Резюме:

this article discusses the process of modeling an acetone production plant using catalytic dehydrogenation of isopropanol with the Aspen HYSYS V10 software environment. A detailed description of the model construction is presented, including the selection of a thermodynamic model, the specification of components, process conditions, and equipment parameters. The material and heat balance is calculated, and key process parameters are analyzed, including temperature-pressure regimes and stream compositions. The results of reactor optimization and heat recovery are described. The data obtained allow us to evaluate the efficiency of the process, identify bottlenecks, and suggest ways to improve the energy efficiency of the plant. The work may be useful for specialists involved in the design and analysis of organic synthesis processes, as well as for educational purposes in the field of chemical technology.

Keywords: acetone, isopropanol, dehydrogenation, Aspen HYSYS, modeling, reactor, heat balance, material balance, catalytic process, organic synthesis.

Borisov S.V. ¹, Kemalov R.A. ¹, Baymagambetov A.I. ¹, Al-shebli M.A. ¹, Stoll A.N. ² MODELING OF THE ACETONE PRODUCTION UNIT THROUGH THE DEHYDROGENATION OF ISOPROPANOL IN ASPENHYSYS V10 // Природные энергоносители и углеродные материалы & Natural energy sources and carbon materials. – 2025. – № 02;
URL: energy-sources.esrae.ru/140-344 (Date Access: 14.12.2025).

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