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306 Chapter 6 ■ Differential Analysis of Fluid Flow<br />

Potential flow solutions<br />

are always approximate<br />

because<br />

the <strong>fluid</strong> is assumed<br />

to be frictionless.<br />

V6.10 Potential<br />

flow<br />

Determining the velocity potential or stream function for a given body shape is a much more<br />

complicated problem.<br />

It is possible to extend the idea of superposition by considering a distribution of sources and<br />

sinks, or doublets, which when combined with a uniform flow can describe the flow around bodies<br />

of arbitrary shape. Techniques are available to determine the required distribution to give a<br />

prescribed body shape. Also, for plane potential flow problems it can be shown that complex<br />

variable theory 1the use of real and imaginary numbers2 can be effectively used to obtain solutions<br />

to a great variety of important flow problems. There are, of course, numerical techniques that can<br />

be used to solve not only plane two-dimensional problems, but the more general three-dimensional<br />

problems. Since potential flow is governed by Laplace’s equation, any procedure that is available<br />

for solving this equation can be applied to the analysis of irrotational flow of frictionless <strong>fluid</strong>s.<br />

Potential flow theory is an old and well-established discipline within the general field of <strong>fluid</strong><br />

<strong>mechanics</strong>. The interested reader can find many detailed references on this subject, including Refs.<br />

2, 3, 4, 5, and 6 given at the end of this chapter.<br />

An important point to remember is that regardless of the particular technique used to obtain<br />

a solution to a potential flow problem, the solution remains approximate because of the<br />

fundamental assumption of a frictionless <strong>fluid</strong>. Thus, “exact” solutions based on potential flow<br />

theory represent, at best, only approximate solutions to real <strong>fluid</strong> problems. The applicability of<br />

potential flow theory to real <strong>fluid</strong> problems has been alluded to in a number of examples considered<br />

in the previous section. As a rule of thumb, potential flow theory will usually provide a reasonable<br />

approximation in those circumstances when we are dealing with a low viscosity <strong>fluid</strong> moving at<br />

a relatively high velocity, in regions of the flow field in which the flow is accelerating. Under<br />

these circumstances we generally find that the effect of viscosity is confined to the thin boundary<br />

layer that develops at a solid boundary. Outside the boundary layer the velocity distribution and<br />

the pressure distribution are closely approximated by the potential flow solution. However, in<br />

those regions of the flow field in which the flow is decelerating 1for example, in the rearward<br />

portion of a bluff body or in the expanding region of a conduit2, the pressure near a solid boundary<br />

will increase in the direction of flow. This so-called adverse pressure gradient can lead to flow<br />

separation, a phenomenon that causes dramatic changes in the flow field which are generally not<br />

accounted for by potential theory. However, as discussed in Chapter 9, in which boundary layer<br />

theory is developed, it is found that potential flow theory is used to obtain the appropriate pressure<br />

distribution that can then be combined with the viscous flow equations to obtain solutions near<br />

the boundary 1and also to predict separation2. The general differential equations that describe<br />

viscous <strong>fluid</strong> behavior and some simple solutions to these equations are considered in the remaining<br />

sections of this chapter.<br />

6.8 Viscous Flow<br />

To incorporate viscous effects into the differential analysis of <strong>fluid</strong> motion we must return to the<br />

previously derived general equations of motion, Eqs. 6.50. Since these equations include both<br />

stresses and velocities, there are more unknowns than equations, and therefore before proceeding<br />

it is necessary to establish a relationship between the stresses and velocities.<br />

6.8.1 Stress–Deformation Relationships<br />

For incompressible Newtonian <strong>fluid</strong>s it is known that the stresses are linearly related to the rates<br />

of deformation and can be expressed in Cartesian coordinates as 1for normal stresses2<br />

s xx p 2m 0u<br />

0x<br />

s yy p 2m 0v<br />

0y<br />

s zz p 2m 0w<br />

0z<br />

(6.125a)<br />

(6.125b)<br />

(6.125c)

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