Question 1 of 6: Rigid water-column transient between two reservoirs
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper: National Exams — 16-Civ-A5 Hydraulic Engineering — December 2019 · 3 hours · closed book (one aid sheet) · six questions, complete any five (all six solved here) · each question 20 marks, equal-value parts.
Reference texts: Chin, Water-Resources Engineering (Pearson); Chow, Open-Channel Hydraulics (McGraw-Hill); Chaudhry, Open-Channel Flow (Springer); Wylie & Streeter, Fluid Transients in Systems (Prentice-Hall); Munson, Young & Okiishi, Fundamentals of Fluid Mechanics (Wiley); Roberson, Cassidy & Chaudhry, Hydraulic Engineering.
Governing relations supplied on the exam cover sheet. Hazen–Williams $Q = 0.278\,C\,D^{2.63}\,S^{0.54}$ with slope $S=\Delta h/L$ (SI, $Q$ in m³/s, $D$ in m); Manning $Q=\tfrac{1}{n}A\,R^{2/3}\,S^{1/2}$; Darcy–Weisbach $\Delta h = 0.0826\,\tfrac{fL}{D^5}Q^2$. Unless stated, local losses and velocity head are neglected, diameters are nominal, and water has $\rho=1000\ \text{kg/m}^3$, $\nu=1.31\times10^{-6}\ \text{m}^2/\text{s}$.
Note on question/figure labels. The transient plots on pages 2–3 are printed as “Figure Q4–A / Q4–B” but belong to Question 1 (the 450 mm and 750 mm pipe responses); “Figure 1” (valve main) is the figure for Question 3 and “Figure 2” (pipe grid) is for Question 4. Labels are given as printed; the figures are matched to their questions by content.
Question 1: Rigid water-column transient between two reservoirs (20 marks)
Given. Two reservoirs connected by a single pipe that starts flowing under a 40 m head difference and then equalises as the reservoirs fill/drain.
Given data — Question 1
Quantity
Symbol
Value
Upstream / downstream start level
$z_1,\ z_2$
80 m, 40 m
Pipe diameter / length
$D,\ L$
0.450 m, 1000 m
Hazen–Williams coefficient
$C$
120
Reservoir surface area (each)
$A_{res}$
5 m²
Pipe cross-section
$A_p=\tfrac{\pi}{4}D^2$
0.15904 m²
Find. (a) the steady discharge at $t=0$; (b) $Q$, $z_1$, $z_2$ over the first two time steps of the rigid-column model; (c) a physical explanation of why the 450 mm pipe response is over-damped while the 750 mm response oscillates.
Figure 1-1. Rigid water-column system: the pipe water mass accelerates under the instantaneous reservoir head difference while the two 5 m² reservoirs slowly equalise.
Approach. Part (a) is a steady balance — with no acceleration the full head difference is spent on friction, so Hazen–Williams gives $Q$. Part (b) advances the rigid-column momentum equation together with reservoir continuity by explicit (Euler) time-stepping. Part (c) reads the two response plots through the damping ratio, which the pipe diameter controls.
Steady discharge at $t=0$ (part a). At steady state $dQ/dt=0$, so the whole head difference is friction head: $\Delta h = z_1-z_2 = 40\ \text{m}$ over $L=1000\ \text{m}$, i.e. $S = 40/1000 = 0.04$. Hazen–Williams:
$$Q_0 = 0.278\,C\,D^{2.63}\,S^{0.54} = 0.278(120)(0.45)^{2.63}(0.04)^{0.54}.$$
Evaluating $(0.45)^{2.63}=0.1225$ and $(0.04)^{0.54}=0.1759$ gives
$$\boxed{Q_0 = 0.718\ \text{m}^3/\text{s}}$$
which agrees with the $t=0$ intercept ($\approx 0.7\ \text{m}^3/\text{s}$) of Figure Q4–A.
Rigid-column governing equations (part b). Treating the pipe water as one incompressible, non-deformable slug, Newton’s second law on the column and mass continuity at each reservoir give
$$\frac{L}{g\,A_p}\frac{dQ}{dt} = (z_1-z_2) - h_f(Q),\qquad \frac{dz_1}{dt}=-\frac{Q}{A_{res}},\quad \frac{dz_2}{dt}=+\frac{Q}{A_{res}},$$
with $h_f(Q)$ the Hazen–Williams friction head at the current $Q$. Here $\dfrac{gA_p}{L}=\dfrac{9.81(0.15904)}{1000}=1.560\times10^{-3}$.
Choose a time step and advance (Euler). The exam does not state $\Delta t$; adopt $\Delta t = 20\ \text{s}$ (small relative to the $\sim$250 s natural period of this mass-oscillation — see the concept note). Update rule: $Q_{k+1}=Q_k+\Delta t\,\tfrac{gA_p}{L}[(z_1-z_2)_k-h_f(Q_k)]$, then $z_{1,k+1}=z_{1,k}-\Delta t\,Q_k/A_{res}$ and $z_{2,k+1}=z_{2,k}+\Delta t\,Q_k/A_{res}$.
At $t=0$: $Q=0.718$, $z_1-z_2=40=h_f$, so $dQ/dt=0$ — the flow is momentarily unchanged while the levels begin to close:
$$z_1(20)=80-20\tfrac{0.718}{5}=77.13\ \text{m},\quad z_2(20)=40+20\tfrac{0.718}{5}=42.87\ \text{m},\quad Q(20)=0.718\ \text{m}^3/\text{s}.$$
Second step: now $z_1-z_2=34.25\ \text{m} \lt h_f(0.718)=40\ \text{m}$, so the column decelerates, $dQ/dt=1.560\times10^{-3}(34.25-40)=-8.97\times10^{-3}$:
$$\boxed{Q(40)=0.539\ \text{m}^3/\text{s},\quad z_1(40)=74.25\ \text{m},\quad z_2(40)=45.75\ \text{m}.}$$
Interpret the two plots (part c). The rigid-column equation is a damped oscillator: inertia $\tfrac{L}{gA_p}\tfrac{dQ}{dt}$ versus the restoring head $(z_1-z_2)$ and the resistive (damping) term $h_f\propto D^{-4.87}$. The initial linear momentum of the slug is $\mathcal{M}=\rho L A_p V_0=\rho L\,Q_0$. Enlarging $D$ from 450 to 750 mm raises $Q_0$ from 0.72 to 2.75 m³/s and $A_p$ by $(750/450)^2=2.8\times$, so $\mathcal{M}$ jumps by roughly eight-fold, while friction (the damping) collapses. The 450 mm column is friction-dominated: it decays almost monotonically to zero with a single small undershoot (Figure Q4–A). The 750 mm column is inertia-dominated (lightly damped): its large stored momentum overshoots the equalised level and it oscillates about $Q=0$ with slowly-decaying amplitude (Figure Q4–B). Diameter sets the damping ratio.
Question 1 — results
Quantity
Value
(a) Steady flow at $t=0$
$Q_0 = 0.718\ \text{m}^3/\text{s}$
(b) $t=20$ s: $Q,\ z_1,\ z_2$
$0.718\ \text{m}^3/\text{s}$; 77.13 m; 42.87 m
(b) $t=40$ s: $Q,\ z_1,\ z_2$
$0.539\ \text{m}^3/\text{s}$; 74.25 m; 45.75 m
(c) 450 mm vs 750 mm
over-damped decay vs under-damped oscillation (inertia $\gg$ friction)