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Phase contact surface and mass-transfer in bubble reactors

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Chemistry and Technology of Fuels and Oils Aims and scope

Conclusions

  1. 1.

    With the aid of photography we have determined the phase contact surface in a model bubble reactor as a function of gas velocity. Simultaneously we have carried out measurements of the rate of mass-transfer in the process of sodium sulfite oxidation in aqueous solution.

  2. 2.

    The true mass-transfer coefficients, calculated from experimental data, coincide satisfactorily with those calculated from the theoretical dependence.

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Authors and Affiliations

  1. Scientific Research Institute of Synthetic Alcohols and Organic Products, USSR

    V. A. Men'shchikov, M. É. Aérov & S. S. Trainina

Authors
  1. V. A. Men'shchikov
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  2. M. É. Aérov
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  3. S. S. Trainina
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Additional information

Deceased.

Translated from Khimiya i Tekhnologiya Topliv i Masel, No. 4, pp. 14–16, April, 1967.

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Men'shchikov, V.A., Aérov, M.É. & Trainina, S.S. Phase contact surface and mass-transfer in bubble reactors. Chem Technol Fuels Oils 3, 237–240 (1967). https://doi.org/10.1007/BF00731743

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  • DOI: https://doi.org/10.1007/BF00731743

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