MA3D1 – Fluid Dynamics and MA4L0 – Advanced Topics in Fluids Lecture notes

Chapter 9 Stokes Flow

In this chapter, we will be considering situations where inertial forces are negligible such that the flows have small Reynolds numbers. Such flows are named Stokes flows after George G. Stokes who first calculated the drag on a sphere moving through a viscous fluid. The applications of Stokes flows are wide ranging, from biological applications at the small scale (e.g. the swimming of microorganisms) to geological applications at the large scale (e.g. the flow of lava).

9.1 Recap: Governing Equations

9.1.1 Navier-Stokes Equations

For an incompressible fluid, the equations for mass and momentum balance are (see §2.8 and §2.9):

𝒖=0andρD𝒖Dt=𝐟+𝑻, (9.1)

where 𝒖 is the velocity, ρ is the constant density, t is time, 𝑻 is the stress tensor and 𝐟 is a body force (i.e. 𝐟=ρ𝐠).

Internal viscous stresses are produced by deformation. The fluid is Newtonian if the relationship between the rate of deformation (γij=ui/xj) and the stress 𝑻 is local, linear, instantaneous and isotropic. If the fluid is also incompressible, the Newtonian constitutive law is

𝑻=p𝑰+μ(𝒖+𝒖T). (9.2)

Substituting this into the momentum balance (9.1) gives the incompressible Navier-Stokes equations:

ρD𝒖Dt=p+μ2𝒖+𝐟 (9.3)

9.1.2 Reynolds number

To non-dimensionalise the problem we write

𝒖=U𝒖~,𝒙=L𝒙~,t=LUt~,p=Pp~, (9.4)

where U is a characteristic velocity scale, L is a characteristic lengthscale, and P is a characteristic pressure scale. Substituting these into equation (9.3) when 𝐟=𝟎 and rearranging we arrive at

ρULμ(𝒖~t~+u~~u~)=PLμU~p~+~2𝒖~, (9.5)

where ~/x~i. We choose the viscous scaling for the pressure P=μU/L (we could have chosen the alternative inertial scaling P=ρU2). This leaves one non-dimensional group called the Reynolds number:

Re=ρULμ=ULνinertiaviscousstresses, (9.6)

where ν=μ/ρ is the kinematic viscosity (μ is denoted the dynamic viscosity). In this section we will be focusing on the limit where Re1 such that inertia is negligible and we can ignore the left-hand side of (9.5). The mass and momentum balance, known as Stokes Equations, are then given by

𝒖=0and𝟎=p+μ2𝒖+𝐟. (9.7)

9.1.3 Energy and Dissipation

Taking the dot product of the full momentum equation (9.1) with the velocity 𝒖 and integrating over a volume Ω gives

Ωρ𝒖𝒖tdΩ+Ωρ𝒖(𝒖𝒖)dΩ=Ω𝒖𝐟dΩ+Ω𝒖(𝐓)dΩ. (9.8)

This can also be written in summation convention

ΩρuiuitdΩ+ΩρuiujuixjdΩ=ΩuifidΩ+ΩuiTijxjdΩ. (9.9)

Rearranging, applying the divergence theorem and mass conservation, the left-hand side becomes

LHS =Ω12t(ρuiui)12uiuiρtdΩ+Ω12xj(ρuiuiuj)12uiuixj(ρuj)dΩ
=ddtΩ12ρuiuidΩ+Ω12ρuiuiujnjdAΩ12uiui(ρt+xj(ρuj))=0dΩ.

Similarly, the right-hand side becomes

RHS =ΩuifidΩ+Ωxj(uiTij)TijuixjdΩ
=ΩuifidΩ+ΩuiTijnjdAΩTijuixjdΩ.

The mechanical energy equation is then written as

ddtΩ12ρu2dΩ(1)+Ω12ρu2𝒖𝐧dA(2)=Ω𝒖𝐟dΩ(3)+ΩuiTijnjdA(4)ΩTijuixjdΩ(5), (9.10)

where

  1. 1.

    the rate of change of kinetic energy in volume Ω is due to:

  2. 2.

    the flux of kinetic energy over the boundary A,

  3. 3.

    the rate of working by body forces 𝐟 in volume Ω,

  4. 4.

    the rate of working of surface forces in A,

  5. 5.

    and the stress working in volume Ω.

