AIChE Symposium Series, Volume 93, Issue 316American Institute of Chemical Engineers, 1997 - Chemical engineering |
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Page 141
... control is also a power control . Two Accufiber ripple pyrometers have also been installed and will be used as the ... PID controllers with standard set point ramp from 400 ° C to 950 ° C at 50 ° C / s . In contrast , the TI3 system ...
... control is also a power control . Two Accufiber ripple pyrometers have also been installed and will be used as the ... PID controllers with standard set point ramp from 400 ° C to 950 ° C at 50 ° C / s . In contrast , the TI3 system ...
Page 143
... PID control , 35 ° C / s ramp , with open loop set point anticipation at the " corner . " 4 Temp . Diff . , stdev , deg C Figure 10. Gain - scheduled PID controllers with 40 ° C / s ramp , set point lead limited to 10 ° C . In order to ...
... PID control , 35 ° C / s ramp , with open loop set point anticipation at the " corner . " 4 Temp . Diff . , stdev , deg C Figure 10. Gain - scheduled PID controllers with 40 ° C / s ramp , set point lead limited to 10 ° C . In order to ...
Page 254
... PID controllers have been very successful in the marketplace . This suggests that adaptive MPC controllers may emerge for SISO loops as adaptive PID technology is generalized to handle more difficult dynamics . Robust Stability of MPC ...
... PID controllers have been very successful in the marketplace . This suggests that adaptive MPC controllers may emerge for SISO loops as adaptive PID technology is generalized to handle more difficult dynamics . Robust Stability of MPC ...
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