Page 366 - Bird R.B. Transport phenomena
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348   Chapter  11  The Equations  of Change for Nonisothermal Systems


                                               — —  I  у  = dimensionless horizontal coordinate  (11.4-41)
                                               fiaHJ  J
                                              (  A V / 2
                                          ф г  = ( —=z J  v z  = dimensionless vertical velocity  (11.4-42)
                                         ф  = I -r—  Vy  = dimensionless horizontal velocity   (11.4-43)
                                          ч    3
                                              \a B/
                           in  which a  = k/pC  and В = pg/3(T 0  -  T ).
                                          p
                                                           }
                               When  the  equations  of  change,  without  the  dashed-underlined  terms,  are  written  in
                           terms  of these dimensionless variables, we get
                                                            дфи  дф
                           Continuity                       ~ ^  +  ^ F ?  =  0               (11.4-44)

                           Motion                  ^  0v T" + <k т?  <fc = ^ т  + ®           (11.4-45)
                                                                      8-j
                                                                        H
                           Energy                     I ф„ ^-  + ф  ^- 10 = — -               (11.4-46)
                                                               г
                           The  preceding boundary  conditions then become

                           B.C.  1:               a t г) = О,  ф  = ф  = Ъ,  0 - 1            (11.4-47)
                                                                   г
                                                               у
                           B.C.  2:               asrj-»*),   ф ^ 0 ,      0^0                (11.4-48)
                                                               2
                           B.C.3:                 at£ = 0,    ф  = О                          (11.4-49)
                                                               г
                           One  can see immediately  from  these equations and boundary  conditions that the dimension-
                           less  velocity  components  ф  and ф  and the dimensionless  temperature  0  will  depend  on 17
                                                       2
                                                 у
                           and  £ and  also on the Prandtl number, Pr. Since the flow is usually very slow in free convec-
                           tion, the terms in which  Pr appears will generally be rather small; setting them equal to zero
                           would  correspond  to the "creeping  flow assumption."  Hence we expect that the dependence
                           of the solution on the Prandtl number will be weak.
                               The average heat flux  from one side of the plate may be written as
                                                                                                - "
                                                           HJ 0  \  -*,)\J*                   (n 4 50)
                           The integral may now be written in terms of the dimensionless quantities
                                                           В  V  м  Г(  дв\
                                                                              лг
                                                               1/4
                                                                 •c

                                                                                "'  •  1/4


                                               =  С • £  (Г  -  T )(GrPr) 1/4                   (11.4-51)
                                                         о   1
                           in  which the grouping Ra = GrPr is referred  to as the Rayleigh number. Because 0  is a  function
                           of  17,  £, and  Pr, the derivative dS/drj  is also a function  of  17, £, and  Pr. Then d<d/dir), evaluated
                           at  17 =  0, depends only on £ and Pr. The definite integral over £ is thus a function  of Pr. From
                           the remarks made earlier, we can infer  that this function,  called  C, will be only a weak  func-
                           tion  of the Prandtl number—that is, nearly a constant.
                               The  preceding  analysis  shows  that,  even  without  solving  the  partial  differential  equa-
                           tions, we can predict that the average heat flux is proportional to the f-power  of the tempera-
                           ture  difference  (T o  -  T }) and  inversely  proportional  to  the J-power  of  H.  Both  predictions
                           have been confirmed  by experiment. The only thing we could not do was to find  С as a  func-
                           tion of Pr.
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