Development of a fluidized bed system for adsorption of phenol from aqueous solutions with commercial macroporous resins
Autor(a) principal: | |
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Data de Publicação: | 2007 |
Outros Autores: | , |
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=S0104-66322007000100002 |
Resumo: | This work is related to removal of phenol from wastewaters by adsorption onto polymeric resins, a current alternative to activated carbon. A closed circuit, bench-scale liquid fluidized bed system was developed for this purpose. Phenol aqueous solutions with initial concentrations in the range of 0.084 to 0.451 kg/m³ were used to fluidize small permeable capsules of stainless steel screen containing a commercial resin at 308 K. Experiments were carried out using a fluidizing velocity 20% above that of the minimum fluidization of the capsules. Typically, 30 passages of the liquid volume circulating through the bed were required to reach a quasi-equilibrium concentration of phenol in the treated effluent. A simple batch adsorption model using the Freundlich isotherm successfully predicted final phenol concentrations. Suspended solids, often present in residual waters and a common cause of fixed bed clogging, were simulated with wood sawdust. |
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Brazilian Journal of Chemical Engineering |
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|
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Development of a fluidized bed system for adsorption of phenol from aqueous solutions with commercial macroporous resinsPhenol adsorptionFluidized bedsMacroporous resinsThis work is related to removal of phenol from wastewaters by adsorption onto polymeric resins, a current alternative to activated carbon. A closed circuit, bench-scale liquid fluidized bed system was developed for this purpose. Phenol aqueous solutions with initial concentrations in the range of 0.084 to 0.451 kg/m³ were used to fluidize small permeable capsules of stainless steel screen containing a commercial resin at 308 K. Experiments were carried out using a fluidizing velocity 20% above that of the minimum fluidization of the capsules. Typically, 30 passages of the liquid volume circulating through the bed were required to reach a quasi-equilibrium concentration of phenol in the treated effluent. A simple batch adsorption model using the Freundlich isotherm successfully predicted final phenol concentrations. Suspended solids, often present in residual waters and a common cause of fixed bed clogging, were simulated with wood sawdust.Brazilian Society of Chemical Engineering2007-03-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322007000100002Brazilian Journal of Chemical Engineering v.24 n.1 2007reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322007000100002info:eu-repo/semantics/openAccessCorrêa,R. A.Calçada,L. A.Peçanha,R. P.eng2007-05-31T00:00:00Zoai:scielo:S0104-66322007000100002Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2007-05-31T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false |
dc.title.none.fl_str_mv |
Development of a fluidized bed system for adsorption of phenol from aqueous solutions with commercial macroporous resins |
title |
Development of a fluidized bed system for adsorption of phenol from aqueous solutions with commercial macroporous resins |
spellingShingle |
Development of a fluidized bed system for adsorption of phenol from aqueous solutions with commercial macroporous resins Corrêa,R. A. Phenol adsorption Fluidized beds Macroporous resins |
title_short |
Development of a fluidized bed system for adsorption of phenol from aqueous solutions with commercial macroporous resins |
title_full |
Development of a fluidized bed system for adsorption of phenol from aqueous solutions with commercial macroporous resins |
title_fullStr |
Development of a fluidized bed system for adsorption of phenol from aqueous solutions with commercial macroporous resins |
title_full_unstemmed |
Development of a fluidized bed system for adsorption of phenol from aqueous solutions with commercial macroporous resins |
title_sort |
Development of a fluidized bed system for adsorption of phenol from aqueous solutions with commercial macroporous resins |
author |
Corrêa,R. A. |
author_facet |
Corrêa,R. A. Calçada,L. A. Peçanha,R. P. |
author_role |
author |
author2 |
Calçada,L. A. Peçanha,R. P. |
author2_role |
author author |
dc.contributor.author.fl_str_mv |
Corrêa,R. A. Calçada,L. A. Peçanha,R. P. |
dc.subject.por.fl_str_mv |
Phenol adsorption Fluidized beds Macroporous resins |
topic |
Phenol adsorption Fluidized beds Macroporous resins |
description |
This work is related to removal of phenol from wastewaters by adsorption onto polymeric resins, a current alternative to activated carbon. A closed circuit, bench-scale liquid fluidized bed system was developed for this purpose. Phenol aqueous solutions with initial concentrations in the range of 0.084 to 0.451 kg/m³ were used to fluidize small permeable capsules of stainless steel screen containing a commercial resin at 308 K. Experiments were carried out using a fluidizing velocity 20% above that of the minimum fluidization of the capsules. Typically, 30 passages of the liquid volume circulating through the bed were required to reach a quasi-equilibrium concentration of phenol in the treated effluent. A simple batch adsorption model using the Freundlich isotherm successfully predicted final phenol concentrations. Suspended solids, often present in residual waters and a common cause of fixed bed clogging, were simulated with wood sawdust. |
publishDate |
2007 |
dc.date.none.fl_str_mv |
2007-03-01 |
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=S0104-66322007000100002 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322007000100002 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/S0104-66322007000100002 |
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.24 n.1 2007 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_ |
1754213172269547520 |