10. Description of Flow past a Sphere 375
We close this section by noting that this flow illustrates three instances where the
solution is counterintuitive. First, small causes can have large effects. If we solve for
the flow of a fluid with zero viscosity around a circular cylinder, we obtain the results
of Chapter 6, Section 9. The inviscid flow has fore-aft symmetry and the cylinder
experiences zero drag. The bottom two panels of Figure 10.17 illustrate the flow for
small viscosity. For viscosity as small as you choose, in the limit viscosity tends
to zero, the flow must look like the last panel in which there is substantial fore-aft
asymmetry, a significant wake, and significant drag. This is because of the necessity
of a boundary layer and the satisfaction of the no-slip boundary condition on the
surface so long as viscosity is not exactly zero. When viscosity is exactly zero, there
is no boundary layer and there is slip at the surface. The resolution of d’Alembert’s
paradox is through the boundary layer, a singular perturbation of the Navier–Stokes
equations in the direction normal to the boundary.
The second instance of counterintuitivity is that symmetric problems can have
nonsymmetric solutions. This is evident in the intermediate Reynolds number middle
panel of Figure 10.17. Beyond a Reynolds number of ≈40 the symmetric wake
becomes unstable and a pattern of alternating vortices called a von Karman vortex
street is established. Yet the equations and boundary conditions are symmetric about a
central plane in the flow. If one were to solve only a half-problem, assuming symmetry,
a solution would be obtained, but it would be unstable to infinitesimal disturbances
and unlikely to be seen in the laboratory.
The third instance of counterintuitivity is that there is a range of Reynolds num-
bers where roughening the surface of the body can reduce its drag. This is true for
all blunt bodies, such as a sphere (to be discussed in the next section). In this range
of Reynolds numbers, the boundary layer on the surface of a blunt body is laminar,
but sensitive to disturbances such as surface roughness, which would cause earlier
transition of the boundary layer to turbulence than would occur on a smooth body.
Although, as we shall see, the skin friction of a turbulent boundary layer is much
larger than that of a laminar boundary layer, most of the drag is caused by incomplete
pressure recovery on the downstream side of a blunt body as shown in Figure 10.21,
rather than by skin friction. In fact, it is because the skin friction of a turbulent bound-
ary layer is much larger, as a result of a larger velocity gradient at the surface, that
a turbulent boundary layer can remain attached farther on the downstream side of a
blunt body, leading to a narrower wake and more complete pressure recovery and thus
reduced drag. The drag reduction attributed to the turbulent boundary layer is shown
in Figure 10.22 for a circular cylinder and Figure 10.23 for a sphere.
10. Description of Flow past a Sphere
Several features of the description of flow over a circular cylinder qualitatively apply
to flows over other two-dimensional blunt bodies. For example, a vortex street is
observed in a flow perpendicular to a flat plate. The flow over a three-dimensional
body, however, has one fundamental difference in that a regular vortex street is absent.
For flow around a sphere at low Reynolds numbers, there is an attached eddy in the
form of a doughnut-shaped ring; in fact, an axial section of the flow looks similar to