Synthesis of dihydrocarvone over dendritic ZSM-5 Zeolite: A comprehensive study of experimental, kinetics, and computational insights

[Display omitted] •Kinetics and mechanism of limonene-1,2-epoxide isomerization.•Dendritic ZSM-5 zeolite is highly selective for formation of dihydrocarvone.•Kinetic modeling based on the reaction network with eight parallel reactions.•Adequate description of kinetics with statistically reliable par...

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Published inChemical engineering journal (Lausanne, Switzerland : 1996) Vol. 498; p. 155377
Main Authors Gallego-Villada, Luis A., Perez-Sena, Wander Y., Sánchez-Velandia, Julián E., Cueto, Jennifer, del Mar Alonso-Doncel, María, Wärmå, Johan, Mäki-Arvela, Päivi, Alarcón, Edwin A., Serrano, David P., Murzin, Dmitry Yu
Format Journal Article
LanguageEnglish
Published Elsevier B.V 15.10.2024
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Abstract [Display omitted] •Kinetics and mechanism of limonene-1,2-epoxide isomerization.•Dendritic ZSM-5 zeolite is highly selective for formation of dihydrocarvone.•Kinetic modeling based on the reaction network with eight parallel reactions.•Adequate description of kinetics with statistically reliable parameters.•Density Functional Theory calculations revealed the preferred pathways for limonene-1,2-epoxide isomerization. This study explores the isomerization of limonene-1,2-epoxide (LE) from kinetic and mechanistic viewpoints, using a dendritic ZSM-5 zeolite (d-ZSM-5) as a highly selective catalyst for the formation of dihydrocarvone (DHC) in the form of diastereoisomers (cis + trans). Ethyl acetate, a green solvent, was used at mild reaction temperatures (50–––70 °C). DHC, which can also be extracted from caraway oil, is widely used as an intermediate for epoxylactone production and as a constituent in flavors and perfumes. Kinetic modeling of LE isomerization was performed using a reaction network with eight parallel reactions and the corresponding rate equations, derived from the assumption of the rate-limiting surface reactions. The large standard errors in the statistical results of some kinetic parameters of the initial data fitting suggested that three of those reactions can be neglected to describe the kinetic model more accurately. This refinement resulted in standard errors in the kinetic parameters lower than ca. 11 %, confirming the statistical reliability of the modified kinetic model. Activation energies of 41.1 and 162 kJ/mol were estimated for the formation of cis-DHC and trans-DHC, respectively. Density Functional Theory (DFT) calculations revealed the preferred pathway for both cis and trans-LE conversion to DHC and carveol. The rate-determining step, carbocation formation (ΔEact = 234 kJ/mol), precedes near-instantaneous dihydrocarvone formation under the studied conditions.
AbstractList [Display omitted] •Kinetics and mechanism of limonene-1,2-epoxide isomerization.•Dendritic ZSM-5 zeolite is highly selective for formation of dihydrocarvone.•Kinetic modeling based on the reaction network with eight parallel reactions.•Adequate description of kinetics with statistically reliable parameters.•Density Functional Theory calculations revealed the preferred pathways for limonene-1,2-epoxide isomerization. This study explores the isomerization of limonene-1,2-epoxide (LE) from kinetic and mechanistic viewpoints, using a dendritic ZSM-5 zeolite (d-ZSM-5) as a highly selective catalyst for the formation of dihydrocarvone (DHC) in the form of diastereoisomers (cis + trans). Ethyl acetate, a green solvent, was used at mild reaction temperatures (50–––70 °C). DHC, which can also be extracted from caraway oil, is widely used as an intermediate for epoxylactone production and as a constituent in flavors and perfumes. Kinetic modeling of LE isomerization was performed using a reaction network with eight parallel reactions and the corresponding rate equations, derived from the assumption of the rate-limiting surface reactions. The large standard errors in the statistical results of some kinetic parameters of the initial data fitting suggested that three of those reactions can be neglected to describe the kinetic model more accurately. This refinement resulted in standard errors in the kinetic parameters lower than ca. 11 %, confirming the statistical reliability of the modified kinetic model. Activation energies of 41.1 and 162 kJ/mol were estimated for the formation of cis-DHC and trans-DHC, respectively. Density Functional Theory (DFT) calculations revealed the preferred pathway for both cis and trans-LE conversion to DHC and carveol. The rate-determining step, carbocation formation (ΔEact = 234 kJ/mol), precedes near-instantaneous dihydrocarvone formation under the studied conditions.
