INCOMPRESSIBLE POTENTIAL FLOWS 51
in elastic arteries modeled by a system of nonlinear hyperbolic partial differen-
tial equations. We also introduce multistep methods for numerically integrating
hyperbolic partial differential equations.
2.1 INCOMPRESSIBLE POTENTIAL FLOWS
Real fluids are all viscous. Viscosity is caused by the redistribution of excessive
momenta among neighboring fluid molecules through the action of intermolecular
collisions. Thus, a viscous force is exerted on the surface of a fluid element where
a local velocity gradient is present. It may be either a shearing force tangent to
the surface, such as the one found in a boundary layer, or a normal force that
exists, for example, within a shock wave.
The importance of the viscous force in comparison with the inertial force is
represented by the Reynolds number, which is the ratio of a characteristic inertial
force to a characteristic viscous force in a flow field. Because of the low viscosity
of air and water, the Reynolds numbers of most flows of practical interest are
usually very high; in other words, in these flows the viscous forces are very small
compared with the inertia.
For a high-Reynolds number flow past a streamlined body from which the
flow does not separate, Prandtl (1904) postulated that the influence of viscosity
is confined to a very thin boundary layer in the immediate neighborhood of
the solid wall, and that in the region outside of the boundary layer the flow
behaves as if there were no viscosity. Prandtl’s postulation has been proven to
be a powerful tool in solving many practical flow problems. For instance, the
inviscid flow theory predicts extremely well the lift and pressure distribution on
an airfoil for angles of attack below the value at which the flow starts to separate
from the body, although the drag has to be found by solving the boundary-layer
equations.
It is known that vorticities are generated by the shearing viscous forces, so that
the boundary-layer flow is a rotational one. On the other hand, in the absence of
viscous and other rotational forces, the originally irrotational flow far upstream
will remain so in the region outside the boundary layer. Letting V denote the
velocity field in this region, the irrotationality condition states that the vorticity
vanishes; that is,
∇ × V = 0 (2.1.1)
The preceding equation is automatically satisfied if a velocity potential φ is
introduced such that
V = ∇φ (2.1.2)
For this reason irrotational flows are also called potential flows.Asaresult
of introducing the velocity potential, the velocity vector generally having three
components is replaced by a single scalar quantity φ.