Transfer Functions of Interconnections

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Transfer Functions of Interconnections

Key Ideas

• It is common practice to build complex dynamical system models as interconnections of simpler subsystems, where some inputs of some subsystems are declared equal to some outputs of others.

• For an interconnection of LTI subsystems, its transfer function H(s) can be found by assuming that every signal in the interconnection is a complex multiple of the same complex exponential e^{st}. This leads to a system of linear equations whose solution gives H(s).

• In many cases the process simplifies to a sequence of additions or multiplications of transfer functions, using the rules for series, parallel, and feedback (Black's formula) connections.

• The task of designing stable interconnections is frequently aided by the Routh-Hurwitz criterion, which checks whether all roots of a polynomial have negative real part without computing the roots explicitly.

Series Connection

In a series connection, the output of the first subsystem feeds directly into the input of the second:

u H₁(s) w H₂(s) y

The overall transfer function (from u to y) is

H(s) = H_2(s)\,H_1(s).

To see this: assuming u(t)=Ue^{st}, w(t)=We^{st}, y(t)=Ye^{st} gives W=H_1(s)U and Y=H_2(s)W, so Y=H_2(s)H_1(s)U.

Python example:

import control as ct
s = ct.tf('s')
H1, H2 = 1/s, 1/(s+1)
H = H2*H1      # H = 1/(s^2+s)

Parallel Connection

In a parallel connection, both subsystems share the same input and their outputs are summed:

u H₁(s) H₂(s) + + y

The overall transfer function is

H(s) = H_1(s) + H_2(s).

Python example (continued):

H = H2 + H1    # H = (2s+1)/(s^2+s)

Feedback Connection and Black's Formula

In a feedback connection, a portion of the output is fed back and compared with the reference input:

r + P(s) y K(s) e

The subsystem with transfer function P(s) has input e and output y; the subsystem with transfer function K(s) has input y and output w; and e = r - w. Black's formula gives the closed-loop transfer function from r to y:

H_{r\to y}(s) = \frac{P(s)}{1 + K(s)P(s)}.

This is memorized as “forward gain divided by one plus total loop gain.” To prove it: assuming r(t)=Re^{st}, e(t)=Ee^{st}, y(t)=Ye^{st}, w(t)=We^{st}, we get Y=P(s)E, W=K(s)Y, and E=R-W. Solving for Y gives Y = \frac{P(s)}{1+K(s)P(s)}R.

Python example (continued):

G12 = ct.feedback(H1, H2)   # H1/(1+H2*H1) = s/(s^2+s+1)
G21 = ct.feedback(H2, H1)   # H2/(1+H1*H2) = (s+1)/(s^2+s+1)

Note the result depends on the order of arguments.

A Worked Example: Arm Position Controlled by Torque with Friction

A model familiar in 6.3100 describes the propeller arm: control torque u(t) drives the arm position \theta(t) in the presence of linear friction. Introducing intermediate signals—arm velocity w(t), friction torque v(t) = bw(t), and net torque f(t) = u(t) - v(t)—we can identify four subsystems:

\dot\theta = w: transfer function H_1(s) = 1/s.

M\dot w = f: transfer function H_2(s) = M/s.

v = bw: transfer function H_3(s) = b.

• Summation: f = u - v.

Using Black's formula, the transfer function from u to w is H_{u\to w}(s) = \frac{M/s}{1+bM/s} = \frac{M}{s+bM}. Then the series connection with 1/s gives the overall transfer function from u to \theta:

H_{u\to\theta}(s) = \frac{1}{s}\cdot\frac{M}{s+bM} = \frac{M}{s(s+bM)}.

Routh-Hurwitz Criterion

It is often useful to know whether all roots of a polynomial have negative real parts without computing the roots. The Routh-Hurwitz criterion gives necessary and sufficient conditions for polynomials with positive leading coefficient:

p(s)=s+p_0 is stable if and only if p_0 > 0.

p(s)=s^2+p_1 s+p_0 is stable if and only if p_0 > 0 and p_1 > 0.

p(s)=s^3+p_2 s^2+p_1 s+p_0 is stable if and only if p_0 > 0, p_1 > 0, p_2 > 0, and p_2 p_1 > p_0.

