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16-Civ-A5 Hydraulic Engineering · May 2016

Question 3 of 6: Transmission main with a control valve

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

Notes on this paper

National Exams — 98-Civ-A5 Hydraulic Engineering — May 2016. Closed book; one aid sheet and a non-communicating calculator permitted. Six questions of equal value (20 marks each); candidates answer any five. All six are solved here as a study resource. Exam-supplied relations: Hazen–Williams $Q = 0.278\,C\,D^{2.63}\,S^{0.54}$ with $S = h_f/L$ (SI, $Q$ in m$^3$/s, $D,L$ in m), Manning $Q=\tfrac{1}{n}A R^{2/3}S^{1/2}$, Darcy–Weisbach $\Delta h = 0.0826\,f\,L\,Q^2/D^5$, valve law $Q=\tau E_s\sqrt{H_{u/s}-H_{d/s}}$, and $\mathrm{TDH}=H_s+H_f$. Water: $\rho=1000$ kg/m$^3$, $\nu=1.31\times10^{-6}$ m$^2$/s.

Reference texts. Mays, Water Resources Engineering, 2nd ed. (pipe networks, branched systems, valves, transmission mains); Chow, Open-Channel Hydraulics (Manning uniform flow, critical depth, specific energy); Crowe, Elger & Roberson, Engineering Fluid Mechanics (pipe force balance, laminar film flow).

Question 3: Transmission main with a control valve (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.

Find. (a) the valve coefficient $\tau$; (b) the downstream reservoir level $h_B$; (c) the new steady discharge when $\tau$ is reduced to 0.3.

Given data
QuantityValue
Pipe length $L$5,000 m
Hazen–Williams $C$110
Inner diameter $D$1,067 mm = 1.067 m
Upstream level $h_A$105 m
Valve constant $E_s$0.35 m$^{5/2}$/s
Case (a) discharge / valve loss1 m$^3$/s / 5 m
Upstream Downstream hA = 105 m Valve hB 4,000 m 1,000 m
Transmission main: upstream reservoir (105 m), 4,000 m of pipe to the valve, 1,000 m to the downstream reservoir.

Approach. The valve law fixes $\tau$ from the (a) operating point. An energy balance between the two reservoir surfaces — friction over the full 5,000 m plus the valve loss — sets the downstream level. Reducing $\tau$ raises the valve loss for a given flow, so (c) is found by balancing pipe friction plus valve loss against the (now fixed) available head.

  1. Valve coefficient (a). The valve law $Q=\tau E_s\sqrt{\Delta h_v}$ rearranges to $\tau=\dfrac{Q}{E_s\sqrt{\Delta h_v}}$. With $Q=1$, $\Delta h_v=5$ m: $$\tau=\frac{1}{0.35\sqrt{5}}=\boxed{1.28}.$$
  2. Pipe friction at $Q=1$ m$^3$/s. Hazen–Williams over the full length: $$h_{f,pipe}=5000\!\left[\frac{1.0}{0.278(110)(1.067)^{2.63}}\right]^{1/0.54}=6.47\text{ m}.$$
  3. Downstream level (b). Energy from surface A to surface B loses pipe friction and valve head: $$h_B=h_A-h_{f,pipe}-\Delta h_v=105-6.47-5.0=\boxed{93.5\ \text{m}}.$$
  4. Discharge when $\tau=0.3$ (c). The available head is unchanged, $h_A-h_B=105-93.5=11.47$ m, and must equal pipe friction plus the new valve loss $\Delta h_v=\left(\dfrac{Q}{\tau E_s}\right)^2=\left(\dfrac{Q}{0.105}\right)^2$: $$h_{f,pipe}(Q)+\left(\frac{Q}{0.105}\right)^2=11.47,\qquad h_{f,pipe}(Q)=5000\!\left[\frac{Q}{0.278(110)(1.067)^{2.63}}\right]^{1/0.54}.$$ Here the tighter valve dominates. Solving iteratively (pipe loss $\approx0.9$ m, valve loss $\approx10.6$ m): $$\boxed{Q\approx0.34\ \text{m}^3/\text{s}}.$$ Throttling the valve from $\tau=1.28$ to $0.3$ cuts the discharge from 1.0 to about 0.34 m$^3$/s.
Final results — Question 3
QuantityValue
(a) Valve coefficient $\tau$1.28
(b) Downstream reservoir level $h_B$93.5 m
(c) Discharge at $\tau=0.3$0.34 m$^3$/s