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22-Mec-A6 Fluid Machinery · December 2018

Question 3 of 6: Laminar Draining of an Oil Tank

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

Notes on this paper

Paper format. National Exams — December 2018, 16-Mec-A6 Advanced Fluid Mechanics. Open book, 3 hours. Six questions of equal value (20 marks); any five constitute a complete paper. All six are solved here.

Reference texts. J.D. Anderson, Modern Compressible Flow, 3rd ed. (Q1); F.M. White, Fluid Mechanics, 8th ed. and Kundu, Cohen & Dowling, Fluid Mechanics, 6th ed. (Q2, Q5); F.M. White, Viscous Fluid Flow, 3rd ed. (Q3, Q4, Q6); Schlichting & Gersten, Boundary-Layer Theory, 8th ed. (Q6); Fox & McDonald, Introduction to Fluid Mechanics, 10th ed. (general).

Question 3: Laminar Draining of an Oil Tank (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. Steady gravity-driven discharge from a large tank through a horizontal pipe; the tank surface is atmospheric and effectively at rest, the pipe exit is atmospheric.

Given data
Specific gravity / density$SG=0.9$, $\rho = 900\ \text{kg/m}^3$
Volume flow$Q = 1.0\ \text{m}^3/\text{h} = 2.78\times10^{-4}\ \text{m}^3/\text{s}$
Pipe diameter$D = 1.3\ \text{cm} = 0.013\ \text{m}$
Pipe length$L = 2\ \text{m}$
Oil depth (driving head)$h = 3\ \text{m}$

Find. (a) the pipe head loss $h_f$; (b) the kinematic viscosity $\nu$; (c) whether the flow is laminar.

oil Q h = 3 m L = 2 m D = 1.3 cm
Figure 3. Oil drains from a large tank through a horizontal pipe; the depth $h$ is the driving head.

Approach. Apply the energy equation from the (still) oil surface to the pipe exit to get the head loss, assume the pipe flow is laminar (Hagen–Poiseuille) to back out the viscosity, then confirm the assumption with the Reynolds number.

  1. Mean pipe velocity. With $A=\tfrac{\pi}{4}D^2 = 1.327\times10^{-4}\ \text{m}^2$, $$V=\frac{Q}{A}=\frac{2.78\times10^{-4}}{1.327\times10^{-4}}=2.09\ \text{m/s}.$$
  2. (a) Head loss. Energy from surface (1, at rest, elevation $h$) to exit (2, velocity $V$, datum), both atmospheric: $$h = \frac{V^{2}}{2g}+h_f \;\Rightarrow\; h_f = h-\frac{V^{2}}{2g}=3-\frac{2.09^{2}}{2(9.81)}.$$ $$\boxed{h_f = 2.78\ \text{m}.}$$
  3. (b) Kinematic viscosity. Assume fully-developed laminar flow, for which $h_f = \dfrac{32\,\mu L V}{\rho g D^{2}}$. Solving for $\mu$ and dividing by $\rho$: $$\mu = \frac{h_f\,\rho g D^{2}}{32 L V}=0.0309\ \text{Pa}\cdot\text{s}, \qquad \boxed{\nu=\frac{\mu}{\rho}=3.44\times10^{-5}\ \text{m}^2/\text{s}.}$$
  4. (c) Laminar? Check the Reynolds number: $$Re=\frac{VD}{\nu}=\frac{(2.09)(0.013)}{3.44\times10^{-5}}=792 .$$ Since $Re = 792 \lt 2300$, the flow is $\boxed{\text{laminar}}$, consistent with the Hagen–Poiseuille assumption used in (b).
Question 3 — results
QuantityValue
Mean velocity $V$$2.09\ \text{m/s}$
Head loss $h_f$$2.78\ \text{m}$
Dynamic viscosity $\mu$$0.0309\ \text{Pa}\cdot\text{s}$
Kinematic viscosity $\nu$$3.44\times10^{-5}\ \text{m}^2/\text{s}$
Reynolds number $Re$$792$ ⇒ laminar