Abstract
The paper presents an analysis of the operational behaviour of the industrial reactor for maleic anhydride synthesis. The kinetic model of the process carried at the elevated benzene concentrations (within the explosivity range) is proposed. The analysis is carried out on the base of the mathematical model of mlultitubular reactor taking account of thermal interaction between heat carrier flowing through the intertubular space and the reactants inside variously positioned catalytic tubes. The influence of process parameters as well as the effect of concurrent and counter-current flow configurations on the operational characteristics of the industrial reactor is examined by means of numerical simulation.
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