Page 106 - Introduction to Computational Fluid Dynamics
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                        4.7 SOURCE TERMS
                        selecting that   for which the thickness is largest. Usually, the largest thickness 11:7  85
                        will correspond to the largest 
   , and for this selected  , we evaluate
                                            |  JN −   JN−1 |             −3
                                                                   ∗
                                       R =                ,       = 10      (say),         (4.73)
                                                    ∗
                        where    is a sufficiently small reference quantity. Since Equation 4.43 is it-
                                  ∗
                        eratively solved, Patankar [52] has suggested the following formula for exact
                        evaluation:
                                                                      n
                                                 ˙ m E (exact) = ˙ m E,std × R ,           (4.74)
                        where, from computational experience, n 
 0.1 is found to be a convenient value
                        in most cases. Thus, when Equation 4.43 has converged, ψ E , as evaluated from

                        Equation 4.72, will provide a correct estimate of total mass flow rate ψ EI = ψ E − ψ I
                        through the boundary layer at the given x. Once this mass flow rate is known, the
                        y dimension and hence the largest boundary layer thickness among all  s can be
                        estimated.



                        4.7 Source Terms

                        4.7.1 Pressure Gradient

                        In external boundary layers, the pressure gradient is specified or indirectly evaluated
                        from
                                                   dp           dU ∞
                                                                     ,                     (4.75)
                                                      =−ρ U ∞
                                                   dx            dx
                        where U ∞ (x) is specified. In internal flows, however, a special procedure must be
                        adopted to specify the pressure gradient. The procedure relies on satisfying the
                        overall mass flow rate balance at every streamwise location x. Thus, in a general
                        duct, let A d (x) represent the duct area between the axis of symmetry (I boundary)
                        and the wall (E boundary). Then

                                                                      dω
                                                    	  E          	  1
                                               A d =    rdy = ψ EI       .                 (4.76)
                                                     I             0  ρ u
                        Therefore,

                                              A d                      ω j
                                                  = C (constant) =        .                (4.77)
                                              ψ EI                    ρ j u j
                           The task now is to replace u j in terms of the pressure gradient. To do this,
                        Patankar [52] writes the discretised version of the momentum equation as
                                      AP j u j = AN j u j+1 + AS j u j−1 + D j −  V j p x ,  (4.78)
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