Example: Stabilizing a Double Integrator with PID

The block diagram below describes a PID controller attempting to stabilize the plant P(s) = 1/s^2:

r + Kd s+Kₚ+Kᵢ/s 1/s² y

By Black's formula the closed-loop transfer function is

H_{r\to y}(s) = \frac{K_d s^2 + K_p s + K_i}{s^3 + K_d s^2 + K_p s + K_i}.

The characteristic polynomial is s^3 + K_d s^2 + K_p s + K_i. By the degree-3 Routh-Hurwitz criterion, stability requires K_i > 0, K_p > 0, K_d > 0, and K_d K_p > K_i.

Beware of Unstable Zero/Pole Cancellations

Consider the feedback loop with K(s) = \frac{s}{s+1} and plant P(s) = 1/s^2. Black's formula gives

H_{r\to y}(s) = \frac{1}{s^2+s+1},

whose poles s = -\tfrac{1}{2} \pm j\tfrac{\sqrt{3}}{2} both have negative real parts—so the system looks stable.

However, consider the transfer function from a plant disturbance input d (injected between the controller and the plant) to the output y:

H_{d\to y}(s) = \frac{1/s^2}{1 + \frac{s}{s+1}\cdot\frac{1}{s^2}} = \frac{s+1}{s(s^2+s+1)},

which has a pole at s = 0—the system is actually unstable with respect to disturbances.

What happened? The controller zero at s=0 cancelled the plant pole at s=0 in H_{r\to y}, masking the instability. This is an unstable zero/pole cancellation. It can be proved that cancelling any zero or pole with \operatorname{Re}(s) \ge 0 is guaranteed to produce an unstable closed-loop system—it is an absolute no-no in feedback control design.

Python example:

import control as ct
s = ct.tf('s')
H1 = s/(s+1)
H2 = 1/(s*s)
H  = H2*H1              # H = s/(s^3+s^2)  -- no cancellation performed
G  = ct.feedback(H, 1)  # G = s/(s^3+s^2+s) -- instability visible

Python's control module correctly refuses to cancel the zero/pole, so the instability is visible in G(s).

Questions

Question 1: Stabilizing a Double Integrator with a First-Order Controller

Consider the feedback system with first-order controller K(s) = c\,\dfrac{s+b}{s+a} and plant P(s) = 1/s^2:

r + c (s+b)/(s+a) 1/s² y

By Black's formula the closed-loop characteristic polynomial is q(s) = s^3 + a s^2 + c s + cb. Apply the degree-3 Routh-Hurwitz conditions: cb > 0, c > 0, a > 0, and a \cdot c > cb (i.e., a > b).

Which combination of conditions on a, b, c yields a stable closed-loop system?

Which Routh-Hurwitz condition is the one that requires the strict inequality a > b (rather than just a, b > 0)?

The condition a > b comes from:

Question 2: Unstable Zero/Pole Cancellation

Consider the standard feedback diagram with plant P(s) = \dfrac{s-1}{s^2} and a desired closed-loop transfer function H_{r\to y}(s) = \dfrac{1}{s+1}.

Solving H = \frac{PK}{1+PK} for K gives K = \frac{H}{(1-H)P}. Substituting:

K(s) = \frac{\dfrac{1}{s+1}}{\left(1-\dfrac{1}{s+1}\right)\dfrac{s-1}{s^2}} = \frac{\dfrac{1}{s+1}}{\dfrac{s}{s+1}\cdot\dfrac{s-1}{s^2}} = \frac{s}{s-1}.

The open-loop product is K(s)P(s) = \dfrac{s}{s-1}\cdot\dfrac{s-1}{s^2} = \dfrac{1}{s}, where the factor (s-1) cancels. Since \operatorname{Re}(1) > 0, this is an unstable zero/pole cancellation.

The unstable cancellation between K(s) and P(s) occurs at s =

Why does this make the controller K(s) = \frac{s}{s-1} unacceptable?