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22-Mec-A6 Fluid Machinery · December 2017

Question 3 of 6: Head to Drive Flow Through an Annulus

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

Notes on this paper

National Exams — December 2017 · 16-Mec-A6 Advanced Fluid Mechanics · 3 hours, open book · six questions, each 20 marks (candidates answer any five; all six are worked here as a study resource).

Reference texts: J. D. Anderson, Modern Compressible Flow (3rd ed.); F. M. White, Fluid Mechanics (7th ed.); I. G. Currie, Fundamental Mechanics of Fluids; B. R. Munson et al., Fundamentals of Fluid Mechanics; Fox & McDonald, Introduction to Fluid Mechanics.

Question 3: Head to Drive Flow Through an Annulus (20 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.

Given data
Inner / outer radii$a=0.04$ m, $b=0.06$ m
Length$L=40$ m
Roughness (commercial steel)$e=0.046$ mm
Water$\rho=1000\ \text{kg/m}^3$, $\nu=1.02\times10^{-6}\ \text{m}^2/\text{s}$
Effective-diameter ratio$D_{\text{eff}}/D_h=0.670$
Target flow$Q=0.01\ \text{m}^3/\text{s}$

Find. The reservoir level $h$ (part a, entrance neglected) and the incremental effect of a sharp vs well-designed entrance (part b).

Approach. Get the mean velocity from continuity, form the hydraulic and effective diameters, obtain the friction factor from the Colebrook equation at the effective Reynolds number, then apply the steady-flow energy equation from the reservoir surface to the annulus exit.

  1. Mean velocity. The annular flow area and mean velocity are $$A=\pi(b^2-a^2)=\pi(0.06^2-0.04^2)=6.283\times10^{-3}\ \text{m}^2,\quad V=\frac{Q}{A}=\frac{0.01}{6.283\times10^{-3}}=1.592\ \text{m/s}.$$
  2. Hydraulic and effective diameters. For a concentric annulus $D_h=4A/P_{\text{wet}}=2(b-a)=0.040$ m, and the given ratio sets $D_{\text{eff}}=0.670\,D_h=0.0268$ m.
  3. Reynolds number and relative roughness. Using the effective diameter to enter the Moody/Colebrook chart (this accounts for the annular shape), $$Re_{\text{eff}}=\frac{V\,D_{\text{eff}}}{\nu}=\frac{1.592\times0.0268}{1.02\times10^{-6}}=4.18\times10^4,\qquad \frac{e}{D_h}=\frac{0.046\times10^{-3}}{0.040}=1.15\times10^{-3}.$$
  4. Friction factor (Colebrook). Solving $$\frac{1}{\sqrt{f}}=-2\log_{10}\!\left(\frac{e/D_h}{3.7}+\frac{2.51}{Re_{\text{eff}}\sqrt{f}}\right)\ \Rightarrow\ f=0.0250.$$
  5. Energy equation, reservoir surface to exit. With both ends at atmospheric pressure, the surface at rest and the exit carrying velocity $V$, neglecting entrance loss, $$h=\underbrace{\frac{V^2}{2g}}_{\text{exit KE}}+\underbrace{f\frac{L}{D_h}\frac{V^2}{2g}}_{\text{friction}}.$$ With $V^2/2g=0.129$ m and $f\,L/D_h=0.0250\times40/0.040=25.0$, $$\boxed{h=0.129+25.0\times0.129=0.129+3.23=3.36\ \text{m}.}$$
  6. (b) Entrance effect. A sharp-edged entrance adds $h_{\text{ent}}=K\,V^2/2g=0.5\times0.129=0.065$ m to the required level; a well-designed (rounded) entrance has $K\approx0.05$, adding only $\approx0.006$ m. Hence $$\boxed{\Delta h_{\text{sharp}}\approx0.065\ \text{m}\ (\sim2\%\text{ of }h),\quad \Delta h_{\text{rounded}}\approx0.006\ \text{m}.}$$ The entrance geometry matters little here because the 40 m of wall friction dominates the head budget.

Check: The effective-diameter method (Reynolds number on $D_{\text{eff}}$, roughness on $D_h$, head loss on $D_h$) gives $h=3.36$ m. Using the hydraulic diameter directly for the Reynolds number ($Re_{D_h}=6.24\times10^4$, $f=0.0238$) gives $h=3.20$ m — a 5% difference, within the accuracy of the noncircular-duct approximation.

Question 3 — results
QuantityResult
Mean velocity $V$1.592 m/s
$D_h$ / $D_{\text{eff}}$0.040 m / 0.0268 m
Friction factor $f$0.0250
Required reservoir level $h$ (a)3.36 m
Sharp-edge entrance penalty (b)+0.065 m (well-designed: +0.006 m)