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%)
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.
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. $$(s+1)Y_1+Y_2=X_1,\qquad -Y_1+(s+2)Y_2=X_1+X_2.$$
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 $1+(s+1)(s+2)=s^2+3s+3$.
(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).
(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: $$y_2(t)=\dfrac13-\dfrac13\,e^{-1.5t}\cos\!\big(\tfrac{\sqrt3}{2}t\big)+\dfrac{\sqrt3}{3}\,e^{-1.5t}\sin\!\big(\tfrac{\sqrt3}{2}t\big).$$
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 $\sqrt{(1/3)^2+(\sqrt3/3)^2}=\tfrac23$.
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 $y_2(\infty)=1/3$.