Anaerobic treatment of wastewater from coffee pulping in upflow anaerobic sludge blanket (UASB) in two stages

Detalhes bibliográficos
Autor(a) principal: Bruno, M. [UNESP]
Data de Publicação: 2008
Outros Autores: Oliveira, R. A. de [UNESP]
Tipo de documento: Artigo de conferência
Idioma: eng
Título da fonte: Repositório Institucional da UNESP
Texto Completo: https://elibrary.asabe.org/azdez.asp?JID=1&AID=25498&CID=lenv2009&T=2
http://hdl.handle.net/11449/70840
Resumo: In this work, the efficiency of two-stage upflow anaerobic sludge blanket (UASB) reactors was evaluated in bench scale, for treating a liquid effluent from coffee pulping. Hydraulic detention times (HDT) were 4.0; 5.2 and 6.2 days, resulting in organic loading rates (OLR) of 5.8; 3.6 and 3.0g total COD per (L-d) in the first reactor (Rl) and HDT of 2.0; 2.6 and 3.1 days with OLR of 5.8; 0.5 and 0.4 g total COD per (L-d) in the second reactor (R2). The medium values of total COD affluent varied from 15.440 to 23.040 mg O 2/L, and in the effluent to the reactors 1 and 2 were from l.lOO to 11.500 mg 0 2/L and 420 to 9.000 mg O 2/L, respectively. The medium values of removal efficiencies of total COD and TSS varied from 66 to 98% and 93 to 97%, respectively, in the system of treatment with the UASB reactors, in two stages. The content of methane in the biogas varied from 69 to 89% in the Rl and from 52 to 73% in the R2. The maximum volumetric methane production of 0.483 m 3 CH 4per (m 3 reactor d) was obtained with OLR of 3.6 g total COD per (L reactor d) and HDT of 6.2 days in the Rl. The volatile fatty acids concentration was kept below 100mg/L with HDT of 5.2 and 6.2 days in the Rl and HDT of 2.6 and 3.1 days in the R2.
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spelling Anaerobic treatment of wastewater from coffee pulping in upflow anaerobic sludge blanket (UASB) in two stagesAnaerobic digestionCoffee wastewaterPhenolsAnaerobic treatmentsLiquid effluentsMethane productionsOrganic loading ratesRemoval efficienciesTwo stagesUasb reactorsUp-flow anaerobic sludge blanket reactorsUp-flow anaerobic sludge blanketsVolatile fatty acidsAgricultureBiogasChemical oxygen demandEffluentsFatty acidsMethaneRemovalWastewaterWastewater treatmentIn this work, the efficiency of two-stage upflow anaerobic sludge blanket (UASB) reactors was evaluated in bench scale, for treating a liquid effluent from coffee pulping. Hydraulic detention times (HDT) were 4.0; 5.2 and 6.2 days, resulting in organic loading rates (OLR) of 5.8; 3.6 and 3.0g total COD per (L-d) in the first reactor (Rl) and HDT of 2.0; 2.6 and 3.1 days with OLR of 5.8; 0.5 and 0.4 g total COD per (L-d) in the second reactor (R2). The medium values of total COD affluent varied from 15.440 to 23.040 mg O 2/L, and in the effluent to the reactors 1 and 2 were from l.lOO to 11.500 mg 0 2/L and 420 to 9.000 mg O 2/L, respectively. The medium values of removal efficiencies of total COD and TSS varied from 66 to 98% and 93 to 97%, respectively, in the system of treatment with the UASB reactors, in two stages. The content of methane in the biogas varied from 69 to 89% in the Rl and from 52 to 73% in the R2. The maximum volumetric methane production of 0.483 m 3 CH 4per (m 3 reactor d) was obtained with OLR of 3.6 g total COD per (L reactor d) and HDT of 6.2 days in the Rl. The volatile fatty acids concentration was kept below 100mg/L with HDT of 5.2 and 6.2 days in the Rl and HDT of 2.6 and 3.1 days in the R2.Doutorando em Microbiologia Agropecuaria FCAV-UNESPDepartamento de Engenharia Rural FCAV-UNESPDoutorando em Microbiologia Agropecuaria FCAV-UNESPDepartamento de Engenharia Rural FCAV-UNESPUniversidade Estadual Paulista (Unesp)Bruno, M. [UNESP]Oliveira, R. A. de [UNESP]2014-05-27T11:23:49Z2014-05-27T11:23:49Z2008-12-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/conferenceObject191-198application/pdfhttps://elibrary.asabe.org/azdez.asp?JID=1&AID=25498&CID=lenv2009&T=2Livestock Environment VIII - Proceedings of the 8th International Symposium, p. 191-198.http://hdl.handle.net/11449/708402-s2.0-631491274012-s2.0-63149127401.pdf4115632587013747Scopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengLivestock Environment VIII - Proceedings of the 8th International Symposiuminfo:eu-repo/semantics/openAccess2024-06-06T15:18:58Zoai:repositorio.unesp.br:11449/70840Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T20:51:50.402392Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false
dc.title.none.fl_str_mv Anaerobic treatment of wastewater from coffee pulping in upflow anaerobic sludge blanket (UASB) in two stages
title Anaerobic treatment of wastewater from coffee pulping in upflow anaerobic sludge blanket (UASB) in two stages
spellingShingle Anaerobic treatment of wastewater from coffee pulping in upflow anaerobic sludge blanket (UASB) in two stages
