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04-BS-7 · May 2015

Question 4 of 13: Electrical Power for a Gasoline Transfer Pump

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

Notes on this paper

04-BS-7 Mechanics of Fluids — May 2015 (National Examinations, three hours, closed book). Section A (Calculative) offers 9 questions and instructs "do seven"; Section B (Analytical) offers 4 questions and instructs "do three." Every question is answered below (13 of 13), so students can use the full paper as a study resource.

Reference texts: F. M. White, Fluid Mechanics, 8th ed. (McGraw-Hill) — fluid statics (Ch. 2), the linear-momentum and energy equations (Ch. 3), pipe friction and the Moody chart (Ch. 6), and drag on immersed bodies (Ch. 7).

Question 4: Electrical Power for a Gasoline Transfer Pump (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
Suction pipe diameter, Ds150 mm
Discharge pipe diameter, Dd100 mm
Discharge gauge elevation above pump centreline+1.5 m
Suction gauge elevation below pump centreline−0.5 m
Discharge gauge pressure150 kPa
Suction gauge pressure−30 kPa
Flow rate, Q0.035 m³/s
Fluid SG (gasoline)0.75
Pump efficiency75%

Find. The electrical power drawn by the pump motor.

Psuction D=150 mmgauge: -30 kPadischarge D=100 mmgauge: 150 kPapump ∷2.0 mElectrical power = 9.37 kW
Fig. Q4 — suction and discharge gauge points sit at different pipe diameters and different elevations, so the pump head must include the velocity-head and elevation-head changes between them, not just the gauge-pressure difference.

Approach. Apply the steady-flow energy equation between the suction and discharge gauge points, with the pump head hp as the only unknown; convert the resulting fluid power to electrical power through the stated efficiency.

  1. Pipe velocities from continuity (A = πD²/4): $$V_s=\frac{Q}{A_s}=\frac{0.035}{\frac{\pi}{4}(0.15)^2}=1.98\ \text{m/s}, \qquad V_d=\frac{Q}{A_d}=\frac{0.035}{\frac{\pi}{4}(0.10)^2}=4.46\ \text{m/s}$$
  2. Energy equation, suction → discharge, pump head hp added between the gauges: $$h_p=\frac{p_d-p_s}{\rho g}+\frac{V_d^2-V_s^2}{2g}+(z_d-z_s)$$
  3. Substitute (ρ = 750 kg/m³; pd−ps = 150−(−30) = 180 kPa; zd−zs = 1.5−(−0.5) = 2.0 m): $$h_p=\frac{180\,000}{750(9.81)}+\frac{4.46^2-1.98^2}{2(9.81)}+2.0 = 24.47+0.81+2.0=\boxed{27.28\ \text{m}}$$
  4. Fluid (hydraulic) power delivered to the gasoline: $$P_{fluid}=\rho g Q h_p = 750(9.81)(0.035)(27.28) = 7024\ \text{W} = 7.02\ \text{kW}$$
  5. Electrical power (fluid power divided by pump efficiency): $$P_{elec}=\frac{P_{fluid}}{\eta}=\frac{7.02}{0.75}=\boxed{9.37\ \text{kW}}$$
QuantityResult
Suction velocity Vs1.98 m/s
Discharge velocity Vd4.46 m/s
Pump head hp27.28 m
Fluid power7.02 kW
Electrical power required9.37 kW