Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in series

Detalhes bibliográficos
Autor(a) principal: Urbinati, Estevão
Data de Publicação: 2014
Outros Autores: Oliveira, Roberto Alves De [UNESP]
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Institucional da UNESP
Texto Completo: http://dx.doi.org/10.1590/S0100-69162014000100014
http://hdl.handle.net/11449/109948
Resumo: In this work it was evaluated the performance of two systems of swine wastewater treatment consisting of two-stage upflow anaerobic sludge blanket (UASB) reactors, with and without post-treatment in sequencing batch reactor (SBR), fed continuously, with aerobic phase. The UASB reactors in the first stage had 908 L in the sets I and II, and in the second stage 350 and 188 L, respectively. In the set II the post-treatment was performed in a SBR of 3,000 L. The hydraulic detention times in the anaerobic treatment systems were 100, 75 and 58 h in the set I; 87, 65 and 51 h in the set II; and 240 and 180 h in the SBR. The volumetric organic load applied in the first stage UASB reactors ranged from 6.9 to 12.6 g total COD (L d)-1 in the set I and 7.5 to 9.8 g total COD (L d)-1 in the set II. The average removal efficiencies of total COD, total phosphorus (Ptotal), and Kjeldahl and organic nitrogen (KN and Norg) in the anaerobic treatment systems were similar and reached maximum values of 97%, 64%, 68%, and 98%. In the SBR, the removal efficiencies of total COD and thermotolerant coliforms were up to 62 and 92% resulting, respectively, in effluent concentrations of 135 mg L-1 and 2x10(4)MPN (100 mL)-1. For Ptotal, total nitrogen (TN) and Norg, the average removal efficiencies in the SBR were up to 58, 25 and 73%, respectively.
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spelling Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in seriesTratamento anaeróbio-aeróbio de águas residuárias de suinocultura com reatores uasb e batelada em sérieColiformsMethanetwo-stage anaerobic reactorsNutrients removalcombined treatmentcoliformesMetanoReator anaeróbio em dois estágiosRemoção de nutrientestratamento combinadoIn this work it was evaluated the performance of two systems of swine wastewater treatment consisting of two-stage upflow anaerobic sludge blanket (UASB) reactors, with and without post-treatment in sequencing batch reactor (SBR), fed continuously, with aerobic phase. The UASB reactors in the first stage had 908 L in the sets I and II, and in the second stage 350 and 188 L, respectively. In the set II the post-treatment was performed in a SBR of 3,000 L. The hydraulic detention times in the anaerobic treatment systems were 100, 75 and 58 h in the set I; 87, 65 and 51 h in the set II; and 240 and 180 h in the SBR. The volumetric organic load applied in the first stage UASB reactors ranged from 6.9 to 12.6 g total COD (L d)-1 in the set I and 7.5 to 9.8 g total COD (L d)-1 in the set II. The average removal efficiencies of total COD, total phosphorus (Ptotal), and Kjeldahl and organic nitrogen (KN and Norg) in the anaerobic treatment systems were similar and reached maximum values of 97%, 64%, 68%, and 98%. In the SBR, the removal efficiencies of total COD and thermotolerant coliforms were up to 62 and 92% resulting, respectively, in effluent concentrations of 135 mg L-1 and 2x10(4)MPN (100 mL)-1. For Ptotal, total nitrogen (TN) and Norg, the average removal efficiencies in the SBR were up to 58, 25 and 73%, respectively.O desempenho de dois sistemas de tratamento de águas residuárias de suinocultura com reatores anaeróbios de fluxo ascendente com manta de lodo (UASB), em dois estágios, foi avaliado com e sem pós-tratamento em reator operado em batelada sequencial alimentada (RBS), com etapa aeróbia. Os reatores UASB do primeiro estágio possuíam 908 L nos conjuntos I e II, e no segundo estágio, 350 e 188 L, respectivamente. No conjunto II foi realizado o pós-tratamento em RBS de 3000 L. Os tempos de detenção hidráulica nos sistemas de tratamento foram de 100; 75 e 58 h no conjunto I; de 87; 65 e 51 h no conjunto II, e de 240 e 180 h no RBS. As cargas orgânicas volumétricas nos reatores UASB do primeiro estágio variaram de 6,9 a 12,6 g DQOtotal (L d)-1 no conjunto I, e de 7,5 a 9,8 g DQOtotal (L d)-1 no conjunto II. As eficiências médias de remoção de DQOtotal, fósforo total (Ptotal), nitrogênio Kjeldahl (NK) e nitrogênio orgânico (Norg.) nos sistemas de tratamento anaeróbio atingiram valores máximos de 97; 64; 68 e 98 %, respectivamente. No RBS, as eficiências de remoção de DQOtotal e coliformes termotolerantes foram de até 62 e 92%, reduzindo para 135 mg L-1 e 2 x 10(4) NMP (100 mL)-1, respectivamente, os valores médios no efluente. Para o Ptotal, nitrogênio total (NT) e Norg, as eficiências de remoção no RBS foram de até 58; 25 e 73%, respectivamente.Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)UNESP Faculdade de Ciências Agrárias e Veterinárias Departamento de Engenharia RuralUNESP Faculdade de Ciências Agrárias e Veterinárias Departamento de Engenharia RuralAssociação Brasileira de Engenharia Agrícola (SBEA)Universidade Estadual Paulista (Unesp)Urbinati, EstevãoOliveira, Roberto Alves De [UNESP]2014-10-01T13:08:42Z2014-10-01T13:08:42Z2014-02-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article124-142application/pdfhttp://dx.doi.org/10.1590/S0100-69162014000100014Engenharia Agrícola. Associação Brasileira de Engenharia Agrícola, v. 34, n. 1, p. 124-142, 2014.0100-6916http://hdl.handle.net/11449/10994810.1590/S0100-69162014000100014S0100-69162014000100014WOS:000334098700014S0100-69162014000100014.pdf41156325870137470000-0003-2832-2848SciELOreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengEngenharia Agrícola0.3870,305info:eu-repo/semantics/openAccess2024-06-06T15:18:43Zoai:repositorio.unesp.br:11449/109948Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T22:04:03.374890Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false
