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§7.4  The Macroscopic Mechanical Energy Balance  203

                                                                                Fig. 7.3-1.  Torque on a
                                                                                tank, showing side view
                                                                                and top view.

                              Side view
                                                        Origin of coordinates is on
                                       Plane 1          tank axis in a plane passing
                                          I             through the axis of the entrance
                            Area  of cross  —L          pipe and parallel to the tank top
                             section is Sj
                                                    -•h-Plane  2
                                Area  of cross
                                 section is S 2




                              Top view  Plane 1






       §7.4  THE MACROSCOPIC MECHANICAL             ENERGY BALANCE

                            Equations 7.1-2, 7.2-2, and  7.3-2 have been set up by applying the laws  of conservation of
                            mass, (linear) momentum, and  angular momentum  over the macroscopic  system in Fig.
                            7.0-1.  The  three  macroscopic  balances  thus  obtained  correspond  to  the  equations  of
                            change in Eqs. 3.1-4,3.2-9, and 3.4-1, and, in fact, they are very similar in structure. These
                            three  macroscopic  balances  can  also  be  obtained  by  integrating  the  three  equations  of
                            change over the volume  of the flow system.
                                Next  we  want  to  set up  the  macroscopic  mechanical  energy  balance,  which  corre-
                            sponds  to the equation  of mechanical  energy in  Eq. 3.3-2. There is no way  to do this di-
                            rectly as we have done in the preceding three sections, since there is no conservation law
                            for  mechanical  energy.  In this instance we must integrate the equation  of change  of me-
                            chanical energy  over  the volume  of the  flow system. The result, which  has made use of
                            the same assumptions  (i-iv) used  above, is the unsteady-state macroscopic mechanical energy
                            balance  (sometimes  called  the  engineering Bernoulli equation). The  equation  is derived  in
                            §7.8; here we state the result and discuss its meaning:

                                                              Pi  ^>l<Pl
                                       rate of increase  rate at which kinetic  rate at which kinetic
                                       of kinetic and  and potential energy  and potential energy
                                       potential energy  enter system at plane 1  leave system at plane 2
                                       in system

                                         +  { Vl{v,)S x -  V2{v 2)S 2) +  W m +  j  p(V • v) dV  +  j  (T:VV) dV  (7.4-1)
                                                                  V(t)          V(t)
                                          net rate at which the  rate of  rate at which  rate at which
                                          surroundings do   doing  mechanical   mechanical
                                          work on the fluid  work on  energy increases  energy
                                          at planes 1 and 2 by  fluid by  or decreases  decreases
                                          the pressure      moving  because of expansion  because of
                                                            surfaces  or compression  viscous
                                                                                       1
                                                                  of    fluid   dissipation

                                1
                                  This interpretation  of the term is valid only for Newtonian fluids; polymeric liquids have elasticity
                            and the interpretation given above no longer holds.
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