GM PM −1 ωφ ωg

1. Errata of ”Process Control - Theory and applications”. Do not hesitate to contact the author for any comment or information: [email protected].
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1 Errata of ”Process Control - Theory and applications” Do not hesitate to contact the author for any comment or information: [email protected]

Page 43: δ(t) = 0 ∀t 6= 0 δ(0) = +∞ R +∞ δ(t)dt = 1 −∞ Z

+∞

f (t)δ(t − t0 )dt = f (t0 ) −∞

Page 215: the black circles were lightly displaced as shows the corrected figure . 2

1/GM

 -

1.5

1

ωφ @ −1@@ Rr

Im

0.5

0

6 -0.5



r

PM

ωg

-1

-1.5

-2 -2

-1.5

-1

-0.5

0 Re

0.5

1

1.5

Equation (8.48)  ∂Yi ∂Uj U =0,k6=j k λij =  ∂Yi ∂Uj Y =0,l6=i 

l

Equation (13.78) S(q)

= q −h 1

s R(q) = K q − 1 + T τI T (q) = R(q)

i

Equation (14.158) d(tc +

p p 2|A| − t2c ) = 0 =⇒ tc = |A| dtc

2

2 Equation (14.295) S = F T [S − S G (GT S G + R)−1 GT S] F + M Q M Equation (15.30) yˆ(t + 1) = 1.97y(t) − 0.97y(t − 1) + 1.2∆u(t) + 0.58∆u(t − 1) yˆ(t + 2) = 2.9109y(t) − 1.9109y(t − 1) +1.2∆u(t + 1) + 2.944∆u(t) + 1.1426∆u(t − 1) yˆ(t + 3) = 3.8236y(t) − 2.8236y(t − 1) +1.2∆u(t + 2) + 2.944∆u(t + 1) + 4.6357∆u(t) + 1.6883∆u(t − 1)

Equation (15.32) yˆ(t + 1|t) = 0.58∆u(t − 1) + 1.97y(t) − 0.97y(t − 1) yˆ(t + 2|t) = 1.1426∆u(t − 1) + 2.9109y(t) − 1.9109y(t − 1) yˆ(t + 3|t) = 1.6883∆u(t − 1) + 3.8236y(t) − 2.8236y(t − 1) Equation (15.35) ∆u(t)

= 0.5181[r(t + 1) − yˆ(t + 1|t)] + 0.1823[r(t + 2) − yˆ(t + 2|t)] −0.0435[r(t + 3) − yˆ(t + 3|t)] = −0.4354∆u(t − 1) − 1.385y(t) + 0.7281y(t − 1) +0.5181r(t + 1) + 0.1823r(t + 2) − 0.0435r(t + 3)

Equation (17.147) u=

v − Lrf h(x) − β1 Lr−1 h(x) − . . . − βr−1 Lf h(x) − βr h(x) f Lg Lr−1 h(x) f