Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor

Detalhes bibliográficos
Autor(a) principal: Cerqueira,A. C.
Data de Publicação: 2013
Outros Autores: Nobrega,R., Sant'Anna Jr,G. L., Dezotti,M.
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=S0104-66322013000400009
Resumo: A highly permeable composite hollow-fibre membrane developed for air separation was used in a membrane aerated biofilm reactor (MABR). The composite membrane consisted of a porous support layer covered with a thin dense film, which was responsible for oxygen enrichment of the permeate stream. Besides oxygen enrichment capability, dense membranes overcome major operational problems that occur when using porous membranes for oxygen transfer to biofilms. Air flow rate and oxygen partial pressure inside the fibres were the variables used to adjust the oxygen transfer rate. The membrane aerated biofilm reactor was operated with hydraulic retention times (HRT) ranging from 1 to 4 hours. High organic load removal rates, like 6.5 kg.m-3.d-1, were achieved due to oxygen transfer rates as high as 107 kg.m-3.d-1. High COD removals, with improved oxygen transfer efficiency, indicate that a MABR is a compact alternative to the conventional activated sludge process and that the selected membrane is suitable for further applications.
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spelling Oxygen air enrichment through composite membrane: application to an aerated biofilm reactorOxygen transferAerationMABRWastewater treatmentBiofilmA highly permeable composite hollow-fibre membrane developed for air separation was used in a membrane aerated biofilm reactor (MABR). The composite membrane consisted of a porous support layer covered with a thin dense film, which was responsible for oxygen enrichment of the permeate stream. Besides oxygen enrichment capability, dense membranes overcome major operational problems that occur when using porous membranes for oxygen transfer to biofilms. Air flow rate and oxygen partial pressure inside the fibres were the variables used to adjust the oxygen transfer rate. The membrane aerated biofilm reactor was operated with hydraulic retention times (HRT) ranging from 1 to 4 hours. High organic load removal rates, like 6.5 kg.m-3.d-1, were achieved due to oxygen transfer rates as high as 107 kg.m-3.d-1. High COD removals, with improved oxygen transfer efficiency, indicate that a MABR is a compact alternative to the conventional activated sludge process and that the selected membrane is suitable for further applications.Brazilian Society of Chemical Engineering2013-12-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322013000400009Brazilian Journal of Chemical Engineering v.30 n.4 2013reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322013000400009info:eu-repo/semantics/openAccessCerqueira,A. C.Nobrega,R.Sant'Anna Jr,G. L.Dezotti,M.eng2014-01-10T00:00:00Zoai:scielo:S0104-66322013000400009Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2014-01-10T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false
dc.title.none.fl_str_mv Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor
title Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor
spellingShingle Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor
Cerqueira,A. C.
Oxygen transfer
Aeration
MABR
Wastewater treatment
Biofilm
title_short Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor
title_full Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor
title_fullStr Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor
title_full_unstemmed Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor
title_sort Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor
author Cerqueira,A. C.
author_facet Cerqueira,A. C.
Nobrega,R.
Sant'Anna Jr,G. L.
Dezotti,M.
author_role author
author2 Nobrega,R.
Sant'Anna Jr,G. L.
Dezotti,M.
author2_role author
author
author
dc.contributor.author.fl_str_mv Cerqueira,A. C.
Nobrega,R.
Sant'Anna Jr,G. L.
Dezotti,M.
dc.subject.por.fl_str_mv Oxygen transfer
Aeration
MABR
Wastewater treatment
Biofilm
topic Oxygen transfer
Aeration
MABR
Wastewater treatment
Biofilm
description A highly permeable composite hollow-fibre membrane developed for air separation was used in a membrane aerated biofilm reactor (MABR). The composite membrane consisted of a porous support layer covered with a thin dense film, which was responsible for oxygen enrichment of the permeate stream. Besides oxygen enrichment capability, dense membranes overcome major operational problems that occur when using porous membranes for oxygen transfer to biofilms. Air flow rate and oxygen partial pressure inside the fibres were the variables used to adjust the oxygen transfer rate. The membrane aerated biofilm reactor was operated with hydraulic retention times (HRT) ranging from 1 to 4 hours. High organic load removal rates, like 6.5 kg.m-3.d-1, were achieved due to oxygen transfer rates as high as 107 kg.m-3.d-1. High COD removals, with improved oxygen transfer efficiency, indicate that a MABR is a compact alternative to the conventional activated sludge process and that the selected membrane is suitable for further applications.
publishDate 2013
dc.date.none.fl_str_mv 2013-12-01
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=S0104-66322013000400009
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322013000400009
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 10.1590/S0104-66322013000400009
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.30 n.4 2013
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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