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Draining Uphill Against Its Own Spin

Irodov 1.324DifficultyDifficulty 4 of 5UniquenessUniqueness 4 of 5

Problem Irodov 1.324

A narrow tube ABAB of length ll lies horizontally and spins at a constant angular velocity ω\omega about a fixed vertical axis passing through its own end AA. The tube is filled with an ideal (incompressible, inviscid) fluid. The end AA is open to the atmosphere; the opposite end BB is closed except for a very small orifice, through which fluid escapes as the tube spins. At some instant a column of fluid of length hh remains inside the tube, occupying the stretch adjacent to the closed end BB (so the fluid’s own free surface, facing the open end AA, sits a distance l−hl-h from the axis). Find the fluid’s speed relative to the tube, as a function of hh.

Side elevation of the tube AB, spinning at ω about the dashed axis through A. The shaded length h next to the closed end B is the fluid that remains, spraying from the orifice at B.

Side elevation of the tube ABAB, spinning at ω\omega about the dashed axis through AA. The shaded length hh next to the closed end BB is the fluid that remains, spraying from the orifice at BB.

Given
  • ll
  • ω\omega
  • hh (remaining fluid column, measured from BB)
Find
The fluid’s speed vv relative to the tube

Solution

Step 1Work in the tube’s own rotating frame

In the frame that spins with the tube, every fluid element also feels a centrifugal force per unit volume ρω2r\rho\omega^2 r directed outward along the tube, where rr is the distance from the axis at AA. This is a conservative force with potential energy per unit volume −ρω2r2/2-\rho\omega^2r^2/2 (minus its gradient is exactly that outward force), so Bernoulli’s equation applies along the tube in this frame with that potential added in.

p+12ρvrel2−12ρω2r2=constp+\dfrac{1}{2}\rho v_{\text{rel}}^2-\dfrac{1}{2}\rho\omega^2 r^2 = \text{const}
(1)
Step 2Identify the two ends of the streamline

The fluid’s own free surface sits at r=l−hr=l-h (the boundary between fluid and the open air stretching back to AA), where the pressure is atmospheric, p=p0p=p_0, and the relative speed is negligible: the orifice at BB is very small compared with the tube’s own bore, so the free surface retreats far more slowly than the fluid escapes through it, exactly as in a draining vessel with s≪Ss\ll S. At the orifice, r=lr=l, the fluid discharges directly into the atmosphere, so p=p0p=p_0 there too, with relative speed vv, the quantity sought.

Step 3Apply the rotating-frame Bernoulli equation between the two ends

Evaluating (1) at r=l−hr=l-h (surface) and at r=lr=l (orifice) and equating, the atmospheric pressure p0p_0 cancels from both sides:

p0+0−12ρω2(l−h)2=p0+12ρv2−12ρω2l212ω2l2−12ω2(l−h)2=12v2\begin{align*}p_0+0-\frac{1}{2}\rho\omega^2(l-h)^2 &= p_0+\frac{1}{2}\rho v^2-\frac{1}{2}\rho\omega^2 l^2 \\ \frac{1}{2}\omega^2 l^2-\frac{1}{2}\omega^2(l-h)^2 &= \frac{1}{2}v^2\end{align*}
v2=ω2[l2−(l−h)2]v^2 = \omega^2\left[l^2-(l-h)^2\right]
(2)
Step 4Simplify the bracket

Expanding the difference of squares in (2),

l2−(l−h)2=l2−(l2−2lh+h2)=h(2l−h),l^2-(l-h)^2 = l^2-\left(l^2-2lh+h^2\right) = h(2l-h),

so

v2=ω2h(2l−h)=ω2h2(2lh−1).v^2 = \omega^2 h(2l-h) = \omega^2 h^2\left(\frac{2l}{h}-1\right).
v=ωh2lh−1v = \omega h\sqrt{\dfrac{2l}{h}-1}
(3)
Check

At h=lh=l (the tube still full) the free surface sits on the axis itself, where the centrifugal potential vanishes, so the fluid falls through the whole centrifugal head ω2l2/2\omega^2l^2/2 and the bracket duly gives v=ωl2−1=ωlv=\omega l\sqrt{2-1}=\omega l. That this matches the tube’s tip speed is a coincidence of magnitude: vv is measured relative to the tube and points along it, whereas the tip speed is absolute and tangential (in the laboratory the fluid leaving at h=lh=l moves at 2 ωl\sqrt{2}\,\omega l, the resultant of the two). As h→0h\to0 (the tube nearly empty), v→0v\to0: with almost nothing left near BB, there is almost no column length for the centrifugal effect to accelerate.

Remark

The result depends on hh through l2−(l−h)2l^2-(l-h)^2, the difference of the squared distances of the two ends of the fluid column from the axis, not through hh alone: draining is driven by centrifugal potential, which goes as r2r^2, so a short column near the rim (h≪lh\ll l) feels a much stronger effective gravity than the same length hh would near the axis. This is the same r2r^2 structure that makes a centrifuge so much more effective at separation than ordinary settling under gravity.