Robust I-PD Controller Design with Case Studies on Boiler Steam Drum and Bioreactor

Integral-proportional-derivative (I-PD) is more effective than PID controller as it provides dual-loop advantage while retaining the same number of tunable parameters. In I-PD controller, Integral action is employed on the error signal whereas PD mode is employed in the inner feedback loop. However, the studies pertaining to I-PD are not unified for unstable and integrating processes with inverse response. Routh criteria augmented with maximum sensitivity (M S ) specification is used to design PD controller. The adjustable parameter (K P ) of the innerloop and integral gain (K I ) are decided from two plots: K P vs M S of inner-loop (M SS ) and K I vs M S of outer-loop (M SP ). Guidelines for choosing K P and K I from the aforementioned plots are also provided. Simulation studies are conducted on models of boiler steam drum and bioreactor that exhibit inverse response behavior. Qualitative and quantitative performance comparison is carried out with some recently reported works.