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04-BS-7 · May 2018

Question 2 of 13: Crosby Gauge Tester — Percent Error

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

Notes on this paper

04-BS-7 Mechanics of Fluids — National Examination, 2018-May. Three (3) hours duration, closed book. Section A (Calculative, 9 questions, do 7) and Section B (Graphical & Analytical, 4 questions, do 3); every question is answered below regardless of the exam's "do N of M" instruction, so the set is a complete study resource.

Reference texts: White, F.M., Fluid Mechanics (8th ed.) — fluid statics and manometry (Ch. 2), Bernoulli and the energy equation (Ch. 3), viscous flow in ducts and the Moody chart (Ch. 6), flow past immersed bodies and drag (Ch. 7), potential flow and the Magnus effect (Ch. 8), open-channel flow and the hydraulic jump (Ch. 10), turbomachinery and jet propulsion (Ch. 11).

Check — assumptions used across this paper:
  • Q1's manometer chain is read off the extraction as a two-stage water–mercury–glycerine–(air)–glycerine–mercury system. The enclosed air pocket between the two glycerine columns is treated as weightless (uniform pressure), so only the one described open end is needed to close the hydrostatic chain back to pipe P; the second "opening" is not load-bearing for this calculation.
  • Q5's wave/hydraulic-jump analysis takes the depth "in front of the wave" (0.15 m, undisturbed, at rest) as the upstream state and "behind the wave" (0.75 m) as the downstream state, per the question's own prose (the raw figure-label ordering in the extraction is a reconstruction and is not used to override the stated text). The classic hydraulic-jump head-loss formula is applied to the given depths, and the swept flow rate uses the measured wave celerity directly — a standard engineering estimate, not a fully momentum-self-consistent bore solution.
  • Q6's air properties are taken at 20°C (domestic ambient, ρ=1.19 kg/m³) since no duct-air temperature is stated.
  • Q7(c)'s "discharged at right angles to the initial direction (20° becomes 0°)" is read as: the reverser's exhaust jet is normally angled 20° forward of the fully-radial (right-angle) direction; part (c) removes that forward lean entirely, leaving a purely radial (90° to the engine axis) discharge with zero axial velocity component.
  • Q8's terminal velocity and Q9's cable drag coefficient are obtained from the Reynolds-number relations the attached charts themselves plot (Morrison's sphere-drag correlation for Q8; the flat subcritical Cd≈1.2 plateau of the smooth-cylinder curve for Q9, since Re≈3×104 falls solidly within it).

Question 2: Crosby Gauge Tester — Percent Error (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
Piston diameter, $D$25 mm
Total mass (weights + piston), $m$9 kg
Gauge reading under test179 kPa
weights piston, D=25 mm Oil gauge Air
Crosby gauge tester: dead weights on a piston set the reference pressure transmitted through oil to the gauge under test.

Find. Actual pressure at the gauge and the percent error of the 179 kPa reading.

Approach. The piston is in static equilibrium: the weight of the dead-load stack is balanced by the pressure force on the piston area, giving the true reference pressure directly.

  1. Piston area. $$A=\frac{\pi}{4}D^2=\frac{\pi}{4}(0.025)^2=4.909\times10^{-4}\ \text{m}^2$$
  2. True (actual) pressure from force balance. $$P_{actual}=\frac{mg}{A}=\frac{(9)(9.81)}{4.909\times10^{-4}}=\boxed{179{,}863\ \text{Pa}\approx179.9\ \text{kPa}}$$
  3. Percent error of the tested gauge. $$\%\,\text{error}=\frac{P_{gauge}-P_{actual}}{P_{actual}}\times100=\frac{179-179.9}{179.9}\times100=\boxed{-0.48\%}$$
QuantityValue
Piston area4.909×10⁻&sup4; m²
True pressure at gauge179.9 kPa
Gauge percent error−0.48% (reads low)