Catalytic wet-air oxidation of lignin in a three-phase reactor with aromatic aldehyde production
Autor(a) principal: | |
---|---|
Data de Publicação: | 2004 |
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=S0104-66322004000200010 |
Resumo: | In the present work a process of catalytic wet air oxidation of lignin obtained from sugar-cane bagasse is developed with the objective of producing vanillin, syringaldehyde and p-hydroxybenzaldehyde in a continuous regime. Palladium supported on g-alumina was used as the catalyst. The reactions in the lignin degradation and aldehyde production were described by a kinetic model as a system of complex parallel and series reactions, in which pseudo-first-order steps are found. For the purpose of producing aromatic aldehydes in continuous regime, a three-phase fluidized reactor was built, and it was operated using atmospheric air as the oxidizer. The best yield in aromatic aldehydes was of 12%. The experimental results were compatible with those values obtained by the pseudo-heterogeneous axial dispersion model (PHADM) applied to the liquid phase. |
id |
ABEQ-1_08f81708bf9de18d553873e4cbfc23ae |
---|---|
oai_identifier_str |
oai:scielo:S0104-66322004000200010 |
network_acronym_str |
ABEQ-1 |
network_name_str |
Brazilian Journal of Chemical Engineering |
repository_id_str |
|
spelling |
Catalytic wet-air oxidation of lignin in a three-phase reactor with aromatic aldehyde productioncatalytic wet air-oxidationligninvanillinsyringaldehyde p-hydroxybenzaldehydepalladium catalystthree-phase fluidized-bed reactorIn the present work a process of catalytic wet air oxidation of lignin obtained from sugar-cane bagasse is developed with the objective of producing vanillin, syringaldehyde and p-hydroxybenzaldehyde in a continuous regime. Palladium supported on g-alumina was used as the catalyst. The reactions in the lignin degradation and aldehyde production were described by a kinetic model as a system of complex parallel and series reactions, in which pseudo-first-order steps are found. For the purpose of producing aromatic aldehydes in continuous regime, a three-phase fluidized reactor was built, and it was operated using atmospheric air as the oxidizer. The best yield in aromatic aldehydes was of 12%. The experimental results were compatible with those values obtained by the pseudo-heterogeneous axial dispersion model (PHADM) applied to the liquid phase.Brazilian Society of Chemical Engineering2004-06-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322004000200010Brazilian Journal of Chemical Engineering v.21 n.2 2004reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322004000200010info:eu-repo/semantics/openAccessSales,F.G.Abreu,C. A. M.Pereira,J. A. F. R.eng2004-05-26T00:00:00Zoai:scielo:S0104-66322004000200010Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2004-05-26T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false |
dc.title.none.fl_str_mv |
Catalytic wet-air oxidation of lignin in a three-phase reactor with aromatic aldehyde production |
title |
Catalytic wet-air oxidation of lignin in a three-phase reactor with aromatic aldehyde production |
spellingShingle |
Catalytic wet-air oxidation of lignin in a three-phase reactor with aromatic aldehyde production Sales,F.G. catalytic wet air-oxidation lignin vanillin syringaldehyde p-hydroxybenzaldehyde palladium catalyst three-phase fluidized-bed reactor |
title_short |
Catalytic wet-air oxidation of lignin in a three-phase reactor with aromatic aldehyde production |
title_full |
Catalytic wet-air oxidation of lignin in a three-phase reactor with aromatic aldehyde production |
title_fullStr |
Catalytic wet-air oxidation of lignin in a three-phase reactor with aromatic aldehyde production |
title_full_unstemmed |
Catalytic wet-air oxidation of lignin in a three-phase reactor with aromatic aldehyde production |
title_sort |
Catalytic wet-air oxidation of lignin in a three-phase reactor with aromatic aldehyde production |
author |
Sales,F.G. |
author_facet |
Sales,F.G. Abreu,C. A. M. Pereira,J. A. F. R. |
author_role |
author |
author2 |
Abreu,C. A. M. Pereira,J. A. F. R. |
author2_role |
author author |
dc.contributor.author.fl_str_mv |
Sales,F.G. Abreu,C. A. M. Pereira,J. A. F. R. |
dc.subject.por.fl_str_mv |
catalytic wet air-oxidation lignin vanillin syringaldehyde p-hydroxybenzaldehyde palladium catalyst three-phase fluidized-bed reactor |
topic |
catalytic wet air-oxidation lignin vanillin syringaldehyde p-hydroxybenzaldehyde palladium catalyst three-phase fluidized-bed reactor |
description |
In the present work a process of catalytic wet air oxidation of lignin obtained from sugar-cane bagasse is developed with the objective of producing vanillin, syringaldehyde and p-hydroxybenzaldehyde in a continuous regime. Palladium supported on g-alumina was used as the catalyst. The reactions in the lignin degradation and aldehyde production were described by a kinetic model as a system of complex parallel and series reactions, in which pseudo-first-order steps are found. For the purpose of producing aromatic aldehydes in continuous regime, a three-phase fluidized reactor was built, and it was operated using atmospheric air as the oxidizer. The best yield in aromatic aldehydes was of 12%. The experimental results were compatible with those values obtained by the pseudo-heterogeneous axial dispersion model (PHADM) applied to the liquid phase. |
publishDate |
2004 |
dc.date.none.fl_str_mv |
2004-06-01 |
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=S0104-66322004000200010 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322004000200010 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/S0104-66322004000200010 |
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.21 n.2 2004 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_ |
1754213171541835776 |