Stokes’ law describes the size of the drag force D
at low Reynolds numberRe≪1
experienced by a spherical object in a steady, uniform flow at velocity U.
Flow field
Imagine a sphere with radius a sinking in a viscous liquid.
To model this situation, let us pretend that the sphere is fixed instead,
and the fluid comes from infinity at velocity U along the z-axis,
flows past the sphere, and continues to infinity at the same U.
The Reynolds number is:
Re=ν2aU
We assume that Re≪1, in which case
the incompressible Navier-Stokes equations
are reduced to the steady Stokes equations:
∇p=η∇2v∇⋅v=0
The goal is to solve for p and v.
We make the following ansatz in
spherical coordinates(r,θ,ϕ),
where q(r), f(r) and g(r) are unknown functions:
p=ηUq(r)cosθvr=Uf(r)cosθvθ=−Ug(r)sinθvϕ=0
The fluid hits the sphere head on,
so the solution is taken to be ϕ-independent due to symmetry.
Note that θ is the angle to the positive z-axis,
which is the direction of U=Ue^z.
Moreover, note that U⋅e^r=Ucosθ
and U⋅e^θ=−Usinθ,
where e^r and e^θ are basis vectors.
To begin with, we insert this ansatz into the incompressibility condition,
yielding:
Substituting g for the expression we found from incompressibility lets us simplify this:
η(∇2v)r=ηU(dr2d2f+r4drdf)cosθ
The Stokes equation says that this must be equal to the r-component of ∇p:
ηU(dr2d2f+r4drdf)cosθ=ηU(−r32C3+C4)cosθ
Where we have inserted dq/dr.
Dividing out ηUcosθ leaves an ODE for f(r),
satisfied by:
f(r)=C1+r3C2+rC3+10C4r2
Then, thanks to our earlier relation again,
we know that g(r) is as follows:
g(r)=C1−2r3C2+2rC3+5C4r2
So what about C1, C2, C3 and C4?
For r→∞, we expect that v→U,
meaning that f(r)→1 and g(r)→1.
This implies that C4=0 and C1=1, leaving:
f(r)=1+r3C2+rC3g(r)=1−2r3C2+2rC3
Furthermore, the viscous no-slip condition demands
that v=0 at the sphere’s surface r=a, so f(a)=g(a)=0 there.
Inserting a into f and g, setting them to zero,
and solving the resulting system of equations
yields C2=a3/2 and C3=−3a/2.
Therefore the full solution is:
From the definition of viscosity,
we know that there must be shear stresses at the sphere surface,
described by the fluid’s Cauchy stress tensorσ^.
The drag force D on the surface is:
D=∮σ^⋅dS=∫02π∫0π(σ^⋅e^r)a2sinθdθdϕ
Where e^r is the sphere’s surface normal vector.
The integrand can be expanded as follows:
σ^⋅e^r=e^rσrr+e^θσθr
To calculate this, we start by taking the gradient of the velocity field v:
Remarkably, the stress at every point on the sphere is purely in the z-direction!
This is not entirely unexpected though: symmetry cancels out all other components.
With this, we can do the integrals for D,
which reduce to a surface area factor 4πa2:
At last, we arrive at Stokes’ law,
which simply expresses the magnitude of D:
D=6πηUa
To arrive at this result,
we assumed that the sphere was fixed, and the fluid was flowing past it.
We can equally well let the fluid be at rest,
with the sphere falling through it at U.
The force of gravity then exerts the following force G on it,
subtracting buoyancy:
G=34πa3(ρs−ρf)g0
Where ρs and ρf are the sphere’s and fluid’s densities,
and g0 is the gravitational acceleration.
Since D acts in the opposite sense of G,
after some time, they cancel out:
6πηUa=34πa3(ρs−ρf)g0
This is an equation for the terminal velocityUt,
which we find to be as follows:
Ut=9η2a2(ρs−ρf)g0
The falling sphere will accelerate until Ut,
and then continue falling at constant speed.
References
B. Lautrup,
Physics of continuous matter: exotic and everyday phenomena in the macroscopic world, 2nd edition,
CRC Press.