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fundamentals of engineering supplied-reference handbook - Ventech!

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An alternative form commonly employed in the chemical<br />

process industry is<br />

Y() s K<br />

= , where<br />

Rs () 2 2<br />

τ s + 2ζτ s+<br />

1<br />

K = steady state gain,<br />

ζ = the damping ratio,<br />

τ = the inverse natural frequency.<br />

Root Locus<br />

The root locus is the locus <strong>of</strong> points in the complex s-plane<br />

satisfying<br />

( s−z1)( s−z2) �(<br />

s−zm) 1+ K = 0 m≤n ( s− p1)( s− p2) �(<br />

s− pn)<br />

as K is varied. The pi and zj are the open-loop poles and<br />

zeros, respectively. When K is increased from zero the locus<br />

has the following properties.<br />

1. Locus branches exist on the real axis to the left <strong>of</strong> an<br />

odd number <strong>of</strong> open-loop poles and/or zeros<br />

2. The locus originates at the open-loop poles p1,…, pn and<br />

terminates at the zeros z1,…, zm. If m < n then (n – m)<br />

branches terminate at infinity at asymptote angles<br />

(2k + 1)180°<br />

α= k = 0, ± 1, ± 2, ± 3, �<br />

n−m with the real axis.<br />

3. The intersection <strong>of</strong> the real axis with the asymptotes is<br />

called the asymptote centroid and is given by<br />

σ =<br />

A<br />

n m<br />

∑ pi − ∑ zi<br />

i= 1 i=<br />

1<br />

Re( ) Re( )<br />

n−m 4. If the locus crosses the imaginary (ω) axis the values <strong>of</strong><br />

K and ω are given by letting s = jω in the defining<br />

equation.<br />

State-Variable Control-System Models<br />

One common state-variable model for dynamic systems has<br />

the form<br />

x�<br />

(t) = Ax(t) + Bu(t) (state equation)<br />

y(t) = Cx(t) + Du(t) (output equation)<br />

where<br />

x(t)<br />

= N by 1 state vector (N state variables),<br />

u(t) = R by 1 input vector (R inputs),<br />

y(t) = M by 1 output vector (M outputs),<br />

A = system matrix,<br />

B = input distribution matrix,<br />

C = output matrix, and<br />

D = feed-through matrix.<br />

90<br />

MEASUREMENT AND CONTROLS (continued)<br />

The orders <strong>of</strong> the matrices are defined via variable<br />

definitions.<br />

State-variable models automatically handle multiple inputs<br />

and multiple outputs. Furthermore, state-variable models<br />

can be formulated for open-loop system components or the<br />

complete closed-loop system.<br />

The Laplace transform <strong>of</strong> the time-invariant state equation is<br />

sX(s) – x(0) = AX(s) + BU(s)<br />

from which<br />

X(s) = Φ(s) x(0) + Φ(s) BU(s)<br />

where the Laplace transform <strong>of</strong> the state transition matrix is<br />

Φ(s) = [sI – A] –1 .<br />

The state-transition matrix<br />

Φ(t) = L –1 {Φ(s)}<br />

(also defined as e At ) can be used to write<br />

x(t) = Φ(t) x(0) + ∫ t<br />

Φ (t – τ) Bu(τ) dτ<br />

0<br />

The output can be obtained with the output equation; e.g.,<br />

the Laplace transform output is<br />

Y(s) = {CΦ(s) B + D}U(s) + CΦ(s) x(0)<br />

The latter term represents the output(s) due to initial<br />

conditions whereas the former term represents the output(s)<br />

due to the U(s) inputs and gives rise to transfer function<br />

definitions.

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