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

### From inside the book

Results 1-3 of 85

Page 51

Identification

distribution network model ; a heat transfer model for the four heat exchangers ;

and a kinetic model for the four fixed - bed catalytic reactors . Each contributing ...

Identification

**input**sequence for Valve A loading . Figure 2 . The control strategy .distribution network model ; a heat transfer model for the four heat exchangers ;

and a kinetic model for the four fixed - bed catalytic reactors . Each contributing ...

Page 239

Including all the required trade - offs in a single objective function means that

relative weights have to be assigned to the value of output setpoint violations ,

output soft constraint violations ,

.

Including all the required trade - offs in a single objective function means that

relative weights have to be assigned to the value of output setpoint violations ,

output soft constraint violations ,

**inputs**moves , and optimal**input**target violations.

Page 247

IH , OS Output Traj | S , Z Output Horizo FH

SMC - Idcom IR , TF L , S . I CD , ID RCV Q [ O ] . . . Q [ I ] , R IH , OH , OS , R Q [ I ,

O ] IHOS S . Z . RT , F Honeywell IAC RMPCT SR , TF , ARX L , S , I CD , ID SVT

Q ...

IH , OS Output Traj | S , Z Output Horizo FH

**Input**Param10 N MM Setpoint IncSMC - Idcom IR , TF L , S . I CD , ID RCV Q [ O ] . . . Q [ I ] , R IH , OH , OS , R Q [ I ,

O ] IHOS S . Z . RT , F Honeywell IAC RMPCT SR , TF , ARX L , S , I CD , ID SVT

Q ...

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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