AIChE Symposium Series, Volume 93, Issue 316American Institute of Chemical Engineers, 1997 - Chemical engineering |
From inside the book
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Page 51
... Model Prediction Disturbances Valve Leading ( % ) 100 90 20- 10- Nonlinear Optimizer Setpoint 0 . 200 400 600 Time ... process control perspective , the process is a 3 x 3 process with 4 disturbances ; this process dimen- sionality is ...
... Model Prediction Disturbances Valve Leading ( % ) 100 90 20- 10- Nonlinear Optimizer Setpoint 0 . 200 400 600 Time ... process control perspective , the process is a 3 x 3 process with 4 disturbances ; this process dimen- sionality is ...
Page 98
... Process Analytical Chemistry ( CPAC ) where a graduate course ( Chemistry 525 : Process Analytical Chemistry ) has ... model be available that , hopefully , describes the process being controlled . Process models can be classified as ...
... Process Analytical Chemistry ( CPAC ) where a graduate course ( Chemistry 525 : Process Analytical Chemistry ) has ... model be available that , hopefully , describes the process being controlled . Process models can be classified as ...
Page 284
... processes accurately . Further- more , application of these models for model - based control has led to significant improvement in the control of these processes . Neural network , Model identification , Model - based control ...
... processes accurately . Further- more , application of these models for model - based control has led to significant improvement in the control of these processes . Neural network , Model identification , Model - based control ...
Contents
Industry Assessment | 1 |
Predictive Control | 5 |
Adaptive and Nonlinear Control Fact or Fantasy? | 9 |
Copyright | |
22 other sections not shown
Common terms and phrases
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