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increasing<br />

Industrial Automation<br />

PID-Controller: influence of parameters<br />

Rise time Overshoot Settling time Steady-State Error<br />

Kp Decrease Increase Small Change Decrease<br />

Ki Decrease Increase Increase Eliminate<br />

Kd Small Change Decrease Decrease Small Change<br />

Empirical formula of Nichols (1942 !)<br />

1.4<br />

1.2<br />

1<br />

0.8<br />

0.6<br />

0.4<br />

0.2<br />

0<br />

step response (open loop)<br />

delay time constant<br />

gain K<br />

0 1 2 3 4 5 6 7 8 9 10<br />

d ~ 0.2, T= 1.5s<br />

1.2 T<br />

Kp = Ti = 2.0 d Td = 0.5 d (Nf = 10)<br />

K d<br />

34/40 2.2 Continuous plants and regulation

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