Proportional$-$Integral and Proportional$-$Integral$-$Derivative control

Present separate figures for the PI and PID control stages of the procedure.

Quantify the performance of both controllers. Depending on whether the response is under$-$ or overdamped,

calculate relevant properties of the closed$-$loop response to a change in the setpoint.

Compare automatic control with manual control: based on a quantitative comparison, determine which option was better for a change in the setpoint from $5$ to $6V.$ Discuss:

$-$Is the derivative term useful for this system?

Are the closed loop responses for the controllers consistent with theoretical expectations for the process model determined earlier?

$-$Would you suggest any changes to the PI or PID controller tunings to improve performance?

Proportional$-$Integral Control

$q,$

Focus