CROSS-CURRENT PACKED TRAY FOR A DIABATIC PRODUCT-CONCENTRATING COLUMN

UDC 66.015.23

  • Nikolay Aleksandrovich Voynov Reshetnev Siberian State University of Science and Technology Email: n.a.voynov@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
  • Olga Petrovna Zhukova Reshetnev Siberian State University of Science and Technology Email: zhukovolga@yandex.ru
  • Vyacheslav Andreevich Chernov Reshetnev Siberian State University of Science and Technology Email: 76895jk@bk.ru
Keywords: diabatic rectification, tray, packing, evaporation, condensation, efficiency, heat transfer coefficient

Abstract

Diabatic rectification is one of the ways to increase the energy efficiency of the mixed distillation process. Diabatic units in which partial condensation of rising vapours and further evaporation of the condensate on contact devices placed on trays have proved effective. Horizontal perforated plate units are promising in this respect. They have low resistance and high efficiency, but have a narrow operating range. To intensify the separation process and increase column productivity, a combined cross-flow packed tray was developed and investigated. It consists of a spiral-prismatic packing placed in coaxial perforated cups and profiled plates, allowing the slurry to flow continuously downwards and preventing condensate from entering the evaporation zone. This type of tray design has made it possible to intensify the process of heat and mass transfer in the vapour and liquid phases and to extend the operating range of the tray.

The results of the experimental study of the developed tray in a pilot rectification column are presented. The distribution of the concentration of ethanol in the liquid flowing down the plates is shown. The effective temperature difference for mist evaporation on the profiled plates and condensation under the plates is determined. The value of the heat transfer coefficient of the heat flow on the plate is determined. Comparison of characteristic parameters of adiabatic column with spiral-prismatic packed countercurrent type with a diabatic column with cross-flow trays is made and the advantage of the latter is shown. For the construction of low tonnage product concentrating columns, also under vacuum, the developed trays are recommended.

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Author Biographies

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

Doctor of Technical Sciences, 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, Senior Lecturer

Olga Petrovna Zhukova , Reshetnev Siberian State University of Science and Technology

Candidate of Technical Sciences, Associate Professor

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

Student

References

Ismagilov R.M., Radbil' A.B., Radbil' B.A. Khimiya rastitel'nogo syr'ya, 2004, no. 2, pp. 73–76. (in Russ.).

Patent 20100137556 (US). 03.06.2010.

Kiss A.A. Journal of Chemical Technology & Biotechnology, 2013, vol. 89(4), pp. 479–498. https://doi.org/10.1002/jctb.4262.

Parhi S.S., Rangaiah G.P., Jana A.K. Separation and Purification Technology, 2021, vol. 260, 118225. https://doi.org/10.1016/j.seppur.2020.118225.

Javed A., Hassan A., Babar M., Azhar U., Riaz A., Mujahid R., Ahmad T., Mu-bashir M., Lim H.R., Show P.L., Khoo K.S. Energies, 2022, vol. 15, no. 18, 6498. https://doi.org/10.3390/en15186498.

Duan C., Li С. Energy, 2023, vol. 263C, 125821. https://doi.org/10.1016/j.energy.2022.125821

Ray S., Das G. Process Equipment and Plant Design, 2020, pp. 427–523. https://doi.org/10.1016/B978-0-12-814885-3.00014-2.

Pavlenko A.N., Pecherkin N.I., Zhukov V.E., Meski G., Houghton P. Renewable and Sustainable Energy Reviews, 2020, vol. 132, 110092. https://doi.org/10.1016/j.rser.2020.110092.

Zakharov M.K., Boichuk A.A. Chemical and Petroleum Engineering, 2019, vol. 54, pp. 901–909. https://doi.org/10.1007/s10556-019-00570-4.

Marin-Gallego M., Mizzi B., Rouzineau D., Gourdon С., Meyer M. Chemical Engineering and Processing – Process Intensification, 2022, vol. 171, 108643. https://doi.org/10.1016/j.cep.2021.108643.

