AIChE Symposium Series, Volume 93, Issue 316American Institute of Chemical Engineers, 1997 - Chemical engineering |
From inside the book
Results 1-3 of 63
Page 142
... temperature distribution to lie between the temperatures at the center and the edge . The temperature uniformity across the entire wafer can therefore be controlled with only two zones . Recent joint work between the University of Texas ...
... temperature distribution to lie between the temperatures at the center and the edge . The temperature uniformity across the entire wafer can therefore be controlled with only two zones . Recent joint work between the University of Texas ...
Page 316
... 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 shown in ...
... 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 shown in ...
Page 317
... temperature profiles for a 154.7 kg pilot plant reactor . The parameters for this first - order reaction are given in Landau et al . and Bequette ( 1995 ) . The initial and final temperatures are 20 ° C and 90 ° C . The minimum ...
... temperature profiles for a 154.7 kg pilot plant reactor . The parameters for this first - order reaction are given in Landau et al . and Bequette ( 1995 ) . The initial and final temperatures are 20 ° C and 90 ° C . The minimum ...
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