Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts
- Autores
- Sepúlveda, Jorge; Manuale, Débora Laura; Santiago, Lucía; Carrara, Nicolás Ricardo; Torres, Gerardo; Goncalves, Maraisa; Carvalho, Wagner; Mandelli, Dalmo
- Año de publicación
- 2016
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- The glycerol hydrogenolysis reaction was performed in a continuous flow trickle bed reactor using a water glycerol feed and both copper chromite and Cu/Al2O3 catalysts. The commercial copper chromite had a higher activity than the laboratory prepared Cu/Al2O3 and was used for most of the tests. Propylene glycol was the main product with both catalysts, acetol being the main by-product. It was found that temperature is the main variable influencing the conversion of glycerol. When the state of the glycerol-water reactant mixture was completely liquid, at temperatures lower than 190 °C, conversion was low and deactivation was observed. At reaction temperatures of 210-230 °C the conversion of glycerol was complete and the selectivity to propylene glycol was stable at about 60-80% all throughout the reaction time span of 10 h, regardless of the hydrogen pressure level (1 to 20 atm). These optimal values could not be improved significantly by using other different reaction conditions or increasing the catalyst acidity. At higher temperatures (245-250 °C) the conversion was also 100%. Under reaction conditions at which copper chromite suffered deactivation, light by-products and surface deposits were formed. The deposits could be completely burned at 250 °C and the catalyst activity fully recovered.
Fil: Sepúlveda, Jorge. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina
Fil: Manuale, Débora Laura. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina
Fil: Santiago, Lucía. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina
Fil: Carrara, Nicolás Ricardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina
Fil: Torres, Gerardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina
Fil: Goncalves, Maraisa. Universidade Federal Do Abc; Brasil
Fil: Carvalho, Wagner. Universidade Federal Do Abc; Brasil
Fil: Mandelli, Dalmo. Universidade Federal Do Abc; Brasil - Materia
-
HYDROGENOLYSIS
COPPER CHROMITE
GLYCEROL CONVERSION - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
- Repositorio
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/43690
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Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 CatalystsSepúlveda, JorgeManuale, Débora LauraSantiago, LucíaCarrara, Nicolás RicardoTorres, GerardoGoncalves, MaraisaCarvalho, WagnerMandelli, DalmoHYDROGENOLYSISCOPPER CHROMITEGLYCEROL CONVERSIONhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2The glycerol hydrogenolysis reaction was performed in a continuous flow trickle bed reactor using a water glycerol feed and both copper chromite and Cu/Al2O3 catalysts. The commercial copper chromite had a higher activity than the laboratory prepared Cu/Al2O3 and was used for most of the tests. Propylene glycol was the main product with both catalysts, acetol being the main by-product. It was found that temperature is the main variable influencing the conversion of glycerol. When the state of the glycerol-water reactant mixture was completely liquid, at temperatures lower than 190 °C, conversion was low and deactivation was observed. At reaction temperatures of 210-230 °C the conversion of glycerol was complete and the selectivity to propylene glycol was stable at about 60-80% all throughout the reaction time span of 10 h, regardless of the hydrogen pressure level (1 to 20 atm). These optimal values could not be improved significantly by using other different reaction conditions or increasing the catalyst acidity. At higher temperatures (245-250 °C) the conversion was also 100%. Under reaction conditions at which copper chromite suffered deactivation, light by-products and surface deposits were formed. The deposits could be completely burned at 250 °C and the catalyst activity fully recovered.Fil: Sepúlveda, Jorge. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; ArgentinaFil: Manuale, Débora Laura. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; ArgentinaFil: Santiago, Lucía. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; ArgentinaFil: Carrara, Nicolás Ricardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; ArgentinaFil: Torres, Gerardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; ArgentinaFil: Goncalves, Maraisa. Universidade Federal Do Abc; BrasilFil: Carvalho, Wagner. Universidade Federal Do Abc; BrasilFil: Mandelli, Dalmo. Universidade Federal Do Abc; BrasilSociedade Brasileira de Química2016-12info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/43690Sepúlveda, Jorge; Manuale, Débora Laura; Santiago, Lucía; Carrara, Nicolás Ricardo; Torres, Gerardo; et al.; Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts; Sociedade Brasileira de Química; Química Nova; 26; 8; 12-2016; 1551-15640100-40421678-7064CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/doi/10.5935/0103-5053.20150123info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-29T10:44:06Zoai:ri.conicet.gov.ar:11336/43690instacron: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:34982025-09-29 10:44:07.048CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
dc.title.none.fl_str_mv |
Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts |
title |
Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts |
spellingShingle |
Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts Sepúlveda, Jorge HYDROGENOLYSIS COPPER CHROMITE GLYCEROL CONVERSION |
title_short |
Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts |
title_full |
Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts |
title_fullStr |
Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts |
