Write and for the lower and upper layer thicknesses. A steady unidirectional velocity with no pressure gradient satisfies the Navier-Stokes equations through in each layer. Continuity of velocity and tangential stress at the interface gives one constant shear stress
The two-layer Couette flow is therefore
The fluid exerts the tangential traction on the upper boundary and on the lower boundary. Equivalently, the boundaries exert and on the fluids, respectively.
The viscous dissipation per unit boundary area is
The rate at which the upper and lower boundaries do work on the fluid, per unit area, is
The definition of gives
which is the required mechanical-energy balance.
Suppose and . Integrating the two velocity profiles gives the volume fluxes per unit span
Here
Consequently
so all dependence on the interface position cancels from the ratio:

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