## American Institute of Chemical Engineers Symposium SeriesAmerican Institute of Chemical Engineers, 1997 - Chemical engineering |

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Page 36

Even though the

computation of the controller involves the

differential equation/inequality (69). A global analytical

feasible ...

Even though the

**solution**is nicely characterized by (68) and (69) the actualcomputation of the controller involves the

**solution**of the nonlinear partialdifferential equation/inequality (69). A global analytical

**solution**is of course notfeasible ...

Page 222

But

arise, let Xp D Xoo denote the set of states which may be steered to the set (3M(x

) along an admissible trajectory. Whereas XT and Xoo , defined above, are ...

But

**solution**of P(x, t) cannot be guaranteed for every x S X. To see why this mayarise, let Xp D Xoo denote the set of states which may be steered to the set (3M(x

) along an admissible trajectory. Whereas XT and Xoo , defined above, are ...

Page 334

Soft constrained MPC: oc-norm

process described by 1.4 -0.61 0.084 -0.0036 A = ,B with the output given by yt = [

0.1 1 -2 1.48]it. There is no input constraint and the state constraint is defined as \

yt\ ...

Soft constrained MPC: oc-norm

**solution**Illustrative Example We consider theprocess described by 1.4 -0.61 0.084 -0.0036 A = ,B with the output given by yt = [

0.1 1 -2 1.48]it. There is no input constraint and the state constraint is defined as \

yt\ ...

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### Contents

Control Technology Challenges for the Future | 1 |

Predictive Control | 5 |

Adaptive and Nonlinear Control Fact or Fantasy? | 9 |

Copyright | |

22 other sections not shown

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