A digital controller is used to control the pressure in a tank by adjusting a purge stream. The control valve is air-to-open, and the process model has been identified as
G= G_{v}G_{p}G_{m}= \frac {-20e^{-s}}{5s+1}
The gain is dimensionless, and the time constant and time delay are in minutes. The sampling period is Δt=1 min.
Compare the closed-loop performance of a discrete PI controller using the ITAE (disturbance) tuning rules in Table below. Approximate the sampler and ZOH by a time delay equal to Δt/2 in the model for the ITAE controller calculation. Use Simulink to check the effect of sampling period for different controllers, with Δt=0.05, 0.25, 0.5, and 1.0 min.
Type of Input | Type of Controller | Mode | A | B |
Disturbance | PI | P | 0.859 | −0.977 |
I | 0.674 | −0.680 | ||
Disturbance | PID | P | 1.357 | −0.947 |
I | 0.842 | −0.738 | ||
D | 0.381 | 0.995 | ||
Set point | PI | P | 0.586 | −0.916 |
I | 1.03 | −0.165 | ||
Set point | PID | P | 0.965 | −0.85 |
I | 0.796 | −0.1465 | ||
D | 0.308 | 0.929 |