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Mathematical model for mixing liquids with a disperse phase in laminar and turbulent regimes in packed-bed flow mixers

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Abstract

A mathematical model for calculating static packed-bed mixers in laminar and turbulent regimes is discussed. The mathematical model is constructed using the theory of mass transfer and turbulent migration of particles when the mass transfer of a finely disperse phase is considered as a kind of diffusion process. Some calculations have been performed and certain dependences of the mixing efficiency on the Reynolds number have been plotted.

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Authors and Affiliations

  1. Kazan State Power Engineering University, ul. Krasnosel’skaya 51, Kazan, 420066, Tatarstan, Russia

    A. G. Laptev & O. G. Dudarovskaya

  2. Inzhekhim Engineering-Promotional Center, ul. Shalyapina 14/83, Kazan, 420049, Tatarstan, Russia

    T. M. Farakhov

Authors
  1. A. G. Laptev
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  2. T. M. Farakhov
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  3. O. G. Dudarovskaya
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Corresponding author

Correspondence to O. G. Dudarovskaya.

Additional information

Original Russian Text © A.G. Laptev, T.M. Farakhov, O.G. Dudarovskaya, 2015, published in Teoreticheskie Osnovy Khimicheskoi Tekhnologii, 2015, Vol. 49, No. 1, pp. 23–31.

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Laptev, A.G., Farakhov, T.M. & Dudarovskaya, O.G. Mathematical model for mixing liquids with a disperse phase in laminar and turbulent regimes in packed-bed flow mixers. Theor Found Chem Eng 49, 21–29 (2015). https://doi.org/10.1134/S004057951501008X

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  • DOI: https://doi.org/10.1134/S004057951501008X

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