This work presents a comparative analysis of PID, DTC and MPC strategies when used to
control SISO processes with dead time considering characteristics commonly found in …

In conventional single feedback control, the corrective action for disturbances does not
begin until the controlled variable deviates from the set point. In this case, a cascade control …

Industrial processes often involve a long time delay, which adversely affects the stability of
closed-loop control systems. The traditional Smith Predictor (SP) is a model-based controller …

In this work, a recently reported two degree of freedom control structure namely the Parallel
Control Structure (PCS) is modified to achieve improved control performance for unstable …

This study addresses an experimental investigation of a novel modified Smith Predictor (SP)
based fractional fuzzy gain-scheduled control scheme in control of a time-delayed thermal …

It is well known that PD controller, though yields good servo response, fails to provide
satisfactory regulatory response for Integrating Plus Time-Delay (IPTD) processes. On the …

Abstract Proportional-Integral-Derivative (PID) controllers are still extensively used in
industrial systems. In the literature, many publications can be found considering PID …

Cascade control is an alternative to conventional single feedback control to improve the
performance of a control system, particularly in the presence of disturbances. However, to …

Tuning formulas for PI/PID controllers for integrating processes are presented in this paper.
The controller parameters are obtained by minimizing various integral performance index …

In this paper, a modified Smith predictor using three controllers, namely, stabilising (Gc), set-
point tracking (Gc 1), and load disturbance rejection (Gc 2) controllers is proposed for …