Abstract
A theoretical study of hydrocarbon dehydrogenation in state-of-the-art packed tubular membrane reactors and in impermeable tubes is performed. Conditions of the efficient operation of apparatuses are found under which a high degree of hydrocarbon conversion and yields of products are attained. The possibility of experimentally determining a number of constants for the such processes is shown. Results of theoretical calculations are compared to experimental data for isobutane dehydrogenation.
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Original Russian Text © V.N. Babak, T.B. Babak, S.E. Zakiev, L.P. Kholpanov, 2009, published in Teoreticheskie Osnovy Khimicheskoi Tekhnologii, 2009, Vol. 43, No. 1, pp. 78–92.
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Babak, V.N., Babak, T.B., Zakiev, S.E. et al. Theoretical study of hydrocarbon dehydrogenation at high temperatures. Theor Found Chem Eng 43, 74–87 (2009). https://doi.org/10.1134/S0040579509010102
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DOI: https://doi.org/10.1134/S0040579509010102