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20-Bio-A2 Process Dynamics and Control · Undated paper

Question 4 of 8: Transfer Function and Step Response from a State-Space Model

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

Notes on this paper

National Exams / EGBC — May 2019 — 04-Bio-A2 Process Dynamics and Control (the paper's own header line alternates between the codes "04-BIO-A2" and "04-BIO-A3" across pages; the subject line and content are unambiguously Process Dynamics and Control, so 04-Bio-A2 is used throughout). Three-hour open-book examination; any non-communicating calculator is permitted. The cover page states that only the first five questions in the answer book are marked, yet all eight problems are printed on the paper — all eight are solved below for completeness, since the full set is a study resource. Content spans the effect of a real zero on step-response overshoot, the Nyquist criterion for an open-loop-unstable process, a two-tank linear-vs-nonlinear-valve comparison, state-space-to-transfer-function conversion, Routh–Hurwitz stability with PI control of an unstable process, inverse Laplace transforms with time delay, Internal Model Control (IMC) design for a dead-time process, and Bode/gain-margin design.

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, Routh stability, Nyquist/Bode frequency response, and Internal Model Control design; G. Stephanopoulos, Chemical Process Control: An Introduction to Theory and Practice (Prentice Hall) — the Nyquist criterion for open-loop-unstable processes and dead-time systems. Standard control conventions (deviation variables; unity valve/sensor gain unless stated) are used throughout.

Problem 4: Transfer Function and Step Response from a State-Space Model (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. Two-state linear ODE system with $\dot x_1=-2.6666x_1+u$, $\dot x_2=0.8333x_1-0.6250x_2$, $y=x_2$; zero initial conditions (deviation variables).

Find. (a) $Y(s)/U(s)$; (b) $y(t)$ for a unit step in $u$.

Approach. Laplace-transform each state equation (zero ICs); the first equation is decoupled from $x_2$, so solve it directly for $X_1(s)/U(s)$ and substitute into the second to eliminate $X_1$; for (b), multiply by $1/s$ and expand in partial fractions using the two real poles.

  1. (a) State 1 (decoupled). $(s+2.6666)X_1(s)=U(s)\Rightarrow X_1(s)=\dfrac{1}{s+2.6666}U(s)$.
  2. (a) State 2, eliminate $X_1$. $(s+0.6250)X_2(s)=0.8333X_1(s)=\dfrac{0.8333}{s+2.6666}U(s)$.
  3. (a) Assemble the transfer function. $$\boxed{\frac{Y(s)}{U(s)}=\frac{0.8333}{(s+2.6666)(s+0.6250)}.}$$ Both poles are real and in the left half-plane ($s=-2.6666,-0.6250$) — a stable, non-oscillatory, overdamped second-order system with no zero (a pure two-pole cascade, unlike Problems 1 and 5 which carry a zero or an unstable pole).
  4. (b) Partial fractions for the unit step. $Y(s)=\dfrac{0.8333}{s(s+2.6666)(s+0.6250)}=\dfrac As+\dfrac{B}{s+2.6666}+\dfrac{C}{s+0.6250}$, with residues evaluated at each pole: $$A=\frac{0.8333}{2.6666\times0.6250}=0.500,\qquad B=\frac{0.8333}{(-2.6666)(-2.6666+0.6250)}=0.1531,\qquad C=\frac{0.8333}{(-0.6250)(-0.6250+2.6666)}=-0.6531.$$ (Check: $A+B+C=0.500+0.153-0.653\approx0=y(0)$, consistent with zero initial conditions.)
  5. (b) Result. $$\boxed{y(t)=0.500+0.1531\,e^{-2.6666t}-0.6531\,e^{-0.6250t}.}$$ At $t=1$: $y=0.161$; at $t=2$: $y=0.314$; at $t=5$: $y=0.471$, approaching the steady-state gain $y(\infty)=A=0.500$ (the slower pole, $s=-0.625$, dominates the settling time).
ResultValue
Transfer function$Y(s)/U(s)=0.8333/[(s+2.6666)(s+0.6250)]$
Step response$y(t)=0.500+0.1531e^{-2.6666t}-0.6531e^{-0.6250t}$
Steady-state gain$y(\infty)=0.500$
Dominant time constant$1/0.625=1.6\ \text{s}$ (slower pole)