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22-Mec-B6 Advanced Fluid Mechanics · December 2013

Question 4 of 7: Question 4 (Part A, Question A4): Glycerol in a Rotating Beaker — Pressure on the Base and the Shape of the Free Surface

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

Notes on this paper

Paper format. National Exams, December 2013 — 07-Mec-B6 Advanced Fluid Mechanics. Three hours, open book, any non-communicating calculator permitted. Part A holds four questions weighted 16 marks each (48 per cent of the paper) and Part B three questions weighted 26 marks each (52 per cent); the candidate answers any three in Part A and any two in Part B. All seven questions are worked here. The paper supplies a four-page aid sheet (compressible-flow and shock relations, the boundary-layer integral equations, the Navier–Stokes equations in Cartesian and cylindrical-polar form, and the potential-flow stream and potential functions); every relation quoted below is taken from that sheet, so the arithmetic matches what a candidate had in front of them.

Reference texts.

Conventions used throughout. Air is treated as a perfect gas with γ = 1.4 and R = 287 J/kg·K except where a question names another gas. Pressure conversions use 1 mm Hg = 133.322 Pa and 1 mm H2O = 9.80665 Pa. Compressible-flow ratios are evaluated from the closed-form aid-sheet relations rather than read off a table, so the third significant figure is exact rather than interpolated.

Question 4 (Part A, Question A4): Glycerol in a Rotating Beaker — Pressure on the Base and the Shape of the Free Surface (16 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.

QuantitySymbolValue
Internal diameter / radiusD, R5 cm, R = 0.025 m
Densityρ1260 kg/m3
Dynamic viscosityμ1.49 Pa·s
Rotation rateω120 rpm = 12.566 rad/s
Fluid depth on the axish03 cm = 0.030 m
Velocity fieldur, uθ, uz0, ωr, 0
Gravityg9.81 m/s2

Find. The pressure distribution over the base of the beaker, the equation of the free surface, and the maximum fluid elevation (at the wall).

zω = 120 rpm = 12.566 rad/srh0 = 3 cmΔz = 5.03 mmD = 5 cm (R = 2.5 cm)g9.81 m/s2Glycerol, ρ = 1260 kg/m3, μ = 1.49 Pa·ssteady solid-body rotation, uθ = ωr
Figure A4 — The rotating beaker at steady state. The free surface is a paraboloid pinned at 3 cm on the axis and rising 5.03 mm at the wall; the figure is drawn to true scale in both directions.

Approach. Substitute the stated rigid-body velocity field into the cylindrical-polar momentum equations from the aid sheet. Every viscous term vanishes because rigid-body rotation has no rate of strain, leaving a two-dimensional hydrostatic balance whose integration gives the pressure field directly; the free surface is then the isobar $P=P_{\text{atm}}$.