The mechanical energy equation above is for a general continuum. We can now look more specifically for a Newtonian viscous fluid with constitutive law,

Tij=pδij+2μeijwhereeij=12(uixj+ujxi). (9.11)

The stress working per unit volume then becomes

Tijuixj=pδijuixj+2μeijuixj. (9.12)

Remembering some properties of the rate of strain and rotation tensors, we know that

δijuixj=uixi=𝒖=0,eij+rij=12(uixj+ujxi)+12(uixjujxi)=uixj, (9.13)
eijrij=14(uixj+ujxi)(uixjujxi)=0. (9.14)

Hence, the stress working, also known as the viscous dissipation Φ, per unit volume is given by

Φ=Tijuixj=2μeijeij. (9.15)

The viscous dissipation Φ describes the rate of loss of mechanical energy due to friction in the volume Ω.

9.1.4 Additional comments

The approximation of Stokes Flow is good if the velocity or length scales U,L are small (e.g. swimming microorganisms), or the dynamic viscosity μ is large (e.g. in geophysics, flow in porous media, or the flow of lava or ice). Some examples are:

L U ρ μ ν Re
Sperm in water: 50μm 200μm/s 103kg/m3 103Pas 106m2/s 𝟏𝟎𝟐
Mantle: 3×103km 1cm/yr 3300kg/m3 1021Pas 3×1017m2/s 𝟑×𝟏𝟎𝟐𝟏

(See E. M. Purcell (1977) Life at Low Reynolds Number, American Journal of Physics).

Refer to caption
Figure 9.1: (a) Swimming sperm. (b) Flow of lava.

When approximating the Reynolds number, there are some caveats. Firstly there may be more than one relevant lengthscale, e.g in Lubrication theory later in the course the vertical lengthscale H is much smaller than the horizontal lengthscale L. These lengthscales may also vary with position e.g. flow past a body where in the far field ReUr/ν where r is the radial distance away from the body. Finally, the time scale may not be L/U but instead may be specified by an external driving force e.g. an oscillating boundary condition with timescale Tω1.

9.2 Properties of Stokes Flows

  1. 1.

    Instantaneity Instantaneity of the flow means there are no time derivatives 𝒖/t, so no inertia. The flow has no memory and only knows about the current boundary conditions and applied forcing, responding immediately to any changes. The flow is said to be “quasi-steady” as 𝒖 can vary in time if the boundary conditions and applied forcing 𝐟(t) varies in time.

    E.g. for a translating body with speed 𝐔(t), the fluid force on the body is proportional to its velocity 𝐟(t)𝐔(t) and not to its acceleration d𝐔(t)/dt.

  2. 2.

    Linearity: Linearity means that the flow is linearly forced whether it is by a boundary motion or body force. In Stokes Equations there is no 𝒖𝒖, so 𝒖(𝒙,t) and p are linear in 𝐟 and the boundary conditions.

    Refer to caption
    Figure 9.2: A translating body.
  3. 3.

    Reversiblity: Reversible in time: if you apply a force 𝐟(t) in 0t<T and then reverse the force and its history 𝐟(t)=𝐟(2Tt) in Tt<2T then the flow reverses and the fluid particles return to their starting position.

    Reversible in space: reversibility in time and the symmetry of geometry can often be used to rule out some components of velocity 𝒖.

    E.g. does a sphere sedimenting next to a vertical wall migrate towards the wall?

    Refer to caption
    Figure 9.3: Sedimenting sphere. Reversing the forcing 𝒈 must reverse the velocity 𝒖 by reversibility in time. Because of the symmetry of the sedimenting sphere we can reverse the system in z. In order for (a) to be the same as (c) we require the sphere to fall vertically with no horizontal component.
  4. 4.

