This is the example studied in [14, Section 3.1].
The example studied is a middle-vessel batch distillation system for separating a ternary mixture.
For the example studied the separation could be improved considerably performing four cycles.
The example studied clearly demonstrated the significant influence of structural nonlinearities on the buffeting response, and reaffirmed the overall versatility of the time domain analysis approach.
In the example studied, the hydrodealkylation of toluene, both the economic and environmental results point towards the alternative of recycling diphenyl to extinction, which is a form of pollution prevention by source reduction.
It is expected that this behaviour occurs wherever solids inertia is important, such as with strong large aggregate formation (the example studied here was wood pulp) or with high solids loading (milled coal suspension).
By employing results of the example studied in the previous section, computational comparisons of the ARD and the ARR with the classical one are made in terms of additions and multiplications.
The example studied here is the optimal temperature control of a stirred-tank catalytic reactor in which the time constant of the catalyst decay is appreciable compared to the mean residence time.
