Page 438 - Bird R.B. Transport phenomena
P. 438

420   Chapter 13  Temperature Distributions in Turbulent Flow
                           From this we  can calculate the local time-averaged  heat flux at the wall:

                                                                 k(T 0  -T,) \                (13.6-22)
                                                                         d
                                                                  p - 1 / 3 D  Y=0
                                                                   r
                           and  the local Nusselt number is then
                                                          q D
                                                 Nu loc  =  k(T 0  0 -  Т )  =  Pr i/3  _  dY  (13.6-23)
                                                              г
                           Then  the  mean  Nusselt  number  over  the wall  surface  for  heat  transfer,  and  the analo-
                           gous  quantity  for  mass  transfer,  are

                                                                 =  Я,Рг 1/ 3  +  Q! 2 Pr 0   (13.6-24)
                                                             y=o

                                           *•-*"•((-#) L)--*"*            +  a Sc° +          (13.6-25)
                                                                             2
                           In  this  last  equation Sh , Э , and  Sc are the mass  transfer  analogs  of Nu , 0,  and  Pr.  We
                                              w
                                                                                       w
                                                  л
                           give the mass transfer  expression  here (rather than wait until Part III) because electrochem-
                           ical mass  transfer  experiments give better precision than heat transfer  experiments and the
                           available  range  of Schmidt numbers is much greater than that of Prandtl numbers.
                               If  the  expansions  in  Eq.  13.6-24  and  25  are  truncated  to  one  term, we  are  led  to
                                    1/3
                           Nu  m  0 е  Рг  and  Sh,, 7  oc Sc . These expressions  are essential  ingredients  in  the  famous
                                                  1/3
                                                 5
                           Chilton-Colburn relations  (see Eqs. 14.3-18 and  19, and Eqs. 22.3-22  to 24). The first term
                           in  Eq. 13.6-24  or 25 also corresponds  to the high Prandtl (or Schmidt) number  asymptote
                           of  Eq.  13.4-20. 6
                              With  the development  of  electrochemical  methods  of  measuring  mass  transfer  at
                           surfaces,  it  has  become  possible  to  investigate  the  second  term  in  Eq.  13.6-25.  In
                           Fig.  13.6-1  are  shown  the  data  of  Shaw  and  Hanratty, who  measured  the  diffusion-
                           limited  current to a wall electrode for  values  of  the Schmidt number  Sc  = /х/рЯЬ  from
                                                                                                АВ
                           693 to 37,200.  These data are fitted 3  very well by  the  expression



                                    v     °  / = 0.0575 + 0.1184 Sc- 1/ 3
                                0.07                  о           0037     -    Fig.  13.6-1.  Turbulent
                                                о       J = 0.0889 Sc"
                                                       /                        mass-transfer  data of
                                                                                D.  A. Shaw  and T. J. Han-
                                    _      О
                                                 о                    о         ratty  [AIChE Journal, 28,
                                                                                23-37,160-169  (1977)]
                                                     О     О    ^ ^ ^ ^ * » i
                                                                    1
                                                     О              О *»        compared to a curve
                                0.06                             о  о           based  on Eq. 13.6-25  (solid
                                                                      8         curve). Shown also is a
                                                                                simple power  law  function
                                        10  3               10  4               obtained by Shaw and
                                                       Sc                       Hanratty.



                               5  T. H. Chilton and A. P. Colburn, Ind. Eng.  Chem., 26,1183-1187 (1934). Thomas Hamilton Chilton
                           (1899-1972) had his entire professional career at the E. I. du Pont de Nemours Company, Inc., in
                           Wilmington, Delaware; he was President of AIChE in 1951.  After  "retiring" he was a guest professor at a
                           dozen or so universities.
                               6  See also О. С Sandall and О. Т. Hanna, AIChE Journal,  25, 290-192 (1979).
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