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Calculation of Hydrodynamic Characteristics of Apparatus with Regular Tubular Packing

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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Among the apparatuses with a regular arrangement of packing elements creating an in-phase mode of vortex interaction, which ensures high efficiency of the processes, it is interesting to use a standard tubular packing. Such packing allows additional advantages associated with heat supply or extraction directly in the contact zone of the interacting phases, which is very important for conducting some chemisorption processes. The research covers such hydrodynamic regularities as hydraulic resistance during a heat carrier movement in pipes and during external flow around a tubular beam, retained liquid amount and gas content of layer in the external flow around the tubular beam with liquid and gas flows. The research was carried out using an experimental setup with a heat and mass transfer apparatus with regular tubular packing. The medium used during experiments is water-air. The research methodology included standard methods for determining hydraulic resistance and retained liquid amount and visual observation and photographing of gas-liquid flows. The novelty of the research was equations – one for calculating the hydraulic resistance in pipes, taking into account local resistances and pipe roughness. The other ones for determining the pressure losses during the external flow around the tubular beam, the retained liquid amount, and the gas content of the layer, taking into account the vortex interaction of gas and liquid flows. Graphical and calculated dependences of the investigated hydrodynamic characteristics were obtained as a result of the conducted research of the hydraulic resistance during the heat carrier movement in the pipes, as well as the hydraulic resistance and the retained liquid amount during the external flow around the tubular beam with a change in the gas velocity and irrigation density. When the heat carrier flows in the pipes, the numerical values of the hydraulic resistance in the transient mode do not exceed 1.5 kPa, in the developed turbulence mode in the range of the Reynolds number from 1·104 to 6·104 ΔР varies from 1.5 to 53 kPa. With the external flow around the tubular beam, in the developed turbulence mode wg=4 m/s and L = 25 m3/m2h, the hydraulic resistance is 85 Pa, the retained liquid amount is 4.5·10-3 m. The change in the irrigation density in this mode (developed turbulence) in the L range from 10 to 100 m3/m2h leads to an increase in the hydraulic resistance from 65 to 160 Pa, the retained liquid amount from 2.16·10-3 to 13.6·10-3 m. The calculated dependencies are the basis of the method for calculating the hydrodynamic characteristics of the apparatus with the regular tubular packing, which can be used to calculate industrial devices.
Rocznik
Tom
Strony
868--882
Opis fizyczny
Bibliogr. 23 poz., rys.
Twórcy
  • M. Auezov South Kazakhstan State Universit
  • M. Auezov South Kazakhstan State Universit
  • M. Auezov South Kazakhstan State Universit
  • M. Auezov South Kazakhstan State Universit
  • M. Auezov South Kazakhstan State Universit
Bibliografia
  • Balabekov, O.S., & Petin, V.F. (2000). Regularity of vortex interaction arising in the separated flow around a gas or liquid flow discretely located along it. Certificate of Scientific Discovery № 144. Moscow: International Association of Authors of Scientific Discoveries.
  • Balabekov, O.S., & Volnenko, A.A. (2015). Calculation and design of heat and mass transfer and dust collectors with movable and regular packing. Shymkent, 184.
  • Balabekov, O.S., Volnenko, A.A., Korganbayev, B.N. (2004). Regularities of the flow around a system of regularly placed elements with different spatial arrangement. Proceedings of International Scientific Conference “Energy and resource saving technologies and equipment, environmentally friendly productions”, V.1. Ivanovo: ISCTU, 340-354.
  • Balabekov, O.S., Volnenko, A.A., Praliyev, S., Korganbayev, B.N., Balabekova, M.O., Viktorov, S.V. (2004). Regularity of formation of parallel moving vortex jets during the flow of a gas or liquid flow through the system across to it located discrete sources. Certificate of Scientific Discovery № 269. Moscow: International Association of Authors of Scientific Discoveries,.
  • Balabekov, OS (1984). Hydrodynamics, mass transfer and dust collection in counterflow and direct-flow two-phase drop and film flows in the layer of a movable packing. [Doctoral dissertation: Moscov], 430.
