Biohydrogen production from cassava wastewater in an anaerobic fluidized bed reactor

Detalhes bibliográficos
Autor(a) principal: Amorim,N. C. S.
Data de Publicação: 2014
Outros Autores: Alves,I., Martins,J. S., Amorim,E. L. C.
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=S0104-66322014000300003
Resumo: The effect of hydraulic retention time (HRT) and organic loading rate (OLR) on biological hydrogen production was assessed using an anaerobic fluidized bed reactor fed with cassava wastewater. The HRT of this reactor ranged from 8 to 1 h (28 to 161 kg COD/m³-d). The inoculum was obtained from a facultative pond sludge derived from swine wastewater treatment. The effluent pH was approximately 5.00, while the influent chemical oxygen demand (COD) measured 4000 mg COD/L. The hydrogen yield production increased from 0.13 to 1.91 mol H2/mol glucose as the HRT decreased from 8 to 2 h. The hydrogen production rate significantly increased from 0.20 to 2.04 L/h/L when the HRT decreased from 8 to 1 h. The main soluble metabolites were ethanol (1.87-100%), acetic acid (0.00-84.80%), butyric acid (0.00-66.78%) and propionic acid (0.00-50.14%). Overall, we conclude that the best hydrogen yield production was obtained at an HRT of 2 h.
id ABEQ-1_1580c783ec879e32a77a9ab709395ed5
oai_identifier_str oai:scielo:S0104-66322014000300003
network_acronym_str ABEQ-1
network_name_str Brazilian Journal of Chemical Engineering
repository_id_str
spelling Biohydrogen production from cassava wastewater in an anaerobic fluidized bed reactorAnaerobic fluidized bed reactorDark fermentationCassava wastewaterHydrogen productionOrganic loading rateThe effect of hydraulic retention time (HRT) and organic loading rate (OLR) on biological hydrogen production was assessed using an anaerobic fluidized bed reactor fed with cassava wastewater. The HRT of this reactor ranged from 8 to 1 h (28 to 161 kg COD/m³-d). The inoculum was obtained from a facultative pond sludge derived from swine wastewater treatment. The effluent pH was approximately 5.00, while the influent chemical oxygen demand (COD) measured 4000 mg COD/L. The hydrogen yield production increased from 0.13 to 1.91 mol H2/mol glucose as the HRT decreased from 8 to 2 h. The hydrogen production rate significantly increased from 0.20 to 2.04 L/h/L when the HRT decreased from 8 to 1 h. The main soluble metabolites were ethanol (1.87-100%), acetic acid (0.00-84.80%), butyric acid (0.00-66.78%) and propionic acid (0.00-50.14%). Overall, we conclude that the best hydrogen yield production was obtained at an HRT of 2 h.Brazilian Society of Chemical Engineering2014-09-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322014000300003Brazilian Journal of Chemical Engineering v.31 n.3 2014reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/0104-6632.20140313s00002458info:eu-repo/semantics/openAccessAmorim,N. C. S.Alves,I.Martins,J. S.Amorim,E. L. C.eng2014-09-17T00:00:00Zoai:scielo:S0104-66322014000300003Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2014-09-17T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false
dc.title.none.fl_str_mv Biohydrogen production from cassava wastewater in an anaerobic fluidized bed reactor
title Biohydrogen production from cassava wastewater in an anaerobic fluidized bed reactor
spellingShingle Biohydrogen production from cassava wastewater in an anaerobic fluidized bed reactor
Amorim,N. C. S.
Anaerobic fluidized bed reactor
Dark fermentation
Cassava wastewater
Hydrogen production
Organic loading rate
title_short Biohydrogen production from cassava wastewater in an anaerobic fluidized bed reactor
title_full Biohydrogen production from cassava wastewater in an anaerobic fluidized bed reactor
title_fullStr Biohydrogen production from cassava wastewater in an anaerobic fluidized bed reactor
title_full_unstemmed Biohydrogen production from cassava wastewater in an anaerobic fluidized bed reactor
title_sort Biohydrogen production from cassava wastewater in an anaerobic fluidized bed reactor
author Amorim,N. C. S.
author_facet Amorim,N. C. S.
Alves,I.
Martins,J. S.
Amorim,E. L. C.
author_role author
author2 Alves,I.
Martins,J. S.
Amorim,E. L. C.
author2_role author
author
author
dc.contributor.author.fl_str_mv Amorim,N. C. S.
Alves,I.
Martins,J. S.
Amorim,E. L. C.
dc.subject.por.fl_str_mv Anaerobic fluidized bed reactor
Dark fermentation
Cassava wastewater
Hydrogen production
Organic loading rate
topic Anaerobic fluidized bed reactor
Dark fermentation
Cassava wastewater
Hydrogen production
Organic loading rate
description The effect of hydraulic retention time (HRT) and organic loading rate (OLR) on biological hydrogen production was assessed using an anaerobic fluidized bed reactor fed with cassava wastewater. The HRT of this reactor ranged from 8 to 1 h (28 to 161 kg COD/m³-d). The inoculum was obtained from a facultative pond sludge derived from swine wastewater treatment. The effluent pH was approximately 5.00, while the influent chemical oxygen demand (COD) measured 4000 mg COD/L. The hydrogen yield production increased from 0.13 to 1.91 mol H2/mol glucose as the HRT decreased from 8 to 2 h. The hydrogen production rate significantly increased from 0.20 to 2.04 L/h/L when the HRT decreased from 8 to 1 h. The main soluble metabolites were ethanol (1.87-100%), acetic acid (0.00-84.80%), butyric acid (0.00-66.78%) and propionic acid (0.00-50.14%). Overall, we conclude that the best hydrogen yield production was obtained at an HRT of 2 h.
publishDate 2014
dc.date.none.fl_str_mv 2014-09-01
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=S0104-66322014000300003
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322014000300003
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 10.1590/0104-6632.20140313s00002458
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.31 n.3 2014
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
_version_ 1754213174321610752