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Raising the Coefficient of Turbulent Diffusion in the Reaction Zone as Means To Improve Technical and Economical Parameters of Polymer Production

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Abstract

Use of a new type of apparatus, high-output small-size tubular turbulent reactors of mainly dif- fuser-confuser design, in very fast processes, including polymerization, is considered. The turbulent diffusion coefficient D t and its distribution over the apparatus volume were calculated as functions of the confuser divergence angle α. The calculations were confirmed by experimental data. New reactor designs for a number of processes of large-tonnage polymer production were proposed and put into practice.

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Authors and Affiliations

  1. Bashkortostan State University, Russia Kazan State Technological University, Ufa, Bashkortostan, Kazan, Tatarstan, Russia

    K. S. Minsker, V. P. Zakharov, R. G. Takhavutdinov, G. S. D'yakonov & Al. Al. Berlin

  2. Semenov Institute of Chemical Physics, Moscow, Russia

    K. S. Minsker, V. P. Zakharov, R. G. Takhavutdinov, G. S. D'yakonov & Al. Al. Berlin

Authors
  1. K. S. Minsker
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  2. V. P. Zakharov
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  3. R. G. Takhavutdinov
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  4. G. S. D'yakonov
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  5. Al. Al. Berlin
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Minsker, K.S., Zakharov, V.P., Takhavutdinov, R.G. et al. Raising the Coefficient of Turbulent Diffusion in the Reaction Zone as Means To Improve Technical and Economical Parameters of Polymer Production. Russian Journal of Applied Chemistry 74, 90–94 (2001). https://doi.org/10.1023/A:1012752101932

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  • DOI: https://doi.org/10.1023/A:1012752101932

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