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Effect of pressure on the activity and selectivity of cobalt-zeolite catalysts for the synthesis of hydrocarbons from CO and H2

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Abstract

The effect of pressure (0.5–2.5 MPa) on the synthesis of hydrocarbons from CO and H2 on Co-zeolite catalysts in a fixed-bed flow reactor was studied. It was found that productivity and selectivity for liquid hydrocarbons increased with pressure, whereas the selectivity of methane formation did not increase. The isoparaffin content of the products of catalysis was inversely proportional to the amount of heavy fractions in the products.

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References

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Authors and Affiliations

  1. Zelinsky Institute of Organic Chemistry, Russian Academy of Sciences, Leninskii pr. 47, Moscow, 119991, Russia

    A. L. Lapidus, O. L. Eliseev & A. S. Volkov

  2. Sunfuel Ltd., Calgary, Canada

    V. S. Budtsov

Authors
  1. A. L. Lapidus
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  2. V. S. Budtsov
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  3. O. L. Eliseev
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  4. A. S. Volkov
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Corresponding author

Correspondence to A. L. Lapidus.

Additional information

Original Russian Text © A.L. Lapidus, V.S. Budtsov, O.L. Eliseev, A.S. Volkov, 2008, published in Khimiya Tverdogo Topliva, 2008, No. 6, pp. 35–38.

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Lapidus, A.L., Budtsov, V.S., Eliseev, O.L. et al. Effect of pressure on the activity and selectivity of cobalt-zeolite catalysts for the synthesis of hydrocarbons from CO and H2 . Soil Fuel Chem. 42, 354–357 (2008). https://doi.org/10.3103/S0361521908060050

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  • DOI: https://doi.org/10.3103/S0361521908060050

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