Automation & Control

PID Controller Tuning (Ziegler-Nichols)

Calculate PID controller parameters using the Ziegler-Nichols open-loop method (step response) for industrial process control.

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💡Ziegler-Nichols gives aggressive tuning — fast response but may overshoot 25–30%. For tighter control, multiply Ti by 1.5 and Td by 0.5. For temperature control, use very long Ti (10–30× Tu). Always test in simulation or with reduced output limits first.
Kp = 1.2/a Ti = 2×Tu Td = 0.5×Tu where a = K×Tu/T (from step test)
ƒ Calculation module
Input
Process gain K iRatio of steady-state output change to input (step) change. From step test: K = Δy / Δu.
output/input
Dead time Tu (L) iTransport delay / dead time in seconds. From step response: time from step until output starts to respond.
s
Process time constant T iTime constant in seconds. From step response: time from start of response to 63.2% of final value minus dead time.
s
Controller type iSelect the controller structure. PID is recommended for most industrial processes.
Result
Factor a = K×Tu/T
Proportional gain Kp
Integral time Ti [s]
Derivative time Td [s]
Integral gain Ki (= Kp/Ti) [1/s]
Derivative gain Kd (= Kp×Td) [s]
📊 Global project table — all calculations
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