Page 178 - Modelling in Transport Phenomena A Conceptual Approach
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158           CHAPTER 6.  STEADY-STATE MACROSCOPIC BALANCES


            The rate of work done on the system by the surroundings is given by
                             w  =  ws  +  (P?m)jn-(P?m),t                    (6.3-8)
                                     *  P
                                   Shaft work       Flow work
            In Figure 6.2, when the stream enters the system, work  is done on the system by
            the surroundings.  When the stream leaves the system, however, work is done by
            the system on the surroundings. Note that the boundaries of  the system are fixed
            in the case of  a steady-state flow system.  Therefore, work associated with volume
            change is not included in Eq. (6.3-8).
               Substitution  of  Eq. (6.3-8) into Eq.  (6.3-7) and  the use  of  the definition of
            enthalpy, i.e., H  =  + PP, gives




            which is known as the steady-state energy equation.
               Kinetic and potential energy terms in Eq.  (6.3-9) are expressed in the form
                                           ..
                                           EK=-v 2                          (6.3-10)
                                                 1
                                                 2
            and
                                            Ep=gh                           (6.3-11)
            where  g  is the  acceleration of  gravity and  h  is the elevation with  respect  to  a
            reference plane.
               Enthalpy, on the other hand, depends on temperature and pressure. Change in
            enthalpy is expressed by
                                   dfi = CpdT + C(1-  8T)dP                 (6.3-12)
            where  is the coeficient of  volume expansion and is defined by


                                                                            (6.3-13)

            Note that
                                    0    for an incompressible fluid
                              8={ 1/T for an ideal gas                      (6.3-14)
               When the changes in the kinetic and potential energies between the inlet and
            outlet of the system are negligible, Eq.  (6.3-9) reduces to




            In terms of  molar quantities, Eqs.  (6.3-9) and (6.3-15) are written as
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