Page 224 - Bird R.B. Transport phenomena
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208  Chapter 7  Macroscopic Balances for Isothermal Flow Systems

                                                H*      120'                      Fig.  7.5-1. Pipeline flow
                                                                                  with friction losses be-
                                                                   "f             cause of fittings. Planes
                                                                    20'           1 and 2 are just under
                                                                   A,    - -  Plane 2  the surface  of the liquid.
                                                  100'

                                      -300'-
                           Pump

                                                90°  elbow
                                      Plane 1





      SOLUTION             The  average velocity in the pipe is

                                                                                                (7.5-11)
                                                         TTR 2  ТГ(1/6)  2
                           and  the Reynolds number is

                                                                                                (7.5-12)

                           Hence the flow is turbulent.
                               The  contribution to E  from the various lengths of pipe will be
                                                v



                                                     2(2.30) (0.0049)  (5 + 300 + 100 + 120 + 20)
                                                           2
                                                         (1/3)
                                                                     2
                                                    =  (0.156)(545) = 85 ft /s 2                (7.5-13)
                           The  contribution to E  from the sudden contraction, the three 90° elbows, and the sudden ex-
                                             v
                           pansion (see Table 7.5-1) will be
                                               Е  (^Ч)/ = ^(2.30) (0.45 + ф + 1) = 8 ft /s 2    (7.5-14)
                                                                    З
                                                             2
                                                                                2
                                               г
                           Then from Eq. 7.5-10 we get
                                                 0 + (32.2X105 -  20) + 0 = W  -  85 -  8       (7.5-15)
                                                                        m
                           Solving for  W  we get
                                       m
                                                                           2
                                                   W  = 2740 + 85 -  8 «  2830  ft /s  2        (7.5-16)
                                                     m
                           This is the work (per unit mass of fluid) done on the fluid in the pump. Hence the pump does
                                 2
                           2830 ft /s 2  or 2830/32.2  = 88 ft lb /lb m  of work  on the fluid passing  through the system. The
                                                      /
                           mass rate of flow is
                                                    w  = (12/60X62.4)  = 12.5 lb /s             (7.5-17)
                                                                          w
                           Consequently
                                           W  = w%  = (12.5X88) = 1100 ft Ybf/s  = 2 hp = 1.5 kW  (7.5-18)
                                             m
                           which is the power delivered by the pump.
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