Management of table olive processing wastewater by an osmotic membrane bioreactor process
[EN] The management of fermentation brines from the table olive processing is very complex due to its characteristics: high salinity and high organic matter concentration including phenolic compounds, which behave as slow degradable compounds when a biological process is performed. In this work, the...
| Autores: | , , , , , , |
|---|---|
| Tipo de recurso: | artículo |
| Fecha de publicación: | 2020 |
| País: | España |
| Institución: | Universitat Politècnica de València (UPV) |
| Repositorio: | RiuNet. Repositorio Institucional de la Universitat Politécnica de Valéncia |
| Idioma: | inglés |
| OAI Identifier: | oai:riunet.upv.es:10251/177256 |
| Acceso en línea: | https://riunet.upv.es/handle/10251/177256 |
| Access Level: | acceso abierto |
| Palabra clave: | Forward osmosis Osmotic membrane bioreactor Wastewater treatment INGENIERIA QUIMICA |
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Management of table olive processing wastewater by an osmotic membrane bioreactor processLujan Facundo, Maria Jose|||0000-0001-6871-0584Mendoza Roca, José AntonioSoler Cabezas, José Luis|||0000-0002-4610-3369Bes-Piá, M.A.|||0000-0001-8005-7450Vincent Vela, Maria Cinta|||0000-0001-8493-0165Cuartas Uribe, Beatriz Elena|||0000-0003-2835-900XPastor-Alcaniz, L.Forward osmosisOsmotic membrane bioreactorWastewater treatmentINGENIERIA QUIMICA[EN] The management of fermentation brines from the table olive processing is very complex due to its characteristics: high salinity and high organic matter concentration including phenolic compounds, which behave as slow degradable compounds when a biological process is performed. In this work, the management of these effluents by an osmotic membrane bioreactor has been assessed. This technique combines a biological reactor with forward osmosis membranes. For the study, a laboratory plant consisting of 1 L reactor and a forward osmosis module equipped with a membrane of 42 cm(2) of active surface has been used. Fermentation brine from table olive processing was fed to the system both as draw solution to set out the driving force for the membrane process and as a part of the feed to the reactor, mixing it with municipal wastewater. The experiments were carried out at a constant feed to microorganism ratio of 0.4 g COD.g SS-1.d(-1). Results indicated that the hypersaline effluent was able to produce the needed driving force by the process. Permeate fluxes ranged between 1 and 1.5 L.m(-2).h(-1) after the flux decay of the first operation days. Concerning the biological reaction, it has to be highlighted that phenols were eliminated after 24 days. Until that day, the biological process was jeopardized due to the quick increase of the conductivity in the reactor (ranging between 30 and 35 mS.cm(-1)), which was caused not only by the salinity of the influent but also by the reverse salt flux phenomenon. Soluble microbial products and extracted extracellular polymeric substances also increased in the reactor during the start-up.This study was supported by the Spanish Ministry of Economy and Competitiveness through the project RTC-2015-3582-5-ARElsevierDepartamento de Ingeniería Química y NuclearEscuela Técnica Superior de Ingeniería Aeroespacial y Diseño IndustrialEscuela Técnica Superior de Ingeniería IndustrialInstituto Universitario de Seguridad Industrial, Radiofísica y MedioambientalMinisterio de Economía y EmpresaRepositorio Institucional de la Universitat Politècnica de València Riunet20202020-10-01journal articlehttp://purl.org/coar/resource_type/c_6501VoRhttp://purl.org/coar/version/c_970fb48d4fbd8a85info:eu-repo/semantics/articleapplication/pdfapplication/pdfhttps://riunet.upv.es/handle/10251/177256reponame:RiuNet. Repositorio Institucional de la Universitat Politécnica de Valénciainstname:Universitat Politècnica de València (UPV)InglésengMinisterio de Economía y Competitividad http://dx.doi.org/10.13039/501100003329 RTC-2015-3582-5Q4618002BC.VALENCIANA Desarrollo de un proceso de biorreactor de membranas para gestión de efluentes salinos. Proyecto ODEONopen accesshttp://purl.org/coar/access_right/c_abf2Reconocimiento - No comercial - Sin obra derivada (by-nc-nd) http://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/openAccessoai:riunet.upv.es:10251/1772562026-06-13T07:49:27Z |
| dc.title.none.fl_str_mv |
Management of table olive processing wastewater by an osmotic membrane bioreactor process |
| title |
Management of table olive processing wastewater by an osmotic membrane bioreactor process |
| spellingShingle |
Management of table olive processing wastewater by an osmotic membrane bioreactor process Lujan Facundo, Maria Jose|||0000-0001-6871-0584 Forward osmosis Osmotic membrane bioreactor Wastewater treatment INGENIERIA QUIMICA |
| title_short |
Management of table olive processing wastewater by an osmotic membrane bioreactor process |
| title_full |
Management of table olive processing wastewater by an osmotic membrane bioreactor process |
| title_fullStr |
Management of table olive processing wastewater by an osmotic membrane bioreactor process |
| title_full_unstemmed |
Management of table olive processing wastewater by an osmotic membrane bioreactor process |
