Page 178 - Bird R.B. Transport phenomena
P. 178

162  Chapter 5  Velocity Distributions in Turbulent Flow

                               (iv)  The  coefficient  of  the fourth  term involves  the third  derivative,  which  may  be
                            obtained  from  Eq. 5.3-8, and this is

                                                              y    dv' y
                                                             г-  -г  Z  -г—
                                                                              2
                                                  i/=o  ^  V  x  ду 2  ду  ду  y  ду 1  y=o
                                                               ох ^11Г)\       = 0              (5.3-11)
                                                                +
                            Here Eq. 5.2-11 has been  used.
                               There appears  to be no reason to set the next coefficient  equal to zero, so we  find  that
                            the  Taylor  series, in dimensionless  quantities, has the form



                            The  coefficient  С has been obtained experimentally, 6  and therefore we have the final  result:

                                                                                     y D
                                              , 1 /  Г  v  Y3M_l(j^Y ...l          < *<5       (5313)
                                                                       +          0
                            The  y 3  term in the brackets  will turn out to be very  important in connection with  turbu-
                            lent heat and mass  transfer  correlations in Chapters 13,14, 21, and 22.
                               For  the  region  5  <  yojv  <  30  no  simple  analytical  derivations  are  available,  and
                            empirical  curve  fits  are sometimes  used.  One  of  these  is  shown  in Fig.  5.5-3  for  circular
                            tubes.


      §5.4  EMPIRICAL     EXPRESSIONS FOR THE
            TURBULENT MOMENTUM FLUX

                            We  now  return to the problem  of  using  the time-smoothed equations  of  change  in Eqs.
                            5.2-11  and  12  to  obtain  the  time-smoothed  velocity  and  pressure  distributions.  As
                            pointed out in the previous  section, some information about the velocity  distribution can
                                                                                                    (0
                            be  obtained  without  having  a  specific  expression  for  the turbulent  momentum flux  т .
                            However,  it has  been  popular  among  engineers  to use  various  empiricisms  for  т  ( 0  that
                            involve velocity  gradients.  We  mention a  few  of  these, and  many more can be  found  in
                            the  turbulence literature.


      The  Eddy Viscosity  of  Boussinesq
                            By analogy  with Newton's law  of viscosity, Eq. 1.1-1, one may write  for a turbulent shear
                            flow 1

                                                           r<?=  V ° ^                           (5.4-1)



                               6
                                 С S. Lin, R. W. Moulton, and G. L. Putnam, Ind. Eng. Chem., 45, 636-640 (1953); the numerical
                            coefficient  was determined from  mass transfer  experiments in circular tubes. The importance of the y 4
                            term in heat and mass transfer was recognized  earlier by E. V. Murphree, Ind. Eng. Chem., 24, 726-736
                            (1932). Eger Vaughn Murphree (1898-1962)  was captain of the University  of Kentucky football  team in
                            1920 and became President of the Standard Oil Development Company.
                               1
                                 J. Boussinesq, Mem. pres. par div. savants a Vacad. sci. de Paris, 23, #1,1-680  (1877), 24, #2,1-64 (1877).
                            Joseph Valentin Boussinesq  (1842-1929), university  professor  in Lille, wrote a two-volume  treatise on
                            heat, and is famous  for the "Boussinesq  approximation" and the idea of "eddy viscosity."
   173   174   175   176   177   178   179   180   181   182   183