MASS TRANSFER IN THE BIOREACTOR DURING GAS DISPERSION FROM THE STIRRER VORTEX CAVITY

UDK 66.015.23

  • Nikolay Aleksandrovich Voynov Reshetnev Siberian State University of Science and Technology Email: n.a.voynov@mail.ru
  • Alexander Sergeevich Frolov Reshetnev Siberian State University of Science and Technology Email: frolov-a84@mail.ru
  • Anastasia Viktorovna Bogatkova Reshetnev Siberian State University of Science and Technology Email: Sonchic-Sveta@yandex.ru
  • Denis Andreevich Zemtsov Reshetnev Siberian State University of Science and Technology Email: zemcovda@sibsau.ru
  • Vyacheslav Andreevich Chernov Reshetnev Siberian State University of Science and Technology Email: 76895jk@bk.ru
Keywords: bioreactor, mass transfer, power, paddle stirrer, gas content, numerical modeling

Abstract

Gas-liquid bioreactors in which the introduction of the gas substrate in the culture liquid is carried out from the vortex cavity formed by the rotation of the stirrer.  In order to simplify the design and intensify mass transfer a new method of dispersing the gas substrate from the vortex cavity is proposed and studied.  It consists in maintaining local zones with reduced pressure in the liquid behind the rotating paddles and creating the necessary conditions for the introduction of the gas substrate. On the basis of numerical simulation the pressure is calculated and the zones of low pressure in liquid behind the stirrer paddles are determined. The value of differential pressure necessary for gas dispersion has been estimated. The angular velocity of liquid rotation depending on the number of partitions on the apparatus wall and the number of mixer revolutions is presented. The gas content in the liquid during the implementation of the investigated method has been determined. The average surface diameter of gas bubbles and interfacial surface of gas-liquid medium were calculated from experimental data. The power spent on stirring in the apparatus has been established and the power criterion with regard to gas content has been determined. Mass transfer at intensive gas dispersion from gas vortex cavity into liquid has been investigated. Criterion dependence for calculation of mass transfer coefficient is presented, taking into account energy dissipation spent on mixing and interfacial surface. The fields of application of bioreactor with new method of gas dispersion are shown.

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Author Biographies

Nikolay Aleksandrovich Voynov, Reshetnev Siberian State University of Science and Technology

Doctor of Technical Sciences, Professor

Alexander Sergeevich Frolov, Reshetnev Siberian State University of Science and Technology

Candidate of Technical Sciences, Associate Professor

Anastasia Viktorovna Bogatkova, Reshetnev Siberian State University of Science and Technology

Candidate of Technical Sciences

Denis Andreevich Zemtsov, Reshetnev Siberian State University of Science and Technology

Candidate of Technical Sciences

Vyacheslav Andreevich Chernov, Reshetnev Siberian State University of Science and Technology

student

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Published
2024-03-12
How to Cite
1. Voynov N. A., Frolov A. S., Bogatkova A. V., Zemtsov D. A., Chernov V. A. MASS TRANSFER IN THE BIOREACTOR DURING GAS DISPERSION FROM THE STIRRER VORTEX CAVITY // chemistry of plant raw material, 2024. № 1. P. 362-371. URL: http://journal.asu.ru/cw/article/view/12574.
Section
Technology