    Forces Balance:

    Since there is no inertia the forces in the system must balance:

    𝑻=𝐟Ω𝑻dΩ=Ω𝐟dΩ. (9.16)

    Applying the divergence theorem then gives

    Ω𝑻𝐧dA+Ω𝐟dΩ=0. (9.17)

    This checks the consistency of the stress boundary conditions. In a similar way, we can check the consistency of the velocity boundary conditions by intergrating the mass balance equation:

    𝒖=0Ω𝒖dΩ=Ω𝒖𝐧dA=0. (9.18)
  5. 5.

    Work Balances Dissipation: Since there is no kinetic energy in the mechanical energy balance, from (9.10) we know that the work done by body and surface forces must balance the viscous dissipation in a given volume:

    ΩΦdΩ=ΩTijuixjdΩ=Ω𝒖𝐟dΩ+ΩuiTijnjdA. (9.19)

 Useful Lemma: Let 𝒖i be an incompressible flow and 𝒖s be a Stokes flow with body force 𝐟s such that

𝒖i=0and𝒖s=0,𝑻s=𝐟s. (9.20)

Then,

2μΩeijseijidΩ=ΩuiiTijsnjdA+ΩuiifisdΩ. (9.21)

Proof: We know that for a Stokes flow 2μeijs=Tijs+psδij. Hence,

2μeijseiji=Tijseiji+psδijeiji=0 (9.22)

due to incompressibility. Also, using the fact that Tij is symmetric and that ui/xj=eij+rij where rij is antisymmetric, we find

2μeijseiji =Tijs(uiixjriji)=TijsuiixjTijsriji=0, (9.23)
=xj(Tijsuii)uiiTijsxj. (9.24)

Integrating over a volume Ω and applying the divergence theorem then gives the result:

2μΩeijseijidΩ=Ωxj(Tijsuii)dΩΩuiiTijsxjdΩ=ΩuiiTijsnjdA+ΩuiifisdΩ. (9.25)

 

  1. 6.

    Uniqueness: Uniqueness means that each Stokes flow is unique but can be represented in many ways. Let 𝒖1 and 𝒖2 be Stokes flows with the same body forcing and boundary conditions, i.e. 𝐟1=𝐟2 in Ω and either 𝒖1=𝒖2 or 𝑻1𝐧=𝑻2𝐧 on Ω. Then 𝒖1=𝒖2.

    To show this we consider the flow 𝒖*=𝒖1𝒖2. From the property of linearity we know that 𝒖* must also be a Stokes flow with 𝐟*=𝟎 and either 𝒖*=𝟎 or 𝑻*𝐧=𝟎 on Ω. From the above lemma, we can show that

    2μΩeij*eij*dΩ=0. (9.26)

    The integrand is positive so must vanish, hence eij*=0. The flow is strain less so must be in solid body motion 𝐔+𝛀×𝒙. Velocity boundary conditions of 𝒖1=𝒖2 on Ω imply that 𝒖1=𝒖2 everywhere. [N.B. Stress conditions can lead to solid body motion].

  2. 7.

    Minimum Dissipation: Among all incompressible flows with the same velocity boundary conditions, the dissipation is minimised by the Stokes flow with no body force.

    Let 𝒖i be an incompressible flow and 𝒖s be a Stokes flow with 𝐟s=𝟎 and 𝒖i=𝒖s=𝐔. We know that

     2μΩ(eijieijs)(eijieijs)dΩ0(positiveintegrand) (9.27)
    =  2μΩ(eijieijieijseijs)dΩ+4μΩ(eijseiji)eijsdΩ=0, (9.28)

    from the lemma above. Therefore the dissipation is minimised for a Stokes flow

    2μΩeijieijidΩ2μΩeijseijsdΩ. (9.29)
  3. 8.

    Geometric bounding: The minimum dissipation theorem can be used to calculate bounds for the flow around more complicated geometries. Consider a cube of side length 2L moving at a velocity 𝑼 in a fluid, with drag force 𝑭C, and Stokes flow 𝒖s(𝒙) outside the cube.

