In fluid dynamics,Stokes problem also known asStokes second problem or sometimes referred to asStokes boundary layer orOscillating boundary layer is a problem of determining the flow created by an oscillating solid surface, named afterSir George Stokes. This is considered one of the simplest unsteady problems that has an exact solution for theNavier–Stokes equations.^[1][2] Inturbulent flow, this is still named a Stokes boundary layer, but now one has to rely onexperiments,numerical simulations orapproximate methods in order to obtain useful information on the flow.

Sources:^[3][4]

Consider an infinitely long plate which is oscillating with a velocity${\displaystyle U\cos \omega t}$ in the${\displaystyle x}$ direction, which is located at${\displaystyle y=0}$ in an infinite domain of fluid, where${\displaystyle \omega }$ is the frequency of the oscillations. The incompressibleNavier–Stokes equations reduce to

${\displaystyle \frac{\mathrm{\partial }u}{\mathrm{\partial }t}=\nu \frac{{\mathrm{\partial }}^{2}u}{\mathrm{\partial }{y}^2}}$

where${\displaystyle \nu }$ is thekinematic viscosity. The pressure gradient does not enter into the problem. The initial,no-slip condition on the wall is

${\displaystyle u(0,t)=U\cos \omega t,u(\mathrm{\infty },t)=0,}$

and the second boundary condition is due to the fact that the motion at${\displaystyle y=0}$ is not felt at infinity. The flow is only due to the motion of the plate, there is no imposed pressure gradient.

Sources:^[5][6]

The initial condition is not required because of periodicity. Since both the equation and the boundary conditions are linear, the velocity can be written as the real part of some complex function

${\displaystyle u=U\mathrm{\Re }\left[e^{i\omega t}f(y)\right]}$

because${\displaystyle \cos \omega t=\mathrm{\Re }\left[e^{i\omega t}\right]}$.

Substituting this into the partial differential equation reduces it to ordinary differential equation

${\displaystyle f^{″}-\frac{i\omega }{\nu }f=0}$

with boundary conditions

${\displaystyle f(0)=1,f(\mathrm{\infty })=0}$

The solution to the above problem is

${\displaystyle f(y)=\exp \left[-\frac{1+i}{\sqrt{2}}\sqrt{\frac{\omega }{\nu }}y\right]}$

${\displaystyle u(y,t)=U{e}^{-\sqrt{\frac{\omega }{2\nu }}y}\cos \left(\omega t-\sqrt{\frac{\omega }{2\nu }}y\right)}$

The disturbance created by the oscillating plate travels as the transverse wave through the fluid, but it is highly damped by the exponential factor. The depth of penetration${\displaystyle \delta =\sqrt{2\nu /\omega }}$ of this wave decreases with the frequency of the oscillation, but increases with the kinematic viscosity of the fluid.

The force per unit area exerted on the plate by the fluid is

${\displaystyle F=\mu {\left(\frac{\mathrm{\partial }u}{\mathrm{\partial }y}\right)}_{y=0}=\sqrt{\rho \omega \mu }U\cos \left(\omega t-\frac{\pi }{4}\right)}$

There is a phase shift between the oscillation of the plate and the force created.

An important observation from Stokes' solution for the oscillating Stokes flow is thatvorticity oscillations are confined to a thin boundary layer and dampexponentially when moving away from the wall.^[7] This observation is also valid for the case of a turbulent boundary layer. Outside the Stokes boundary layer – which is often the bulk of the fluid volume – the vorticity oscillations may be neglected. To good approximation, the flow velocity oscillations areirrotational outside the boundary layer, andpotential flow theory can be applied to the oscillatory part of the motion. This significantly simplifies the solution of these flow problems, and is often applied in the irrotational flow regions ofsound waves andwater waves.

If the fluid domain is bounded by an upper, stationary wall, located at a height${\displaystyle y=h}$, the flow velocity is given by

${\displaystyle u(y,t)=\frac{U}{2(\cosh 2\lambda h-\cos 2\lambda h)}[e^{-\lambda (y-2h)}\cos (\omega t-\lambda y)+e^{\lambda (y-2h)}\cos (\omega t+\lambda y)-e^{-\lambda y}\cos (\omega t-\lambda y+2\lambda h)-e^{\lambda y}\cos (\omega t+\lambda y-2\lambda h)]}$

where${\displaystyle \lambda =\sqrt{\omega /(2\nu )}}$.

