23-Chem-A6 Process Dynamics and Control · December 2013
Question 3 of 8: State-Space Model → Transfer Function & Step Response
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams / EGBC — December 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. The paper is almost entirely quantitative — linearisation, transfer functions, step/pulse/ramp responses, Routh and frequency-response (Bode/Nyquist) stability, and IMC design — and every boxed number.
Reference texts: D. E. Seborg, T. F. Edgar, D. A. Mellichamp & F. J. Doyle III, Process Dynamics and Control (4th ed., Wiley) — linearisation, transfer functions, frequency response, IMC design; G. Stephanopoulos, Chemical Process Control: An Introduction to Theory and Practice (Prentice Hall) — Routh array, Bode and Nyquist stability, dead-time systems; D. R. Coughanowr & S. E. LeBlanc, Process Systems Analysis and Control (3rd ed., McGraw-Hill) — first-order dynamics and step/pulse/ramp response. Standard control conventions are used (deviation variables about a steady state; unity valve/sensor gains unless stated).
Problem 3: State-Space Model → Transfer Function & Step Response (20%)
Given. A two-state linear model (already in deviation form, zero initial conditions):
Equation
Coefficients
$\dot x_1$
$-2.4048\,x_1+7u$
$\dot x_2$
$0.8333\,x_1-2.2381\,x_2-1.117\,u$
output
$y=x_2$
input
$u=$ unit step (part b)
Find. (a) $Y(s)/U(s)$; (b) $y(t)$ for a unit step in $u$.
Approach. Laplace-transform each state equation (zero ICs), eliminate $X_1$, and assemble $Y=X_2$ over $U$. For part (b) multiply by $1/s$ and invert by partial fractions into a constant plus two decaying exponentials.
Transform and solve for $X_1$. $(s+2.4048)X_1=7U\Rightarrow X_1=\dfrac{7U}{s+2.4048}$.
Substitute into the $X_2$ equation. $(s+2.2381)X_2=0.8333X_1-1.117U=\left[\dfrac{0.8333\cdot7}{s+2.4048}-1.117\right]U=\dfrac{5.8331-1.117(s+2.4048)}{s+2.4048}\,U.$ The numerator collapses to $-1.117s+3.147$.
(a) Transfer function. $$\boxed{\dfrac{Y(s)}{U(s)}=\dfrac{-1.117s+3.147}{(s+2.4048)(s+2.2381)}=\dfrac{-1.117s+3.147}{s^{2}+4.643s+5.382}.}$$ The DC gain is $Y/U|_{s=0}=3.147/5.382=0.585$; note the negative-$s$ numerator term (a left-half-plane zero at $s=+2.82$, i.e. an RHP zero — this system shows a mild inverse-response tendency).
(b) Unit-step response. With $U=1/s$, expand $Y(s)=\dfrac{-1.117s+3.147}{s(s+2.4048)(s+2.2381)}=\dfrac{A}{s}+\dfrac{B}{s+2.4048}+\dfrac{C}{s+2.2381}$. The residues are $A=0.585$ (the DC gain), $B=+14.55$ and $C=-15.14$, so $$\boxed{y(t)=0.585+14.55\,e^{-2.405t}-15.14\,e^{-2.238t}.}$$
Sanity checks. $y(0)=0.585+14.55-15.14\approx0$ (correct, $x_2$ starts at rest) and $y(\infty)=0.585$ (the DC gain). The two closely-spaced poles give large, nearly-cancelling residues; the response rises, overshoots slightly toward $\approx0.60$ near $t\approx0.6\,$s, then settles to $0.585$ (see figure).
Problem 3(b): unit-step response $y(t)=0.585+14.55e^{-2.405t}-15.14e^{-2.238t}$. Starting from zero it rises quickly, peaks just above the final value near $t\approx0.6\,$s, and settles at the DC gain $0.585$.