Properties of Heat and Mass Transfer Processes in the Tubular Grids with the Heat Exchanger as a Stabilizer

  • Viktor Moiseev
  • Oleksandr LiaposhchenkoEmail author
  • Peter Trebuna
  • Eugenia Manoilo
  • Oleg Khukhryanskiy
Conference paper
Part of the Lecture Notes in Mechanical Engineering book series (LNME)


In article considers hydrodynamic and heat mass transfer performances of simultaneous implementation of the heat mass transfer processes on tubular gratings with the stabilizer and a heat exchanger. The optimal service conditions for the absorber are determined. Analyzing the obtained data, we can conclude that high efficiency of using foam devices with the stabilization of the built-in heat exchangers at the stage of absorption of sulfur trioxide in the sulfuric acid production is shown. Efficient heat dissipation with the help of internal refrigerators provides the de-sired temperature mode of absorption, which allows eliminating all the bulky heat exchange economy in existing systems. The high performance activity of an absorber of the investigated construction is exhibited during the implementation of simultaneous processes. The industrial implementation of the stabilization method of the gas-liquid layer greatly extends the scope of foaming devices and opens up new possibilities for the intensification of the technological processes creating the low-waste technologies in chemical technology and other industries.


Hydrodynamics Heat exchanger Mass transfer Stabilization Foam layer Tubular grids Absorber Efficiency 


  1. 1.
    Tarat, E.Ya., Mukhlenov, I.P., Tubolkin, A.F., Tumarkina, E.S.: Churn Flow Regime and Foam Apparatuses. Chemistry, Leningrad (1977)Google Scholar
  2. 2.
    Braunshtein, B.I., Shchegolev, V.V.: Hydrodynamics and Mass and Heat Transfer in Columnar Apparatuses. Chemistry, Leningrad (1988)Google Scholar
  3. 3.
    Mukhlenov, I.P.: Absorption and dedusting in the production of mineral fertilizers. Chemistry, Moscow (1978)Google Scholar
  4. 4.
    Pozin, M.E., Mukhlenov, I.P., Tumarkina, E.S., Tarat, E.Ya.: Foam-Based Method of Gas and Liquid Treatment. Goskhimizdat, Leningrad (1955)Google Scholar
  5. 5.
    Voloshko, A.A., Sazonov, S.V.: Heat transfer during bubble formation in a liquid layer. Theor. Found. Chem. Technol. 32(6), 595 (1998)Google Scholar
  6. 6.
    Kunii, D., Levenshpil, O.: Industrial Fluidization. Chemistry, Moscow (1976)Google Scholar
  7. 7.
    Bogatykh, S.A.: Integrated Air Treatment in Foam Apparatuses. Sudostroenie, Leningrad (1974)Google Scholar
  8. 8.
    Pavlenko, A.N., Zhukov, V.E., Pecherkin, N.I., Surtaev, A.S., Volodin, O.A., Moiseev, M.I., Li, X., Gao, X., Zhang, L., Sui, H., Li, H.B.: A new approach to increase efficiency of distillation columns with a structured packing. In: Shalygin, M.G. (ed.) The Trends in Development of Engineering and Technologies, Coll. pap. of the Int. Sci. Tech. Conf., pp. 3–13, Tver (2015)Google Scholar
  9. 9.
    Komissarov, Y.A., Gordeev, L.S., Vent, D.P.: Processes and Apparatuses of Chemical Technology. Chemistry, Moscow (2011)Google Scholar
  10. 10.
    Elizarov, V.I., Elizarov, D.V., Merzlyakov, S.A., D’yakonov, S.G.: Calculating the number of actual separation stages in mass transfer columns. Theor. Found. Chem. Eng. 46(6), 567–575 (2012)CrossRefGoogle Scholar
  11. 11.
    Terasaka, K., Sun, W.-Y., Prakoso, T., Tsuge, H.: Measurement of heat transfer coefficient for direct-contact condensation during bubble growth in liquid. J. Chem. Eng. Jpn 32(5), 594 (1999)CrossRefGoogle Scholar
  12. 12.
    Polyanin, A.D., Vyaz’min, A.V.: Mass and heat exchange of drops and bubbles with flow. Theor. Found. Chem. Technol. 29(3), 249 (1995)Google Scholar
  13. 13.
    Moiseev, V., Manoilo, E., Ponomaryova N., Repko, K., Davydov, D.: Methodology of calculation of construction and hydrodynamic parameters of a foam layer apparatus for mass-transfer processes. In: Bulletin of NTU “KhPI”. Series: New solutions in modern technologies, vol. 16, no. 1292, p. 165. NTU “KhPI” (2018)CrossRefGoogle Scholar
  14. 14.
    Jang, J.: CFD simulation of a pharmaceutical bubbling bed drying process at three different scales. Powder Technol. 263, 14–25 (2014)CrossRefGoogle Scholar
  15. 15.
    Moiseev, V., Manoilo, E., Liaposhchenko, A., Khukhryansky, O., Ponomaryova, N.: Foam layer structure on countercurrent contact elements with stabilization. In: Bulletin of NTU “KhPI”. Series: New solutions in modern technologies, vol. 26, no. 1302, pp. 83–93. NTU “KhPI”, Kharkiv (2018)CrossRefGoogle Scholar

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© Springer Nature Switzerland AG 2020

Authors and Affiliations

  1. 1.National Technical University “Kharkiv Polytechnic Institute”KharkivUkraine
  2. 2.Sumy State UniversitySumyUkraine
  3. 3.Technical University of KosiceKosiceSlovak Republic
  4. 4.PJSC “UKRHIMPROEKT”SumyUkraine

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