title_full_unstemmed |
Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts |
title_sort |
Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts |
dc.creator.none.fl_str_mv |
Sepúlveda, Jorge Manuale, Débora Laura Santiago, Lucía Carrara, Nicolás Ricardo Torres, Gerardo Goncalves, Maraisa Carvalho, Wagner Mandelli, Dalmo |
author |
Sepúlveda, Jorge |
author_facet |
Sepúlveda, Jorge Manuale, Débora Laura Santiago, Lucía Carrara, Nicolás Ricardo Torres, Gerardo Goncalves, Maraisa Carvalho, Wagner Mandelli, Dalmo |
author_role |
author |
author2 |
Manuale, Débora Laura Santiago, Lucía Carrara, Nicolás Ricardo Torres, Gerardo Goncalves, Maraisa Carvalho, Wagner Mandelli, Dalmo |
author2_role |
author author author author author author author |
dc.subject.none.fl_str_mv |
HYDROGENOLYSIS COPPER CHROMITE GLYCEROL CONVERSION |
topic |
HYDROGENOLYSIS COPPER CHROMITE GLYCEROL CONVERSION |
purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
dc.description.none.fl_txt_mv |
The glycerol hydrogenolysis reaction was performed in a continuous flow trickle bed reactor using a water glycerol feed and both copper chromite and Cu/Al2O3 catalysts. The commercial copper chromite had a higher activity than the laboratory prepared Cu/Al2O3 and was used for most of the tests. Propylene glycol was the main product with both catalysts, acetol being the main by-product. It was found that temperature is the main variable influencing the conversion of glycerol. When the state of the glycerol-water reactant mixture was completely liquid, at temperatures lower than 190 °C, conversion was low and deactivation was observed. At reaction temperatures of 210-230 °C the conversion of glycerol was complete and the selectivity to propylene glycol was stable at about 60-80% all throughout the reaction time span of 10 h, regardless of the hydrogen pressure level (1 to 20 atm). These optimal values could not be improved significantly by using other different reaction conditions or increasing the catalyst acidity. At higher temperatures (245-250 °C) the conversion was also 100%. Under reaction conditions at which copper chromite suffered deactivation, light by-products and surface deposits were formed. The deposits could be completely burned at 250 °C and the catalyst activity fully recovered. Fil: Sepúlveda, Jorge. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina Fil: Manuale, Débora Laura. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina Fil: Santiago, Lucía. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina Fil: Carrara, Nicolás Ricardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina Fil: Torres, Gerardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica ; Argentina Fil: Goncalves, Maraisa. Universidade Federal Do Abc; Brasil Fil: Carvalho, Wagner. Universidade Federal Do Abc; Brasil Fil: Mandelli, Dalmo. Universidade Federal Do Abc; Brasil |
description |
The glycerol hydrogenolysis reaction was performed in a continuous flow trickle bed reactor using a water glycerol feed and both copper chromite and Cu/Al2O3 catalysts. The commercial copper chromite had a higher activity than the laboratory prepared Cu/Al2O3 and was used for most of the tests. Propylene glycol was the main product with both catalysts, acetol being the main by-product. It was found that temperature is the main variable influencing the conversion of glycerol. When the state of the glycerol-water reactant mixture was completely liquid, at temperatures lower than 190 °C, conversion was low and deactivation was observed. At reaction temperatures of 210-230 °C the conversion of glycerol was complete and the selectivity to propylene glycol was stable at about 60-80% all throughout the reaction time span of 10 h, regardless of the hydrogen pressure level (1 to 20 atm). These optimal values could not be improved significantly by using other different reaction conditions or increasing the catalyst acidity. At higher temperatures (245-250 °C) the conversion was also 100%. Under reaction conditions at which copper chromite suffered deactivation, light by-products and surface deposits were formed. The deposits could be completely burned at 250 °C and the catalyst activity fully recovered. |
publishDate |
2016 |
dc.date.none.fl_str_mv |
2016-12 |
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/11336/43690 Sepúlveda, Jorge; Manuale, Débora Laura; Santiago, Lucía; Carrara, Nicolás Ricardo; Torres, Gerardo; et al.; Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts; Sociedade Brasileira de Química; Química Nova; 26; 8; 12-2016; 1551-1564 0100-4042 1678-7064 CONICET Digital CONICET |
url |
http://hdl.handle.net/11336/43690 |
identifier_str_mv |
Sepúlveda, Jorge; Manuale, Débora Laura; Santiago, Lucía; Carrara, Nicolás Ricardo; Torres, Gerardo; et al.; Selective Hydrogenolysis of Glycerol to Propylene Glycol in a Continuous Flow Trickle Bed Reactor Using Copper Chromite and Cu/Al2O3 Catalysts; Sociedade Brasileira de Química; Química Nova; 26; 8; 12-2016; 1551-1564 0100-4042 1678-7064 CONICET Digital CONICET |
dc.language.none.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
info:eu-repo/semantics/altIdentifier/doi/10.5935/0103-5053.20150123 |
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 application/pdf |
dc.publisher.none.fl_str_mv |
Sociedade Brasileira de Química |
publisher.none.fl_str_mv |
Sociedade Brasileira de Química |
dc.source.none.fl_str_mv |
reponame:CONICET Digital (CONICET) instname:Consejo Nacional de Investigaciones Científicas y Técnicas |
reponame_str |
CONICET Digital (CONICET) |
collection |
CONICET Digital (CONICET) |
instname_str |
Consejo Nacional de Investigaciones Científicas y Técnicas |
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 |
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1844614477923745792 |
score |
13.070432 |