  • Bekibayev, NS (2008). Scientific foundations of coupled heat and mass transfer processes in in-phase vortex apparatuses. [Doctoral dissertation, South Kazakhstan State University named by. M.Auezov, Shymkent].
  • Domansky, I.V., Isakov, V.P., Ostrovsky, G.M. (1982). Machines and devices for chemical productions: Examples and tasks. (Under the general editorship of Sokolov V.N). L.: Mechanical engineering.
  • Einstein, V.G., Zakharov, M.K., Nosov, G.A. (2002). General course of processes and chemical engineering apparatuses: Textbook: in 2 volumes. Moscow: Logos; Higher school.
  • Idelchik, I.E. (1992). Handbook of hydraulic resistances. (Under the editorship of M.O. Steinberg. 3rd ed., rev. and add). Mosсow: Mechanical engineering.
  • Kagan, AM (2013) Contact packings of industrial heat and mass transfer apparatuses. Kazan.
  • Korganbayev, BN (1999). Hydrodynamics and heat-mass transfer in devices with regularly rotating packings. [Disertation candidate technical sciences, South Kazakhstan State University named by. M.Auezov, Shymkent].
  • Kumisbekov, SA (1999). Hydrodynamics and mass transfer in an apparatus with a regular lamellar vibrating packing. [Disertation candidate technical sciences, South Kazakhstan State University named by. M.Auezov, Shymkent].
  • Laptev, A.G., Basharov, M.M., Lapteva, E.A. (2017). Separation and energy efficiency of packed apparatuses for purifying gases from aerosols, Theoretical Foundations of Chemical Engineering, 51(5), 639-646. DOI: https://doi.org/10.1134/S0040579517050335
  • Lapteva. E.A. (2019). Efficiency of transfer phenomena in gas-liquid media during desorption and cooling of liquids. Kazan.
  • Ramm, V.M. (1976). Gas absorption. Mosсov: Chemistry. http://booksonchemistry.com/index.php?id1=3&category=other&author=ramm-vm&book=1976
  • Sabyrkhanov, DS (1996). Development, calculation and implementation of mass transfer and dust collecting devices with movable and regular packing. [Doctoral dissertation, South Kazakhstan State University named by. M.Auezov, Shymkent].
  • Seitkhanov, NT (2002). Structure of flows and contact heat and mass transfer in a device with a regular lammelar packing. [Disertation candidate technical sciences, South Kazakhstan State University named by. M.Auezov, Shymkent].
  • Serikuly, Z., Volnenko, A., Kumisbekov, S. (2020). Optimum Values Regular Structure Converters for Converting the Vibration into Electric Energy International Review of Mechanical Engineering (IREME), 14(6), 388-395. DOI: https://doi.org/10.15866/ireme.v14i6.18844
  • Serikuly, Zh (2015). Development and calculation of heat and mass transfer apparatuses with a movable packing taking into account a large-scale transition. [Dissertation PhD. South Kazakhstan State University named by. M.Auezov, Shymkent]
  • Volnenko AA (1999). Scientific bases for the development and calculation of vortex mass transfer and dust collecting devices. [Doctoral dissertation, South Kazakhstan State University named by. M.Auezov, Shymkent], 300.
  • Volnenko, A.A., & Balabekov, O.S. (2016). Calculation of heat and mass transfer and dust collectors with weighted and regular packing. Examples and tasks. Shymkent.
  • Volnenko, A.A., Balabekov, O.S., Korganbayev, B.N., Khussanov, Zh.Ye., Bekibayev, N.S. (2013) Innovative patent № 27719 of the Republic of Kazakhstan, IPC B01D 53/20, B01D 47/14. Apparatus with a packing for heat and mass transfer and dust collection. Bul. 12(4). URL: https://kzpatents.com/4-ip27719-apparat-s-nasadkojjdlya-teplomassoobmena-i-pyleulavlivaniya.html
  • Yesskendirov, MZ (2005). System-element-wise modeling of the processes of coagulation and deposition of aerosols in direct-flow multiphase flows of organized vortex structure. [Doctoral dissertation, South Kazakhstan State University named by. M.Auezov, Shymkent].
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-478ffc02-2c1b-4342-9c63-0e38ea277d40
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