Stokes flow (named after George Gabriel Stokes), also named creeping flow or creeping motion, is a type of fluid flow where advective inertial forces are small compared with viscous forces. The Reynolds number is low, i.e.
R
e
≪
1
{\displaystyle \mathrm {Re} \ll 1}
. This is a typical situation in flows where the fluid velocities are very slow, the viscosities are very large, or the length-scales of the flow are very small. Creeping flow was first studied to understand lubrication. In nature, this type of flow occurs in the swimming of microorganisms and sperm. In technology, it occurs in paint, MEMS devices, and in the flow of viscous polymers generally.
The equations of motion for Stokes flow, called the Stokes equations, are a linearization of the Navier–Stokes equations, and thus can be solved by a number of well-known methods for linear differential equations. The primary Green's function of Stokes flow is the Stokeslet, which is associated with a singular point force embedded in a Stokes flow. From its derivatives, other fundamental solutions can be obtained. The Stokeslet was first derived by Carl Wilhelm Oseen in 1927, although it was not named as such until 1953 by G. J. Hancock. The closed-form fundamental solutions for the generalized unsteady Stokes and Oseen flows associated with arbitrary time-dependent translational and rotational motions have been derived for the Newtonian and micropolar fluids.
Contents
Stokes equations
The equation of motion for Stokes flow can be obtained by linearizing the steady state Navier–Stokes equations. The inertial forces are assumed to be negligible in comparison to the viscous forces, and eliminating the inertial terms of the momentum balance in the Navier–Stokes equations reduces it to the momentum balance in the Stokes equations:
∇
⋅
σ
+
f
=
0
{\displaystyle {\boldsymbol {\nabla }}\cdot \sigma +\mathbf {f} ={\boldsymbol {0}}}
where
σ
{\displaystyle \sigma }
is the stress (sum of viscous and pressure stresses), and
f
{\displaystyle \mathbf {f} }
an applied body force. The full Stokes equations also include an equation for the conservation of mass, commonly written in the form:
∂
ρ
∂
t
+
∇
⋅
(
ρ
u
Properties
The Stokes equations represent a considerable simplification of the full Navier–Stokes equations, especially in the incompressible Newtonian case. They are the leading-order simplification of the full Navier–Stokes equations, valid in the distinguished limit
R
e
→
0.
{\displaystyle \mathrm {Re} \to 0.}
Instantaneity
A Stokes flow has no dependence on time other than through time-dependent boundary conditions. This means that, given the boundary conditions of a Stokes flow, the flow can be found without knowledge of the flow at any other time.
Time-reversibility
An immediate consequence of instantaneity, time-reversibility means that a time-reversed Stokes flow solves the same equations as the original Stokes flow. This property can sometimes be used (in conjunction with linearity and symmetry in the boundary conditions) to derive results about a flow without solving it fully. Time reversibility means that it is difficult to mix two fluids using creeping flow.
While these properties are true for incompressible Newtonian Stokes flows, the non-linear and sometimes time-dependent nature of non-Newtonian fluids means that they do not hold in the more general case.
An interesting property of Stokes flow is known as the Stokes' paradox: that there can be no Stokes flow of a fluid around a disk in two dimensions; or, equivalently, the fact there is no non-trivial solution for the Stokes equations around an infinitely long cylinder.
Demonstration of time-reversibility
A Taylor–Couette system can create laminar flows in which concentric cylinders of fluid move past each other in an apparent spiral. A fluid such as corn syrup with high viscosity fills the gap between two cylinders, with colored regions of the fluid visible through the transparent outer cylinder.
The cylinders are rotated relative to one another at a low speed, which together with the high viscosity of the fluid and thinness of the gap gives a low Reynolds number, so that the apparent mixing of colors is actually laminar and can then be reversed to approximately the initial state. This creates a dramatic demonstration of seemingly mixing a fluid and then unmixing it by reversing the direction of the mixer.