ArticleNumber 155377
Author Gallego-Villada, Luis A.
Sánchez-Velandia, Julián E.
Cueto, Jennifer
Perez-Sena, Wander Y.
Mäki-Arvela, Päivi
Wärmå, Johan
del Mar Alonso-Doncel, María
Serrano, David P.
Alarcón, Edwin A.
Murzin, Dmitry Yu
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  givenname: Luis A.
  surname: Gallego-Villada
  fullname: Gallego-Villada, Luis A.
  email: alfonso.gallego@udea.edu.co
  organization: Laboratory of Industrial Chemistry and Reaction Engineering, Johan Gadolin Process Chemistry Centre, Åbo Akademi University, Henriksgatan 2, 20500 Turku/Åbo, Finland
– sequence: 2
  givenname: Wander Y.
  surname: Perez-Sena
  fullname: Perez-Sena, Wander Y.
  organization: Laboratory of Industrial Chemistry and Reaction Engineering, Johan Gadolin Process Chemistry Centre, Åbo Akademi University, Henriksgatan 2, 20500 Turku/Åbo, Finland
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  givenname: Julián E.
  surname: Sánchez-Velandia
  fullname: Sánchez-Velandia, Julián E.
  organization: Sustainable and Supramolecular Research Group, Universidad Jaume I, Av. Vicent Sos Baynot, s/n, 12006, Castelló de la Plana, Spain
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  givenname: Jennifer
  surname: Cueto
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  givenname: María
  surname: del Mar Alonso-Doncel
  fullname: del Mar Alonso-Doncel, María
  organization: Thermochemical Processes Unit, IMDEA Energy Institute, Avda. Ramón de la Sagra, 3, 28935, Móstoles, Madrid, Spain
– sequence: 6
  givenname: Johan
  surname: Wärmå
  fullname: Wärmå, Johan
  organization: Laboratory of Industrial Chemistry and Reaction Engineering, Johan Gadolin Process Chemistry Centre, Åbo Akademi University, Henriksgatan 2, 20500 Turku/Åbo, Finland
– sequence: 7
  givenname: Päivi
  surname: Mäki-Arvela
  fullname: Mäki-Arvela, Päivi
  organization: Laboratory of Industrial Chemistry and Reaction Engineering, Johan Gadolin Process Chemistry Centre, Åbo Akademi University, Henriksgatan 2, 20500 Turku/Åbo, Finland
– sequence: 8
  givenname: Edwin A.
  surname: Alarcón
  fullname: Alarcón, Edwin A.
  organization: Environmental Catalysis Research Group, Chemical Engineering Faculty, Universidad de Antioquia, Medellín, Colombia
– sequence: 9
  givenname: David P.
  surname: Serrano
  fullname: Serrano, David P.
  email: david.serrano@imdea.org
  organization: Thermochemical Processes Unit, IMDEA Energy Institute, Avda. Ramón de la Sagra, 3, 28935, Móstoles, Madrid, Spain
– sequence: 10
  givenname: Dmitry Yu
  surname: Murzin
  fullname: Murzin, Dmitry Yu
  email: dmitry.murzin@abo.fi
  organization: Laboratory of Industrial Chemistry and Reaction Engineering, Johan Gadolin Process Chemistry Centre, Åbo Akademi University, Henriksgatan 2, 20500 Turku/Åbo, Finland
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Keywords Dihydrocarvone
Dendritic zeolite
Limonene epoxide
Kinetic modeling
Density Functional Theory (DFT)
ZSM-5
Language English
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Snippet [Display omitted] •Kinetics and mechanism of limonene-1,2-epoxide isomerization.•Dendritic ZSM-5 zeolite is highly selective for formation of...
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StartPage 155377
SubjectTerms Dendritic zeolite
Density Functional Theory (DFT)
Dihydrocarvone
Kinetic modeling
Limonene epoxide
ZSM-5
Title Synthesis of dihydrocarvone over dendritic ZSM-5 Zeolite: A comprehensive study of experimental, kinetics, and computational insights
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