Bruno, M. [UNESP]
Anaerobic digestion
Coffee wastewater
Phenols
Anaerobic treatments
Liquid effluents
Methane productions
Organic loading rates
Removal efficiencies
Two stages
Uasb reactors
Up-flow anaerobic sludge blanket reactors
Up-flow anaerobic sludge blankets
Volatile fatty acids
Agriculture
Biogas
Chemical oxygen demand
Effluents
Fatty acids
Methane
Removal
Wastewater
Wastewater treatment
title_short Anaerobic treatment of wastewater from coffee pulping in upflow anaerobic sludge blanket (UASB) in two stages
title_full Anaerobic treatment of wastewater from coffee pulping in upflow anaerobic sludge blanket (UASB) in two stages
title_fullStr Anaerobic treatment of wastewater from coffee pulping in upflow anaerobic sludge blanket (UASB) in two stages
title_full_unstemmed Anaerobic treatment of wastewater from coffee pulping in upflow anaerobic sludge blanket (UASB) in two stages
title_sort Anaerobic treatment of wastewater from coffee pulping in upflow anaerobic sludge blanket (UASB) in two stages
author Bruno, M. [UNESP]
author_facet Bruno, M. [UNESP]
Oliveira, R. A. de [UNESP]
author_role author
author2 Oliveira, R. A. de [UNESP]
author2_role author
dc.contributor.none.fl_str_mv Universidade Estadual Paulista (Unesp)
dc.contributor.author.fl_str_mv Bruno, M. [UNESP]
Oliveira, R. A. de [UNESP]
dc.subject.por.fl_str_mv Anaerobic digestion
Coffee wastewater
Phenols
Anaerobic treatments
Liquid effluents
Methane productions
Organic loading rates
Removal efficiencies
Two stages
Uasb reactors
Up-flow anaerobic sludge blanket reactors
Up-flow anaerobic sludge blankets
Volatile fatty acids
Agriculture
Biogas
Chemical oxygen demand
Effluents
Fatty acids
Methane
Removal
Wastewater
Wastewater treatment
topic Anaerobic digestion
Coffee wastewater
Phenols
Anaerobic treatments
Liquid effluents
Methane productions
Organic loading rates
Removal efficiencies
Two stages
Uasb reactors
Up-flow anaerobic sludge blanket reactors
Up-flow anaerobic sludge blankets
Volatile fatty acids
Agriculture
Biogas
Chemical oxygen demand
Effluents
Fatty acids
Methane
Removal
Wastewater
Wastewater treatment
description In this work, the efficiency of two-stage upflow anaerobic sludge blanket (UASB) reactors was evaluated in bench scale, for treating a liquid effluent from coffee pulping. Hydraulic detention times (HDT) were 4.0; 5.2 and 6.2 days, resulting in organic loading rates (OLR) of 5.8; 3.6 and 3.0g total COD per (L-d) in the first reactor (Rl) and HDT of 2.0; 2.6 and 3.1 days with OLR of 5.8; 0.5 and 0.4 g total COD per (L-d) in the second reactor (R2). The medium values of total COD affluent varied from 15.440 to 23.040 mg O 2/L, and in the effluent to the reactors 1 and 2 were from l.lOO to 11.500 mg 0 2/L and 420 to 9.000 mg O 2/L, respectively. The medium values of removal efficiencies of total COD and TSS varied from 66 to 98% and 93 to 97%, respectively, in the system of treatment with the UASB reactors, in two stages. The content of methane in the biogas varied from 69 to 89% in the Rl and from 52 to 73% in the R2. The maximum volumetric methane production of 0.483 m 3 CH 4per (m 3 reactor d) was obtained with OLR of 3.6 g total COD per (L reactor d) and HDT of 6.2 days in the Rl. The volatile fatty acids concentration was kept below 100mg/L with HDT of 5.2 and 6.2 days in the Rl and HDT of 2.6 and 3.1 days in the R2.
publishDate 2008
dc.date.none.fl_str_mv 2008-12-01
2014-05-27T11:23:49Z
2014-05-27T11:23:49Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/conferenceObject
format conferenceObject
status_str publishedVersion
dc.identifier.uri.fl_str_mv https://elibrary.asabe.org/azdez.asp?JID=1&AID=25498&CID=lenv2009&T=2
Livestock Environment VIII - Proceedings of the 8th International Symposium, p. 191-198.
http://hdl.handle.net/11449/70840
2-s2.0-63149127401
2-s2.0-63149127401.pdf
4115632587013747
url https://elibrary.asabe.org/azdez.asp?JID=1&AID=25498&CID=lenv2009&T=2
http://hdl.handle.net/11449/70840
identifier_str_mv Livestock Environment VIII - Proceedings of the 8th International Symposium, p. 191-198.
2-s2.0-63149127401
2-s2.0-63149127401.pdf
4115632587013747
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Livestock Environment VIII - Proceedings of the 8th International Symposium
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv 191-198
application/pdf
dc.source.none.fl_str_mv Scopus
reponame:Repositório Institucional da UNESP
instname:Universidade Estadual Paulista (UNESP)
instacron:UNESP
instname_str Universidade Estadual Paulista (UNESP)
instacron_str UNESP
institution UNESP
reponame_str Repositório Institucional da UNESP
collection Repositório Institucional da UNESP
repository.name.fl_str_mv Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)
repository.mail.fl_str_mv
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