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                        4.8 TREATMENT OF TURBULENT FLOWS
                        Laminar-to-Turbulent Transition                            May 25, 2005  11:7  89
                        To predict laminar-to-turbulent transition, the effective value of 
   is written as
                                                          µ        µ t
                                                 
  ,eff =   + ϒ       ,                   (4.98)
                                                         Pr       Pr t,
                        where the intermittancy factor ϒ is given [1] by

                                                                 x − x ts
                                             ϒ = 1 − exp   −5              .               (4.99)
                                                                x te − x ts
                        In this equation, x ts and x te denote the start and the end of transition, respectively.
                        When x = x te , ϒ = 1 and a fully turbulent state is reached. For x = x ts , ϒ = 0 and
                        the flow is laminar. There are several empirical relations proposed in the literature
                        for estimating x ts and x te ; here, two will be given.


                        Abu-Ghannam and Shaw Model
                        In the Abu-Ghannam and Shaw [1] model


                                              U ∞ δ 2,s                    Tu
                                      Re δ 2 ,s =     = 163 + exp m    1 −       ,        (4.100)
                                                 ν                         6.91
                                                                 2
                        where m (K > 0) = 6.91−12.75K + 63.64K and m (K < 0) = 6.91− 2.48K −
                                            2
                               2
                        12.27K and K =−δ /ν (dU ∞ /dx). Here, δ 2,s is the boundary layer momentum
                                            2
                        thickness at x = x ts . These relations thus identify x ts . The value of x te is identified
                        with
                                                                ν ∞ σ o
                                                  x te = x ts + 4.6   ,                   (4.101)
                                                                u ∞ B
                                                                                  3.5 0.5
                        where B(K < 0) = 1, B(K > 0) = 1 + 1710 K  1.4  exp −(1 + Tu ) , and σ 0 =
                                                  3.5 −1
                           5
                                        3.5
                        10 (2.7 − 2.5 Tu )(1 + Tu ) . Here, Tu is the turbulence intensity in the free
                        stream.
                        Cebeci Model
                        In the Cebeci [4] model

                                                             22400      0.46
                                                = 1.174 1 +          Re    ,              (4.102)
                                            Re δ 2                      x
                                                               Re x
                                                                 ν ∞    −2/3
                                                    x te = x ts + 60  Re x  ,             (4.103)
                                                                 U ∞
                        where Re x = U ∞ x /ν.


                        4.8.2 e–  Model

                        In this model, the turbulent viscosity is determined from solution of two partial
                        differential equations for scalar quantities e (turbulent kinetic energy) and
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