NivaarExam PrepOfficial exam papers ↗

04-BS-7: May 2017

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

  1. Question 1 Capillary Rise in a Rectangular Channel
  2. Question 2 Reservoir Flip-Gate — Open or Remain Closed?
  3. Question 3 Helium Balloon — Mass and Altitude Volume Change
  4. Question 4 VDI Orifice Meter — Differential Pressure Reading
  5. Question 5 Hydraulic Jump — Flow Rate from Depths
  6. Question 6 Hydraulic Jump — Head, Energy and Power Loss
  7. Question 7 Head Loss in a Rectangular Ventilation Duct
  8. Question 8 CANDU Fuel Bundle — Coolant Pressure Drop
  9. Question 9 Falling-Sphere Viscometer — Oil Viscosity
  10. Question 10 Significance of the Laminar Sublayer
  11. Question 11 Floating Square Bar — Stable Orientation
  12. Question 12 Duct Bend Head Loss — Orientation of a Rectangular Bend
  13. Question 13 Barge Passing Over an Aqueduct — Change in Pillar Load

Start with Question 1 →

04-BS-7 Mechanics of Fluids — National Examination, 2017-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 capillarity (Ch. 2), integral analysis and buoyancy (Ch. 3), viscous flow in ducts, pipe friction and the Moody chart (Ch. 6), flow past immersed bodies and drag (Ch. 7), open-channel flow and the hydraulic jump (Ch. 10).

Check — assumptions used across this paper:
  • Q2's figure shows the vertical leaf of the gate rising above the free surface, so water acts over the full depth x = 2.0 m; both "0.3 m" dimensions locate the centre of gravity (0.3 m right of the vertical leaf, 0.3 m above the arm). Reservoir water also fills the space beneath the 1.2 m arm (the vertical lines below O are dimension extension lines, not a wall), so the arm carries uplift at pressure ρgx, and the arm tip bears up against a lip on the spillway crest — the gate can only open by rotating clockwise, vertical leaf toward the spillway.
  • Q4's flow coefficient K ≈ 0.69 is read from the attached VDI chart on the Do/D1 = 0.50 curve (third from the top, the one that levels off at 0.62) at the approach Reynolds number R ≈ 2550. The printed curve gives 0.695 at R = 2000 and 0.684 at R = 3000; a reading of 0.68–0.70 moves the answer by only ±0.3 kPa.
  • Q7 and Q8 friction factors are obtained from the Colebrook–White/Haaland equation the Moody chart itself plots (smooth-wall case, as both problems specify or imply smooth surfaces).
  • Q9's sphere drag coefficient vs. Reynolds number is obtained from the Schiller–Naumann correlation $C_D=\tfrac{24}{Re}\left(1+0.15\,Re^{0.687}\right)$, which reproduces the published sphere-drag curve (the same curve reprinted in the attachment) to within a few percent for $Re<1000$ — used here because the resulting Reynolds number (≈19–20) is well above the range where the simple Stokes'-law formula ($C_D=24/Re$) alone is valid.