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Control over selectivity and rate of hydrocarbon synthesis from carbon monoxide and hydrogen

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Abstract

A mathematical model was developed for hydrocarbon synthesis from CO and H2 in a tubular fixed-bed reactor over a cobalt catalyst. On the basis of the model, optimal conditions for the process in the cases when the desired products are C7H16 and C17H36 are recommended.

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Authors and Affiliations

  1. South-Russia State Technical University (Novocherkassk Polytechnic Institute), Novocherkassk, Russia

    A. P. Savost’yanov & N. V. Vysochin

  2. Synfuel Ltd., Calgary, Alberta, Canada

    V. S. Budtsov

  3. Zelinsky Institute of Organic Chemistry, Russian Academy of Sciences, Moscow, Russia

    A. L. Lapidus

Authors
  1. A. P. Savost’yanov
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  2. V. S. Budtsov
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  3. N. V. Vysochin
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  4. A. L. Lapidus
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Corresponding author

Correspondence to A. P. Savost’yanov.

Additional information

Original Russian Text © A.P. Savost’yanov, V.S. Budtsov, N.V. Vysochin, A.L. Lapidus, 2007, published in Khimiya Tverdogo Topliva, 2007, No. 6, pp. 58–64.

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Savost’yanov, A.P., Budtsov, V.S., Vysochin, N.V. et al. Control over selectivity and rate of hydrocarbon synthesis from carbon monoxide and hydrogen. Soil Fuel Chem. 41, 370–375 (2007). https://doi.org/10.3103/S0361521907060092

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  • DOI: https://doi.org/10.3103/S0361521907060092

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