Page 61 - Modelling in Transport Phenomena A Conceptual Approach
P. 61

42                              CHAPTER 3.  INTERPHASE TRANSPORT










                               -  L   ,
                               Figure 3.1  Flow on a flat plate.

             As an engineer we are interested in the determination of the total drag force, i.e.,
          the component of  the force in the direction of flow, exerted by the flowing stream
          on the plate.  This force can be calculated by integrating the total momentum flux
          at the wall over the surface area. The total momentum flux at the wall, 7ryZly=o,  is
                                                                            (3.1-1)
          where  7yzly,o  is  the  value of  the  shear  stress at the  wall.  Since the  plate  is
          stationary, the fluid which is in contact with the plate is also stagnant'  and both
          v,  and vy are zero at y = 0.  Therefore, Eq.  (3.1-1) reduces to
                                                                            (3.1-2)
          and the drag force, FD, on one side of  the plate can be calculated from

                                    FD = Jd"  Jd"  Tw dxdz                  (3.1-3)

             Evaluation of  the  integral in  Eq.  (3.1-3) requires the value of  the  velocity
          gradient at the wall, which can be obtained from the solution of  the equations
          of  change.  Since this is almost an impossible task in most cases, it is customary
          in engineering practice to replace rw by a dimensionless term called the fnction
          factor, f, such that
                                       I     1      I
                                                                            (3.1-4)

          Substitution of Eq.  (3.1-4) into Eq.  (3.1-3) gives
                                         L
                       FD = 1 pv& Jd"  Jd  f dxdz = (WL)                    (3.1-5)
                             2
          where (f) is the friction factor averaged over the area of the plate2, i.e.,
                                 rW  rL
                                        f dxdz
                                                & Jd"  1" f dxdz            (3.1-6)



            'This  is known as the no-slip  boundary condition.
            2See Section A.2 in Appendix A.
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