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2.4  Reduced  Forms  of the  Navier-Stokes  Equations                  59



         approximation  to  Eqs.  (2.2.45)-(2.2.47),  with  77 locally  normal  to  the  surface
         and  all the  viscous  terms  associated  with  derivatives  neglected,  we  obtain

                                 dQ    dE    OF
                                 —-  H     1       Re  drj                  (2.4.7)
                                 dr    <9£   dr\
         where

                                             0
                                       r] xmi  +  rj ym2
                     - 1
                    J                                                     (2.4.8a)
                                       Vxm2  +  r} ym3
                                                  um
                         rj x(umi  +  vrri2 +  777,4) +  Vy( 2  +  vrri3 +  777,5)
         with
                                 m i  =           2r  v
                                       3 ^ ^     ~ 1y v)



                                 7773  =  - ( - 2 7 7 ^  +  477^^)
                                                                          (2.4.8b)
                                           M       5  /  2x
                                 7774  =
                                       Pr( 7
                                           V       9  (  2N
                                 7775
                                       P r ( 7 - 1 )  '^77
            Equation  (2.4.7)  is  strictly  for  laminar  flows.  As  is  shown  in  Chapter  3,  its
         extension  to  turbulent  flows  is usually  carried  out  by  using  eddy  viscosity  (e m)
         and  turbulent  Prandtl  number  (Pr$)  concepts.  This  is  done  by  replacing  the
         coefficient  of  viscosity  /i  by
                                         /i +  QS m                        (2.4.9)

                                                              (
         and  by  replacing  the  coefficient  of thermal  conductivity  k =  fiC p/Pr)  with
                                                                          (2.4.10)

         The  relations  can  easily  be  incorporated  into  Eq.  (2.4.7)  by  replacing  \i  in  the
         definitions  of  777,1, ^7,2,  777,3 by

                                       /7(1  +£m/v)                       (2.4.11)
         and  [/i/Pr(7  —  1)]  in the  definitions  of  7774 and  7775 by

                                     M     f 1,  P r  £m
                                                                          (2.4.12)
                                      -  1)  V  Prt  v
                                  Pr( 7
         Unlike  /i  and  fc,  however,  the  parameters  e m  and  Pr^  are  not  properties  of  the
         fluid  but  depend  on the  flowfield  and  are related to the velocity and  temperature
         field  by  empirical  formulas.
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