Mechanistic Kinetic Modeling of the Selective Methanol Oxidation Based on Christiansen Mathematics

ABSTRACT Green oxygenates are of importance as future sustainable building blocks or platform chemicals. It is possible to synthesize the oxygenates dimethoxymethane, dimethyl ether, and methyl formate simultaneously at a single‐VO x catalyst via selective methanol oxidation (SMO) in one reactive process step. The reaction is characterized as a valorization of green methanol only with O 2 at ambient pressure and low temperatures, in contrast to conventional production processes. In order to conduct model‐based reactor and process optimization, a mechanistic kinetic approach is desirable, providing a higher validity and transferability. A new detailed catalytic network and coupled catalytic cycles for the heterogeneously catalyzed methanol oxidation, considering different redox and acid sites, are presented. On the basis of Christiansen's mathematics, the kinetics of several different subnetworks were successfully modeled mechanistically.

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Publication Details

Journal
Chemie Ingenieur Technik
Published
2026-04-10
DOI
https://doi.org/10.1002/cite.70105
Primary Topic
Catalysis and Oxidation Reactions
Type
article
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article

Mechanistic Kinetic Modeling of the Selective Methanol Oxidation Based on Christiansen Mathematics

Christof Hamel, Thomas Friederici, Jan Paul Walter, Lea Hilfert
Chemie Ingenieur Technik
Catalysis and Oxidation Reactions
article

Mechanistic Kinetic Modeling of the Selective Methanol Oxidation Based on Christiansen Mathematics

Christof Hamel, Thomas Friederici, Jan Paul Walter, Lea Hilfert
article en

Abstract

ABSTRACT Green oxygenates are of importance as future sustainable building blocks or platform chemicals. It is possible to synthesize the oxygenates dimethoxymethane, dimethyl ether, and methyl formate simultaneously at a single‐VO x catalyst via selective methanol oxidation (SMO) in one reactive process step. The reaction is characterized as a valorization of green methanol only with O 2 at ambient pressure and low temperatures, in contrast to conventional production processes. In order to conduct model‐based reactor and process optimization, a mechanistic kinetic approach is desirable, providing a higher validity and transferability. A new detailed catalytic network and coupled catalytic cycles for the heterogeneously catalyzed methanol oxidation, considering different redox and acid sites, are presented. On the basis of Christiansen's mathematics, the kinetics of several different subnetworks were successfully modeled mechanistically.

Chemie Ingenieur TechnikVol. 98(5)
Otto-von-Guericke-Universität Magdeburg (DE)
Openalex Percentile: Top 34%
Catalysis and Oxidation Reactions
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