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Two-Layer Torricelli

Irodov 1.318DifficultyDifficulty 2 of 5UniquenessUniqueness 3 of 5

Problem Irodov 1.318

A wide vessel contains a layer of water of thickness h1=30h_1 = 30 cm at the bottom, topped by a layer of kerosene of thickness h2=20h_2 = 20 cm, with a small hole pierced in the base. Neglecting viscosity, find the speed of the water jet leaving the hole.

Water below, kerosene floating above it, draining through a small hole in the base.

Water below, kerosene floating above it, draining through a small hole in the base.

Given
  • h1=30h_1 = 30 cm
  • h2=20h_2 = 20 cm
Find
Find vv, the velocity of the water jet leaving the hole in the bottom

Solution

Step 1Pressure at the hole from the two overlying layers

The vessel is wide, so the free surface sinks negligibly slowly and the liquid above the hole is, at every instant, very nearly in hydrostatic equilibrium. Building the pressure up from the free surface (atmospheric, p0p_0) through the kerosene layer and then the water layer down to the hole gives

phole=p0+ρ2gh2+ρ1gh1.(1) p_{\text{hole}} = p_0 + \rho_2 g h_2 + \rho_1 g h_1. \tag{1}
Step 2Bernoulli in the water, from the hole to the open jet

Follow a streamline in the water from a point at the hole’s level, where the water is essentially at rest at pressure pholep_{\text{hole}}, out to the free jet just outside, at atmospheric pressure p0p_0 and exit speed vv. With negligible height change at the hole itself, Bernoulli’s equation along this streamline gives

phole=p0+12ρ1v2.(2) p_{\text{hole}} = p_0 + \frac{1}{2}\rho_1 v^2. \tag{2}
Step 3Combine and solve for vv

Substituting the pressure (1) into the Bernoulli relation (2) equates the two expressions for pholep_{\text{hole}}; dividing through by 12ρ1\frac{1}{2}\rho_1 then isolates v2v^2.

ρ2gh2+ρ1gh1=12ρ1v2v2=2ρ1(ρ2gh2+ρ1gh1)=2g(h1+h2ρ2ρ1).\begin{align*}\rho_2 g h_2 + \rho_1 g h_1 &= \frac{1}{2}\rho_1 v^2 \\ v^2 &= \frac{2}{\rho_1}\left(\rho_2 g h_2 + \rho_1 g h_1\right) \\ &= 2g\left(h_1 + h_2\frac{\rho_2}{\rho_1}\right).\end{align*}

Taking the square root gives the exit speed.

v=2g(h1+h2ρ2ρ1)v = \sqrt{2g\left(h_1+h_2\dfrac{\rho_2}{\rho_1}\right)}
(3)
Step 4Evaluate

With ρ1=1.00×103\rho_1 = 1.00\times10^3 kg/m3^3 (water) and ρ2=0.80×103\rho_2 = 0.80\times10^3 kg/m3^3 (kerosene),

v=2(9.8)(0.30+0.20×0.8)=19.6×0.46 m/s.v = \sqrt{2(9.8)\left(0.30 + 0.20\times0.8\right)} = \sqrt{19.6\times0.46} \text{ m/s}.
v=2g(h1+h2ρ2ρ1)≈3.0 m/sv = \sqrt{2g\left(h_1+h_2\dfrac{\rho_2}{\rho_1}\right)} \approx 3.0\ \text{m/s}
(4)
Check

With no kerosene at all (h2=0h_2=0) the result collapses to v=2gh1v=\sqrt{2gh_1}, the ordinary Torricelli speed for a single liquid, exactly as it should: the second layer only matters through the extra pressure its weight adds.

Remark

The kerosene layer enters only through h2ρ2/ρ1h_2\rho_2/\rho_1: it behaves exactly like an extra h2ρ2/ρ1h_2\rho_2/\rho_1 of water stacked on top, an equivalent head that any immiscible layer above the hole can be converted to before summing. Stack a third, fourth liquid on top and the same trick just adds one more term, each layer’s own thickness rescaled by its density ratio to the flowing fluid.