ADSORPTION OF THE DYE REACTIVE BLUE 5G IN RETORTED SHALE
Autor(a) principal: | |
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Data de Publicação: | 2015 |
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=S0104-66322015000100269 |
Resumo: | Abstract In this study the influence of the volumetric flow rate and feed concentration was investigated for the adsorption of the reactive dye Blue 5G. Experiments were carried out in a bed packed with retorted shale, at 30 ºC. The ranges investigated were flow rate 2 -10 mL/min and the feed concentration 13-105 mg/L. Mathematical models were used to represent the dynamic sorption. The double resistance model considers the effects of the axial dispersion and the mass transfer resistance of the external film and inside the particles. As a result, the mass transfer coefficient of the external film and the internal mass transfer coefficient were estimated. The Thomas model was used to simulate the experimental data. In this model the fitted parameter was the adsorption kinetic constant. The first model provided an acceptable representation of the dynamic uptake of the reactive dye Blue 5G. |
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Brazilian Journal of Chemical Engineering |
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ADSORPTION OF THE DYE REACTIVE BLUE 5G IN RETORTED SHALEMathematical modelingPacked bedReactive dyeAdsorptionShaleAbstract In this study the influence of the volumetric flow rate and feed concentration was investigated for the adsorption of the reactive dye Blue 5G. Experiments were carried out in a bed packed with retorted shale, at 30 ºC. The ranges investigated were flow rate 2 -10 mL/min and the feed concentration 13-105 mg/L. Mathematical models were used to represent the dynamic sorption. The double resistance model considers the effects of the axial dispersion and the mass transfer resistance of the external film and inside the particles. As a result, the mass transfer coefficient of the external film and the internal mass transfer coefficient were estimated. The Thomas model was used to simulate the experimental data. In this model the fitted parameter was the adsorption kinetic constant. The first model provided an acceptable representation of the dynamic uptake of the reactive dye Blue 5G.Brazilian Society of Chemical Engineering2015-03-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322015000100269Brazilian Journal of Chemical Engineering v.32 n.1 2015reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/0104-6632.20150321s00001715info:eu-repo/semantics/openAccessLambrecht,R.Barros,M. A. S. D. deArroyo,P. A.Borba,C. E.Silva,E. A. daeng2015-05-12T00:00:00Zoai:scielo:S0104-66322015000100269Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2015-05-12T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false |
dc.title.none.fl_str_mv |
ADSORPTION OF THE DYE REACTIVE BLUE 5G IN RETORTED SHALE |
title |
ADSORPTION OF THE DYE REACTIVE BLUE 5G IN RETORTED SHALE |
spellingShingle |
ADSORPTION OF THE DYE REACTIVE BLUE 5G IN RETORTED SHALE Lambrecht,R. Mathematical modeling Packed bed Reactive dye Adsorption Shale |
title_short |
ADSORPTION OF THE DYE REACTIVE BLUE 5G IN RETORTED SHALE |
title_full |
ADSORPTION OF THE DYE REACTIVE BLUE 5G IN RETORTED SHALE |
title_fullStr |
ADSORPTION OF THE DYE REACTIVE BLUE 5G IN RETORTED SHALE |
title_full_unstemmed |
ADSORPTION OF THE DYE REACTIVE BLUE 5G IN RETORTED SHALE |
title_sort |
ADSORPTION OF THE DYE REACTIVE BLUE 5G IN RETORTED SHALE |
author |
Lambrecht,R. |
author_facet |
Lambrecht,R. Barros,M. A. S. D. de Arroyo,P. A. Borba,C. E. Silva,E. A. da |
author_role |
author |
author2 |
Barros,M. A. S. D. de Arroyo,P. A. Borba,C. E. Silva,E. A. da |
author2_role |
author author author author |
dc.contributor.author.fl_str_mv |
Lambrecht,R. Barros,M. A. S. D. de Arroyo,P. A. Borba,C. E. Silva,E. A. da |
dc.subject.por.fl_str_mv |
Mathematical modeling Packed bed Reactive dye Adsorption Shale |
topic |
Mathematical modeling Packed bed Reactive dye Adsorption Shale |
description |
Abstract In this study the influence of the volumetric flow rate and feed concentration was investigated for the adsorption of the reactive dye Blue 5G. Experiments were carried out in a bed packed with retorted shale, at 30 ºC. The ranges investigated were flow rate 2 -10 mL/min and the feed concentration 13-105 mg/L. Mathematical models were used to represent the dynamic sorption. The double resistance model considers the effects of the axial dispersion and the mass transfer resistance of the external film and inside the particles. As a result, the mass transfer coefficient of the external film and the internal mass transfer coefficient were estimated. The Thomas model was used to simulate the experimental data. In this model the fitted parameter was the adsorption kinetic constant. The first model provided an acceptable representation of the dynamic uptake of the reactive dye Blue 5G. |
publishDate |
2015 |
dc.date.none.fl_str_mv |
2015-03-01 |
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=S0104-66322015000100269 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322015000100269 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/0104-6632.20150321s00001715 |
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.32 n.1 2015 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_ |
1754213174676029440 |