Book ChapterDOI
An Overview of Tuning Rules for the PI and PID Continuous-Time Control of Time-Delayed Single-Input, Single-Output (SISO) Processes
Aidan O'Dwyer
- pp 3-44
TLDR
This chapter will provide an outline of tuning rules for continuous-time PI and PID control of time-delayed single-input, single-output (SISO) processes.Abstract:
The ability of PI and PID controllers to compensate many practical processes has led to their wide acceptance in industrial applications The requirement to choose two or three controller parameters is most easily done using tuning rules Starting with a general discussion of industrial practice, the chapter will provide an outline of tuning rules for continuous-time PI and PID control of time-delayed single-input, single-output (SISO) processesread more
Citations
More filters
Robust and optimal tuning of PI and PID Controllers
TL;DR: In this paper, a general controller evaluation method based on three performance and robustness criteria is presented, which can be used to compare controllers of different structures, but also as a design method to find the optimal parameter setting for a controller of given structure.
Journal ArticleDOI
Neural Network Control System of UAV Altitude Dynamics and Its Comparison with the PID Control System
TL;DR: A comparative method to assess the performance of artificial neural network’s direct inverse control (DIC-ANN) with the PID control system found better achievement in the altitude dynamics was attained by the Dic-ANN compared to PID control method.
Journal ArticleDOI
PID Controller Tuning via Dominant Pole Placement in Comparison with Ziegler-Nichols Tuning
Jaromír Fišer,Pavel Zítek +1 more
TL;DR: The dominant three-pole placement approach to the PID tuning is designed for oscillatory, aperiodic and integrating plants of the third-order and is demonstrated overcoming well-known Ziegler-Nichols (Z-N) tuning rule.
Journal ArticleDOI
PID Control With Higher Order Derivative Degrees for IPDT Plant Models
TL;DR: The main new finding is that HO-PID control enables faster transients by simultaneously reducing the negative effects of measurement noise and increasing the closed-loop robustness.
References
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Journal ArticleDOI
Distillate Cascade Composition Control Using a Two-Temperature Measurement Secondary Component
TL;DR: In this paper, the authors proposed a two-temperature cascade controller for distillate cascade control, where a primary component is driven by the distillation measurement and a secondary component is controlled by two temperature measurements located at the most sensitive trays of the stripping and rectifying sections.
Proceedings ArticleDOI
On the consideration of FOPTD and SOPTD responses ab bounds of PI tuning
F. Mesa,J.L. Lonano,L. Marin +2 more
TL;DR: In this paper, a model-based approach is presented to tune a PI controller for first-order plus time delay (FOPTD) plants using SOPTD and FOPTD responses.
Simple Tuning Rules of PID Controllers for Integrator/Dead time Processes
TL;DR: In this paper, simple rules for tuning PID controllers for integrator/dead time processes are derived by the optimization of a discrete-time error integral criterion called the switch time weighted summation of squared error (SWSSE) criterion.
Proceedings ArticleDOI
Advanced PID tuning for integrating processes with a new robustness specification
Jianghua Xu,Huihe Shao +1 more
TL;DR: A simple PID controller tuning method for integrating processes with time delay to meet a new robust specification can obtain a loop transfer function with the real part close to -0.5, which guarantees both robustness and performance.