Enter Ku and Tu to compute Kp, Ki, Kd, then run the live simulation below.
Kp, Ki, Kd)| Controller | Kp |
Ki |
Kd |
Notes |
|---|---|---|---|---|
| P | 0.50 Ku |
0 |
0 |
Proportional only |
| PI | 0.45 Ku |
0.54 Ku / Tu |
0 |
From Ti=Tu/1.2 and Ki=Kp/Ti |
| PID | 0.60 Ku |
1.20 Ku / Tu |
0.075 Ku Tu |
From Ti=Tu/2, Td=Tu/8 |
Units: Ki is 1/time, Kd is time. Controller form: u(t)=Kpe + Ki∫e\,dt + Kd de/dt.
Plant model: first-order dy/dt = ( -y + K·u ) / τ. Derivative on measurement; simple anti-windup via integral clamping when saturated.