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04-BS-7 · December 2019

Question 1 of 13: Absolute Pressure in a Pipe from a Multi-Fluid Manometer

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

Notes on this paper

04-BS-7 Mechanics of Fluids — December 2019 (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. Constants used throughout (from the paper's own Constants page): g = 9.81 m/s², patm = 100 kPa, ρwater = 1000 kg/m³, SGglycerine = 1.26, SGmercury = 13.56, ρconcrete = 2400 kg/m³, ρair = 1.19 kg/m³ (20°C) / 1.21 kg/m³ (15°C), μwater = 1.0×10⁻³ N·s/m², μair = 1.8×10⁻⁵ N·s/m², Rair = 287 J/kg·K.

Reference texts: F. M. White, Fluid Mechanics, 8th ed. (McGraw-Hill) — fluid statics and manometry (Ch. 2), hydrostatic forces and the middle-third rule (Ch. 2), buoyancy and equilibrium (Ch. 2), dimensional analysis and drag (Ch. 5, 7), pipe friction and the Moody/Colebrook relation (Ch. 6), control-volume momentum and propeller/actuator-disk theory (Ch. 3, 11); J. D. Anderson, Fundamentals of Aerodynamics — wave/compressibility drag divergence (Ch. 5) for the Boeing 747 wind-tunnel chart used in Question 9.

Question 1: Absolute Pressure in a Pipe from a Multi-Fluid Manometer (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.

the recovered figure shows TWO U-tube manometers in series, but only the FIRST (left) loop, from the pipe down through water and mercury and up through glycerine to its own open vent, is needed to solve for P. The second loop's readings (323 mm, 30 mm) are additional figure detail, confirmed identical to 2016-May's own unused second-loop numbers, which is itself strong evidence the reconstruction is correct.

Given.

QuantityValue
Water column below the pipe (to the mercury surface)80 mm
Net mercury column (first loop)60 mm
Glycerine column (mercury surface up to the open vent)100 mm
SG glycerine / SG mercury (Constants, p.12)1.26 / 13.56
Atmospheric head (as instructed)10 m of water = 98.10 kPa
P water 80 mm datum (pipe C/L, 0 mm) mercury net 60 mm glycerine 100 mm open to atm. Fig. Q1 — first-loop path used to solve for P: water (80 mm) and net mercury (60 mm) down, glycerine (100 mm) up to atm.
Fig. Q1 — traced manometer path: water (80 mm) and mercury (60 mm net) below the pipe, glycerine (100 mm) up to the open, atmospheric top.

Find. The absolute pressure P in the pipe, in kPa.

Approach. Trace the pressure from the pipe, through each fluid layer of the first (left) loop, to the open (atmospheric) top of its right-hand leg — adding ρgh going down, subtracting going up — then add the given atmospheric head to convert the resulting gauge pressure to absolute.

  1. Set up the manometer equation (gauge, at the pipe). Starting at P and working down through water, down through the net mercury column, then up through glycerine to the open vent (gauge = 0 there): $$P + \rho_w g(0.080) + \rho_w g(0.060)\,\text{SG}_{Hg} - \rho_w g(0.100)\,\text{SG}_{gly} = 0$$
  2. Solve for the gauge pressure. $$P = \rho_w g\Big[(0.100)(1.26) - (0.080) - (0.060)(13.56)\Big]$$ $$P = 9810\big[0.1260 - 0.0800 - 0.8136\big] = 9810(-0.7676) = \boxed{-7.53\ \text{kPa (gauge)}}$$
  3. Convert to absolute using the given atmospheric head. $$P_{atm} = \rho_w g(10) = 1000(9.81)(10) = 98.10\ \text{kPa}$$ $$P_{abs} = P_{gauge} + P_{atm} = -7.53 + 98.10 = \boxed{90.57\ \text{kPa (absolute)}}$$
QuantityResult
Gauge pressure in the pipe−7.53 kPa
Absolute pressure in the pipe P90.57 kPa
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