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23-Chem-A6 Process Dynamics and Control · May 2013

Question 7 of 8: Multivariable Model — Transfer Functions and Response

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

National Exams / EGBC — May 2013 — 04-Chem-A6 Process Dynamics & Control. Three-hour open-book examination; any non-communicating calculator is permitted. Eight problems are printed and any five constitute a complete paper (each worth 20%); all eight are solved below for completeness. Most parts are quantitative (modelling, transfer functions, step/pulse responses, Routh, Nyquist/Bode and IMC design); qualitative sketches are drawn as real figures where the paper asks for them.

Reference texts: D. E. Seborg, T. F. Edgar, D. A. Mellichamp & F. J. Doyle III, Process Dynamics and Control (4th ed., Wiley) — Laplace-domain modelling, transfer functions, feedback stability, frequency response and IMC design; G. Stephanopoulos, Chemical Process Control: An Introduction to Theory and Practice (Prentice Hall) — Routh test, Nyquist criterion, Bode stability and dead-time systems; D. R. Coughanowr & S. E. LeBlanc, Process Systems Analysis and Control (3rd ed., McGraw-Hill) — first-order tank dynamics, step/pulse response and block-diagram algebra. Standard control conventions (deviation variables, unity valve/sensor gains unless stated) are used throughout.

Problem 7: Multivariable Model — Transfer Functions and Response (20%)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Given. The coupled linear state model $\dot y_1=-y_1-y_2+x_1$, $\dot y_2=y_1-2y_2+x_1+x_2$, zero initial conditions (deviation variables).

Find. (a) $Y_2/X_1$ and $Y_2/X_2$; (b) $y_2(t)$ for $x_1=0$, unit step $x_2$.

Approach. Laplace-transform both ODEs, giving two algebraic equations in $Y_1,Y_2$; eliminate $Y_1$ (Cramer/substitution) to express $Y_2$ in terms of $X_1,X_2$, read off the two transfer functions, then invert the specified input by partial fractions.

  1. Transform the model. With zero initial conditions, $sY_1=-Y_1-Y_2+X_1$ and $sY_2=Y_1-2Y_2+X_1+X_2$, i.e. $$(s+1)Y_1+Y_2=X_1,\qquad -Y_1+(s+2)Y_2=X_1+X_2.$$
  2. Eliminate $Y_1$. From the first equation $Y_1=(X_1-Y_2)/(s+1)$; substituting into the second and clearing $(s+1)$: $-(X_1-Y_2)+(s+1)(s+2)Y_2=(s+1)(X_1+X_2)$. Collecting $Y_2$: $Y_2\big[1+(s+1)(s+2)\big]=(s+2)X_1+(s+1)X_2$, and $1+(s+1)(s+2)=s^2+3s+3$.
  3. (a) Transfer functions. $$\boxed{\dfrac{Y_2}{X_1}=\dfrac{s+2}{s^2+3s+3}},\qquad \boxed{\dfrac{Y_2}{X_2}=\dfrac{s+1}{s^2+3s+3}}.$$ The common denominator $s^2+3s+3$ has roots $s=-1.5\pm j\,\tfrac{\sqrt3}{2}$ (damping ratio $\zeta=1.5/\sqrt3=0.866$, underdamped).
  4. (b) Response to a unit step in $x_2$ ($x_1=0$). $Y_2=\dfrac{s+1}{s(s^2+3s+3)}$. Partial fractions give $\dfrac{1/3}{s}-\dfrac{1}{3}\cdot\dfrac{s}{s^2+3s+3}$. Completing the square, $s^2+3s+3=(s+1.5)^2+(\tfrac{\sqrt3}{2})^2$, and inverting: $$y_2(t)=\dfrac13-\dfrac13\,e^{-1.5t}\cos\!\big(\tfrac{\sqrt3}{2}t\big)+\dfrac{\sqrt3}{3}\,e^{-1.5t}\sin\!\big(\tfrac{\sqrt3}{2}t\big).$$
  5. Interpret. The response starts at $y_2(0)=0$, overshoots slightly (a damped oscillation, $\omega_d=\sqrt3/2\approx0.866$), and settles at $\boxed{y_2(\infty)=\tfrac13}$ — the DC gain $Y_2/X_2\big|_{s=0}=1/3$. The combined transient amplitude is $\sqrt{(1/3)^2+(\sqrt3/3)^2}=\tfrac23$.
0 1 2 3 4 5 6 7 0 0.1667 0.3333 0.5 time t y₂(t) P7(b): y₂(t) for x₁=0, unit step x₂ (damped, →1/3)
Problem 7(b): $y_2(t)$ for $x_1=0$ and a unit step in $x_2$. Complex poles $-1.5\pm j0.866$ produce a lightly damped oscillation that settles at the DC gain $y_2(\infty)=1/3$.
ResultExpression
$Y_2/X_1$$(s+2)/(s^2+3s+3)$
$Y_2/X_2$$(s+1)/(s^2+3s+3)$
Response $y_2(t)$ (step $x_2$)$\tfrac13-\tfrac13e^{-1.5t}\cos\omega_d t+\tfrac{\sqrt3}{3}e^{-1.5t}\sin\omega_d t$
Damped frequency / final value$\omega_d=\sqrt3/2\approx0.866$; $y_2(\infty)=1/3$