INFLUENCE OF GEOMETRIC PARAMETERS OF REGULAR STRUCTURED PACKING ON HYDRODYNAMICS AND MASS TRANSFER

UDC 66.021.3

  • Vaytsekhovich Petr Yevgen’yevich – DSc (Engineering), Professor, Professor, the Department of Machines and Apparatus for Chemical and Silicate Production. Belarusian State Technological University (13a, Sverdlova str., Minsk, 220006, Republic of Belarus). E-mail: vpe51@mail.ru

  • Mytsko Dzmitry Yur’yevich – PhD student, the Department of Machines and Apparatus for Chemical and Silicate Production. Belarusian State Technological University (13a, Sverdlova str., Minsk, 220006, Republic of Belarus). E-mail: mytko.dmitrij@mail.ru

  • Volk Anatoliy Matveevich – PhD (Engineering), Assistant Professor, the Department of Higher Mathematics. Belarusian State Technological University (13a, Sverdlova str., Minsk, 220006, Republic of Belarus). E-mail: Anatoliyvolk@mail.ru

Key words: desorption, hydrodynamics, mass transfer, regularly structured packing, transfer unit height.

For citation: Vaytsekhovich P. Ye., Mytsko D. Yu., Volk A. M. Influence of geometric parameters of regular structured packing on hydrodynamics and mass transfer. Proceedings of BSTU, issue 2, Chemical Engineering, Biotechnologies, Geoecology, 2021, no. 2 (247), pp. 67−71 (In Russian). DOI: https://doi.org/10.52065/2520-2669-2021-247-2-67-71.

Abstract

This paper describes the benefits of a regular structured zigzag packing. The task of further research has been determined. To carry out the experiment and further comparison, three types of zigzag packing were developed, the difference of which was in the length of the side of the cross section of the cell channel. Each of the packages was installed with a twist of twenty degrees from each other. For comparison, one of them was aligned coaxially. The research aims to study fluid dynamics and mass transfer efficiency. Based on the experimental data, graphical dependences of the hydraulic resistance of the dry and irrigated packing, as well as the efficiency of mass transfer for the gas-liquid system, were constructed. The hydrodynamic modes of operation of the nozzles and at what speed the entrainment of liquid drops is achieved are determined. Based on the results of the experiment, the height of the transfer unit was calculated. A conclusion is made about the influence of the length of the side of the cross-section of the cell channel on the hydraulic resistance, the efficiency of mass transfer and the height of the equivalent theoretical plate of regularly-structured zigzag nozzles.

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27.05.2021