  1. Reduce the momentum equations to two ordinary derivatives of pressure. With $u_r=u_z=0$, $u_\theta=\omega r$ and no dependence on $\theta$ or $t$, every convective term except the centripetal one disappears. Crucially the viscous stresses vanish too: the aid sheet gives $\tau_{r\theta}=\mu\left[r\,\partial(u_\theta/r)/\partial r+r^{-1}\partial u_r/\partial\theta\right]$, and since $u_\theta/r=\omega$ is a constant, $\tau_{r\theta}=0$. Rigid-body rotation deforms no fluid element, so the viscosity plays no part in the final answer. The r- and z-momentum equations collapse to $$\begin{aligned} -\rho\frac{u_\theta^{2}}{r}&=-\frac{\partial P}{\partial r} \;\;\Rightarrow\;\; \frac{\partial P}{\partial r}=\rho\omega^{2}r\\ 0&=-\frac{\partial P}{\partial z}-\rho g \;\;\Rightarrow\;\; \frac{\partial P}{\partial z}=-\rho g \end{aligned}$$
  2. Integrate to the general pressure field. The two partial derivatives are each functions of one variable only, so the field integrates immediately: $$\boxed{\ P(r,z)=\frac{\rho\omega^{2}r^{2}}{2}-\rho g z+C\ }$$ The constant is fixed by the one point whose pressure and position we know: on the axis at the free surface, $r=0$ and $z=h_0$, where $P=P_{\text{atm}}$. Hence $C=P_{\text{atm}}+\rho g h_0$ and $$P(r,z)=P_{\text{atm}}+\rho g\left(h_0-z\right)+\frac{\rho\omega^{2}r^{2}}{2}.$$
  3. Evaluate the pressure along the bottom of the beaker. Setting $z=0$, $$P(r,0)=P_{\text{atm}}+\rho g h_0+\frac{\rho\omega^{2}r^{2}}{2} =P_{\text{atm}}+370.8+9948.6\,r^{2}\ \ \text{Pa}\quad(r\ \text{in m}),$$ using $\rho g h_0=1260\times9.81\times0.030=370.8\ \text{Pa}$ and $\rho\omega^{2}/2=1260\times157.914/2=99\,486\ \text{Pa/m}^{2}$. In gauge terms the base pressure rises parabolically from 370.8 Pa on the axis to $$P_{\text{gauge}}(R)=370.8+\tfrac{1}{2}\times1260\times157.914\times0.025^{2} =370.8+62.2=433.0\ \text{Pa}$$ at the wall — a 17 per cent increase across the base.
  4. Obtain the free surface as the atmospheric isobar. The free surface is the locus of $P=P_{\text{atm}}$. Putting that into the pressure field and solving for $z$, $$\boxed{\ z_s(r)=h_0+\frac{\omega^{2}r^{2}}{2g}\ }$$ a paraboloid of revolution. Numerically $\omega^{2}/2g=157.914/19.62=8.049\ \text{m}^{-1}$, so $$z_s(r)=0.030+8.049\,r^{2}\ \ \text{m}.$$ The surface is independent of density — the same paraboloid would form in water or in mercury — because both the centrifugal and gravitational terms carry one factor of ρ.
  5. Compute the maximum fluid elevation. The highest point is at the wall, $r=R=0.025\ \text{m}$: $$z_{\max}=0.030+8.049\times(0.025)^{2}=0.030+0.005030,$$ so $$\boxed{\ z_{\max}=0.03503\ \text{m}=35.0\ \text{mm}\ }$$ The surface climbs 5.03 mm above the centre, and the total rise from axis to wall, $\omega^{2}R^{2}/2g$, is exactly the velocity head $u_\theta^{2}(R)/2g$ of the rim — a useful sanity check.
  6. Confirm the physical assumptions hold. Two are worth testing. First, the rotational Reynolds number is $\text{Re}=\rho\omega R^{2}/\mu=1260\times12.566\times0.025^{2}/1.49=6.6$, so the flow is deep in the creeping regime and no secondary circulation or turbulence disturbs the rigid-body state. Second, the spin-up time scales as $R^{2}/\nu$ with $\nu=\mu/\rho=1.18\times10^{-3}\ \text{m}^{2}/\text{s}$, giving $0.025^{2}/1.18\times10^{-3}\approx0.53\ \text{s}$: the "initial start-up period" mentioned in the question is well under a second for a liquid this viscous, so steady state is reached almost at once. Finally the surface never spills or exposes the base, since the total rise is only 5 mm on a 30 mm depth.
QuantityResult
General pressure fieldP(r, z) = Patm + ρg(h0 − z) + ρω2r2/2
Pressure along the base (z = 0), gaugeP = 370.8 + 99 486 r2 Pa (r in m)
Base gauge pressure on the axis / at the wall370.8 Pa / 433.0 Pa
Free-surface equationzs(r) = 0.030 + 8.049 r2 m
Rise from axis to wallω2R2/2g = 5.03 mm
Maximum fluid elevationzmax = 35.0 mm at r = R
Rotational Reynolds number (check)Re = ρωR2/μ = 6.6 (creeping)