Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-up

Detalhes bibliográficos
Autor(a) principal: Cavaleiro, A. J.
Data de Publicação: 2009
Outros Autores: Salvador, A. F., Alves, J. I., Alves, M. M.
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/1822/9467
Resumo: Mineralization of a synthetic effluent containing 50% COD as oleic acid was achieved in a continuous anaerobic reactor at organic loading rates up to 21 kg COD m−3 day−1, HRT of 9 h, attaining 99% of COD removal efficiency and a methane yield higher than 70%. A maximum specific methane production rate of 1170 ± 170 mg COD-CH4 g VS−1 day−1 was measured during the reactor’s operation. A start-up strategy combining feeding phases and batch degradation phases was applied to promote the development of an anaerobic community efficient for long chain fatty acids (LCFA) mineralization. Through the start-up period, the methane yield increased gradually from 67% to 91%, and LCFA accumulated onto the sludge only during the first 60 days of operation. For the first time, it is demonstrated that a step feeding start-up is required to produce a specialized and efficient anaerobic community for continuous high rate anaerobic treatment of LCFA-rich wastewater.
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spelling Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-upScience & TechnologyMineralization of a synthetic effluent containing 50% COD as oleic acid was achieved in a continuous anaerobic reactor at organic loading rates up to 21 kg COD m−3 day−1, HRT of 9 h, attaining 99% of COD removal efficiency and a methane yield higher than 70%. A maximum specific methane production rate of 1170 ± 170 mg COD-CH4 g VS−1 day−1 was measured during the reactor’s operation. A start-up strategy combining feeding phases and batch degradation phases was applied to promote the development of an anaerobic community efficient for long chain fatty acids (LCFA) mineralization. Through the start-up period, the methane yield increased gradually from 67% to 91%, and LCFA accumulated onto the sludge only during the first 60 days of operation. For the first time, it is demonstrated that a step feeding start-up is required to produce a specialized and efficient anaerobic community for continuous high rate anaerobic treatment of LCFA-rich wastewater.Fundação para a Ciência e a Tecnologia (FCT) - POCTI/CTA/46328/2002, PTDC/BIO/69745/ 2006, SFRH/24256/2005European Commission (EC) - LIFE03 ENV/P/000501American Chemical SocietyUniversidade do MinhoCavaleiro, A. J.Salvador, A. F.Alves, J. I.Alves, M. M.2009-042009-04-01T00:00:00Zinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/1822/9467eng“Environmental Science and Technology”. ISSN 0013-936X. 43:8 (2009) 2931–2936.0013-936X10.1021/es803126419475973http://pubs.acs.org/doi/full/10.1021/es8031264info:eu-repo/semantics/openAccessreponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãoinstacron:RCAAP2023-07-21T12:04:34Zoai:repositorium.sdum.uminho.pt:1822/9467Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireopendoar:71602024-03-19T18:54:52.514626Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãofalse
dc.title.none.fl_str_mv Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-up
title Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-up
spellingShingle Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-up
Cavaleiro, A. J.
Science & Technology
title_short Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-up
title_full Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-up
title_fullStr Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-up
title_full_unstemmed Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-up
title_sort Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-up
author Cavaleiro, A. J.
author_facet Cavaleiro, A. J.
Salvador, A. F.
Alves, J. I.
Alves, M. M.
author_role author
author2 Salvador, A. F.
Alves, J. I.
Alves, M. M.
author2_role author
author
author
dc.contributor.none.fl_str_mv Universidade do Minho
dc.contributor.author.fl_str_mv Cavaleiro, A. J.
Salvador, A. F.
Alves, J. I.
Alves, M. M.
dc.subject.por.fl_str_mv Science & Technology
topic Science & Technology
description Mineralization of a synthetic effluent containing 50% COD as oleic acid was achieved in a continuous anaerobic reactor at organic loading rates up to 21 kg COD m−3 day−1, HRT of 9 h, attaining 99% of COD removal efficiency and a methane yield higher than 70%. A maximum specific methane production rate of 1170 ± 170 mg COD-CH4 g VS−1 day−1 was measured during the reactor’s operation. A start-up strategy combining feeding phases and batch degradation phases was applied to promote the development of an anaerobic community efficient for long chain fatty acids (LCFA) mineralization. Through the start-up period, the methane yield increased gradually from 67% to 91%, and LCFA accumulated onto the sludge only during the first 60 days of operation. For the first time, it is demonstrated that a step feeding start-up is required to produce a specialized and efficient anaerobic community for continuous high rate anaerobic treatment of LCFA-rich wastewater.
publishDate 2009
dc.date.none.fl_str_mv 2009-04
2009-04-01T00:00:00Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://hdl.handle.net/1822/9467
url http://hdl.handle.net/1822/9467
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv “Environmental Science and Technology”. ISSN 0013-936X. 43:8 (2009) 2931–2936.
0013-936X
10.1021/es8031264
19475973
http://pubs.acs.org/doi/full/10.1021/es8031264
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
dc.publisher.none.fl_str_mv American Chemical Society
publisher.none.fl_str_mv American Chemical Society
dc.source.none.fl_str_mv reponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
instacron:RCAAP
instname_str Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
instacron_str RCAAP
institution RCAAP
reponame_str Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
collection Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
repository.name.fl_str_mv Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
repository.mail.fl_str_mv
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