessRights Abierto es_ES
dc.date.embargoEndDate 2019-08-15 es_ES
dc.contributor.affiliation Universitat Politècnica de València. Departamento de Ingeniería Química y Nuclear - Departament d'Enginyeria Química i Nuclear es_ES
dc.contributor.affiliation Universitat Politècnica de València. Departamento de Economía y Ciencias Sociales - Departament d'Economia i Ciències Socials es_ES
dc.description.bibliographicCitation Lujan Facundo, MJ.; Soler Cabezas, JL.; Mendoza Roca, JA.; Vincent Vela, MC.; Bes-Piá, M.; Doñate Hernández, S. (2017). A study of the osmotic membrane bioreactor process using a sodium chloride solution and an industrial effluent as draw solutions. Chemical Engineering Journal. 322:603-610. doi:10.1016/j.cej.2017.04.062 es_ES
dc.description.accrualMethod S es_ES
dc.relation.publisherversion http://dx.doi.org/10.1016/j.cej.2017.04.062 es_ES
dc.description.upvformatpinicio 603 es_ES
dc.description.upvformatpfin 610 es_ES
dc.type.version info:eu-repo/semantics/publishedVersion es_ES
dc.description.volume 322 es_ES
dc.relation.pasarela S\337550 es_ES
dc.contributor.funder Ministerio de Economía, Industria y Competitividad es_ES


Este ítem aparece en la(s) siguiente(s) colección(ones)

Mostrar el registro sencillo del ítem