Incompressible flow of Newtonian fluids
In the common case of an incompressible Newtonian fluid, the Stokes equations take the (vectorized) form:
μ
∇
2
u
−
∇
p
+
f
=
0
∇
⋅
u
=
0
{\displaystyle {\begin{aligned}\mu \nabla ^{2}\mathbf {u} -{\boldsymbol {\nabla }}p+\mathbf {f} &={\boldsymbol {0}}\\{\boldsymbol {\nabla }}\cdot \mathbf {u} &=0\end{aligned}}}
where
u
{\displaystyle \mathbf {u} }
is the velocity of the fluid,
∇
p
{\displaystyle {\boldsymbol {\nabla }}p}
is the gradient of the pressure,
μ
{\displaystyle \mu }
Cartesian coordinates
With the velocity vector expanded as
u
=
(
u
,
v
,
w
)
{\displaystyle \mathbf {u} =(u,v,w)}
and similarly the body force vector
f
=
(
f
x
,
f
y
,
f
z
)
{\displaystyle \mathbf {f} =(f_{x},f_{y},f_{z})}
, we may write the vector equation explicitly,
μ
(
∂
2
u
∂
x
2
Methods of solution
The equation for an incompressible Newtonian Stokes flow can be solved by the stream function method in planar or in 3-D axisymmetric cases
The linearity of the Stokes equations in the case of an incompressible Newtonian fluid means that a Green's function,
J
(
r
)
{\displaystyle \mathbb {J} (\mathbf {r} )}
, exists. The Green's function is found by solving the Stokes equations with the forcing term replaced by a point force acting at the origin, and boundary conditions vanishing at infinity:
μ
∇
2
u
−
∇
p
=
−
F
⋅
δ
(
r
)
∇
⋅
u
=
0
|
Some geometries
Hele-Shaw flow
Hele-Shaw flow is an example of a geometry for which inertia forces are negligible. It is defined by two parallel plates arranged very close together with the space between the plates occupied partly by fluid and partly by obstacles in the form of cylinders with generators normal to the plates.
Slender-body theory
Slender-body theory in Stokes flow is a simple approximate method of determining the irrotational flow field around bodies whose length is large compared with their width. The basis of the method is to choose a distribution of flow singularities along a line (since the body is slender) so that their irrotational flow in combination with a uniform stream approximately satisfies the zero normal velocity condition.
Spherical coordinates
Horace Lamb's general solution arises from the fact that the pressure
p
{\displaystyle p}
satisfies the Laplace equation, and can be expanded in a series of solid spherical harmonics in spherical coordinates. As a result, the solution to the Stokes equations can be written:
u
=
∑
n
=
−
∞
,
n
≠
−
1
n
=
∞
[
(
n
+
3
)
r
2
∇
p
n
2
μ
(
n
Theorems
Stokes solution and related Helmholtz theorem
The drag resistance to a moving sphere, also known as Stokes' solution, is here summarised. Given a sphere of radius
a
{\displaystyle a}
, travelling at velocity
U
{\displaystyle U}
, in a Stokes fluid with dynamic viscosity
μ
{\displaystyle \mu }
, the drag force
F
D
{\displaystyle F_{D}}
is given by:
F
D
=
6
π
μ
a
U
{\displaystyle F_{D}=6\pi \mu aU}
The Stokes solution dissipates less energy than any other solenoidal vector field with the same boundary velocities: this is known as the Helmholtz minimum dissipation theorem.
Lorentz reciprocal theorem
The Lorentz reciprocal theorem states a relationship between two Stokes flows in the same region. Consider fluid filled region
V
{\displaystyle V}
bounded by surface
S
{\displaystyle S}
. Let the velocity fields
u
{\displaystyle \mathbf {u} }
and
u
′
{\displaystyle \mathbf {u} '}
solve the Stokes equations in the domain
V
{\displaystyle V}
, each with corresponding stress fields
σ
{\displaystyle \mathbf {\sigma } }
and
σ
′
{\displaystyle \mathbf {\sigma } '}
. Then the following equality holds:
∫
S
u
⋅
Faxén's laws
Faxén's laws are direct relations that express the multipole moments in terms of the ambient flow and its derivatives. First developed by Hilding Faxén to calculate the force,
F
{\displaystyle \mathbf {F} }
, and torque,
T
{\displaystyle \mathbf {T} }
on a sphere, they take the following form:
F
=
6
π
μ
a
(
1
+
a
2
6
∇
2
)
v
∞
(
x
)
|
x
=
0
−
6