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16-Civ-A5 Hydraulic Engineering · May 2015

Question 1 of 6: Equivalent-pipe network flow

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

Worked solutions. Closed-book format, 3 hours; six questions, candidates complete any five — all six are solved here as a study resource. All questions are of equal value (20 marks).

Reference texts. Mays, Water Resources Engineering, 2nd ed. (pipe systems, equivalent pipes, valves, network analysis, rigid water-column / mass-oscillation model); Chow, Open-Channel Hydraulics (Manning uniform flow, critical depth, specific energy); Crowe, Elger & Roberson, Engineering Fluid Mechanics (unsteady flow, St. Venant equations). Exam-supplied relations: Hazen–Williams $Q = 0.278\,C\,D^{2.63}\,S^{0.54}$ with $S = h_f/L$ (SI units), Manning $Q=\tfrac{1}{n}A R^{2/3}S^{1/2}$, and Total Dynamic Head $\mathrm{TDH}=H_S+H_f$.

Question 1: Equivalent-pipe network flow (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. Seven identical pipes connect reservoir A (head 100 m) to reservoir B (head 70 m); each pipe has $L=1{,}000\text{ m}$, $C=120$, $D=250\text{ mm}=0.25\text{ m}$. Available head $\Delta H = 100-70 = 30\text{ m}$.

ABRes. ARes. BPipe 1Pipe 3Pipe 4Pipe 2Pipe 5Pipe 6Pipe 7
Figure 1. Pipe network: A—P1—J1, then two parallel routes (P3+P4) and (P2+P5) to J2, then P6—P7—B.

Find. The total discharge $Q$ delivered A→B, and the discharge carried by pipe 5.

Approach. Because every pipe is identical, write each pipe loss as $h_f=kQ^{1.852}$, reduce the network by series–parallel rules to a single equivalent line, and set the summed loss equal to the 30 m of available head.

  1. Per-pipe resistance. Inverting Hazen–Williams, $h_f = L\left(\dfrac{Q}{0.278\,C\,D^{2.63}}\right)^{1/0.54}=kQ^{1.852}$, with $$k=\frac{L}{(0.278\,C\,D^{2.63})^{1.852}}=\frac{1000}{(0.278\cdot120\cdot0.25^{2.63})^{1.852}}=1293\ \text{s}^{1.852}\text{m}^{-4.556}.$$
  2. Read the topology. Pipe 1 is in series from A to junction J1. Between J1 and J2 there are two routes in parallel — the upper route P3+P4 and the lower route P2+P5 — each route being two identical pipes in series. Pipes 6 and 7 are again in series from J2 to B.
  3. Split the parallel block. The two routes are identical, so they share the flow equally: each carries $Q/2$. The head loss across the parallel block (two pipes in series, each passing $Q/2$) is $$\Delta H_{\text{block}} = 2k\left(\tfrac{Q}{2}\right)^{1.852}.$$
  4. Assemble the equivalent line. Pipes 1, 6 and 7 each pass the full $Q$, so $$\underbrace{3\,kQ^{1.852}}_{\text{P1, P6, P7}}+\underbrace{2k\left(\tfrac{Q}{2}\right)^{1.852}}_{\text{parallel block}} = kQ^{1.852}\big[\,3+2\cdot2^{-1.852}\,\big]=3.554\,kQ^{1.852}=30\text{ m}.$$
  5. Solve for total flow. $Q^{1.852}=\dfrac{30}{3.554\cdot1293}=6.53\times10^{-3}$, hence $$\boxed{Q = 0.0661\ \text{m}^3/\text{s} \approx 66.1\ \text{L/s}.}$$
  6. Flow in pipe 5. Pipe 5 lies on the lower parallel route, which carries half the total: $$\boxed{Q_5 = \tfrac{Q}{2}=0.0330\ \text{m}^3/\text{s} \approx 33.0\ \text{L/s}.}$$

A direct nodal (Hardy–Cross-free) solve of all seven pipes reproduces these values to four significant figures and gives junction heads $H_{J1}=91.6\text{ m}$, $H_{J2}=86.9\text{ m}$, confirming the reduction.

Final results — Question 1
QuantityValue
Per-pipe resistance $k$1293 (SI)
Total system flow $Q$0.0661 m³/s (66.1 L/s)
Flow in pipe 50.0330 m³/s (33.0 L/s)
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