    Refer to caption
    Figure 9.4: Stokes flow around a translating cube

    We can write down the dissipation (using the Stokes flow property that work balances dissipation) as

    vol.outsidecube2μeijseijsdΩ=cubeUiTijnjdA=𝑼cube𝑻𝒏dA=𝑼𝑭C. (9.30)

    We are considering the dissipation in the volume outside of the cube so the normal to the surface points inwards. This is the opposite to calculating drag on the sphere and hence a minus sign is introduced. Now consider a sphere that just contains the cube so have side length 3L. We can define an incompressible flow 𝒖(𝒙)i outside the cube made up of a Stokes flow outside the sphere and a flow with constant flow velocity 𝑼 between the sphere and the cube:

    𝒖i(𝒙)={𝒖(𝒙)(Stokesflowpastsphere)𝒙outsidesphere𝑼betweensphereandcube (9.33)

    The dissipation for this flow is given by

    vol.outsidecube2μeijieijidΩ=vol.outsidesphere2μeijieijidΩ=𝑼𝑭sphere=6πμ3L𝑼𝑼, (9.34)

    where we have used the fact that the strain rate for a flow with constant velocity is zero (Ui/xj=0) and the drag on a sphere of radius a=3L is 𝑭=6πμa𝑼. Finally, we know that the dissipation is minimised for a Stokes flow, and hence

    6πμ3L𝑼𝑼𝑼𝑭C. (9.35)

    This gives an upper bound on the drag force on the cube. We can go through a similar argument to find a lower bound by considering the flow outside of a sphere that just fits inside the cube, with radius a=L. We won’t repeat the analysis here but the result should give

    6πμ3L𝑼𝑼𝑼𝑭C6πμL𝑼𝑼. (9.36)
  4. 9.

    Reciprocal theorem: Consider Stokes flows 𝒖1(𝒙) and 𝒖2(𝒙) in a given volume with different boundary conditions and no body forces. Taking the first flow to be the Stokes flow 𝒖s=𝒖1(𝒙), the second flow to be the incompressible flow 𝒖i=𝒖2(𝒙) and using the above 𝑙𝑒𝑚𝑚𝑎 we have

    2μΩeij1eij2dΩ=Ωui2Tij1njdA. (9.37)

    If we instead take the second flow to be the Stokes flow 𝒖s=𝒖2(𝒙), in a similar manner we have

    2μΩeij2eij1dΩ=Ωui2Tij1njdA. (9.38)

    Equating the two we find that the rate of working of surface forces of flow 1 against flow 2 equals the rate of working of surface forces of flow 2 against flow 1 (reciprocal theorem):

    Ωui2Tij1njdA=Ωui2Tij1njdA. (9.39)

    If the boundary conditions are a uniform translation velocity 𝑼1,2, the reciprocal theorem reduces to

    𝑼1𝑭2=𝑼2𝑭1, (9.40)

    where 𝑭1,2 are the corresponding surface forces.

9.3 Stokes Flow Solutions

9.3.1 Representation as Harmonic Functions

Consider Stokes equations with body force 𝐟=𝟎:

p+μ2𝒖=𝟎,𝒖=0. (9.41)
1. (p+μ2𝒖)=02p=0 (9.42)
2. ×(p+μ2𝒖)=𝟎2𝝎=𝟎where𝝎=×𝒖 (9.43)
3. 2(p+μ2𝒖)=𝟎4𝒖=𝟎. (9.44)

Hence, p and 𝝎 are harmonic and 𝒖 is biharmonic.

