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Oxidative conversion of ethane over VMoTeNb oxide catalyst

  • Catalysis in Chemical and Petrochemical Industry
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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).

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Authors and Affiliations

  1. Boreskov Institute of Catalysis, Russian Academy of Sciences, Novosibirsk, 630090, Russia

    V. M. Bondareva, E. V. Ishchenko, L. A. Shadrina & V. I. Sobolev

  2. Novosibirsk State University, Novosibirsk, 630090, Russia

    E. V. Ishchenko

Authors
  1. V. M. Bondareva
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  2. E. V. Ishchenko
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  3. L. A. Shadrina
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  4. V. I. Sobolev
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Corresponding author

Correspondence to V. M. Bondareva.

Additional information

Original Russian Text © V.M. Bondareva, E.V. Ishchenko, L.A. Shadrina, V.I. Sobolev, 2015, published in Kataliz v Promyshlennosti.

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Bondareva, V.M., Ishchenko, E.V., Shadrina, L.A. et al. Oxidative conversion of ethane over VMoTeNb oxide catalyst. Catal. Ind. 8, 112–115 (2016). https://doi.org/10.1134/S2070050416020033

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  • DOI: https://doi.org/10.1134/S2070050416020033

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