Fractionation of benzene/n-hexane mixtures by pervaporation using polyurethane membranes

Detalhes bibliográficos
Autor(a) principal: CUNHA,V. S.
Data de Publicação: 1999
Outros Autores: NOBREGA,R., HABERT,A. 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=S0104-66321999000300008
Resumo: In the present work polyurethane membranes obtained from different polyester/MDI-based polymers were used to separate benzene/n-hexane mixtures by pervaporation. In pervaporation experiments, with a 50% wt feed at room temperature, permeate fluxes in the range of 0.3 to 3.2 Kg/m2h (10 <FONT FACE="Symbol">m</font>m membrane thickness) and selectivity in the range of 3.8 to 5.6 were obtained. The permeate was always enriched in benzene. Taking into account the compromise between flux and selectivity, the best performance membrane was selected for complementary sorption and pervaporation experiments. Results show that selectivity increases and the permeation flux decreases when the benzene concentration in the feed decreases. In the present application, results also show that sorption is the main factor for selectivity. Using the distillation azeotropic mixture as feed, almost no influence of temperature on selectivity was observed in the range of 25oC to 56oC. The permeate flux increases seven-fold, while selectivity remains constant near 8.0.
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spelling Fractionation of benzene/n-hexane mixtures by pervaporation using polyurethane membranesPervaporationpolyurethane membranesorganic separationIn the present work polyurethane membranes obtained from different polyester/MDI-based polymers were used to separate benzene/n-hexane mixtures by pervaporation. In pervaporation experiments, with a 50% wt feed at room temperature, permeate fluxes in the range of 0.3 to 3.2 Kg/m2h (10 <FONT FACE="Symbol">m</font>m membrane thickness) and selectivity in the range of 3.8 to 5.6 were obtained. The permeate was always enriched in benzene. Taking into account the compromise between flux and selectivity, the best performance membrane was selected for complementary sorption and pervaporation experiments. Results show that selectivity increases and the permeation flux decreases when the benzene concentration in the feed decreases. In the present application, results also show that sorption is the main factor for selectivity. Using the distillation azeotropic mixture as feed, almost no influence of temperature on selectivity was observed in the range of 25oC to 56oC. The permeate flux increases seven-fold, while selectivity remains constant near 8.0.Brazilian Society of Chemical Engineering1999-09-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66321999000300008Brazilian Journal of Chemical Engineering v.16 n.3 1999reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66321999000300008info:eu-repo/semantics/openAccessCUNHA,V. S.NOBREGA,R.HABERT,A. C.eng1999-12-16T00:00:00Zoai:scielo:S0104-66321999000300008Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:1999-12-16T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false
dc.title.none.fl_str_mv Fractionation of benzene/n-hexane mixtures by pervaporation using polyurethane membranes
title Fractionation of benzene/n-hexane mixtures by pervaporation using polyurethane membranes
spellingShingle Fractionation of benzene/n-hexane mixtures by pervaporation using polyurethane membranes
CUNHA,V. S.
Pervaporation
polyurethane membranes
organic separation
title_short Fractionation of benzene/n-hexane mixtures by pervaporation using polyurethane membranes
title_full Fractionation of benzene/n-hexane mixtures by pervaporation using polyurethane membranes
title_fullStr Fractionation of benzene/n-hexane mixtures by pervaporation using polyurethane membranes
title_full_unstemmed Fractionation of benzene/n-hexane mixtures by pervaporation using polyurethane membranes
title_sort Fractionation of benzene/n-hexane mixtures by pervaporation using polyurethane membranes
author CUNHA,V. S.
author_facet CUNHA,V. S.
NOBREGA,R.
HABERT,A. C.
author_role author
author2 NOBREGA,R.
HABERT,A. C.
author2_role author
author
dc.contributor.author.fl_str_mv CUNHA,V. S.
NOBREGA,R.
HABERT,A. C.
dc.subject.por.fl_str_mv Pervaporation
polyurethane membranes
organic separation
topic Pervaporation
polyurethane membranes
organic separation
description In the present work polyurethane membranes obtained from different polyester/MDI-based polymers were used to separate benzene/n-hexane mixtures by pervaporation. In pervaporation experiments, with a 50% wt feed at room temperature, permeate fluxes in the range of 0.3 to 3.2 Kg/m2h (10 <FONT FACE="Symbol">m</font>m membrane thickness) and selectivity in the range of 3.8 to 5.6 were obtained. The permeate was always enriched in benzene. Taking into account the compromise between flux and selectivity, the best performance membrane was selected for complementary sorption and pervaporation experiments. Results show that selectivity increases and the permeation flux decreases when the benzene concentration in the feed decreases. In the present application, results also show that sorption is the main factor for selectivity. Using the distillation azeotropic mixture as feed, almost no influence of temperature on selectivity was observed in the range of 25oC to 56oC. The permeate flux increases seven-fold, while selectivity remains constant near 8.0.
publishDate 1999
dc.date.none.fl_str_mv 1999-09-01
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=S0104-66321999000300008
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66321999000300008
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 10.1590/S0104-66321999000300008
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.16 n.3 1999
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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