## AIChE Symposium Series, Volume 93, Issue 316American Institute of Chemical Engineers, 1997 - Chemical engineering |

### From inside the book

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Page 26

If a nonlinearity measure indicates that a system is

and synthesis methods will probably suffice . ( Exceptions include the case where

a nonlinear performance objective is sought . ) If considerable nonlinearity is ...

If a nonlinearity measure indicates that a system is

**linear**, then**linear**analysisand synthesis methods will probably suffice . ( Exceptions include the case where

a nonlinear performance objective is sought . ) If considerable nonlinearity is ...

Page 207

This is indeed true since ( 2k – Iklk ) is an exponentially converging sequence

due to the assumption of a stable

continuous . Hence , the stability results established for the state feedback case

remain ...

This is indeed true since ( 2k – Iklk ) is an exponentially converging sequence

due to the assumption of a stable

**linear**observer , and f ( xk ) is Lipschitzcontinuous . Hence , the stability results established for the state feedback case

remain ...

Page 219

controlled is

E are specified by

which efficient software exists . But optimality does not imply stability ; the version

...

controlled is

**linear**. When the system is**linear**, the cost quadratic , the sets N andE are specified by

**linear**inequalities , FHP reduces to a quadratic program forwhich efficient software exists . But optimality does not imply stability ; the version

...

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### Contents

Industry Assessment | 1 |

Predictive Control | 5 |

Adaptive and Nonlinear Control Fact or Fantasy? | 9 |

Copyright | |

23 other sections not shown

### Common terms and phrases

achieve adaptive control addition algorithm analysis applications approach associated batch behavior bounded changes chemical closed complex Conference consider constant constraints continuous control system defined described determine developed direction discrete discussed disturbance dynamic effective engineering equations error estimation example exist factor Figure function future given horizon hybrid systems identification IEEE implementation important improved increase industrial initial input issues limited linear loop machine manufacturing matrix measurement methods monitoring networks nonlinear nonlinear control objective obtained on-line operating optimization output parameter performance plant possible practice present problem process control programming properties Pulp reactor represent respect response robust scheduling set point setpoint shown shows significant simulation solution solved specifications stability step structure techniques temperature theory tion transition trend uncertainty variables vector wafer