Mechanism analysis and chemical equilibrium modelling for liquid phase glycerol hydrogenolysis
- Autores
- Gatti, Martín Nicolás; Pérez, Federico Martín; Santori, Gerardo Fabián; Pompeo, Francisco
- Año de publicación
- 2025
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- In this work, the chemical equilibrium of the glycerol (GLY) hydrogenolysis in the liquid phase was studied from the mechanism of the C–O and C–C bond cleavage and hydrogenation reactions using the commercial simulator UniSim Design ® in the range T = 423–533 K, P = 4–10 MPa and molar ratios H2/reactant = 0.4–2. The equilibrium constants were calculated from the Gibbs free energy, enthalpy and entropy of the reactions involved, employing the group contribution method to estimate the formation properties of the compounds. The results showed that the formation of EG through GLY and the hydrogenation reactions of acetol (AcOH) and 3- hydroxypropionaldehyde (3-HPA) to produce 1,2-propylene glycol (1,2-PG) and 1,3-propylene glycol (1,3-PG) respectively, are limited by thermodynamic equilibrium. For glycols, the formation of 1,2-PG is favored over that of 1,3-PG, and for propanols, the formation of 2-propanol (2-POH) is favored over that of 1-propanol (1-POH). In addition, the formation of EG from 1,2-PG is more feasible, and the formation of ethanol (EtOH) and methanol (MeOH) depend on alternative routes involving EG and 1,3-PG as intermediates, respectively. These results not only show good agreement with previously reported experimental data, but also provide relevant information for the design of bifunctional catalysts that are active and selective towards specific products in the liquid phase glycerol hydrogenolysis.
Centro de Investigación y Desarrollo en Ciencias Aplicadas - Materia
-
Química
Chemical equilibrium
Hydrogenolysis
Glycerol
Liquid phase
Mechanism - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- http://creativecommons.org/licenses/by/4.0/
- Repositorio
- Institución
- Universidad Nacional de La Plata
- OAI Identificador
- oai:sedici.unlp.edu.ar:10915/181596
Ver los metadatos del registro completo
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Mechanism analysis and chemical equilibrium modelling for liquid phase glycerol hydrogenolysisGatti, Martín NicolásPérez, Federico MartínSantori, Gerardo FabiánPompeo, FranciscoQuímicaChemical equilibriumHydrogenolysisGlycerolLiquid phaseMechanismIn this work, the chemical equilibrium of the glycerol (GLY) hydrogenolysis in the liquid phase was studied from the mechanism of the C–O and C–C bond cleavage and hydrogenation reactions using the commercial simulator UniSim Design ® in the range T = 423–533 K, P = 4–10 MPa and molar ratios H2/reactant = 0.4–2. The equilibrium constants were calculated from the Gibbs free energy, enthalpy and entropy of the reactions involved, employing the group contribution method to estimate the formation properties of the compounds. The results showed that the formation of EG through GLY and the hydrogenation reactions of acetol (AcOH) and 3- hydroxypropionaldehyde (3-HPA) to produce 1,2-propylene glycol (1,2-PG) and 1,3-propylene glycol (1,3-PG) respectively, are limited by thermodynamic equilibrium. For glycols, the formation of 1,2-PG is favored over that of 1,3-PG, and for propanols, the formation of 2-propanol (2-POH) is favored over that of 1-propanol (1-POH). In addition, the formation of EG from 1,2-PG is more feasible, and the formation of ethanol (EtOH) and methanol (MeOH) depend on alternative routes involving EG and 1,3-PG as intermediates, respectively. These results not only show good agreement with previously reported experimental data, but also provide relevant information for the design of bifunctional catalysts that are active and selective towards specific products in the liquid phase glycerol hydrogenolysis.Centro de Investigación y Desarrollo en Ciencias Aplicadas2025-06info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionArticulohttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfhttp://sedici.unlp.edu.ar/handle/10915/181596enginfo:eu-repo/semantics/altIdentifier/issn/2667-3126info:eu-repo/semantics/altIdentifier/doi/10.1016/j.ctta.2025.100186info:eu-repo/semantics/openAccesshttp://creativecommons.org/licenses/by/4.0/Creative Commons Attribution 4.0 International (CC BY 4.0)reponame:SEDICI (UNLP)instname:Universidad Nacional de La Platainstacron:UNLP2025-09-03T11:21:22Zoai:sedici.unlp.edu.ar:10915/181596Institucionalhttp://sedici.unlp.edu.ar/Universidad públicaNo correspondehttp://sedici.unlp.edu.ar/oai/snrdalira@sedici.unlp.edu.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:13292025-09-03 11:21:23.67SEDICI (UNLP) - Universidad Nacional de La Platafalse |
dc.title.none.fl_str_mv |
Mechanism analysis and chemical equilibrium modelling for liquid phase glycerol hydrogenolysis |
title |
Mechanism analysis and chemical equilibrium modelling for liquid phase glycerol hydrogenolysis |
spellingShingle |
Mechanism analysis and chemical equilibrium modelling for liquid phase glycerol hydrogenolysis Gatti, Martín Nicolás Química Chemical equilibrium Hydrogenolysis Glycerol Liquid phase Mechanism |
title_short |
Mechanism analysis and chemical equilibrium modelling for liquid phase glycerol hydrogenolysis |
