Oxidative conversion of ethane over VMoTeNb oxide catalyst


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Abstract

The oxidative conversion of ethane over a multicomponent oxide catalyst with the composition V0.3Mo1Te0.23Nb0.12 was studied in the temperature range of 360–450°C. It was found that temperature did not affect the contribution from the parallel and consecutive paths of reaction product formation. The obtained data could be useful in developing applications for the process, particularly in choosing the type and design of a reactor (tubular fixed bed, fluidized bed, and so on).

About the authors

V. M. Bondareva

Boreskov Institute of Catalysis

Author for correspondence.
Email: valent@catalysis.ru
Russian Federation, Novosibirsk, 630090

E. V. Ishchenko

Boreskov Institute of Catalysis; Novosibirsk State University

Email: valent@catalysis.ru
Russian Federation, Novosibirsk, 630090; Novosibirsk, 630090

L. A. Shadrina

Boreskov Institute of Catalysis

Email: valent@catalysis.ru
Russian Federation, Novosibirsk, 630090

V. I. Sobolev

Boreskov Institute of Catalysis

Email: valent@catalysis.ru
Russian Federation, Novosibirsk, 630090

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