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 $\mathrm{TDH}=H_S+H_f$.
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 $\Delta H = 100-70 = 30\text{ m}$.
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.
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 $$k=\frac{L}{(0.278\,C\,D^{2.63})^{1.852}}=\frac{1000}{(0.278\cdot120\cdot0.25^{2.63})^{1.852}}=1293\ \text{s}^{1.852}\text{m}^{-4.556}.$$
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.
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 $$\Delta H_{\text{block}} = 2k\left(\tfrac{Q}{2}\right)^{1.852}.$$
Assemble the equivalent line. Pipes 1, 6 and 7 each pass the full $Q$, so $$\underbrace{3\,kQ^{1.852}}_{\text{P1, P6, P7}}+\underbrace{2k\left(\tfrac{Q}{2}\right)^{1.852}}_{\text{parallel block}} = kQ^{1.852}\big[\,3+2\cdot2^{-1.852}\,\big]=3.554\,kQ^{1.852}=30\text{ m}.$$
Solve for total flow. $Q^{1.852}=\dfrac{30}{3.554\cdot1293}=6.53\times10^{-3}$, hence $$\boxed{Q = 0.0661\ \text{m}^3/\text{s} \approx 66.1\ \text{L/s}.}$$
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.