In this paper we present simple and effective tuning formulas for PID controllers with guaranteed phase margin when they are applied to first-order plus dead-time processes. We have discovered that for our controllers and some controllers suggested by our researchers, the integral gain alone could be used for the purpose of achieving set-point response and disturbance rejection tradeoff. The study has also shown that, while the tradeoff between set-point response and disturbance rejection is limited by normalised dead-time, the set-point response performance is solely limited by the dead-time of the FOPDT precess
Abstract-This paper derives proportional-integral (PI) control algorithms for first-order plants wit...
In this paper, measurable disturbance compensation techniques are analyzed, focusing the problem on ...
This paper revisites the direct synthesis tuning method of continuous-time low-order controllers, an...
In this paper we present simple and effective tuning formulas for PID controllers with guaranteed ph...
In this paper, we provide a theoretical basis for a modified IMC-PID controller and its associated s...
In this paper, we shall present simple and effective tuning\ud formulas for IMC controllers when the...
This work addresses a set of tuning rules for PID controllers based on Internal Model Control (IMC) ...
This manuscript presents an extension of the IMC-PID tuning method. A higher-order structure is adop...
An open-loop unstable process with dead-time is commonly encountered in process industry. A PID cont...
IMC-PID controllers supply exceptional set point tracking but slow disturbance refutation, because o...
Abstract: PID Controller is used for tuning of three constants (P,I&D).It stabilize the system b...
In the paper we present tuning rules for PI and PID controllers and the first order plus dead time (...
When controlling industrial processes, setpoint tracking and disturbance rejection play an important...
The modulus optimum (MO) criterion can be used for analytical design of the PID controller for linea...
The aim of this paper is to present analytic tuning rules which are as simple as possible and still ...
Abstract-This paper derives proportional-integral (PI) control algorithms for first-order plants wit...
In this paper, measurable disturbance compensation techniques are analyzed, focusing the problem on ...
This paper revisites the direct synthesis tuning method of continuous-time low-order controllers, an...
In this paper we present simple and effective tuning formulas for PID controllers with guaranteed ph...
In this paper, we provide a theoretical basis for a modified IMC-PID controller and its associated s...
In this paper, we shall present simple and effective tuning\ud formulas for IMC controllers when the...
This work addresses a set of tuning rules for PID controllers based on Internal Model Control (IMC) ...
This manuscript presents an extension of the IMC-PID tuning method. A higher-order structure is adop...
An open-loop unstable process with dead-time is commonly encountered in process industry. A PID cont...
IMC-PID controllers supply exceptional set point tracking but slow disturbance refutation, because o...
Abstract: PID Controller is used for tuning of three constants (P,I&D).It stabilize the system b...
In the paper we present tuning rules for PI and PID controllers and the first order plus dead time (...
When controlling industrial processes, setpoint tracking and disturbance rejection play an important...
The modulus optimum (MO) criterion can be used for analytical design of the PID controller for linea...
The aim of this paper is to present analytic tuning rules which are as simple as possible and still ...
Abstract-This paper derives proportional-integral (PI) control algorithms for first-order plants wit...
In this paper, measurable disturbance compensation techniques are analyzed, focusing the problem on ...
This paper revisites the direct synthesis tuning method of continuous-time low-order controllers, an...