Simple Tuning formulae are provided for optimal PID controller settings for
unstable first order plus time delay systems. The method is based on minim
ization of integral squared errors (ISE). A method of calculating the set p
oint weighting parameter is proposed to reduce the overshoot for servo prob
lems. The performances of the proposed PID settings are compared with the s
ettings recently proposed by Huang and Chen (1997, 1999) for both the servo
and regulatory problems. The performance of the controller is also evaluat
ed under parameter uncertainty in time delay and separately in process gain
. Tuning formulae are given for PI controller along with the set point weig
hting. The performance of the PI controller is compared with that of Poulin
and Pomerleau (1996). Two simulation studies, one on control of an unstabl
e nonlinear bioreactor and a second on an unstable chemical reactor using t
he proposed PID controller settings, show improved performances both for se
rvo and regulatory problems.