Viscous Flow#

Viscosity is what potential flow leaves out, and these are the handful of problems simple enough that adding it back in still yields an exact, closed-form answer. Couette and Poiseuille flow show how the same viscous term produces a straight-line profile under a moving wall but a parabola under a pressure gradient; Stokes drag captures the opposite extreme, where viscosity so dominates inertia that a settling sphere never notices its own momentum; the Reynolds number sweep shows that same Stokes-drag physics recast to make a different point – that a single dimensionless ratio, not the sphere’s size or the fluid’s identity separately, decides the flow regime; and the Blasius boundary layer shows what happens in between – a thin viscous layer clinging to a wall in an otherwise fast, nearly inviscid stream, thickening as the square root of downstream distance. Watch how thin that layer stays even at a middling free-stream speed, and how the wall shear stress it predicts falls off as the flow moves downstream.

The Blasius laminar boundary layer

The Blasius laminar boundary layer

Couette versus Poiseuille flow

Couette versus Poiseuille flow

The Reynolds number: one ratio, regardless of size or fluid

The Reynolds number: one ratio, regardless of size or fluid

Stokes drag and the terminal velocity of a settling sphere

Stokes drag and the terminal velocity of a settling sphere