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23-Chem-A6 Process Dynamics and Control · December 2013

Question 6 of 8: Transport Delay in a Pipe Feeding an Integrating Tank

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 6: Transport Delay in a Pipe Feeding an Integrating Tank (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. 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.

u (in) pipe, length L = 10 m v (out) tank, A = 1 m² h transport delay θ = L/u = 10 s
Problem 6: liquid enters the pipe at velocity $u$ and, after a transport delay $\theta=L/u$, discharges into the tank (area $A$, level $h$). With no outflow the tank integrates the delayed inflow, so the open-loop path is a pure delay in series with an integrator.

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.

  1. (a) Transport delay. A fluid element traverses the pipe in $$\boxed{\theta=\dfrac{L}{u}=\dfrac{10}{1}=10\ \mathrm{s}.}$$
  2. (b) Model and open-loop transfer function. The flow reaching the tank is the inlet flow delayed by $\theta$; with the pipe cross-section absorbed into the input (or unit pipe area), the volumetric balance on the outlet-free tank is $A\,\dfrac{dh}{dt}=u(t-\theta)$. In deviation/Laplace form ($A=1$): $$\boxed{\dfrac{H(s)}{U(s)}=\dfrac{e^{-\theta s}}{A s}=\dfrac{e^{-10s}}{s}}$$ — a pure integrator preceded by a $10\,$s dead time (no steady-state gain; level is non-self-regulating).
  3. (c) Closed-loop transfer function. With $G_c=K_c$ and $G_p=e^{-10s}/s$, $$\dfrac{H(s)}{H_{sp}(s)}=\dfrac{K_cG_p}{1+K_cG_p}=\boxed{\dfrac{K_c\,e^{-10s}}{s+K_c\,e^{-10s}}.}$$
  4. Stability note. An integrator-plus-delay under pure proportional control is only conditionally stable: the phase $-90^\circ-10\omega$ reaches $-180^\circ$ at $\omega_{pc}=\pi/20=0.157\ \mathrm{rad/s}$, where $|G_p|=1/\omega$, so the ultimate gain is $K_{cu}=\omega_{pc}=0.157$. The loop is stable only for $0<K_c<0.157\ \mathrm{s^{-1}}$ — the dead time imposes a hard speed limit.
Check — modelling assumption

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.

ResultExpression
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$0<K_c<0.157\ \mathrm{s^{-1}}$