title_full |
Mechanism analysis and chemical equilibrium modelling for liquid phase glycerol hydrogenolysis |
title_fullStr |
Mechanism analysis and chemical equilibrium modelling for liquid phase glycerol hydrogenolysis |
title_full_unstemmed |
Mechanism analysis and chemical equilibrium modelling for liquid phase glycerol hydrogenolysis |
title_sort |
Mechanism analysis and chemical equilibrium modelling for liquid phase glycerol hydrogenolysis |
dc.creator.none.fl_str_mv |
Gatti, Martín Nicolás Pérez, Federico Martín Santori, Gerardo Fabián Pompeo, Francisco |
author |
Gatti, Martín Nicolás |
author_facet |
Gatti, Martín Nicolás Pérez, Federico Martín Santori, Gerardo Fabián Pompeo, Francisco |
author_role |
author |
author2 |
Pérez, Federico Martín Santori, Gerardo Fabián Pompeo, Francisco |
author2_role |
author author author |
dc.subject.none.fl_str_mv |
Química Chemical equilibrium Hydrogenolysis Glycerol Liquid phase Mechanism |
topic |
Química Chemical equilibrium Hydrogenolysis Glycerol Liquid phase Mechanism |
dc.description.none.fl_txt_mv |
In this work, the chemical equilibrium of the glycerol (GLY) hydrogenolysis in the liquid phase was studied from the mechanism of the C–O and C–C bond cleavage and hydrogenation reactions using the commercial simulator UniSim Design ® in the range T = 423–533 K, P = 4–10 MPa and molar ratios H2/reactant = 0.4–2. The equilibrium constants were calculated from the Gibbs free energy, enthalpy and entropy of the reactions involved, employing the group contribution method to estimate the formation properties of the compounds. The results showed that the formation of EG through GLY and the hydrogenation reactions of acetol (AcOH) and 3- hydroxypropionaldehyde (3-HPA) to produce 1,2-propylene glycol (1,2-PG) and 1,3-propylene glycol (1,3-PG) respectively, are limited by thermodynamic equilibrium. For glycols, the formation of 1,2-PG is favored over that of 1,3-PG, and for propanols, the formation of 2-propanol (2-POH) is favored over that of 1-propanol (1-POH). In addition, the formation of EG from 1,2-PG is more feasible, and the formation of ethanol (EtOH) and methanol (MeOH) depend on alternative routes involving EG and 1,3-PG as intermediates, respectively. These results not only show good agreement with previously reported experimental data, but also provide relevant information for the design of bifunctional catalysts that are active and selective towards specific products in the liquid phase glycerol hydrogenolysis. Centro de Investigación y Desarrollo en Ciencias Aplicadas |
description |
In this work, the chemical equilibrium of the glycerol (GLY) hydrogenolysis in the liquid phase was studied from the mechanism of the C–O and C–C bond cleavage and hydrogenation reactions using the commercial simulator UniSim Design ® in the range T = 423–533 K, P = 4–10 MPa and molar ratios H2/reactant = 0.4–2. The equilibrium constants were calculated from the Gibbs free energy, enthalpy and entropy of the reactions involved, employing the group contribution method to estimate the formation properties of the compounds. The results showed that the formation of EG through GLY and the hydrogenation reactions of acetol (AcOH) and 3- hydroxypropionaldehyde (3-HPA) to produce 1,2-propylene glycol (1,2-PG) and 1,3-propylene glycol (1,3-PG) respectively, are limited by thermodynamic equilibrium. For glycols, the formation of 1,2-PG is favored over that of 1,3-PG, and for propanols, the formation of 2-propanol (2-POH) is favored over that of 1-propanol (1-POH). In addition, the formation of EG from 1,2-PG is more feasible, and the formation of ethanol (EtOH) and methanol (MeOH) depend on alternative routes involving EG and 1,3-PG as intermediates, respectively. These results not only show good agreement with previously reported experimental data, but also provide relevant information for the design of bifunctional catalysts that are active and selective towards specific products in the liquid phase glycerol hydrogenolysis. |
publishDate |
2025 |
dc.date.none.fl_str_mv |
2025-06 |
dc.type.none.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion Articulo http://purl.org/coar/resource_type/c_6501 info:ar-repo/semantics/articulo |
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article |
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dc.identifier.none.fl_str_mv |
http://sedici.unlp.edu.ar/handle/10915/181596 |
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http://sedici.unlp.edu.ar/handle/10915/181596 |
dc.language.none.fl_str_mv |
eng |
language |
eng |
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info:eu-repo/semantics/altIdentifier/issn/2667-3126 info:eu-repo/semantics/altIdentifier/doi/10.1016/j.ctta.2025.100186 |
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info:eu-repo/semantics/openAccess http://creativecommons.org/licenses/by/4.0/ Creative Commons Attribution 4.0 International (CC BY 4.0) |
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openAccess |
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http://creativecommons.org/licenses/by/4.0/ Creative Commons Attribution 4.0 International (CC BY 4.0) |
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