Page 172 - Water Engineering Hydraulics, Distribution and Treatment
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                                          Chapter 5
                                                   Water Hydraulics, Transmission, and Appurtenances
                                      EXAMPLE 5.45 MASS FLOW OF INCOMPRESSIBLE FLUID
                                      Determine the mass-flow rate at section B of a pipe line if the static pressure at section A is 102 psig (707.9 kPa = 707.0 kN/m )and
                                      the 4-in. (101.6-mm)-diameter pipe is flowing full with turbulent flow at an average velocity of 32 ft/s (9.75 m/s).
                                      Solution 1 (US Customary System):
                                         Q = Av.
                                           Q =   Av = mass flow
                                                     3
                                            = (62.4lb∕ft )[(  ∕4)(4∕12) ft ](32 ft∕s).
                                         Mass flow = 174 lb/s.
                                      Solution 2 (SI System):   2  2                                                            2
                                         Q = Av.
                                           Q =   Av = mass flow
                                                     3           2  2
                                            = (9.8kN∕m )[(  ∕4)(0.1016) m ](9.75 m∕s).
                                         Mass flow = 0.77 kN/s.
                                         Mass flow rate is the same at all sections. Mass flow at Section A equals mass flow at Section B
                                      EXAMPLE 5.46 MASS FLOW OF COMPRESSIBLE FLUID
                                      Determine the mass-flow rate of air traveling in a long length of 1-in. (25.4-mm)-diameter pipe. At section A, the pressure is 31
                                                                                ◦
                                                                                        ◦
                                                              2
                                      psia (215.14 kPa = 215.14 kN/m ), the temperature is 300 F (148.88 C), and the air velocity is 32 ft/s (9.75 m/s). At the downflow
                                                                                                              2
                                      section B, the pressure has been reduced by friction and heat loss to 21 psig (145.7 kPa = 145.7 kN/m )(R , the gas constant of air =
                                                                                                                  g
                                                ◦
                                      53.34 ft-lb/lb- R (286.9 J/kg-K); 1 J = 0.101972 kg-m; and 1 N = 0.101972 kg.)
                                      Solution 1 (US Customary System):
                                         R = PV/T.
                                          g
                                                  ◦
                                                                            ◦
                                                                2
                                         53.4 ft-lb/lb- R = (31 × 144 lb/ft )(V)/(300 + 460 R).
                                                 3
                                         V = 9.081 ft /lb.
                                                                   3
                                                        3
                                            = 1∕V = 1∕9.081 ft /lb = 0.11 lb/ft .
                                         Mass flow =   Q =   Av
                                                                       2
                                                          3
                                                                     2
                                                 = (0.11 lb∕ft )[(  ∕4)(1∕12) ft ](32 ft∕s)
                                                 = 0.019 lb∕s.
                                      Solution 2 (SI System):
                                         R = PV/T.
                                          g
                                                                             2
                                         286.9 J/kg-K × (0.101972 kg-m/J) = (215.14 kN/m )V/(148.88 +275)K.
                                                  3
                                         V = 57.36 m /kN.
                                                                  3
                                            = 1∕V = 1∕57.46 = 0.0174 kN/m .
                                         Mass flow =   Q =   Av
                                                             3
                                                                         2
                                                                            2
                                                 = (0.0174 kN∕m )[(  ∕4)(0.0254) m ](9.75 m∕s)
                                                 = 0.0000859 kN∕s
                                                 = 0.00875 kg∕s
                                                 = 8.75 g∕s.
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