Title :
Simulation Tests of Multidelay Observer-Based Compensation Including Feedforward Decoupling
Author_Institution :
Chemical Engineering Department, Texas A & M University, College Station, Texas
Abstract :
Multidelay compensators are considered with dynamic decoupling. Response results are shown for tests of multidelay predictor control of a simulated (2Ã2)-interactive process of first order lags with deadtime. The process model originated in the literature as a dynamic model for a binary distillation column. The set-point response results confirm that very good decoupling is achieved under ideal conditions. Such conditions are defined when the model is a perfect match of the process. Also, load response results are shown for cases with and without process parameter changes. For these cases, response comparisons are made between the Smith predictor method and an "observer-based" scheme which incorporates additional controllers applied to the model. Interaction in the disturbance feedback path appears to be beneficial for the cases tested.
Keywords :
Chemical engineering; Delay; Distillation equipment; Feeds; Open loop systems; Pi control; Predictive models; Proportional control; Steady-state; Testing;
Conference_Titel :
American Control Conference, 1983
Conference_Location :
San Francisco, CA, USA