Madyshev I.N., Kharkov V.V., Dmitrieva O.S., Zinurov V.E. Thermal Science and Engineering Progress, 2022, vol. 34, 101431. https://doi.org/10.1016/j.tsep.2022.101431.

Kooijman H.A., Sorensen E. Chemical Engineering Research and Design, 2022, vol. 188, pp. 473–482. https://doi.org/10.1016/j.cherd.2022.10.005.

Voinov N.A., Bogatkova A.V., Zemtsov D.A. ChemEngineering, 2022, vol. 6, no. 2, p. 29. https://doi.org/10.3390/chemengineering6020029.

Mello G.N., Battisti R., Urruth N.S., Machado R.A.F., Marangoni C. Chemical Engineering Research and Design, 2020, vol. 159, pp. 424–438. https://doi.org/10.1016/J.CHERD.2020.05.001.

Fonyo Z., Benko N. Chemical Engineering Research and Design, 1998, vol. 76, pp. 348–360. https://doi.org/10.1205/026387698524776.

Battisti R., Machado R.A.F., Marangoni C. Chemical Engineering and Processing – Process Intensification, 2020, vol. 150, 107873. https://doi.org/10.1016/j.cep.2020.107873.

Biasi L.C.K., Batista F.R.M., Zemp R.J., Romano A.L.R., Heinkenschloss M., Meirelles A.J.A. Chemical Engineering and Processing – Process Intensification, 2021, vol. 162, 108334. https://doi.org/10.1016/j.cep.2021.108334.

Alves J.L.F., da Silva Filho V.F., Machado R.A.F., Marangoni С. Process Safety and Environmental Protection, 2020, vol. 139, pp. 69–75. https://doi.org/10.1016/j.psep.2020.03.039.

Madyshev I.N., Kharkov V.V., Dmitrieva O.S., Zinurov V.E. Thermal Science and Engineering Progress, 2022, vol. 34, 101431. https://doi.org/10.1016/j.tsep.2022.101431.

Madyshev I.N., Dmitrieva O.S., Mayasova A.O., Nikolaev A.N. Chemical and Petroleum Engineering, 2022, vol. 58, no. 3–4, pp. 259–265. https://doi.org/10.1007/s10556-022-01084-2.

Madyshev I.N., Dmitrieva O.S., Mayasova A.O., Nikolaev A.N. Chemical and Petroleum Engineering, 2022, vol. 58, pp. 537–544. https://doi.org/10.1007/s10556-023-01126-3

Voinov N.A., Zemtsov D.A., Deryagina N.V., Bogatkova A.V., Zhukova O.P. Chemical Engineering Research and Design, 2022, vol. 185, pp. 1–13. https://doi.org/10.1016/j.cherd.2022.06.033.

Patent 2607730C1 (RU). 2017. (in Russ.).

Peton – tekhnologicheskiy inzhiniringovyy kholding. [Peton – a technology engineering holding]. URL: https://oldsite.peton.ru/pages.php?p=189. (in Russ.).

Mareshova L.A., Bogatykh K.F., Rol'nik L.Z., Yagafarova G.G. Elektronnyy Nauchnyy Zhurnal Neftegazovoye delo, 2007, no. 1, pp. 74–85. (in Russ.).

Patent 2803963 (RU). 2023. (in Russ.).

Voynov A.N., Zhukova O.P., Pan'kov V.A., Voynov N.A. Tekhnika i tekhnologiya pishchevykh produktov, 2012, no. 4, pp. 95–99. (in Russ.).

Shagivaliyev A.A., Nikolayev N.A. Khraneniye i pererabotka sel'khozsyr'ya, 2001, no. 7, pp. 14–17. (in Russ.).

Published
2024-12-04
How to Cite
1. Voynov N. A., Bogatkova A. V., Zemtsov D. A., Zhukova O. P., Chernov V. A. CROSS-CURRENT PACKED TRAY FOR A DIABATIC PRODUCT-CONCENTRATING COLUMN // Chemistry of plant raw material, 2024. № 4. P. 405-415. URL: https://journal.asu.ru/cw/article/view/14048.
Section
Technology