Page 351 - Bird R.B. Transport phenomena
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§11.1  The Energy Equation  335

                         disintegrations  have  not  been  included  in  the  energy  balance.  In Chapter  19,
                         where  the energy  equation  for  mixtures  with  chemical reactions  is  considered,
                         the  chemical  heat  source  S c  appears  naturally,  as  does  a  "diffusive  source
                         term," S (j a  • j.
                                     g
                                ft
                    We  now  translate  Eq.  11.1-1 into mathematical terms. The rate  of  increase  of  kinetic
                 and internal energy  within  the volume  element  Ax  Ay  Az  is

                                            Ax  Ay Az — (\pv 2  + pU)                (11.1-2)

                 Here  U  is  the  internal^ energy  per  unit  mass  (sometimes  called  the  "specific  internal en-
                                                                                         2
                 ergy").  The product pU  is the internal energy  per unit volume, and \pv 2  = \p{v\ + v 2  + v )
                                                                                          z
                 is the kinetic energy  per unit volume.
                    Next  we  have  to know  how  much energy  enters  and  leaves  across  the  faces  of  the
                 volume  element  Ax  Ay  Az.
                            Ay  Az(e \  -  e \  )  +  Ax  Az(e | y y  -  е |  )  +  Ax  Ayfe | 2 2  -  e \ ^ )  (11.1-3)
                                                                           z z+/
                                                                               z
                                  x x
                                                         у у+Ду
                                       x x+Ax
                 Keep  in mind  that the e vector  includes  the convective  transport  of  kinetic and internal
                 energy, the heat conduction, and the work  associated  with  molecular  processes.
                    The rate at which  work  is done on the  fluid  by  the external  force  is  the dot product
                 of  the  fluid velocity  v and the force  acting on the  fluid  (p Ax  Ay  Az)g, or
                                          p Ax  Ay bz(v g  + v g  +  v g )           (11.1-4)
                                                    x x   y  y  z z
                    We  now  insert  these various  contributions into Eq.  11.1-1 and  then divide  by  Ax  Ay
                 Az. When  Ax,  Ay, and  Az are allowed  to go  to zero, we  get
                                              де х       +p{Vxgx   + v  + Vz8z)
                             dt {                       ч            >*>             (11.1-5)

                 This equation may be written more compactly in vector notation as
                                       f  ( > 2  + pU)  = -(V  •  e)  + p(v  • g)
                                        t  2                                         (11.1-6)

                 Next we  insert the expression  for  the e vector  from  Eq. 9.8-5 to get the equation of energy:

                                   |  (W  + u) = -(V  •  O  2  + pLDv) -  (V  •  q)
                                            P
                                   rate of increase of  rate of energy addition  rate of energy addition
                                   energy per unit  per unit volume by  per unit volume by
                                   volume        convective transport  heat conduction
                                     -(V-pv)     - ( V - [ T - V ] >  + p(v • g)     (11.1-7)
                                     rate of work  rate of work done  rate of work done
                                     done on fluid  per on fluid  per unit  on fluid per unit
                                     unit volume by  volume by  viscous  volume by external
                                     pressure  forces  forces  forces


                 This equation does  not include nuclear, radiative, electromagnetic, or chemical forms  of
                 energy.  For viscoelastic  fluids,  the next-to-last  term has  to be reinterpreted by  replacing
                 "viscous"  by  "viscoelastic."
                     Equation  11.1-7 is  the main result  of  this  section, and  it provides  the basis  for  the re-
                 mainder  of the chapter. The equation can be written in another form  to include the poten-
                 tial  energy  per unit mass,  Ф, which  has  been  defined  earlier  by  g  =  — VO  (see  §3.3). For
                 moderate  elevation  changes,  this  gives  Ф = gh,  where  h  is  a  coordinate in  the direction
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