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88                                                    3.  Turbulence  Models


         3.4  Two-Equation     Models

         There  are  several  two-equation  models.  Three  of  the  more  popular,  accurate
         and  widely  used  models  are  the  k-e  model  of  Jones  and  Launder  [16], the  k-uj
         model  of  Wilcox  [1] and  the  SST  model  of  Menter  which  blends  the  k-e  model
         in the  outer  region  and  k-uj model  in the  near  wall  region  [17]. All three  models
         can  be  used  for a range  of  flow  problems  with  good  accuracy  as  discussed  in
         [1-3].  Here  we discuss the  k-e  model  which  is the  most  popular  and  widely  used
         two-equation  eddy  viscosity  model.  For a discussion  of  the  other  two  models,
         the  reader  is  referred  to  [1-3].
            In  this  model, e m is  given  by  Eq.  (3.1.4).  The  kinetic  energy k and  rate  of
         dissipation  e  are  obtained  from  the  turbulence  kinetic  energy  equation  written
         as                                        _    _
               —   =  —   IYi/+ — ^ —    1 +£   (—   +  ^ \  —   - £       (3 4  1)
                Dt    dxk  \\   &k )  dxk  J  m  \ dxj  dxi  J  dxj
        and  the  dissipation  equation

           —   =—\(v+—}—]             +c   -e   f^i^^l\^i_ c          £^   (342)
                                  x
           Dt    dxk  |A    °e)  d k\    £l  k  m  \dxj  dxi)  dxj  £2  k
           For  boundary-layer  flows  at  high  Reynolds  number,  Eqs.  (3.4.1)  and  (3.4.2)
        become
                         dk     dk _  d  femdk\         (du\ 2              (<IAO\
                        U     V                      m
                         dx     dy    dy\a kdyj          \dyJ
                  de     de    d  /e mde\       e    (du\ 2      e 2        .  A  A.
                 U  +V      =             +   £m                        ( 3 A 4 )
                  0- X d-y    0-y{^dy) ^k        {0-y)     ~ ^T
        The  parameters  c^,  c £l ,  c £2 ,  a^  and  a £  are  given  by

              Cy,  =  0.09,  c £l  =  1.44,  c £2  =  1.92,  a k  =  1.0,  a £  =  1.3  (3.4.5)

           The  set  of equations  comprising  conservation  of  mass  and  momentum,  Eqs.
         (2.2.2)  to  (2.2.4)  together  with  Eqs.  (3.4.1)  and  (3.4.2),  or  with  boundary-layer
        approximations,  Eqs.  (2.3.33),  (2.3.34),  (3.4.3)  and  (3.4.5)  for  two-dimensional
        flows together  with  the boundary  conditions  discussed  below,  represent  a  closed
        set  in which the equations  for  mean  momentum,  turbulence  energy,  and  dissipa-
        tion  rate  have the  same  form  and  can  generally be  solved  by the  same  numerical
        method.
           The  above equations  given  by Eqs.  (3.4.1)  to  (3.4.5)  apply  only to  free  shear
        flows.  For  wall  boundary-layer  flows,  they  require  modifications  to  account  for
        the  presence  of  the  wall. Without  wall  functions,  it  is  necessary  to  replace  the
        true  boundary  conditions  at  y  — 0  by  new  "boundary  conditions"  defined  at
        some distance  yo outside the  viscous sublayer  to  avoid  integrating the  equations
        through  the  region  of  large  y  gradients  near  the  surface  as  discussed  in  [2, 3].
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