AIChE Symposium Series, Volume 93, Issue 316American Institute of Chemical Engineers, 1997 - Chemical engineering |
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Page 50
... increase in the valve C loading . The initial direct response will be a decrease in the first pass inlet tempera- ture ( as a result of increased cold feed by - pass to this stage ) ; but because the increased by - pass through valve C ...
... increase in the valve C loading . The initial direct response will be a decrease in the first pass inlet tempera- ture ( as a result of increased cold feed by - pass to this stage ) ; but because the increased by - pass through valve C ...
Page 73
... increase equipment productivity and yields from raw materials . to increase human productivity through automation . • to control product quality . • to increase operations flexibility . It also identifies two food industry specific ...
... increase equipment productivity and yields from raw materials . to increase human productivity through automation . • to control product quality . • to increase operations flexibility . It also identifies two food industry specific ...
Page 348
... increase when the filter time constant increases . Consistent tunability is necessary for our algorithm to find filter time constants which satisfy interaction specifications , as well as set point response specifications . The ...
... increase when the filter time constant increases . Consistent tunability is necessary for our algorithm to find filter time constants which satisfy interaction specifications , as well as set point response specifications . The ...
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