AIChE Symposium Series, Volume 93, Issue 316American Institute of Chemical Engineers, 1997 - Chemical engineering |
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Page 287
... reactors including ( a ) a reactor with a classical reaction and a decreasing reactor - jacket overall heat - transfer coefficient , ( b ) a catalytic reactor with catalyst deactivition , and ( c ) a methyl methacrylate batch polymerization ...
... reactors including ( a ) a reactor with a classical reaction and a decreasing reactor - jacket overall heat - transfer coefficient , ( b ) a catalytic reactor with catalyst deactivition , and ( c ) a methyl methacrylate batch polymerization ...
Page 313
... reactor as the first subsystem ; the extractor , the flash drum , and the distillation column as the second subsystem . In the DAU8 mode , three subsystems are produced the reactor as the first subsystem ; the extractor and the flash ...
... reactor as the first subsystem ; the extractor , the flash drum , and the distillation column as the second subsystem . In the DAU8 mode , three subsystems are produced the reactor as the first subsystem ; the extractor and the flash ...
Page 316
... Reactor Temperature Trajectory A common operating procedure is to ramp the batch reactor from an initial charge temperature to a final temperature where it is maintained constant ( isothermal operation ) for most of the batch time , as ...
... Reactor Temperature Trajectory A common operating procedure is to ramp the batch reactor from an initial charge temperature to a final temperature where it is maintained constant ( isothermal operation ) for most of the batch time , as ...
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