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Kinetic investigation of the solvent-free hydrogenation of dehydroisophytol

Kinetic investigation of the solvent-free hydrogenation of dehydroisophytol
Kinetic investigation of the solvent-free hydrogenation of dehydroisophytol
Isophytol is a key intermediate in the industrial synthesis of vitamins, produced by selective hydrogenation of dehydroisophytol. This work presents a study of the kinetics of this process in the absence of any solvent. The experimental data were modeled using power-law kinetic expressions and mechanistic models based on Langmuir–Hinshelwood kinetics. The hypothesis of noncompetitive adsorption between hydrogen and organics was chosen in order to describe the changes in the reactivity of the system at varying temperatures (313–353 K) and pressures (5.0–9.0 bar). A simplified approach was used to describe the kinetics of the overhydrogenation reaction to the corresponding alkane. A list of the relevant kinetic and adsorption parameters, the result of an optimization procedure, is reported. The mathematical model, successfully validated, allows the prediction of the influence of the operating conditions and of the addition of quinoline, as reaction modifier, on the selectivity of the process.
0888-5885
4929-4937
Vernuccio, S.
4bafd7f3-0943-4f6c-bc78-b4026516ccdb
Meier, Adrian
e67022ff-0d48-45c7-bdfe-fc6890e00ce3
Von Rohr, P.R.
66b46a1a-1897-4173-8217-f54c55984164
Vernuccio, S.
4bafd7f3-0943-4f6c-bc78-b4026516ccdb
Meier, Adrian
e67022ff-0d48-45c7-bdfe-fc6890e00ce3
Von Rohr, P.R.
66b46a1a-1897-4173-8217-f54c55984164

Vernuccio, S., Meier, Adrian and Von Rohr, P.R. (2017) Kinetic investigation of the solvent-free hydrogenation of dehydroisophytol. Industrial and Engineering Chemistry Research, 56 (17), 4929-4937. (doi:10.1021/acs.iecr.7b00458).

Record type: Article

Abstract

Isophytol is a key intermediate in the industrial synthesis of vitamins, produced by selective hydrogenation of dehydroisophytol. This work presents a study of the kinetics of this process in the absence of any solvent. The experimental data were modeled using power-law kinetic expressions and mechanistic models based on Langmuir–Hinshelwood kinetics. The hypothesis of noncompetitive adsorption between hydrogen and organics was chosen in order to describe the changes in the reactivity of the system at varying temperatures (313–353 K) and pressures (5.0–9.0 bar). A simplified approach was used to describe the kinetics of the overhydrogenation reaction to the corresponding alkane. A list of the relevant kinetic and adsorption parameters, the result of an optimization procedure, is reported. The mathematical model, successfully validated, allows the prediction of the influence of the operating conditions and of the addition of quinoline, as reaction modifier, on the selectivity of the process.

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Accepted/In Press date: 6 April 2017
Published date: 6 April 2017

Identifiers

Local EPrints ID: 495701
URI: http://eprints.soton.ac.uk/id/eprint/495701
ISSN: 0888-5885
PURE UUID: 8348794e-5833-4fef-b927-290ff45e5cd7
ORCID for S. Vernuccio: ORCID iD orcid.org/0000-0003-1254-0293

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Date deposited: 20 Nov 2024 17:46
Last modified: 21 Nov 2024 03:11

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Contributors

Author: S. Vernuccio ORCID iD
Author: Adrian Meier
Author: P.R. Von Rohr

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