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Approximate mathematical model of the statics of the second stage of the hydrocracking process in a fixed catalyst bed

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Chemistry and Technology of Fuels and Oils Aims and scope

Conclusions

  1. 1.

    An equation to describe the kinetics of catalytic cracking and a mathematical model of the statics of the second stage of this process in a fixed catalyst bed have been proposed.

  2. 2.

    The mathematical model obtained for the statics of the hydrocracking process can be used for optimization of process control.

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Literature cited

  1. G. M. Panchenkov and Yu. M. Zhorov, Use of Mathematical Descriptions for Optimization of Chemical Processes in the Refining and Petrochemical Industry [in Russian], TsNIITÉneftekhim (1967).

  2. I. B. Rapoport, Synthetic Liquid Fuel, part 1 [in Russian], Gostoptekhizdat (1949).

  3. V. I. Karzhev, Destructive Hydrogenation of Organic Compounds, Trudy VNIGI, No. 5, Gostoptekhizdat (1953).

  4. V. A. Khavkin, Candidate Dissertation, All-Union Scientific-Research Institute for Petroleum and Gas Processing and the Production of Synthetic Liquid Fuel (1967).

  5. A. P. Zinov'eva and D. I. Orochko, The Principles of the Control by Reaction Units for the Hydrogenation of Fuels, Trudy VNIGI, No. 2, Gostoptekhizdat (1950).

  6. D. Hudson, Statistics for Physicists [Russian translation], Mir (1967).

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Authors
  1. V. A. Filimonov
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  2. A. A. Popov
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Additional information

Translated from Khimiya i Tekhnologiya Topliv i Masel, No. 9, pp. 5–8, September, 1970.

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Filimonov, V.A., Popov, A.A. Approximate mathematical model of the statics of the second stage of the hydrocracking process in a fixed catalyst bed. Chem Technol Fuels Oils 6, 646–650 (1970). https://doi.org/10.1007/BF00716536

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  • DOI: https://doi.org/10.1007/BF00716536

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