Question 4 of 6: Two elevated tanks — quasi-steady drawdown
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams — 16-Civ-A5 Hydraulic Engineering — December 2017. 3 hours, closed book (one 8.5×11 aid sheet permitted). Six questions of equal value; candidates answer any five. All six are solved here as a study resource. Unless stated, local losses and velocity head are neglected; water ρ = 1000 kg/m³, ν = 1.31×10−6 m²/s.
Reference texts: D. A. Chin, Water-Resources Engineering (3rd ed.), Ch. 2 (flow in closed conduits) & Ch. 7 (water-distribution systems); A. Osman Akan, Open Channel Hydraulics; M. Hanif Chaudhry, Open-Channel Flow (2nd ed.), Ch. 3 (hydraulic jump); Chadwick, Morfett & Borthwick, Hydraulics in Civil and Environmental Engineering.
Question 4: Two elevated tanks — quasi-steady drawdown (20 marks)
Given. Two constant-diameter tanks drain through identical pipes to a common node, whose valve discharges to atmosphere.
Given data
Tank diameter (both) / plan area
5 m / 19.635 m²
Initial levels: Tank 1 / Tank 2
96 m / 89 m
Valve coefficient $C_v$ (to atmosphere)
0.15 m5/2/s
Pipe C / D / L (both)
100 / 250 mm / 300 m
Time step $\Delta t$ / number of steps
15 s / 3
Find. The node pressure head $H$ and the two pipe flows $Q_1,Q_2$ over the first three time steps.
Figure 4. Two elevated tanks feeding a common demand node H; the node valve discharges to atmosphere. Node elevation is taken as the datum, so H is the node pressure head.
Approach. Each step is a steady network solve: find the node head $H$ that satisfies continuity $Q_1+Q_2 = Q_{\text{valve}}$, then advance the tank levels by the volume drawn, $\Delta z_i = Q_i\,\Delta t / A_{\text{tank}}$, and repeat.
Check (inconsistent given, per NOTE 1): the stated “initial valve flow 350 L/s” implies a node head $H=(0.350/0.15)^2 = 5.44$ m; but at $H=5.44$ m the 96 m and 89 m tanks would drive roughly 1.1 m³/s through the two pipes — far more than 0.35 m³/s, so continuity cannot hold. The simulation below therefore starts from the continuity-consistent initial state ($H_0 = 20.13$ m, $Q_v = 673$ L/s) and the stated 350 L/s is treated as an inconsistent datum.
Nodal equations. Taking the node elevation as datum, each pipe carries $Q_i = 0.278\,C\,D^{2.63}\left[(z_i-H)/L\right]^{0.54}$ and the valve passes $Q_v = C_v\sqrt{H}$. The unknown $H$ closes continuity:
$$Q_1(z_1,H)+Q_2(z_2,H) = C_v\sqrt{H}.$$
Advance the tank levels. Over $\Delta t = 15$ s, $\Delta z_i = Q_i\Delta t / A_{\text{tank}}$ with $A_{\text{tank}} = \tfrac{\pi}{4}(5)^2 = 19.635\ \text{m}^2$; e.g. Tank 1 drops $0.3453\cdot15/19.635 = 0.264$ m to 95.74 m, Tank 2 drops 0.250 m to 88.75 m.
Repeat for the next steps. Re-solving continuity at each new pair of levels gives the small monotonic decline tabulated below — the node head barely moves because the large tanks lose only ~0.25 m per step.