Suppose the extent of the fluid domain be with${\displaystyle y=h}$ representing a free surface. Then the solution as shown byChia-Shun Yih in 1968^[8] is given by

${\displaystyle u(y,t)=\frac{U\cos h/\delta \mathrm{c}\mathrm{o}\mathrm{s}\mathrm{h}h/\delta }{2({\cos }^{2}h/\delta +{\mathrm{s}\mathrm{i}\mathrm{n}\mathrm{h}}^{2}h/\delta )}\mathrm{\Re }\left\{W+W^{\ast }-i\mathrm{t}\mathrm{a}\mathrm{n}\mathrm{h}h/\delta \tan h/\delta (W-W^{\ast })\right\},W=\mathrm{c}\mathrm{o}\mathrm{s}\mathrm{h}[(1+i)(h-y)/\delta ]e^{i\omega t}}$

where${\displaystyle \delta =\sqrt{2\nu /\omega }}$ and${\displaystyle W^{\ast }}$ is the complex conjugate of${\displaystyle W.}$

The case for an oscillatingfar-field flow, with the plate held at rest, can easily be constructed from the previous solution for an oscillating plate by usinglinear superposition of solutions. Consider a uniform velocity oscillation${\displaystyle u(\mathrm{\infty },t)=U_{\mathrm{\infty }}\cos \omega t}$ far away from the plate and a vanishing velocity at the plate${\displaystyle u(0,t)=0}$. Unlike the stationary fluid in the original problem, the pressure gradient here at infinity must be a harmonic function of time. The solution is then given by

${\displaystyle u(y,t)=U_{\mathrm{\infty }}\left[\cos \omega t-{\text{e}}^{-\sqrt{\frac{\omega }{2\nu }}y}\cos \left(\omega t-\sqrt{\frac{\omega }{2\nu }}y\right)\right],}$

which is zero at the wally = 0, corresponding with theno-slip condition for a wall at rest. This situation is often encountered insound waves near a solid wall, or for the fluid motion near the sea bed inwater waves. The vorticity, for the oscillating flow near a wall at rest, is equal to the vorticity in case of an oscillating plate but of opposite sign.

Consider an infinitely long cylinder of radius${\displaystyle a}$ exhibiting torsional oscillation with angular velocity${\displaystyle \mathrm{\Omega }\cos \omega t}$ where${\displaystyle \omega }$ is the frequency. Then the velocity approaches after the initial transient phase to^[9]

${\displaystyle v_{\theta }=a\mathrm{\Omega }\mathrm{\Re }\left[\frac{K_1(r\sqrt{i\omega /\nu })}{K_1(a\sqrt{i\omega /\nu })}{e}^{i\omega t}\right]}$

where${\displaystyle K_1}$ is the modified Bessel function of the second kind. This solution can be expressed with real argument^[10] as:

where

${\displaystyle \mathrm{\Psi }={\left[{\text{kei}}_1^2\left(\sqrt{R_{\omega }}\right)+{\text{ker}}_1^2\left(\sqrt{R_{\omega }}\right)\right]}^{-1},}$

${\displaystyle \mathrm{k}\mathrm{e}\mathrm{i}}$ and${\displaystyle \mathrm{k}\mathrm{e}\mathrm{r}}$ areKelvin functions and${\displaystyle R_{\omega }}$ is to the dimensionless oscillatory Reynolds number defined as${\displaystyle R_{\omega }=\omega a^2/\nu }$, being${\displaystyle \nu }$ the kinematic viscosity.

If the cylinder oscillates in the axial direction with velocity${\displaystyle U\cos \omega t}$, then the velocity field is

${\displaystyle u=U\mathrm{\Re }\left[\frac{K_0(r\sqrt{i\omega /\nu })}{K_0(a\sqrt{i\omega /\nu })}{e}^{i\omega t}\right]}$

where${\displaystyle K_0}$ is the modified Bessel function of the second kind.

Source:^[11]

In theCouette flow, instead of the translational motion of one of the plate, an oscillation of one plane will be executed. If we have a bottom wall at rest at${\displaystyle y=0}$ and the upper wall at${\displaystyle y=h}$ is executing an oscillatory motion with velocity${\displaystyle U\cos \omega t}$, then the velocity field is given by

${\displaystyle u=U\mathrm{\Re }\left\{e^{-i\omega t}\frac{\sin ky}{\sin kh}\right\},\text{where}k=\frac{1+i}{\sqrt{2}}\sqrt{\frac{\omega }{\nu }}.}$

The frictional force per unit area on the moving plane is${\displaystyle -\mu U\mathrm{\Re }\{k\cot kh\}}$ and on the fixed plane is${\displaystyle \mu U\mathrm{\Re }\{k\csc kh\}}$.

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