Page 170 - Mechanical Engineers' Handbook (Volume 4)
P. 170

1 Conduction Heat Transfer  159



























                                               Figure 2 Heat transfer by extended surfaces.


                                                     dT    hC
                                                      2
                                                              (T   T )   0

                                                     dx 2  kA
                              The solution of this equation depends on the boundary conditions existing at the tip,
                           i.e., at x   L. Table 11 shows the temperature distribution and heat-transfer rate for fins of
                           uniform cross section subjected to a number of different tip conditions, assuming a constant
                           value for the heat-transfer coefficient, h.
                              Two terms are used to evaluate fins and their usefulness. The first of these is the fin
                           effectiveness, defined as the ratio of the heat-transfer rate with the fin to the heat-transfer
                           rate that would exist if the fin were not used. For most practical applications, the use of a
                           fin is justified only when the fin effectiveness is significantly greater than 2. A second term
                           used to evaluate the usefulness of a fin is the fin efficiency,   , This term represents the ratio
                                                                          ƒ

            Table 11 Temperature Distribution and Heat-Transfer Rate at the Fin Base (m   
hc/kA)

                                                    T   T                        Heat-Transfer Rate
            Condition at x   L                      T   T                        q/mkA (T b   T   )
                                                     b
                   T )   k                         h                                 h
                           dT
            h(T x L                   cosh m(L   x)    sinh m(L   x)        sinh mL    cosh mL
                           dx                      mk                               mk
                              x L
              (convection)                         h                                 h
                                          cosh mL    mk  sinh mL            cosh mL    mk  sinh mL
                                      cosh m(L   x)                         tanh mL
             dT
              dx  x L    0              cosh mL
              (insulated)
                                      (T   T )/(T   T ) sinh mx   sinh m(L   x)  cosh mL   (T   T )/(T   T )
            T x L   T L                 L      b                                      L      b
              (prescribed temperature)              sinh ml                          sinh ml
                                      e  mx                                 1
            T x L   T
              (infinitely long fin, L →  )
   165   166   167   168   169   170   171   172   173   174   175