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Abstract.
A systematic procedure for control structure selection is applied to
the evaporation process of Newell and Lee (1989). First, promising
sets of controlled variables are selected, based on steady-state
economic criteria. The objective is to nd sets of controlled variables
which with constant setpoints keep the process close to the economic
optimum ("self-optimizing control") in face of disturbances and
implementation errors. Second, stabilization and controllability
analysis is performed for the most promising sets of economic
controlled variables.