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04-BS-7 · May 2014

Question 4 of 13: Head Loss in a Reservoir-Fed Pipe

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

Notes on this paper

04-BS-7 Mechanics of Fluids — National Examinations, May 2014. Three (3) hours, closed book. Section A: Calculative (9 questions, do 7); Section B: Analytical/Graphical (4 questions, do 3). Ten questions constitute a complete paper (50 marks). Every printed question is solved below, including the two "extra" questions in each Section beyond the minimum required.

Reference texts: White, Fluid Mechanics, 8th ed. (fluid statics & capillarity Ch.2; Bernoulli/energy equation Ch.3; pipe friction & the Moody chart Ch.6; drag on immersed bodies Ch.7; buoyancy Ch.2; momentum & jet propulsion Ch.3).

Question 4 — Head Loss in a Reservoir-Fed Pipe (5 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.

QuantityValue
Pipe entrance elevation6 m
Reservoir surface above entrance3 m → surface at z = 9 m
Pipe exit elevation (open to atm.)4 m
Pipe diameter50 mm
Pipe length120 m
Measured flow rate, Q0.006 m³/s

Find. The total head loss between the reservoir surface and the pipe exit.

reservoir water surface, z = 9 m (6 m + 3 m head) z = 6 m pipe, D = 50 mm, L = 120 m z = 4 m, open to atm. V2 datum
Fig. Q4 — reservoir feeding a 50 mm pipe that discharges to atmosphere 5 m lower than the reservoir surface; total head loss is found from the energy equation.

Approach. Write the general energy equation between the reservoir free surface (large area, V₁≈0, p=atm.) and the open pipe exit (p=atm., V₂=exit velocity), solving for hL as the only unknown.

  1. Exit velocity from continuity. $$A = \frac{{\pi}}{{4}}(0.050)^2 = 1.9635\times10^{{-3}}\text{{ m}}^2,\quad V_2=\frac{{Q}}{{A}}=\frac{{0.006}}{{1.9635\times10^{{-3}}}}=3.056\text{{ m/s}}$$
  2. Energy equation, reservoir surface (1) to pipe exit (2). $$\frac{{p_1}}{{\rho g}}+z_1+\frac{{V_1^2}}{{2g}} = \frac{{p_2}}{{\rho g}}+z_2+\frac{{V_2^2}}{{2g}}+h_L$$ With p₁=p₂=0 (gauge), V₁≈0, z₁=9 m, z₂=4 m: $$h_L = (z_1-z_2)-\frac{{V_2^2}}{{2g}} = 5-\frac{{3.056^2}}{{2\times9.81}} = 5-0.476$$ $$h_L = \boxed{{4.52\text{{ m}}}}$$
QuantityResult
Exit velocity, V₂3.06 m/s
Velocity head, V₂²/2g0.476 m
Total head loss, hL4.52 m