Conclusions
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1.
The impairment of the kinetic characteristics of heterogeneous chemical processes in a fluidized bed of catalyst in comparison with a stationary bed is due both to mixing of the gas phase in the bed and to nonideality of phase contact.
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2.
The effect due to inadequate contact of the interacting phases is more marked than that due to mixing of the gaseous reagents.
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3.
The coefficient of utilization of the interphase contact surface can be increased by using more active catalysts and by partitioning the fluidized bed.
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Translated from Khimiya i Tekhnologiya Topliv i Masel, No. 12, pp. 15–19, December, 1969.
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Lyandres, S.É., Martyushin, E.I. & Akopyan, L.A. How fluidization nonuniformity affects a first-order catalytic reaction. Chem Technol Fuels Oils 5, 864–869 (1969). https://doi.org/10.1007/BF01110754
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DOI: https://doi.org/10.1007/BF01110754