Chemical reactors, heat exchangers, level-loops, and distillation columns are commonly encountered in the chemical process industry, and these are having a significant role in the …
This paper investigates a repositioned inner-loop stabilized internal model control technique for demanding inverse response industrial processes and bioreactors with …
The coupled systems with numerous interdependent variables pose considerable control and stability issues in commercial chemical processes. These systems exhibit complex …
A dual-degree of freedom (dual-DOF) propor-tional-integral proportional-derivative (PI-PD) controller is developed for integrating-type chemical processes with delay. The interior-loop …
While terminal sliding mode control provides faster responses and reduces steady-state errors, it has the disadvantage of having singularity and chattering issues. This study …
This study proposes a direct synthesis-based two-degree-of-freedom (2-DOF) controller for various types of integrating processes with time delays. This 2-DOF controller includes a …
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 …
E Cokmez, I Kaya - International Journal of Systems Science, 2024 - Taylor & Francis
Disturbance rejection has always been a major phenomenon in control theory. Disturbances that arise in control of unstable or integrating unstable processes with time delay present …
HA ElDemery, HM Hasanien, M Alharbi, C Sun… - Ain Shams Engineering …, 2024 - Elsevier
The optimal design of the proportional-integral (PI) controller using the walrus optimization algorithm (WOA) with the aim to enhance the dynamic performance of a grid-connected …