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time domain<br />

Laplace domain<br />

Industrial Automation<br />

PID controller: Equations<br />

t ⎛ 1<br />

de(<br />

t)<br />

⎞<br />

= K ⎜<br />

⎟<br />

⎜<br />

+ ∫ p e(<br />

t)<br />

e(<br />

τ ) dτ<br />

) + T<br />

⎟<br />

⎝ Ti<br />

dt<br />

t0<br />

⎠<br />

m d<br />

F(<br />

p)<br />

=<br />

K<br />

p<br />

⎛<br />

⎜<br />

⎜1+<br />

⎜<br />

⎜<br />

⎝<br />

1<br />

sT<br />

+<br />

( 1<br />

Td<br />

s<br />

Nf<br />

+<br />

T<br />

Real differentiators include a filtering<br />

i<br />

d<br />

s)<br />

31/40 2.2 Continuous plants and regulation<br />

⎞<br />

⎟<br />

⎟<br />

⎟<br />

⎟<br />

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