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26 Fluid Mechanics, Thermodynamics of Turbomachinery
                          a blade in a compressor or turbine cascade caused by the deflection or acceleration
                          of fluid passing the blades.
                            Considering a system of mass m, the sum of all the body and surface forces acting
                          on m along some arbitrary direction x is equal to the time rate of change of the total
                          x-momentum of the system, i.e.
                                     d
                              F x D   .mc x /.                                            (2.9)
                                     dt
                          For a control volume where fluid enters steadily at a uniform velocity c x1 and leaves
                          steadily with a uniform velocity c x2 , then
                                            c x1 /                                        (2.9a)
                              F x DPm.c x2
                          Equation (2.9a) is the one-dimensional form of the steady flow momentum equation.

                          Euler’s equation of motion

                            It can be shown for the steady flow of fluid through an elementary control volume
                          that, in the absence of all shear forces, the relation
                              1
                                dp C cdc C gdz D 0                                        (2.10)

                          is obtained. This is Euler’s equation of motion for one-dimensional flow and is
                          derived from Newton’s second law. By shear forces being absent we mean there
                          is neither friction nor shaft work. However, it is not necessary that heat transfer
                          should also be absent.
                          Bernoulli’s equation

                            The one-dimensional form of Euler’s equation applies to a control volume whose
                          thickness is infinitesimal in the stream direction (Figure 2.3). Integrating this equa-
                          tion in the stream direction we obtain
                              Z
                                2
                                 1      1  2   2
                                   dp C .c 2  c / C g.z 2  z 1 / D 0                     (2.10a)
                                               1
                               1        2

















                                           FIG. 2.3. Control volume in a streaming fluid.
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