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Effect of leakage of volatile synthesis products on silicon carbide yield in an electrothermal fluidized bed reactor

https://doi.org/10.32362/2410-6593-2024-19-2-163-173

Abstract

Objectives. To calculate the effect of leakage of volatile synthesis products on silicon carbide yield in an electrothermal fluidized bed reactor, as well as to develop a general model of the synthesis of finely divided silicon carbide. This will be achieved by particularizing a mathematical model of leakage of volatile products of chemical reactions from the reaction volume of the reactor with the fluidizing inert gas.

Methods. As a method to produce silicon carbide, synthesis in an electrothermal fluidized bed was studied. The model of leakage of volatile products was validated by comparing the calculation results with existing experimental data on the SiC synthesis in a hightemperature fluidized bed reactor. The comparison parameters were: mass yield of silicon carbide, and the total synthesis time in a reactor with batch loading of silicon dioxide into the reaction volume.

Results. The value of the parameter p in the general model of SiC synthesis in a fluidized bed was established. The parameter p is equal to the ratio of the number of carbon-containing particles involved in the formation of SiO, to the total number of silicon dioxide particles. It also characterizes the composition of stable complexes of particles of the charge at various operating temperatures of the fluidized bed. The discrepancy between the calculated and experimental values of the masses of the synthesized silicon carbide was shown not to exceed 15.5% at a high temperature of the fluidized bed (T = 1800°C) and decreases with a decrease in the operating temperature to 4.7% at T = 1450°C.

Conclusions. The general computational model for silicon carbide synthesis with a built-in procedure for calculating the leakage of volatile products of chemical reactions enables the variants of SiC production in electrothermal fluidized bed reactors to be analyzed. In this case, it is important to establish an energy-efficient working cycle without preliminary expensive experimental studies.

About the Authors

V. S. Kuzevanov
National Research University “MPEI”, Volzhsky Branch
Russian Federation

Vyacheslav S. Kuzevanov, Dr. Sci. (Eng.), Professor, Department of Energy

Scopus Author ID 57204855036

69, Lenina pr., Volzhsky, Volgograd oblast, 404110, Russia



S. S. Zakozhurnikov
MIREA — Russian Technological University
Russian Federation

Sergey S. Zakozhurnikov, Cand. Sci. (Eng.), Associate Professor, Department of Higher Mathematics-3, Institute for Advanced Technologies and Industrial Programming

Scopus Author ID 57198768825,
ResearcherID ABG-4696-2020

78, Vernadskogo pr., Moscow, 119454, Russia



G. S. Zakozhurnikova
Volgograd State Technical University
Russian Federation

Galina S. Zakozhurnikova, Cand. Sci. (Eng.), Associate Professor, Department of Heat Engineering and Hydraulics

Scopus Author ID 57198782591,
ResearcherID HHY-8485-2022

28, Lenina pr., Volgograd, 400005, Russia



References

1. Vasil’eva E.V., Cherkasova T.G., Nevedrov A.V., Papin A.V., Subbotin S.P. The possibility of modernizing coke chemical production using a computer program for predicting the yield of chemical coking products. In: Chemistry and Chemical Technology: Achievements and Prospects: Proceedings of the Fifth All-Russian Conference. 2020. P. 83.1–83.3 (in Russ).

2. Ryabov G.A., Folomeev O.M. Problems of Hydrodynamics and Heat Transfer in Interconnected Bed Reactors for CO2 Capture and Obtaining Hydrogen. Therm. Eng. 2023;70(4):311–322. https://doi.org/10.1134/S0040601523040055

3. Prado D.S., Vilarrasa-García E., Sampronha E., et al. Multiple approaches for large-scale CO2 capture by adsorption with 13X zeolite in multi-stage fluidized beds assessment. Adsorption. 2023. https://doi.org/10.1007/s10450-023-00422-x

4. Sun L., Yin F., Cao J., et al. Numerical Study on the Process of Chemical Looping Hydrogen Production with Multiple Circulating Fluidized Bed Reactors. J. Therm. Sci. 2023;32(5):1945–1954. https://doi.org/10.1007/s11630-023-1872-1

5. Ryabov G.A. A Review of the Research Results into the Technologies of Solid-Fuel Combustion in a Circulating Fluidized Bed Conducted Abroad and in Russia. Therm. Eng. 2021;68(2): 117–135. https://doi.org/10.1134/S0040601521020051

6. Semeiko K.V., Kustovskyi S.S., Kupriyanchuk S.V., et al. Dependence of the Pyrocarbon Structure on the Parameters of the Process of Pyrolysis of Hydrocarbon Gases in an Electrothermal Fluidized Bed. J. Eng. Phy. Thermophys. 2020;93(3):677–684. https://doi.org/10.1007/s10891-020-02166-9

7. Mitrofanov A.V., Mizonov V.E., Vasilevich S.V., Mal’ko M.V. Experimental-calculated study of hydro-mechanical processes within electrothermal fluidized bed. Kosygin International Forum. MNTS Planovsky-2021. 2021. V. 1. P. 54–57 (in Russ.).

8. MitrofanovA.V.,Vasilevich S.V., Mal’ko M.V., Ovchinnikov L.N., Shpeinova N.S. Development of a mathematical model of fl of particles in presence of internal heat sources. Vestnik Ivanovskogo gosudarstvennogo energeticheskogo universiteta (Vestnik IGEU) = Vestnik of Ivanovo State Power Engineering University (Vestnik IGEU). 2022;6:49–57 (in Russ.).