9.3.2 Papkovich-Neuber Solutions

A method for finding the solution of Stokes flows comes from the Papkovich-Neuber representation. Suppose we can write the pressure p=2Π. Then

2(Π+μ𝒖)=𝟎μ𝒖=Π𝚽where2𝚽=𝟎. (9.45)

Using the incompressibility condition, we have

μ𝒖=(Π𝚽)=02Π=𝚽Π=12(𝒙𝚽+χ)where2χ=0. (9.46)

We can check this last relation:

2Πxixi =2xixi(12xjΦj+12χ)=12xi(xjxiΦj+xjΦjxi)+122χxixi=0 (9.47)
=12xi(δijΦj+xjΦjxi)=12(Φixi+δijΦjxi+xj2Φjxixi=0)=Φixi. (9.48)

 Any Stokes flow with 𝐟=𝟎 can be written in terms of a harmonic vector 𝚽 and a harmonic scalar χ:

2μ𝒖=(𝒙𝚽+χ)2𝚽andp=𝚽. (9.49)

 

9.3.3 Spherical Harmonic Solutions

Spherical harmonic functions are used for solutions involving points, spheres and cylinders that have no preferred direction or orientation. Let the radial coordinate r=|𝒙|(𝒙𝒙)1/2. We can show that 21r=0, except when r=0:

2xjxj((xixi)1/2) =xj((xkxk)3/2xiδij)=xj((xkxk)3/2xj) (9.50)
=3(xkxk)3/2+3(xmxm)5/2xkxjδkj=0. (9.51)

All other harmonic functions ϕ with ϕ0 and r are made up of

1r,1r,1r,1r, (9.52)

Harmonic functions that are bounded at r=0 are made up of

r1r,r31r,r51r,r2n+1n1r, (9.53)

These solutions only depend on r and 𝒙 and have no preferred orientation. Some useful derivatives to remember are:

1. (𝒙)ij=xixj=δij(identity) (9.54)
2. (r)i=xir (9.55)
3. (1r)i=xir3 (9.56)
4. (f(r))i=f(r)(r)i=f(r)xir (9.57)

Since we know that Stokes flows are linear in boundary conditions and forcing, we can form Papkovich-Neuber solutions by multiplying them by constant scalars, vectors, tensors, and forming dot-products, for example

𝑨1r,B1r,𝑪1r, (9.58)

9.3.4 Tensors and Pseudotensors

When building these solutions there are some properties it is useful to recall about tensors. An nth-rank tensor is a set of objects that transform like a product of n vectors. For example, if Ti1i2in is an nth-rank tensor, then

Tj1j2jn=Oj1i1Oj2i2OjninTi1i2in, (9.59)

where Oij is a transformation matrix. Symmetry properties are tensor invariant, so if Ti1i2in is symmetric (antisymmetric) under an exchange of i1 and i2 then Tj1j2jn is also symmetric (antisymmetric) under an exchange of j1 and j2. Examples of tensors in our problems would be

velocity𝒖,force𝑭=𝑻𝐧dA,position𝒙,grad,identity𝑰. (9.60)

In contrast, pseudotensors, such as the Levi-Civita ϵijk, change sign under transformation by reflections. Examples of pseudotensors we will come across are

angularvelocity𝛀,couple𝑮=𝒙×(𝑻𝐧)dA,crossproduct𝒖×𝒙,vorticity𝝎=×𝒖. (9.61)

If we want to find the velocity 𝒖 using the Papkovich-Neuber representation, then we want 𝚽 and χ to be tensors.

9.3.5 Point Force and Source Flow

Point force (Stokeslet): We want to find the velocity field for a point force. Consider the following:

𝑻 =μ2𝒖p=𝑭δ(𝒙) (9.62)
𝒖 =0,𝒖𝟎as|𝒙|. (9.63)

We know that

  1. by linearity, the velocity field must be linear in the forcing 𝑭

  2. solution must decay in the far field

  3. there is no preferred direction in the problem, can use spherical harmonics

  4. the velocity field 𝒖 must be made up of tensors

Using this information, we can now try to build harmonic functions 𝚽 and χ using the solutions in (9.52)-(9.53). Let’s try the following ansatzes:

𝚽 =α𝑭r (9.64)
𝚽 =α𝑭1r(equivalentlyχ=β𝑭1r)toosingularatr=0× (9.65)
𝚽 =α𝑭×1rpseudotensor× (9.66)

The first ansatz is the only one that decays in the far field and will not blow up at the origin. We proceed by substituting 𝚽 into the solution (9.49):

2μ𝒖=(α𝑭𝒙r)2α𝑭r=α(𝑭r+(𝑭𝒙)𝒙r3). (9.67)

