Page 299 - Modelling in Transport Phenomena A Conceptual Approach
P. 299

8.2.  ENERGY TRANSPORT WITHOUT CONVECTION                           279

             Integration of  Eqs.  (8.2-69) and (8.270) over the cross-sectional area of  the fin
          gives the boundary conditions associated with Eq.  (8.2-77) as

                                      at  z=O     (T)=Tw                   (8.2-78)
                                                  -
                                      at  r=L     d(T)  =O                 (8.2-79)
                                                   dz
          It is important to note that Eqs.  (8.2-64) and (8.2-77) are at two different scales.
          Equation (8.2-77) is obtained by  averaging Eq.  (8.2-64) over the cross-sectional
          area perpendicular to the direction of energy flux. In this way the boundary condi-
          tion, i.e., the heat transfer coefficient, is incorporated into the governing equation.
          Accuracy of  the measurements dictates the equation to work with since the scale
          of  the measurements should be compatible with the scale of  the equation.
             The term 2/B in Q.  (8.2-77) represents the heat transfer area per unit volume
          of  the fin, i.e.,
                                2
                               _-   2 LW    Heat transfer area             (8.2-80)
                                B-BLW=         Fin volume
          The physical significance and the order of  magnitude5 of  the terms in Eq.  (8.2-77)
          are given in Table 8.7.



          Table 8.7  The physical significance and the order of  magnitude of  the terms in
          Eq.  (8.2-77).

                Term            Physical Significance   Order of  Magnitude
                                 Rate of  conduction

            2(h)             Rate of heat transfer from   2(~)(Tw - Tco)
             B
            - ((T) - Tco)    the fin to the surroundings        B


          Therefore, the ratio of the rate of  heat transfer from the fin surface to the rate of
          conduction is given by

                    Rate of heat transfer  -  2(h)(Tw - T,)/B  - 2(h)L2    (8.2-81)
                                       -
                                                         --
                    Rate of conduction    k(Tw - T,)/L2      kB
             5The order of  magnitude or  scale  analysis is a powerful tool  for those interested  in  mathe-
          matical modelling.  As stated by Astarita (1997), “Very often more than nine-tenths of  what one
          can ever hope to know about a problem can be obtained from this tool, without actually solving
          the problem; the remaining one-tenth  requires painstaking algebra and/or  lots of computer time,
          it adds very  little to our  understanding  of  the problem,  and  if  we  have not  done the first part
          right,  all that the algebra and the computer  will produce will be a lot of nonsense.  Of  course,
          when nonsense comes out of  a computer  people have a lot of  respect  for  it, and that is exactly
          the problem.”  For more details on the order of  magnitude  analysis, see Bejan  (1984), Whitaker
          (1976).
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