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4.4 The Reynolds Transport Theorem 177<br />

V A = Absolute velocity of A<br />

V B<br />

V CV<br />

W B = Velocity of<br />

W A = Velocity of<br />

B relative<br />

V CV<br />

A relative<br />

to control F I G U R E 4.22<br />

to control<br />

volume Relationship between absolute and relative<br />

volume<br />

velocities.<br />

The Reynolds transport<br />

theorem for a<br />

moving control volume<br />

involves the<br />

relative velocity.<br />

velocity, V, and the control volume velocity, V cv , will not be in the same direction so that the<br />

relative and absolute velocities will have different directions 1see Fig. 4.222.<br />

The Reynolds transport theorem for a moving, nondeforming control volume can be derived<br />

in the same manner that it was obtained for a fixed control volume. As is indicated in Fig. 4.23, the<br />

only difference that needs be considered is the fact that relative to the moving control volume the<br />

<strong>fluid</strong> velocity observed is the relative velocity, not the absolute velocity. An observer fixed to<br />

the moving control volume may or may not even know that he or she is moving relative to some<br />

fixed coordinate system. If we follow the derivation that led to Eq. 4.19 1the Reynolds transport<br />

theorem for a fixed control volume2, we note that the corresponding result for a moving control<br />

volume can be obtained by simply replacing the absolute velocity, V, in that equation by the relative<br />

velocity, W. Thus, the Reynolds transport theorem for a control volume moving with constant<br />

velocity is given by<br />

DB sys<br />

Dt<br />

where the relative velocity is given by Eq. 4.22.<br />

0 0t <br />

cv<br />

rb dV cs<br />

rb W nˆ dA<br />

(4.23)<br />

4.4.7 Selection of a Control Volume<br />

Any volume in space can be considered as a control volume. It may be of finite size or it may be<br />

infinitesimal in size, depending on the type of analysis to be carried out. In most of our cases,<br />

the control volume will be a fixed, nondeforming volume. In some situations we will consider<br />

control volumes that move with constant velocity. In either case it is important that considerable<br />

thought go into the selection of the specific control volume to be used.<br />

The selection of an appropriate control volume in <strong>fluid</strong> <strong>mechanics</strong> is very similar to the selection<br />

of an appropriate free-body diagram in dynamics or statics. In dynamics, we select the body in which<br />

we are interested, represent the object in a free-body diagram, and then apply the appropriate governing<br />

laws to that body. The ease of solving a given dynamics problem is often very dependent on the<br />

specific object that we select for use in our free-body diagram. Similarly, the ease of solving a given<br />

<strong>fluid</strong> <strong>mechanics</strong> problem is often very dependent on the choice of the control volume used. Only by<br />

practice can we develop skill at selecting the “best” control volume. None are “wrong,” but some are<br />

“much better” than others.<br />

Solution of a typical problem will involve determining parameters such as velocity, pressure,<br />

and force at some point in the flow field. It is usually best to ensure that this point is located on<br />

the control surface, not “buried” within the control volume. The unknown will then appear in the<br />

convective term 1the surface integral2 of the Reynolds transport theorem. If possible, the control<br />

Control volume<br />

and system at time t<br />

System at time<br />

t + δt<br />

Pathlines as<br />

seen from the<br />

moving control<br />

volume<br />

W = V – V CV<br />

Flow as seen by an<br />

observer moving with<br />

velocity V CV<br />

F I G U R E 4.23<br />

Control volume and system as seen<br />

by an observer moving with the<br />

control volume.

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