| title_sort |
Management of table olive processing wastewater by an osmotic membrane bioreactor process |
| dc.creator.none.fl_str_mv |
Lujan Facundo, Maria Jose|||0000-0001-6871-0584 Mendoza Roca, José Antonio Soler Cabezas, José Luis|||0000-0002-4610-3369 Bes-Piá, M.A.|||0000-0001-8005-7450 Vincent Vela, Maria Cinta|||0000-0001-8493-0165 Cuartas Uribe, Beatriz Elena|||0000-0003-2835-900X Pastor-Alcaniz, L. |
| author |
Lujan Facundo, Maria Jose|||0000-0001-6871-0584 |
| author_facet |
Lujan Facundo, Maria Jose|||0000-0001-6871-0584 Mendoza Roca, José Antonio Soler Cabezas, José Luis|||0000-0002-4610-3369 Bes-Piá, M.A.|||0000-0001-8005-7450 Vincent Vela, Maria Cinta|||0000-0001-8493-0165 Cuartas Uribe, Beatriz Elena|||0000-0003-2835-900X Pastor-Alcaniz, L. |
| author_role |
author |
| author2 |
Mendoza Roca, José Antonio Soler Cabezas, José Luis|||0000-0002-4610-3369 Bes-Piá, M.A.|||0000-0001-8005-7450 Vincent Vela, Maria Cinta|||0000-0001-8493-0165 Cuartas Uribe, Beatriz Elena|||0000-0003-2835-900X Pastor-Alcaniz, L. |
| author2_role |
author author author author author author |
| dc.contributor.none.fl_str_mv |
Departamento de Ingeniería Química y Nuclear Escuela Técnica Superior de Ingeniería Aeroespacial y Diseño Industrial Escuela Técnica Superior de Ingeniería Industrial Instituto Universitario de Seguridad Industrial, Radiofísica y Medioambiental Ministerio de Economía y Empresa Repositorio Institucional de la Universitat Politècnica de València Riunet |
| dc.subject.none.fl_str_mv |
Forward osmosis Osmotic membrane bioreactor Wastewater treatment INGENIERIA QUIMICA |
| topic |
Forward osmosis Osmotic membrane bioreactor Wastewater treatment INGENIERIA QUIMICA |
| description |
[EN] The management of fermentation brines from the table olive processing is very complex due to its characteristics: high salinity and high organic matter concentration including phenolic compounds, which behave as slow degradable compounds when a biological process is performed. In this work, the management of these effluents by an osmotic membrane bioreactor has been assessed. This technique combines a biological reactor with forward osmosis membranes. For the study, a laboratory plant consisting of 1 L reactor and a forward osmosis module equipped with a membrane of 42 cm(2) of active surface has been used. Fermentation brine from table olive processing was fed to the system both as draw solution to set out the driving force for the membrane process and as a part of the feed to the reactor, mixing it with municipal wastewater. The experiments were carried out at a constant feed to microorganism ratio of 0.4 g COD.g SS-1.d(-1). Results indicated that the hypersaline effluent was able to produce the needed driving force by the process. Permeate fluxes ranged between 1 and 1.5 L.m(-2).h(-1) after the flux decay of the first operation days. Concerning the biological reaction, it has to be highlighted that phenols were eliminated after 24 days. Until that day, the biological process was jeopardized due to the quick increase of the conductivity in the reactor (ranging between 30 and 35 mS.cm(-1)), which was caused not only by the salinity of the influent but also by the reverse salt flux phenomenon. Soluble microbial products and extracted extracellular polymeric substances also increased in the reactor during the start-up. |
| publishDate |
2020 |
| dc.date.none.fl_str_mv |
2020 2020-10-01 |
| dc.type.none.fl_str_mv |
journal article http://purl.org/coar/resource_type/c_6501 VoR http://purl.org/coar/version/c_970fb48d4fbd8a85 |
| dc.type.openaire.fl_str_mv |
info:eu-repo/semantics/article |
| format |
article |
| dc.identifier.none.fl_str_mv |
https://riunet.upv.es/handle/10251/177256 |
| url |
https://riunet.upv.es/handle/10251/177256 |
| dc.language.none.fl_str_mv |
Inglés eng |
| language_invalid_str_mv |
Inglés |
| language |
eng |
| dc.relation.none.fl_str_mv |
Ministerio de Economía y Competitividad http://dx.doi.org/10.13039/501100003329 RTC-2015-3582-5Q4618002BC.VALENCIANA Desarrollo de un proceso de biorreactor de membranas para gestión de efluentes salinos. Proyecto ODEON |
| dc.rights.none.fl_str_mv |
open access http://purl.org/coar/access_right/c_abf2 Reconocimiento - No comercial - Sin obra derivada (by-nc-nd) http://creativecommons.org/licenses/by-nc-nd/4.0/ |
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info:eu-repo/semantics/openAccess |
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open access http://purl.org/coar/access_right/c_abf2 Reconocimiento - No comercial - Sin obra derivada (by-nc-nd) http://creativecommons.org/licenses/by-nc-nd/4.0/ |
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openAccess |
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application/pdf application/pdf |
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Elsevier |
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Elsevier |
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reponame:RiuNet. Repositorio Institucional de la Universitat Politécnica de Valéncia instname:Universitat Politècnica de València (UPV) |
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Universitat Politècnica de València (UPV) |
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