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Stokes' law calculator

Estimate terminal settling or rising speed for a small rigid sphere in a Newtonian fluid.

Calculator

Terminal velocity, downward positive
0.00054481
Particle diameter
0.001
Dynamic viscosity (Pa s)
1.00000000
Dynamic viscosity (cP)
1,000.00000000
Particle density
2,000
Medium density
1,000
Gravity
9.80665
Particle Reynolds number
0.00054481
Drag magnitude at terminal speed
0.00000513
Creeping-flow check
Creeping-flow estimate is plausible

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How this calculator works

At terminal speed, gravity minus buoyancy balances the Stokes drag on a sphere. A denser particle settles, while a lighter particle rises; downward velocity is positive here. Stokes drag assumes a rigid isolated sphere, a Newtonian fluid, negligible wall effects and a particle Reynolds number much smaller than one. A numerical result does not establish those assumptions, so the output includes a Reynolds check. It does not model the time needed to reach terminal speed.

Formula

F_drag = 3 pi mu d abs(v); v_terminal = g(rho_particle-rho_medium)d^2/(18 mu); Re_particle = rho_medium abs(v)d/mu.

Worked example

With g = 10 m/s2, density difference 1000 kg/m3, diameter 0.001 m and viscosity 1 Pa s, terminal speed is 0.000555556 m/s downward. Halving diameter reduces it to 0.000138889 m/s.

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Frequently asked questions

Can the terminal velocity be negative?

Yes. A particle less dense than its medium rises, which is negative under the downward-positive convention.

Why include Reynolds number?

The Stokes relation becomes inaccurate when inertial effects are no longer negligible.

Does this work for bubbles?

A mobile bubble interface has different drag. This model assumes a rigid no-slip sphere.

Sources

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