New differential equations are derived for optimal control of a consecutive
reaction system in a batch reactor. These equations can be solved easily w
ith a one-dimensional optimum search technique in terms of the initial conc
entrations of each component. The computations are readily carried out on-l
ine in real time, and the optimal temperature profile can be calculated at
each time-step based on the current values of the states. Optimization is c
onsidered in terms of the temperature, but also in terms of an operation va
riable. For a consecutive reaction system, the optimal equations are formul
ated and optimal profiles are numerically calculated.