Abstract
Abstract The paper concerns integrated computing system with distributed data bases of laboratory experiment for automation of research, modeling and optimal design of chemical engineering processes. The computation methods of kinetic experiment for establishing the probable mechanism and composing kinetic models of complex reaction has been discussed The selection of accurate, single-valued and complete kinetic models allows to find theoretically optimum temperature distribution for substantiation of reactor type. Identification procedures of the mathematical models in static and dynamics of catalytic reactors have been suggested and the calculations of concentration and temperature fields were made on these bases stability conditions of stationary slates and transient processes have been determined.The packages of programmed modules permitting the realization of algorithms modeling and optimum calculation of catalytic processes in the framework of CAD in terms data base have been developed. The results that obtained from the mathematical models and optimum parameters and control design of new oxidation-dchydrogenation processes using this systems will be presented in the conclusion.
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