This paper presents a method of interactive or real-time predictive control which can be implemented without a stored program computer. By restricting the process dy namic model to a second-order-plus-dead-time format, a configuration which is satisfactory for many chemical or petroleum processing systems, a time-optimal controller can be built entirely on a small analog/hybrid computer. For set-point changes, the controller utilizes an analog model of the process to search out the predicted optimum input switching sequence and continuously maintains the process on the time-optimal trajectory. Because of the predictive nature of the method there is no necessity to include the time-delay term in the high-speed model; the predicted switches in the process input are simply ad vanced in time by the amount of the time-delay.
[1]
R. Hannen,et al.
An application of an analog computer to solve the two-point boundary-value problem for a fourth-order optimal control problem
,
1967,
IEEE Transactions on Automatic Control.
[2]
J. H. Eaton.
An iterative solution to time-optimal control*
,
1962
.
[3]
L. B. Koppel,et al.
Time-Optimum Control of Chemical Processes for Set-Point Changes
,
1967
.
[4]
L. B. Koppel,et al.
Feedback Time-Optimum Process Controllers
,
1968
.
[5]
L. B. Koppel,et al.
Time Optimum Control of Second-Order Overdamped Systems with Transportation Lag
,
1965
.
[6]
L. Neustadt.
Synthesizing time optimal control systems
,
1960
.