Abstract: Catalytic oxidation of volatile organic compounds (VOCs) has several advantages over thermal methods: a lower temperature for the oxidation reaction, higher efficiency of oxidation of VOCs, and most importantly, significant decrease of energy consumption in comparison with noncatalytic combustion. From the view-point of compliance with the criteria of energy efficiency, ease, and safety in use and maintenance, adsorption–catalytic processes (ACPs) based on the combination of the principles of adsorption and catalytic technologies are of particular interest. The considered designs of reactors require the setting of three-dimensional mathematical models, because the ongoing processes have an inhomogeneous radial distribution in the reactor. In ACP, it was assumed that there were no reactions in the flow, and the conversion occurred in the pores of the pellet, on inner surface of the adsorbent–catalyst.

Cite: Zazhigalov S. , Elyshev A. , Zagoruiko A.
Modeling of Unsteady-State Catalytic and Adsorption–Catalytic Processes: Novel Reactor Designs
Monography chapter Mathematical Modeling of Complex Reaction Systems in the Oil and Gas Industry. – Wiley., 2024. – C.138-167. – ISBN 9781394220052. DOI: 10.1002/9781394220052.ch4 Scopus OpenAlex

Dates:

Published online:

Jul 26, 2024

Identifiers:

Scopus:	2-s2.0-85205613014
OpenAlex:	W4401011679

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