AIChE Symposium Series, Volume 93, Issue 316American Institute of Chemical Engineers, 1997 - Chemical engineering |
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Page 84
... Given the importance of the task , it is surprising that very little attention has been given to this area by the research community with respect to developing tools and methodologies that are effective in both meeting the goals in this ...
... Given the importance of the task , it is surprising that very little attention has been given to this area by the research community with respect to developing tools and methodologies that are effective in both meeting the goals in this ...
Page 88
... given by ( 7 ) . It can be shown that ( Box and Jenkins , 1976 ) 2 1 of 2 o 1 - λ a 2 ( 12 ) and that Omv is equal to o , with f = 0 . Hence , a bound limit for CLP in this example would be given by CLP = 1 - λ2 ( 13 ) If the estimated ...
... given by ( 7 ) . It can be shown that ( Box and Jenkins , 1976 ) 2 1 of 2 o 1 - λ a 2 ( 12 ) and that Omv is equal to o , with f = 0 . Hence , a bound limit for CLP in this example would be given by CLP = 1 - λ2 ( 13 ) If the estimated ...
Page 111
... given . temperature and pressure , the solution corresponding to the global minimum of Gibbs free energy of the overall system is thermodynamically stable ( Baker et al . , 1982 ) . Although this approach will be adopted for the ...
... given . temperature and pressure , the solution corresponding to the global minimum of Gibbs free energy of the overall system is thermodynamically stable ( Baker et al . , 1982 ) . Although this approach will be adopted for the ...
Contents
Industry Assessment | 1 |
Predictive Control | 5 |
Adaptive and Nonlinear Control Fact or Fantasy? | 9 |
Copyright | |
22 other sections not shown
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adaptive control AIChE algorithm analysis analytical applications approach auto-correlation batch behavior changes Chem Chemical Engineering chemical process chip closed-loop constraints continuous control problems control system controller design defined developed discrete disturbance dynamic equations estimation example feedback control Figure finite Grafcet horizon hybrid systems identification IEEE implementation input linear control loop manufacturing matrix measured methods model predictive control monitoring Morari multivariable neural networks nonlinear control nonlinear model nonlinear systems on-line operating optimal control output error paper machine parameters Petri net PID controllers plant Proc process control process model programming Pulp and Paper quadratic quadratic program reactor robust robust control scheduling sensors sequence set point significant simulation snack food solution specifications stability step structure synthesis TAPPI Press techniques temperature theory tion trajectory transfer function trend trol uncertainty valve variables variance vector wafer