Real-time self tuning control was implemented on a coupled tank pilot plant using a microcomputer. Three different algorithms namely, generalized minimum variance, pole placement and extended horizon were used. The performances of these controllers are evaluated for set-point tracking experiments and load disturbance experiments
The set of two interacting tanks in the Chemical Engineering Lab is a prototype process that can be ...
The set of two interacting tanks in the Chemical Engineering Lab is a prototype process that can be ...
A digital predictor-based self-tuning control with constraints for the pressure plants, which is abl...
A self-tuning controller which automatically assigns weightings to control and set-point following i...
A brief overview of adaptive control methods relating to the design of self-tuning proportional-inte...
This paper deals with a one possibility of improvement of a self-tuning controller reliability and p...
The research reported in this thesis develops strategies for applying self-tuning control theory to ...
In this paper the design and the implementation of a self-tuning PID controller is presented. The pr...
A simple parameter adaptive controller design methodology is introduced in which steady-state servo ...
Extended horizon and k-incremental self-tuning controllers were implemented using a microcomputer on...
The paper gives a review of pole-placement design for systems with known parameters, then focuses en...
Parameter estimation of linear Discrete-time systems by linear programming using two error criteria,...
Feedback control is an essential part of chemical engineering. Over the years, new and better techno...
This contribution presents a usage of Self-Tuning Controllers Simulink Library (STCSL) for control o...
The paper presents an improved recursive instrumental variable (RIV) estimation method known as the ...
The set of two interacting tanks in the Chemical Engineering Lab is a prototype process that can be ...
The set of two interacting tanks in the Chemical Engineering Lab is a prototype process that can be ...
A digital predictor-based self-tuning control with constraints for the pressure plants, which is abl...
A self-tuning controller which automatically assigns weightings to control and set-point following i...
A brief overview of adaptive control methods relating to the design of self-tuning proportional-inte...
This paper deals with a one possibility of improvement of a self-tuning controller reliability and p...
The research reported in this thesis develops strategies for applying self-tuning control theory to ...
In this paper the design and the implementation of a self-tuning PID controller is presented. The pr...
A simple parameter adaptive controller design methodology is introduced in which steady-state servo ...
Extended horizon and k-incremental self-tuning controllers were implemented using a microcomputer on...
The paper gives a review of pole-placement design for systems with known parameters, then focuses en...
Parameter estimation of linear Discrete-time systems by linear programming using two error criteria,...
Feedback control is an essential part of chemical engineering. Over the years, new and better techno...
This contribution presents a usage of Self-Tuning Controllers Simulink Library (STCSL) for control o...
The paper presents an improved recursive instrumental variable (RIV) estimation method known as the ...
The set of two interacting tanks in the Chemical Engineering Lab is a prototype process that can be ...
The set of two interacting tanks in the Chemical Engineering Lab is a prototype process that can be ...
A digital predictor-based self-tuning control with constraints for the pressure plants, which is abl...