New PI-PD Controller Design Strategy for Industrial Unstable and Integrating Processes with Dead Time and Inverse Response

Industrial processes of unstable/integrating nature having a dead time and inverse response characteristics are challenging to control. For controlling such processes, double-loop control structures have proven to be more efficient than conventional PID controllers in a unity feedback configuration. Therefore, a new design method to obtain PI-PD controller settings is proposed for a set of unstable/integrating plant models with dead time and inverse response. The stabilizing proportional-derivative (PD) controller is designed using maximum sensitivity considerations and Routh-Hurwitz stability criteria. The PI controller settings are obtained by comparing the first and second derivatives of expected and actual closed-loop transfer functions about the origin of the s-plane. Adjustable parameters of the inner and outer loops are selected such that the desired value of maximum sensitivity is achieved. Simulation studies are conducted on some benchmark linear and nonlinear plant models used in literature. Robustness of the proposed design is analyzed with perturbed plant models, and quantitative performance measures are computed. It is found that the proposed design yields enhanced and robust closed-loop response than some contemporary works.

Automated summary

A new design method is proposed to obtain PI-PD controller settings for a set of unstable/integrating plant models with dead time and inverse response, utilizing maximum sensitivity considerations and stability criteria. Simulation studies on benchmark plant models show that the proposed design yields enhanced and robust closed-loop response compared to contemporary works. The PD controller is designed based on stability considerations, while the PI controller settings are obtained by comparing derivatives of the expected and actual closed-loop transfer functions.