To fully specify the solution we need to find α. Going back to the problem statement, we want the solution to satisfy

𝒖=0r=R𝒖𝒏dA=0, (9.68)

(this is built into the Papkovich-Neuber representation), and

𝑭δ(𝒙)=𝑻𝑭=r=R𝑻𝒏dA. (9.69)

On a sphere r=R, 𝒙=R𝒏, the normal velocity can be calculated

𝒖𝒏|r=R=α2μ(𝑭R+(𝑭R𝒏)R𝒏R3)𝒏=α(𝑭𝒏)μR (9.70)
r=R𝒖𝒏dA=α𝑭μRr=R𝒏dA=0,isotropic=0. (9.71)

The normal stress can also be calculated, but requires a bit more algebra:

𝑻𝒏|r=R=(p𝑰+μ(𝒖+𝒖T))𝒏|r=R (9.72)

with

p=(α𝑭r)=α𝑭𝒙r3,𝒖=α2μ((𝑭𝒙)𝑰r33(𝑭𝒙)𝒙𝒙r5), (9.73)
𝑻𝒏|r=R=3α(𝑭𝒏)𝒏R2r=R𝑻𝒏|r=RdA=3α𝑭R2r=R𝒏𝒏dA𝑨=3α𝑭R24πR2𝑰3 (9.74)

Here, we have noticed that the integral marked 𝑨 is an isotropic second rank tensor so must be δij. We can determine the constant of proportionality by calculating the trace, Aii=4πR2. Hence, α=1/4π. Notice that α is independent of R. If we had chosen one of the other harmonic solutions with higher powers of 1/r, they would be too singular to satisfy the force condition.

Source Flow (Point mass source): We want to find the velocity field for a point source in three-dimensions. Consider the following:

𝑻 =μ2𝒖p=𝟎 (9.75)
𝒖 =Qδ(𝒙),𝒖𝟎as|𝒙|. (9.76)

Strictly speaking this flow is only incompressible for r>0 as volume is not conserved at r=0 but generated there instead.

We know that

  1. by linearity, the velocity field must be linear in the source flux Q

  2. solution must decay in the far field

  3. there is no preferred direction in the problem, can use spherical harmonics

  4. the velocity field 𝒖 must be made up of tensors

Let’s try harmonic function

χ=βQr(equivalently𝚽=β^Q1r). (9.77)

In a similar manner to the point force, the other harmonic solutions with higher powers of 1/r would be too singular to satisfy the source condition. Substituting into the solution (9.49) we find:

2μ𝒖=(βQr)𝒖=βQ𝒙2μr3. (9.78)

To find β, we use the source condition at r=0:

𝒖 =Qδ(𝒙)Q=r=R𝒖𝒏dA=βQ2μR2r=R𝒏𝒏dA=βQ2μR24πR2. (9.79)

Hence, β=μ/2π. The velocity field then becomes 𝒖=Q𝒙/4πr3 which is independent of viscosity μ. This is the three-dimensional extension of the potential flow for a point source studied in §6.

9.3.6 Motion of a rigid particle

A sphere of radius r=a translating with velocity 𝐔 and rotating with angular velocity 𝛀 moves with velocity

𝒖|r=a=𝐔+𝛀×𝒙 (9.80)

and exerts a force 𝐅 and couple 𝐆 on the fluid. The dissipation in the fluid due to the particle is (using work balances dissipation)

ΩΦdΩ =Ω𝒖𝑻𝐧dA=particle(𝐔+𝛀×𝒙)𝑻𝐧dA (9.81)
=𝐔particle𝑻𝐧dA+𝛀particle𝒙×(𝑻𝐧)dA (9.82)
=𝐔𝐅+𝛀𝐆, (9.83)

where the normal points out of the fluid into the body, with

force𝑭=particle𝑻𝐧dAandcouple𝑮=particle𝒙×(𝑻𝐧)dA (9.84)

exerted on the fluid by the sphere.

