Ethyl oleate production by means of pervaporation-assisted esterification using heterogeneous catalysis
Autor(a) principal: | |
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Data de Publicação: | 2010 |
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=S0104-66322010000400013 |
Resumo: | Pervaporation-assisted esterification of oleic acid and ethanol was investigated by means of heterogeneous acid catalysis with the aim of increasing the ethyl oleate yield. The experimental strategy comprised kinetic tests with Amberlyst 15 Wet (Rohm & Haas), the characterization of hydrophilic Pervap 1000 membrane (Sulzer) and the evaluation of the membrane-assisted reactor. Kinetic tests were carried out to study the effect of temperature, catalyst loading and ethanol/organic acid molar ratio for the esterification of oleic acid and ethanol. The ester yield and initial reaction rate were used as response. The hydrophilic poly(vinyl alcohol) membrane was able to remove water from the reaction medium and, hence, the ester yield was increased. The potential of coupling esterification and pervaporation was demonstrated, with a two-fold increase in the reaction yield of ethyl oleate. |
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Brazilian Journal of Chemical Engineering |
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|
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Ethyl oleate production by means of pervaporation-assisted esterification using heterogeneous catalysisPervaporationEsterificationHeterogeneous catalysisOleic acidMembrane-assisted reactorPervaporation-assisted esterification of oleic acid and ethanol was investigated by means of heterogeneous acid catalysis with the aim of increasing the ethyl oleate yield. The experimental strategy comprised kinetic tests with Amberlyst 15 Wet (Rohm & Haas), the characterization of hydrophilic Pervap 1000 membrane (Sulzer) and the evaluation of the membrane-assisted reactor. Kinetic tests were carried out to study the effect of temperature, catalyst loading and ethanol/organic acid molar ratio for the esterification of oleic acid and ethanol. The ester yield and initial reaction rate were used as response. The hydrophilic poly(vinyl alcohol) membrane was able to remove water from the reaction medium and, hence, the ester yield was increased. The potential of coupling esterification and pervaporation was demonstrated, with a two-fold increase in the reaction yield of ethyl oleate.Brazilian Society of Chemical Engineering2010-12-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322010000400013Brazilian Journal of Chemical Engineering v.27 n.4 2010reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322010000400013info:eu-repo/semantics/openAccessFigueiredo,K. C. S.Salim,V. M. M.Borges,C. P.eng2011-01-04T00:00:00Zoai:scielo:S0104-66322010000400013Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2011-01-04T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false |
dc.title.none.fl_str_mv |
Ethyl oleate production by means of pervaporation-assisted esterification using heterogeneous catalysis |
title |
Ethyl oleate production by means of pervaporation-assisted esterification using heterogeneous catalysis |
spellingShingle |
Ethyl oleate production by means of pervaporation-assisted esterification using heterogeneous catalysis Figueiredo,K. C. S. Pervaporation Esterification Heterogeneous catalysis Oleic acid Membrane-assisted reactor |
title_short |
Ethyl oleate production by means of pervaporation-assisted esterification using heterogeneous catalysis |
title_full |
Ethyl oleate production by means of pervaporation-assisted esterification using heterogeneous catalysis |
title_fullStr |
Ethyl oleate production by means of pervaporation-assisted esterification using heterogeneous catalysis |
title_full_unstemmed |
Ethyl oleate production by means of pervaporation-assisted esterification using heterogeneous catalysis |
title_sort |
Ethyl oleate production by means of pervaporation-assisted esterification using heterogeneous catalysis |
author |
Figueiredo,K. C. S. |
author_facet |
Figueiredo,K. C. S. Salim,V. M. M. Borges,C. P. |
author_role |
author |
author2 |
Salim,V. M. M. Borges,C. P. |
author2_role |
author author |
dc.contributor.author.fl_str_mv |
Figueiredo,K. C. S. Salim,V. M. M. Borges,C. P. |
dc.subject.por.fl_str_mv |
Pervaporation Esterification Heterogeneous catalysis Oleic acid Membrane-assisted reactor |
topic |
Pervaporation Esterification Heterogeneous catalysis Oleic acid Membrane-assisted reactor |
description |
Pervaporation-assisted esterification of oleic acid and ethanol was investigated by means of heterogeneous acid catalysis with the aim of increasing the ethyl oleate yield. The experimental strategy comprised kinetic tests with Amberlyst 15 Wet (Rohm & Haas), the characterization of hydrophilic Pervap 1000 membrane (Sulzer) and the evaluation of the membrane-assisted reactor. Kinetic tests were carried out to study the effect of temperature, catalyst loading and ethanol/organic acid molar ratio for the esterification of oleic acid and ethanol. The ester yield and initial reaction rate were used as response. The hydrophilic poly(vinyl alcohol) membrane was able to remove water from the reaction medium and, hence, the ester yield was increased. The potential of coupling esterification and pervaporation was demonstrated, with a two-fold increase in the reaction yield of ethyl oleate. |
publishDate |
2010 |
dc.date.none.fl_str_mv |
2010-12-01 |
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=S0104-66322010000400013 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322010000400013 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/S0104-66322010000400013 |
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.27 n.4 2010 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_ |
1754213173157691392 |