9. Borodulya V.A., Vinogradov L.M., Greben’kov A.Zh., Mikhailov A.A., Sidorovich A.M. Carbide-thermal reduction of SiO2 and formation of silicon carbide in an electrothermal fluidized bed. In: Teplo i Massoperenos – 2012. Minsk: A.V. Lykov ITMO, NAS of Belarus; 2013. P. 121–127 (in Russ.).

10. Borodulya V.A., Vinogradov L.M., Greben’kov A.Zh., Mikhailov A.A. Synthesis of silicon carbide in electrothermal reactor with fluidized bed of carbon particles. Gorenie i Plazmokhimiya. 2015;13(2):92–102 (in Russ.).

11. Borodulya V.A., Greben’kov A.Zh., Mikhailov A.A. Features of the formation of various structural modifications of silicon carbide during its carbothermal synthesis in an electrothermal fluidized bed reactor. In: Teploi Massoperenos – 2018. Minsk: A.V. Lykov ITMO, NAS of Belarus; 2019. P. 107–114 (in Russ.).

12. Borodulya V.A., Vinogradov L.M., Greben’kov A.Zh., Mikhailov A.A. Method and plant for obtaining silicon carbide: Eur. Pat. 27539. Publ. 31.08.2017 (in Russ.).

13. Kuzevanov V.S., Garyaev A.B., Zakozhurnikov S.S., Zakozhurnikova G.S. Model of continuous production of fi silicon carbid. IOP Conf. Ser.: Mater. Sci. Eng. 2019;537(3): 032106. https://doi.org/10.1088/1757-899X/537/3/032106

14. Kuzevanov V.S., Zakozhurnikov S.S., Zakozhurnikova G.S., Garyaev A.B. Finely dispersed silicon carbide synthesis model in the electrothermal reactor with periodic batch loading. J. Phys.: Conf. Ser.: Hydrodynamics and Heat and Mass Transfer. 2020;1683: 022054. https://doi.org/10.1088/1742-6596/1683/2/022054

15. Kuzevanov V.S., Zakozhurnikov S.S., Zakozhurnikova G.S. Model and results of a study of the synthesis of finely dispersed silicon carbide in an electro-thermal reactor. Solid State Phenomena. 2021;316:147–152. https://doi.org/10.4028/www.scientific.net/SSP.316.147

16. Simeiko K.V., Malinouski A.I., Grebenkov A.Zh., Sayenko S.Yu., Lobach K.V., Kustovskaya A.D., Liaposhchenko O.O., Sklabinskyi V.I. Development of technologies of silicon carbide producing (Review). Vestnik NYaTs RK = NNC RK Bulletin. 2021;2:30–41 (in Russ.). https://doi.org/10.52676/1729-7885-2021-2-30-41

17. Higher Transcendental Function: in 3 v. V. I. McGraw – Hill Book Company. Inc.; 1953. 395 p.

18. Fikhtengolts G.M. Kurs differentsial’nogo i integral’nogo ischisleniya (Course of Differential and Integral Calculus): in 3 v. Moscow–Leningrad: Gostekhizdat; 1948. V. 2. 793 p. (in Russ.).

19. Barabanov N.N., Zemskova V.T., Mitrofanov A.D., Ermolaeva E.V. Mathematical modeling of the process of carbidization of syntactic foams. Izv. Vyssh. Uchebn. Zaved. Khim. Khim. Tekhnol. = ChemChemTech. 1998;41(5): 32–34 (in Russ.).

20. Li X., Zhang G., Tronstad R., Ostrovski O. Reduction of quartz to silicon monoxide by methane-hydrogen mixtures. Metall. Mater. Trans. B: Process Metall. Mater. Processing Sci. 2016;47(4):2197–2204. https://doi.org/10.1007/s11663-016-0670-5

21. Wallis G. Odnomernye dvukhfaznye techeniya (One-Dimensional Two-Phase Flows): transl. from Engl. Moscow: Mir; 1972. 440 p. (in Russ.). [Wallis G. One-Dimensional Two-Phase Flows. NY: McGraw-Hill; 1969. 408 p.]

22. Ageev O.A. Karbid kremniya: tekhnologiya, svoistva, primenenie (Silicon Carbide: Technology, Properties, Applications). Kharkov: ISMA; 2010. 531 p. (in Russ.). ISBN 978-966-02-5445-9


Supplementary files

1. Effect of synthesis time on silicon carbide yield at 1450°C
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Type Результаты исследования
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  • The effect of leakage of volatile synthesis products on silicon carbide yield in an electrothermal fluidized bed reactor was calculated.
  • A general model of the synthesis of finely divided silicon carbide by particularizing a mathematical model of leakage of volatile products of chemical reactions from the reaction volume of the reactor with the fluidizing inert gas was developed.
  • The general computational model for silicon carbide synthesis with a built-in procedure for calculating the leakage of volatile products of chemical reactions enables the variants of SiC production in electrothermal fluidized bed reactors to be analyzed. In this case, it is important to establish an energy-efficient working cycle without preliminary expensive experimental studies.

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For citations:


Kuzevanov V.S., Zakozhurnikov S.S., Zakozhurnikova G.S. Effect of leakage of volatile synthesis products on silicon carbide yield in an electrothermal fluidized bed reactor. Fine Chemical Technologies. 2024;19(2):163-173. https://doi.org/10.32362/2410-6593-2024-19-2-163-173

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