9.3.7 Translating Rigid Sphere

Velocity Field: We would like to calculate the velocity field for a rigid sphere of radius r=a translating with velocity 𝒖=𝑼. Consider the following:

𝑻=μ2𝒖p=𝟎,𝒖=0, (9.85)
𝒖=𝑼atr=a,𝒖𝟎as|𝒙|. (9.86)

We know that

  1. by linearity, the velocity field must be linear in the forcing 𝑼

  2. solution must decay in the far field

  3. there is no preferred direction in the problem, can use spherical harmonics

  4. the velocity field 𝒖 must be made up of tensors

Let’s try

𝚽2μ=α𝑼randχ2μ=β𝑼1r. (9.87)

This then gives velocity field

𝒖=(α𝑼𝒙rβ𝑼𝒙r3)2α𝑼r=α[𝑼r(𝑼𝒙)𝒙r3]+β[𝑼r3+3(𝑼𝒙)𝒙r5]. (9.88)

Applying the boundary condition 𝒖=𝑼 at r=a gives

1=αaβa3,0=αa+3βa3α=3a4,β=a34, (9.89)

and

𝒖=3𝑼4(ar+a33r3)+3(𝑼𝒙)𝒙4(ar3a3r5). (9.90)

The pressure field can also be calculated

p=3μa𝑼21r=3μa(𝑼𝒙)2r3. (9.91)

When finding the velocity field for the point force and point source, we were restricted with the possible harmonic functions to choose from because of the behaviour at r=0. For the translating sphere this is no longer the case. You will notice that if we set either α or β to zero we can no longer satisfy the boundary condition on r=a.

Force and stress on the sphere: We start by calculating the stress 𝑻 from the velocity and pressure fields,

𝑻= p𝑰+μ(𝒖+𝒖T) (9.92)
= 3μa(𝑼𝒙)𝑰2r3+μ{34(ar3a3r5)(𝑼𝒙+𝒙𝑼)+32(3ar5+5a3r7)(𝑼𝒙)𝒙𝒙 (9.93)
+34(ar3a3r5)[2(𝑼𝒙)𝑰+𝑼𝒙+𝒙𝑼]} (9.94)

On r=a, 𝒙=a𝒏, the stress is

𝑻𝒏|r=a=3μ𝑼2a. (9.95)

The stress on the sphere is constant. Calculating the force, or drag, on the sphere is then relatively straightforward

drag=𝑭=r=a3μ𝑼2adA=6πμa𝑼. (9.96)

Gravitational settling: Now that we have the drag on a sphere translating at a given velocity, we can reverse the problem and ask what is the settling speed of a sphere falling under gravity.

Refer to caption
Figure 9.5: Sketch of settling sphere with forces.

Balancing the forces on a steady fall we have

𝟎(1)=4πa3ρ𝒈3(2)4πa3ρf𝒈3(3)6πμa𝑼(4)𝑼=2Δρa2𝒈9μ. (9.97)

where

  1. 1.

    no inertia (steady fall, no acceleration)

  2. 2.

    weight of the sphere, density ρ

  3. 3.

    buoyancy (weight of displaced fluid, density ρf)

  4. 4.

    Stokes drag

E.g. For a ball bearing with density ρ=8g/cm3 we can calculate the sedimenting speed for different fluids:

a ρf Δρ μ U Re
Water: 1μm 1g/cm3 7g/cm3 103Pas 15μm/s 1041
Golden syrup: 1mm 1.4g/cm3 6.6g/cm3 60 Pas 0.24mm/s 3×1051

This experiment can be used to calculate the viscosity of different fluids.

Far-field approximation: Far away from the sphere, we can show that the disturbance looks like a point force. The velocity field when r is

𝒖=3a𝑼4r+3a(𝑼𝒙)𝒙4r3. (9.98)

The force exerted across ‘r=’ must balance the force exerted across r=a so the strength of the point force 𝑭=6πμa𝑼. Substituting this into the velocity field gives

𝒖=18πμ(𝑭r+(𝑭𝒙)𝒙r3). (9.99)

This disturbance flow only knows the total force exerted and is independent of particle radius a.