Abstract
The paper concerns automation of a chemical engineering experiment for oxidative dehydration of n- butenes over commercial catalysts. The automation of physical and chemical data processing by means of a computer has been discussed. Theoretical optimization of the process has been carried out to select the best contact apparatus. The results are given for the identification of a mathematical model (both static and dynamic) of a multiple-bed adiabatic reactor with intermediate heat exchange which made it possible to develop a computerized automatic control system.
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