Continuous high rate anaerobic treatment of oleic acid based wastewater is possible after a step feeding start-up
Autor(a) principal: | |
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Data de Publicação: | 2009 |
Outros Autores: | , , |
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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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 |
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Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação |
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RCAAP |
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RCAAP |
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Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) |
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Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) |
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Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação |
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1799132332025708544 |