20-Bio-A2 Process Dynamics and Control · May 2018
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
National Exams / EGBC — May 2018 — 04-Bio-A2 Process Dynamics and Control. 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 second-order Bode/phase-margin analysis, feedback stability with a non-minimum-phase sensor, dead-time Nyquist/gain-margin design, zero-location effects on step response, nonlinear radiative-heat-transfer linearization, Internal Model Control (IMC) of a dead-time process, PI-controller stability/response, and nonlinear-CSTR linearization. Note: Problem 2's printed sub-part weights (10%+20%=30%) exceed its stated 20% problem total — both sub-parts are fully answered below.
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, linearization and IMC design; G. Stephanopoulos, Chemical Process Control: An Introduction to Theory and Practice (Prentice Hall) — Nyquist criterion and dead-time systems. Standard control conventions (deviation variables; unity valve gain unless stated) are used throughout.
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. $G_p(s)=\dfrac1s$ (integrating tank level), proportional controller gain $K$, sensor $G_m(s)=\dfrac{s-1}{(s+1)^2}$ (note: numerator zero at $s=+1$ — a right-half-plane, non-minimum-phase sensor).
Find. (1) the feedback block diagram and closed-loop transfer function $Y(s)/R(s)$; (2) the range of $K$ for closed-loop stability.
Approach. Write the closed-loop transfer function for a non-unity-feedback loop, $Y/R=KG_p/(1+KG_pG_m)$, clear fractions to get a polynomial characteristic equation in $s$, and apply the Routh–Hurwitz array.
| Result | Value |
|---|---|
| Closed-loop TF | $Y/R=K(s+1)^2/[s(s+1)^2+K(s-1)]$ |
| Characteristic equation | $s^3+2s^2+(1+K)s-K=0$ |
| Stability range | $-\tfrac23\lt K\lt0$ |