Abstract
The optimal control of a batch reactor often involves that the reaction should be conducted adiabatically at first. By taking observations during the adiabatic part of the reaction information about the kinetics of the reaction can be obtained and later used to program the heat control of the reactor to achieve the desired conversion in the minimum time. In this first part a general perspective of the whole scheme is given and the peculiar problems of determining the unknown kinetics are discussed and illustrated by extensive simulation calculations.
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