Couette flow with a slipping lower wall

ID: couette-flow-with-a-slipping-lower-wall

Consider steady flow of a Newtonian fluid in incompressible flow with constant dynamic viscosity between parallel plates at and . The bottom plate is stationary and obeys the Navier slip boundary condition with slip length . The top plate moves at velocity and obeys the no-slip boundary condition. There is no streamwise pressure gradient or body force. The Couette flow solution is
Here is the constant shear stress magnitude. The lower wall's Navier slip boundary condition holds exactly because . At the top, is exactly the prescribed no-slip boundary condition; no finite upper-wall slip length is imposed in this example.
For a numerical example, stipulate , , and . The bottom velocity is and the shear stress is , compared with when both plates obey the no-slip boundary condition. The extrapolated profile reaches zero at .
Figure 1.
Couette profiles reveal slip length by extrapolation beneath the lower wall
. The bottom wall is stationary with slip length ; the upper wall at moves at velocity with a no-slip boundary condition. Solid lines show Couette flow for , and . Dashed continuations inside the shaded solid reach zero at . Increasing slip length reduces the shear rate required for the same upper-wall velocity. Details.
For fixed , and , recovers . As , throughout the gap and : the moving upper wall selects the limiting uniform velocity, while the lower wall approaches a stress-free boundary condition. The dynamic viscosity stays positive; the disappearing shear stress comes from the disappearing velocity gradient.
A short derivation uses unidirectional flow: the convective acceleration vanishes and the Navier-Stokes equation reduces to . Write . The bottom condition gives and the top condition gives .

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