Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction

A review is presented here of our previous contributions concerning the production of ultrapure hydrogen through the dry reforming of methane conducted in a membrane reactor. The reaction equilibration ratio is the criterion to compare the catalytic performance of the La-based catalysts used in thes...

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Autores: Múnera Agudelo, John Fernando, Coronel, Leandro, Faroldi, Betina María Cecilia, Carrara, Carlos Roberto, Lombardo, Eduardo Agustin, Cornaglia, Laura Maria
Tipo de recurso: artículo
Estado:Versión publicada
Fecha de publicación:2010
País:Argentina
Institución:Consejo Nacional de Investigaciones Científicas y Técnicas
Repositorio:CONICET Digital (CONICET)
Idioma:inglés
OAI Identifier:oai:ri.conicet.gov.ar:11336/53943
Acceso en línea:http://hdl.handle.net/11336/53943
Access Level:acceso abierto
Palabra clave:MEMBRANE REACTOR
METHANE
RH
RU
https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
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oai_identifier_str oai:ri.conicet.gov.ar:11336/53943
network_acronym_str AR
network_name_str Argentina
repository_id_str
dc.title.none.fl_str_mv Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction
title Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction
spellingShingle Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction
Múnera Agudelo, John Fernando
MEMBRANE REACTOR
METHANE
RH
RU
https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
title_short Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction
title_full Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction
title_fullStr Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction
title_full_unstemmed Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction
title_sort Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction
dc.creator.none.fl_str_mv Múnera Agudelo, John Fernando
Coronel, Leandro
Faroldi, Betina María Cecilia
Carrara, Carlos Roberto
Lombardo, Eduardo Agustin
Cornaglia, Laura Maria
author Múnera Agudelo, John Fernando
author_facet Múnera Agudelo, John Fernando
Coronel, Leandro
Faroldi, Betina María Cecilia
Carrara, Carlos Roberto
Lombardo, Eduardo Agustin
Cornaglia, Laura Maria
author_role author
author2 Coronel, Leandro
Faroldi, Betina María Cecilia
Carrara, Carlos Roberto
Lombardo, Eduardo Agustin
Cornaglia, Laura Maria
author2_role author
author
author
author
author
dc.subject.none.fl_str_mv MEMBRANE REACTOR
METHANE
RH
RU
https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
topic MEMBRANE REACTOR
METHANE
RH
RU
https://purl.org/becyt/ford/2.4
https://purl.org/becyt/ford/2
description A review is presented here of our previous contributions concerning the production of ultrapure hydrogen through the dry reforming of methane conducted in a membrane reactor. The reaction equilibration ratio is the criterion to compare the catalytic performance of the La-based catalysts used in these studies. The solids were characterized by Laser Raman, X- ray photoelectron spectroscopy, X-ray diffraction and temperature-programmed reduction. The different behaviors are discussed taking into account the characterization results. To predict the influence of key process variables on conversion and product composition, a mathematical model is proposed to simulate the membrane reactor built around a palladium-silver membrane with 100% hydrogen selectivity. This study uses the kinetic equations developed for the dry reforming reaction on a Rh/La2O3 catalyst.
publishDate 2010
dc.date.none.fl_str_mv 2010-01
dc.type.none.fl_str_mv info:eu-repo/semantics/article
info:eu-repo/semantics/publishedVersion
http://purl.org/coar/resource_type/c_6501
info:ar-repo/semantics/articulo
format article
status_str publishedVersion
dc.identifier.none.fl_str_mv http://hdl.handle.net/11336/53943
Múnera Agudelo, John Fernando; Coronel, Leandro; Faroldi, Betina María Cecilia; Carrara, Carlos Roberto; Lombardo, Eduardo Agustin; et al.; Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction; John Wiley & Sons Inc; Asia-pacific Journal Of Chemical Engineering; 5; 1; 1-2010; 35-47
1932-2143
CONICET Digital
CONICET
url http://hdl.handle.net/11336/53943
identifier_str_mv Múnera Agudelo, John Fernando; Coronel, Leandro; Faroldi, Betina María Cecilia; Carrara, Carlos Roberto; Lombardo, Eduardo Agustin; et al.; Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction; John Wiley & Sons Inc; Asia-pacific Journal Of Chemical Engineering; 5; 1; 1-2010; 35-47
1932-2143
CONICET Digital
CONICET
dc.language.none.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv info:eu-repo/semantics/altIdentifier/doi/10.1002/apj.380
info:eu-repo/semantics/altIdentifier/url/https://onlinelibrary.wiley.com/doi/abs/10.1002/apj.380
dc.rights.none.fl_str_mv info:eu-repo/semantics/openAccess
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
eu_rights_str_mv openAccess
rights_invalid_str_mv https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.format.none.fl_str_mv application/pdf
application/pdf
dc.publisher.none.fl_str_mv John Wiley & Sons Inc
publisher.none.fl_str_mv John Wiley & Sons Inc
dc.source.none.fl_str_mv reponame:CONICET Digital (CONICET)
instname:Consejo Nacional de Investigaciones Científicas y Técnicas
instname_str Consejo Nacional de Investigaciones Científicas y Técnicas
reponame_str CONICET Digital (CONICET)
collection CONICET Digital (CONICET)
repository.name.fl_str_mv CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas
repository.mail.fl_str_mv dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar
_version_ 1799195275354439680
spelling Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reactionMúnera Agudelo, John FernandoCoronel, LeandroFaroldi, Betina María CeciliaCarrara, Carlos RobertoLombardo, Eduardo AgustinCornaglia, Laura MariaMEMBRANE REACTORMETHANERHRUhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2A review is presented here of our previous contributions concerning the production of ultrapure hydrogen through the dry reforming of methane conducted in a membrane reactor. The reaction equilibration ratio is the criterion to compare the catalytic performance of the La-based catalysts used in these studies. The solids were characterized by Laser Raman, X- ray photoelectron spectroscopy, X-ray diffraction and temperature-programmed reduction. The different behaviors are discussed taking into account the characterization results. To predict the influence of key process variables on conversion and product composition, a mathematical model is proposed to simulate the membrane reactor built around a palladium-silver membrane with 100% hydrogen selectivity. This study uses the kinetic equations developed for the dry reforming reaction on a Rh/La2O3 catalyst.Fil: Múnera Agudelo, John Fernando. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; ArgentinaFil: Coronel, Leandro. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; ArgentinaFil: Faroldi, Betina María Cecilia. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; ArgentinaFil: Carrara, Carlos Roberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; ArgentinaFil: Lombardo, Eduardo Agustin. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; ArgentinaFil: Cornaglia, Laura Maria. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; ArgentinaJohn Wiley & Sons Inc2010-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/53943Múnera Agudelo, John Fernando; Coronel, Leandro; Faroldi, Betina María Cecilia; Carrara, Carlos Roberto; Lombardo, Eduardo Agustin; et al.; Production of ultrapure hydrogen in a Pd-Ag membrane reactor using noble metal supported on La-based oxides. Modeling for the dry reforming of methane reaction; John Wiley & Sons Inc; Asia-pacific Journal Of Chemical Engineering; 5; 1; 1-2010; 35-471932-2143CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/doi/10.1002/apj.380info:eu-repo/semantics/altIdentifier/url/https://onlinelibrary.wiley.com/doi/abs/10.1002/apj.380info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2024-05-08T13:47:46Zoai:ri.conicet.gov.ar:11336/53943instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982024-05-08 13:47:46.685CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse
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