AnSBBR applied to biomethane production for vinasse treatment: effects of organic loading, feed strategy and temperature

Detalhes bibliográficos
Autor(a) principal: Almeida,W. A.
Data de Publicação: 2017
Outros Autores: Ratusznei,S. M., Zaiat,M., Rodrigues,J. A. D.
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Brazilian Journal of Chemical Engineering
Texto Completo: http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300759
Resumo: Abstract This study assessed the feasibility of an anaerobic sequencing batch and fed-batch biofilm reactor (AnSBBR) with mechanical stirring for vinasse treatment and biomethane production. The amount of liquid medium used was 3 L, and the treated volume was 1 L per cycle. The cycle time was 8 h, with feeding times of 10 min (batch mode) and 240 min (fed-batch mode). Methane productivity increased with the increase in organic load from 1.0 to 10.0 gCOD.L-1.d-1. The maximum molar productivity and yield of methane were 123.4 molCH4.m-3.d-1 and 13.8 mmolCH4.gCOD-1 (88% of the theoretical), respectively. These parameters were lower in fed-batch mode than in batch mode and were lower at 45°C than at 30°C due to biomass adaptation. In general, the values of the kinetic parameters increased with organic load and were similar for the batch and fed-batch modes. Therefore, the increase in organic load positively influenced the process by increased COD removal and lower volatile acids accumulation as the load increased. The batch mode performed better than did the fed-batch mode and 30°C was more suitable than 45°C to produce methane under the studied conditions.
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spelling AnSBBR applied to biomethane production for vinasse treatment: effects of organic loading, feed strategy and temperatureAnSBBRbiomethaneapplied organic loadfeed strategytemperatureAbstract This study assessed the feasibility of an anaerobic sequencing batch and fed-batch biofilm reactor (AnSBBR) with mechanical stirring for vinasse treatment and biomethane production. The amount of liquid medium used was 3 L, and the treated volume was 1 L per cycle. The cycle time was 8 h, with feeding times of 10 min (batch mode) and 240 min (fed-batch mode). Methane productivity increased with the increase in organic load from 1.0 to 10.0 gCOD.L-1.d-1. The maximum molar productivity and yield of methane were 123.4 molCH4.m-3.d-1 and 13.8 mmolCH4.gCOD-1 (88% of the theoretical), respectively. These parameters were lower in fed-batch mode than in batch mode and were lower at 45°C than at 30°C due to biomass adaptation. In general, the values of the kinetic parameters increased with organic load and were similar for the batch and fed-batch modes. Therefore, the increase in organic load positively influenced the process by increased COD removal and lower volatile acids accumulation as the load increased. The batch mode performed better than did the fed-batch mode and 30°C was more suitable than 45°C to produce methane under the studied conditions.Brazilian Society of Chemical Engineering2017-07-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300759Brazilian Journal of Chemical Engineering v.34 n.3 2017reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/0104-6632.20170343s20150584info:eu-repo/semantics/openAccessAlmeida,W. A.Ratusznei,S. M.Zaiat,M.Rodrigues,J. A. D.eng2018-02-01T00:00:00Zoai:scielo:S0104-66322017000300759Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2018-02-01T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false
dc.title.none.fl_str_mv AnSBBR applied to biomethane production for vinasse treatment: effects of organic loading, feed strategy and temperature
title AnSBBR applied to biomethane production for vinasse treatment: effects of organic loading, feed strategy and temperature
spellingShingle AnSBBR applied to biomethane production for vinasse treatment: effects of organic loading, feed strategy and temperature
Almeida,W. A.
AnSBBR
biomethane
applied organic load
feed strategy
temperature
title_short AnSBBR applied to biomethane production for vinasse treatment: effects of organic loading, feed strategy and temperature
title_full AnSBBR applied to biomethane production for vinasse treatment: effects of organic loading, feed strategy and temperature
title_fullStr AnSBBR applied to biomethane production for vinasse treatment: effects of organic loading, feed strategy and temperature
title_full_unstemmed AnSBBR applied to biomethane production for vinasse treatment: effects of organic loading, feed strategy and temperature
title_sort AnSBBR applied to biomethane production for vinasse treatment: effects of organic loading, feed strategy and temperature
author Almeida,W. A.
author_facet Almeida,W. A.
Ratusznei,S. M.
Zaiat,M.
Rodrigues,J. A. D.
author_role author
author2 Ratusznei,S. M.
Zaiat,M.
Rodrigues,J. A. D.
author2_role author
author
author
dc.contributor.author.fl_str_mv Almeida,W. A.
Ratusznei,S. M.
Zaiat,M.
Rodrigues,J. A. D.
dc.subject.por.fl_str_mv AnSBBR
biomethane
applied organic load
feed strategy
temperature
topic AnSBBR
biomethane
applied organic load
feed strategy
temperature
description Abstract This study assessed the feasibility of an anaerobic sequencing batch and fed-batch biofilm reactor (AnSBBR) with mechanical stirring for vinasse treatment and biomethane production. The amount of liquid medium used was 3 L, and the treated volume was 1 L per cycle. The cycle time was 8 h, with feeding times of 10 min (batch mode) and 240 min (fed-batch mode). Methane productivity increased with the increase in organic load from 1.0 to 10.0 gCOD.L-1.d-1. The maximum molar productivity and yield of methane were 123.4 molCH4.m-3.d-1 and 13.8 mmolCH4.gCOD-1 (88% of the theoretical), respectively. These parameters were lower in fed-batch mode than in batch mode and were lower at 45°C than at 30°C due to biomass adaptation. In general, the values of the kinetic parameters increased with organic load and were similar for the batch and fed-batch modes. Therefore, the increase in organic load positively influenced the process by increased COD removal and lower volatile acids accumulation as the load increased. The batch mode performed better than did the fed-batch mode and 30°C was more suitable than 45°C to produce methane under the studied conditions.
publishDate 2017
dc.date.none.fl_str_mv 2017-07-01
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300759
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300759
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 10.1590/0104-6632.20170343s20150584
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv text/html
dc.publisher.none.fl_str_mv Brazilian Society of Chemical Engineering
publisher.none.fl_str_mv Brazilian Society of Chemical Engineering
dc.source.none.fl_str_mv Brazilian Journal of Chemical Engineering v.34 n.3 2017
reponame:Brazilian Journal of Chemical Engineering
instname:Associação Brasileira de Engenharia Química (ABEQ)
instacron:ABEQ
instname_str Associação Brasileira de Engenharia Química (ABEQ)
instacron_str ABEQ
institution ABEQ
reponame_str Brazilian Journal of Chemical Engineering
collection Brazilian Journal of Chemical Engineering
repository.name.fl_str_mv Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)
repository.mail.fl_str_mv rgiudici@usp.br||rgiudici@usp.br
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