Processes that exhibit dynamic behaviors of inverse response and time delay increase the
difficulty of control system design. This paper presents the design concepts that lead to …

This communication addresses the robust tuning of a One-Degree-Of-Freedom (1DOF) PID
controller for both acceptable load disturbance attenuation (Regulator mode) and setpoint …

In this work, optimal tuning rules for PI/PID controllers for stable and integrating first-order
inverse response processes are reported. Integral performance criteria (ISTE, IST 2 E and …

This work addresses a set of tuning rules for PID controllers based on Internal Model Control
(IMC) for inverse-response second-order systems with dead time. The transfer function, and …

Nonminimum-phase (NMP) processes are frequently encountered in chemical plants, where
the presence of right half-plane zeros and time delays often imposes limitations on the …

This paper aims to examine the efficacy of the Internal Model Control Proportional-Integral-
Derivative (IMC-PID) controller with a dead time compensator using two different filters. The …

In this paper new tuning rules for Proportional Integral Derivative (PID) are presented, which
are based on Internal Model Control (IMC). This set of equations minimizes the performance …

This communication addresses the set-point robust proportional-integrative-derivative (PID)
tuning for stable first order plus time delay systems from a general min− max model …

The PID controller is the most common option in the realm of control applications and is
dominant in the process control industry. Among the related analytical methods, Internal …

ABSTRACT A two-degree-of-freedom (2-DOF) control method with parallel control structure
(PCS) is proposed for inverse response process plus time delay. The parallel control …