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78  Aerodynamics for  Engineering Students








               Fig. 2.19


               But here $ is a function of (r, Q) and again
                                                      a$
                                           6$ = -6r  -t -60                       (2.58)
                                                dr     dB
               and equating terms in Eqns (2.57) and (2.58)
                                                     a$
                                              qt  1 --                           (2.58a)
                                                     dr

                                                                                 (2.58b)

               these being velocity components at a point r, Q in a flow given by stream function $.
                 In general terms the velocity q in any direction s is  found by differentiating the
               stream function $ partially with  respect to the direction  II  normal  to q where n is
               taken in the anti-clockwise sense looking along q (Fig. 2.19):
                                                q=- a$
                                                   dn


                 2.6  The momentum equation

               The momentum equation for two- or three-dimensional  flow embodies the applica-
               tion of Newton’s second law of motion (mass times acceleration = force, or rate of
               change of momentum  = force) to an infinitesimal control volume in a fluid flow (see
               Fig. 2.8). It takes the form of a set of partial differential equations. Physically it states
               that the rate of increase in momentum within the control volume plus the net rate at
               which momentum flows out of the control volume equals the force acting on the fluid
               within the control volume.
                 There are two distinct classes of  force that act on the fluid particles  within  the
               control volume.
               (i)  Body forces. Act on all the fluid within the control volume. Here the only body
                  force of interest is the force of gravity or weight of the fluid.
               (ii)  Surface forces. These only act  on the control  surface; their  effect on the fluid
                  inside the  control  volume  cancels out. They  are always expressed in  terms  of
                  stress (force per unit area). Two main types of surface force are involved namely:
                 (a)  Pressure force. Pressure, p, is a stress that always acts perpendicular to the control
                     surface and in the opposite direction to the unit normal (see Fig. 1.3). In other words
                     it always tends to compress the fluid in the control volume. Although p  can vary
                     from point to point in the flow field it is invariant with direction at a particular point
                     (in other words irrespective of the orientation of the infinitesimal control volume the
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