Influence of the composition of the reaction mixture on the catalytic properties of the MoVSbNbСeOx/SiO2 catalyst in the reaction of oxidative dehydrogenation of ethane to ethylene

The influence of the reaction mixture composition on the catalytic properties of the Mo 1 V 0.24 Sb 0.23 Nb 0.08 Ce 0.01 O x /50 wt.% SiO 2 catalyst in the reaction of oxidative dehydrogenation of ethane into ethylene at a temperature of 400-440 °C was investigated. It has been shown that at a high concentration of ethane in the reaction mixture C 2 H 6 :O 2 = 74:26 (% vol.) and C 2 H 6 :O 2 = 80:20 (% vol.), the productivity of the process for ethylene is 153-157 g C2H6 /(kg cat. h). The catalyst stable work in highly concentrated reaction mixtures at 400–420 °C. This allows the process of oxidative dehydrogenation of ethane to be carried out with recycling of the reaction mixture at an ethane conversion of 20–30%.

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Publication Details

Journal
Kataliz v promyshlennosti
Published
2025-06-19
DOI
https://doi.org/10.18412/1816-0387-2025-3-30-36
Primary Topic
Catalysis and Oxidation Reactions
Type
article
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article

Influence of the composition of the reaction mixture on the catalytic properties of the MoVSbNbСeOx/SiO2 catalyst in the reaction of oxidative dehydrogenation of ethane to ethylene

Г. А. Зенковец, В. И. Соболев, В. М. Бондарева, А. А. Шутилов
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Kataliz v promyshlennosti
Catalysis and Oxidation Reactions
article

Influence of the composition of the reaction mixture on the catalytic properties of the MoVSbNbСeOx/SiO2 catalyst in the reaction of oxidative dehydrogenation of ethane to ethylene

Г. А. Зенковец, В. И. Соболев, В. М. Бондарева, А. А. Шутилов
article en

Abstract

The influence of the reaction mixture composition on the catalytic properties of the Mo 1 V 0.24 Sb 0.23 Nb 0.08 Ce 0.01 O x /50 wt.% SiO 2 catalyst in the reaction of oxidative dehydrogenation of ethane into ethylene at a temperature of 400-440 °C was investigated. It has been shown that at a high concentration of ethane in the reaction mixture C 2 H 6 :O 2 = 74:26 (% vol.) and C 2 H 6 :O 2 = 80:20 (% vol.), the productivity of the process for ethylene is 153-157 g C2H6 /(kg cat. h). The catalyst stable work in highly concentrated reaction mixtures at 400–420 °C. This allows the process of oxidative dehydrogenation of ethane to be carried out with recycling of the reaction mixture at an ethane conversion of 20–30%.

Kataliz v promyshlennostiVol. 25(3)
Boreskov Institute of Catalysis (RU)
Openalex Percentile: Top 93%
Catalysis and Oxidation Reactions
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