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

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. Beside...

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Main Authors: A. C. Cerqueira, R. Nobrega, G. L. Sant'Anna Jr, M. Dezotti
Format: Article
Language:English
Published: Brazilian Society of Chemical Engineering 2013-12-01
Series:Brazilian Journal of Chemical Engineering
Subjects:
Online Access:http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322013000400009&lng=en&tlng=en
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spelling doaj-65ad181180ef46e8ab5159661539d4e62020-11-24T23:01:17ZengBrazilian Society of Chemical EngineeringBrazilian Journal of Chemical Engineering0104-66322013-12-0130477177910.1590/S0104-66322013000400009S0104-66322013000400009Oxygen air enrichment through composite membrane: application to an aerated biofilm reactorA. C. Cerqueira0R. Nobrega1G. L. Sant'Anna Jr2M. Dezotti3Universidade Federal do Rio de JaneiroUniversidade Federal do Rio de JaneiroUniversidade Federal do Rio de JaneiroUniversidade Federal do Rio de JaneiroA 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.http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322013000400009&lng=en&tlng=enOxygen transferAerationMABRWastewater treatmentBiofilm
collection DOAJ
language English
format Article
sources DOAJ
author A. C. Cerqueira
R. Nobrega
G. L. Sant'Anna Jr
M. Dezotti
spellingShingle A. C. Cerqueira
R. Nobrega
G. L. Sant'Anna Jr
M. Dezotti
Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor
Brazilian Journal of Chemical Engineering
Oxygen transfer
Aeration
MABR
Wastewater treatment
Biofilm
author_facet A. C. Cerqueira
R. Nobrega
G. L. Sant'Anna Jr
M. Dezotti
author_sort A. C. Cerqueira
title Oxygen air enrichment through composite membrane: application to an aerated biofilm reactor
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
publisher Brazilian Society of Chemical Engineering
series Brazilian Journal of Chemical Engineering
issn 0104-6632
publishDate 2013-12-01
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.
topic Oxygen transfer
Aeration
MABR
Wastewater treatment
Biofilm
url http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322013000400009&lng=en&tlng=en
work_keys_str_mv AT accerqueira oxygenairenrichmentthroughcompositemembraneapplicationtoanaeratedbiofilmreactor
AT rnobrega oxygenairenrichmentthroughcompositemembraneapplicationtoanaeratedbiofilmreactor
AT glsantannajr oxygenairenrichmentthroughcompositemembraneapplicationtoanaeratedbiofilmreactor
AT mdezotti oxygenairenrichmentthroughcompositemembraneapplicationtoanaeratedbiofilmreactor
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