dc.title.none.fl_str_mv Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in series
Tratamento anaeróbio-aeróbio de águas residuárias de suinocultura com reatores uasb e batelada em série
title Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in series
spellingShingle Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in series
Urbinati, Estevão
Coliforms
Methane
two-stage anaerobic reactors
Nutrients removal
combined treatment
coliformes
Metano
Reator anaeróbio em dois estágios
Remoção de nutrientes
tratamento combinado
title_short Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in series
title_full Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in series
title_fullStr Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in series
title_full_unstemmed Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in series
title_sort Anaerobic-aerobic treatment of swine wastewater in uasb and batch reactors in series
author Urbinati, Estevão
author_facet Urbinati, Estevão
Oliveira, Roberto Alves De [UNESP]
author_role author
author2 Oliveira, Roberto Alves De [UNESP]
author2_role author
dc.contributor.none.fl_str_mv Universidade Estadual Paulista (Unesp)
dc.contributor.author.fl_str_mv Urbinati, Estevão
Oliveira, Roberto Alves De [UNESP]
dc.subject.por.fl_str_mv Coliforms
Methane
two-stage anaerobic reactors
Nutrients removal
combined treatment
coliformes
Metano
Reator anaeróbio em dois estágios
Remoção de nutrientes
tratamento combinado
topic Coliforms
Methane
two-stage anaerobic reactors
Nutrients removal
combined treatment
coliformes
Metano
Reator anaeróbio em dois estágios
Remoção de nutrientes
tratamento combinado
description In this work it was evaluated the performance of two systems of swine wastewater treatment consisting of two-stage upflow anaerobic sludge blanket (UASB) reactors, with and without post-treatment in sequencing batch reactor (SBR), fed continuously, with aerobic phase. The UASB reactors in the first stage had 908 L in the sets I and II, and in the second stage 350 and 188 L, respectively. In the set II the post-treatment was performed in a SBR of 3,000 L. The hydraulic detention times in the anaerobic treatment systems were 100, 75 and 58 h in the set I; 87, 65 and 51 h in the set II; and 240 and 180 h in the SBR. The volumetric organic load applied in the first stage UASB reactors ranged from 6.9 to 12.6 g total COD (L d)-1 in the set I and 7.5 to 9.8 g total COD (L d)-1 in the set II. The average removal efficiencies of total COD, total phosphorus (Ptotal), and Kjeldahl and organic nitrogen (KN and Norg) in the anaerobic treatment systems were similar and reached maximum values of 97%, 64%, 68%, and 98%. In the SBR, the removal efficiencies of total COD and thermotolerant coliforms were up to 62 and 92% resulting, respectively, in effluent concentrations of 135 mg L-1 and 2x10(4)MPN (100 mL)-1. For Ptotal, total nitrogen (TN) and Norg, the average removal efficiencies in the SBR were up to 58, 25 and 73%, respectively.
publishDate 2014
dc.date.none.fl_str_mv 2014-10-01T13:08:42Z
2014-10-01T13:08:42Z
2014-02-01
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://dx.doi.org/10.1590/S0100-69162014000100014
Engenharia Agrícola. Associação Brasileira de Engenharia Agrícola, v. 34, n. 1, p. 124-142, 2014.
0100-6916
http://hdl.handle.net/11449/109948
10.1590/S0100-69162014000100014
S0100-69162014000100014
WOS:000334098700014
S0100-69162014000100014.pdf
4115632587013747
0000-0003-2832-2848
url http://dx.doi.org/10.1590/S0100-69162014000100014
http://hdl.handle.net/11449/109948
identifier_str_mv Engenharia Agrícola. Associação Brasileira de Engenharia Agrícola, v. 34, n. 1, p. 124-142, 2014.
0100-6916
10.1590/S0100-69162014000100014
S0100-69162014000100014
WOS:000334098700014
S0100-69162014000100014.pdf
4115632587013747
0000-0003-2832-2848
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Engenharia Agrícola
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dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
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dc.format.none.fl_str_mv 124-142
application/pdf
dc.publisher.none.fl_str_mv Associação Brasileira de Engenharia Agrícola (SBEA)
publisher.none.fl_str_mv Associação Brasileira de Engenharia Agrícola (SBEA)
dc.source.none.fl_str_mv SciELO
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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