Take positive away from the wall into the liquid, and write for atmospheric pressure. For a constant-mass density Newtonian fluid, the two-dimensional Navier-Stokes equation and continuity equation are
The stationary wall imposes the no-slip boundary condition and no-penetration boundary condition, at . For a flat free surface with negligible air shear stress, the stress boundary condition is , at ; the kinematic boundary condition is there.
For steady flow independent of , these equations give , and . Two integrations and the boundary conditions give the uniform gravity-driven Newtonian film:
Its surface velocity is , while its mean velocity is .
Define the aspect ratio and the thickness-based Reynolds number by
Use the nondimensionalization
The small transverse velocity scale follows from incompressibility. Dropping stars, the base fields become and . Before subtracting the base state, the dimensionless Navier-Stokes equation reads
For example, division of the downslope momentum equation by makes the inertial coefficient and the pressure gradient coefficient . The transverse equation has been divided instead by after using its smaller velocity scale; this gives the displayed coefficient.
Now substitute , , . Since , , and the base fields have no or dependence, subtraction gives
These are nonlinear equations for the deviations; small amplitude has not been assumed. The later asymptotic expansion takes as , or more generally requires the retained inertial correction to remain small.
The two wall boundary conditions are
Define the capillary parameter for a falling film
Retain in the long-wave approximation. Thus surface tension is retained in the leading normal stress balance even though geometric slope corrections are small. For in the rescaled coordinates, the dimensional surface slope is .
The three free surface boundary conditions, accurate through , are
The first is the kinematic boundary condition; the second is the zero tangential traction condition. For the third, the dimensional liquid-side pressure is, to the required order,
Division by gives in dimensionless variables. Subtracting gives the stated perturbation condition. The additional slope-times-shear contribution to normal stress vanishes at this order because the tangential traction is zero. The omitted geometric and tangential-stress corrections are under this ordering.
Use an asymptotic expansion at fixed , evaluating the boundary conditions at the instantaneous . At leading order, the downslope equation gives . The wall condition and the surface condition imply
Here denotes the total leading velocity, to distinguish it from the dimensional scale . The continuity equation and wall impermeability then give
The transverse momentum equation gives . The normal stress condition therefore yields
The leading volume flux per unit width is . Consequently mass conservation gives . This relation eliminates inside the first inertial correction:
Set . The downslope equation and boundary conditions are
Two integrations give
The pressure correction is not needed for this calculation because its downslope pressure gradient enters only at .
Integrating the total velocity across the film gives
Indeed the three inertial polynomial terms integrate to . Integrating the continuity equation and using the kinematic boundary condition gives . Hence the Benney equation is
Normal gravity smooths height variations on the upper side of the slope, while the inertial correction can amplify them. Surface tension suppresses sufficiently short wavelengths.

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