23-Chem-A6 Process Dynamics and Control · December 2013
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
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).
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. Pipe $L=10\ \mathrm{m}$, liquid speed $u=1\ \mathrm{m/s}$; tank area $A=1\ \mathrm{m^{2}}$, level $h$; the tank has an inflow only (no drain specified), so it integrates.
Find. (a) the delay $\theta$; (b) the ODE and $H(s)/U(s)$; (c) the closed-loop $H/H_{sp}$ under proportional control.
Approach. The pipe is a pure transport delay $\theta=L/u$; the tank with no outlet is an integrator. Combine them for the open loop, then close the proportional loop with the standard $L/(1+L)$ formula.
The problem states an inlet velocity $u$ but no pipe diameter or tank outflow. We take the volumetric inflow proportional to $u$ (unit effective pipe area) and the tank as outlet-free, which is the standard reading of this classic dead-time-plus-integrator exercise. If a finite outlet resistance $R$ were intended, the integrator $1/s$ would become a first-order lag $R/(A R s+1)$ and $H/U=R\,e^{-10s}/(ARs+1)$; the delay term and its stability implications are unchanged.
| Result | Expression |
|---|---|
| Transport delay | $\theta=L/u=10\ \mathrm{s}$ |
| Tank ODE | $A\,dh/dt=u(t-\theta)$ |
| Open-loop TF | $H/U=e^{-10s}/s$ |
| Closed-loop TF | $H/H_{sp}=K_ce^{-10s}/(s+K_ce^{-10s})$ |
| Stability limit | $0<K_c<0.157\ \mathrm{s^{-1}}$ |