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16-Civ-A5 Hydraulic Engineering · December 2017

Question 2 of 6: Ten-pipe system between two reservoirs

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 2: Ten-pipe system between two reservoirs (20 marks)

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. Ten identical pipes join reservoir A to reservoir B. Figure 2 (as printed on the exam page) shows they form two independent A→B routes: an upper route of three pipes in series (A–J2–J3–B), and a lower route in which a single pipe runs from A to junction J1, from which three parallel two-pipe branches (via J4, J5, J6) run on to B (3 + 1 + 3×2 = 10 pipes).

Given data
Upstream reservoir A / downstream reservoir B80 m / 65 m
Available head $\Delta H$15 m
Elevation of all pipes25 m
Pipe diameter / length / C (all identical)350 mm / 350 m / 130
Topology (Figure 2)upper: 3 in series; lower: 1 feeder + 3 parallel 2-pipe branches

Find. (a) the total discharge A→B; (b) the maximum and minimum pressure head in the system (at the junction nodes).

J1J2J3J4J5J6A (80 m)B (65 m)
Figure 2. Ten-pipe system as drawn on the exam: upper route A–J2–J3–B (three pipes in series); lower route A–J1 (one pipe), then three parallel two-pipe branches J1–J4/J5/J6–B. Not to scale.
the printed drawing instead shows the two-route layout above (one feeder pipe from A to a hub junction that fans into three branches, plus a separate three-pipe upper route). The solution follows the printed drawing.

Approach. Write every pipe loss as $h_f=k\,Q^{1.852}$. The two routes share only the reservoirs, so each spans the full 15 m on its own: reduce each route to an equivalent resistance, solve its flow, and add the two. Then trace the HGL along each route and subtract the 25 m pipe elevation.

  1. Per-pipe resistance. With $a=0.278\,C\,D^{2.63}$, $$k = \dfrac{L}{a^{1/0.54}} = \dfrac{350}{\left(0.278\cdot130\cdot0.350^{2.63}\right)^{1.852}} = 75.76 \quad(Q\ \text{in m}^3/\text{s},\ h_f\ \text{in m}).$$
  2. Upper route (3 pipes in series) carries $Q_u$. Series losses add, $3k\,Q_u^{1.852}=15$: $$Q_u=\left(\dfrac{15}{3(75.76)}\right)^{0.54}=0.230\ \text{m}^3/\text{s},$$ and each upper pipe drops $15/3 = 5.0$ m.
  3. Lower route carries $Q_l$. The feeder A–J1 carries all of $Q_l$; the three identical branches split it equally ($Q_l/3$ each), and each branch is two pipes in series: $$k\,Q_l^{1.852}\left[1+2\left(\tfrac13\right)^{1.852}\right]=15,\qquad 1+2\left(\tfrac13\right)^{1.852}=1.2615,$$ $$Q_l=\left(\dfrac{15}{75.76(1.2615)}\right)^{0.54}=0.368\ \text{m}^3/\text{s}.$$
  4. Total flow (part a). $$Q_t = Q_u + Q_l = 0.230 + 0.368 = \boxed{0.598\ \text{m}^3/\text{s}}\ \ (598\ \text{L/s}).$$
  5. HGL at the junctions. Feeder loss $k\,Q_l^{1.852}=11.89$ m; each branch pipe $k\,(Q_l/3)^{1.852}=1.55$ m. Hence $$\text{HGL}_{J2}=80-5.0=75.0,\quad \text{HGL}_{J3}=70.0,\quad \text{HGL}_{J1}=80-11.89=68.11,\quad \text{HGL}_{J4,J5,J6}=68.11-1.55=66.56\ \text{m},$$ and both routes close on 65.0 m at B (upper: $70.0-5.0$; lower: $66.56-1.55$).
  6. Maximum and minimum pressure head (part b). Pressure head = HGL − 25 m: $$p/\gamma\big|_{\max} = 75.0-25 = \boxed{50.0\ \text{m (at J2)}},\qquad p/\gamma\big|_{\min} = 66.56-25 = \boxed{41.6\ \text{m (at J4, J5, J6)}}.$$ Along the pipes themselves the pressure head is bounded by the reservoir ends, 55 m where the pipes leave A and 40 m where they enter B.
Final results — Question 2
QuantityValue
Upper-route flow $Q_u$ / lower-route flow $Q_l$0.230 / 0.368 m³/s
(a) Total discharge $Q_t$0.598 m³/s (598 L/s)
(b) Maximum nodal pressure head (J2)50.0 m
(b) Minimum nodal pressure head (J4, J5, J6)41.6 m
Pipe-end bounds (leaving A / entering B)55 m / 40 m