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In this article we consider a control system modelling a batch reactor in which
three species X, X, X are reacting according to the
scheme X → X → X, each reaction being irreversible. The control is the temperature T of the reactions or the derivative of this
temperature with respect to time. The terminal constraint is to obtain a given concentration of the product X2 at the end of the batch.
The objective of our study is to introduce and to apply all the mathematical tools to compute the time...
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