23-Chem-A6 Process Dynamics and Control · May 2013
Question 2 of 8: Draining Tank — Step and Pulse Response
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams / EGBC — May 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. Most parts are quantitative (modelling, transfer functions, step/pulse responses, Routh, Nyquist/Bode and IMC design); qualitative sketches are drawn as real figures where the paper asks for them.
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, feedback stability, frequency response and IMC design; G. Stephanopoulos, Chemical Process Control: An Introduction to Theory and Practice (Prentice Hall) — Routh test, Nyquist criterion, Bode stability and dead-time systems; D. R. Coughanowr & S. E. LeBlanc, Process Systems Analysis and Control (3rd ed., McGraw-Hill) — first-order tank dynamics, step/pulse response and block-diagram algebra. Standard control conventions (deviation variables, unity valve/sensor gains unless stated) are used throughout.
Problem 2: Draining Tank — Step and Pulse Response (20%)
Given. A gravity-drained tank with a linear resistance:
Quantity
Symbol
Value
Cross-section area
$A$
$1\ \mathrm{m^2}$
Initial level
$h_0$
$7\ \mathrm{m}$
Outflow law
$F_1$
$R_1 h,\ R_1=4\ \mathrm{m^2/min}$
Pulse duration
$t_p$
$5\ \mathrm{min}$
Find. The deviation level $h'(t)=h(t)-h_0$ for (a) a unit step and (b) a unit pulse of width $t_p$ in $F_0$.
Problem 2: single gravity-drained tank, inflow $F_0$, level $h$ ($A=1\ \mathrm{m^2}$, $h_0=7\ \mathrm{m}$), linear outflow $F_1=R_1 h$ through valve $R_1=4\ \mathrm{m^2/min}$.
Approach. Write the linear tank balance, reduce it to standard first-order form to read off $\tau$ and gain $K$, then apply the step solution directly and build the pulse as the superposition of a step and a delayed negative step.
Model and standard form. $A\,\dfrac{dh}{dt}=F_0-R_1 h$. In deviation variables about the initial steady state ($F_{0s}=R_1 h_0=4\times7=28\ \mathrm{m^3/min}$): $\dfrac{dh'}{dt}=F_0'-4h'$. Dividing by $R_1$ puts it in standard form with $$\tau=\dfrac{A}{R_1}=0.25\ \mathrm{min},\qquad K=\dfrac{1}{R_1}=0.25,$$ so $\dfrac{H'(s)}{F_0'(s)}=\dfrac{K}{\tau s+1}=\dfrac{0.25}{0.25 s+1}=\dfrac{1}{s+4}.$
(a) Unit-step response. For $F_0'=1$ (a $1\ \mathrm{m^3/min}$ step), the first-order step response is $$h'(t)=K\!\left(1-e^{-t/\tau}\right)=0.25\left(1-e^{-4t}\right).$$ The level rises from $7\ \mathrm{m}$ toward $\boxed{h(\infty)=7.25\ \mathrm{m}}$ with time constant $0.25\ \mathrm{min}$ (~99% settled in $5\tau\approx1.25\ \mathrm{min}$).
(b) Unit-pulse response — superposition. A unit pulse of width $t_p$ is a unit step at $t=0$ minus a unit step at $t=t_p$. By linearity, for $0\le t\le t_p$ the response equals the step result, $h'(t)=0.25(1-e^{-4t})$; for $t>t_p$ the delayed negative step is added: $$h'(t)=0.25\Big[e^{-4(t-5)}-e^{-4t}\Big],\qquad t>5\ \mathrm{min}.$$
Interpret the pulse. Because $\tau=0.25\ \mathrm{min}\ll t_p=5\ \mathrm{min}$, the level essentially reaches the new steady state during the pulse: at $t=t_p$, $h'(5)=0.25(1-e^{-20})\approx\boxed{0.25\ \mathrm{m}}$ (peak, $h\approx7.25\ \mathrm{m}$). After the pulse ends the tank drains back to $7\ \mathrm{m}$ with the same $0.25\ \mathrm{min}$ time constant — a near-rectangular rise-and-decay bump of height $0.25\ \mathrm{m}$.