Page 117 - Fundamentals of The Finite Element Method for Heat and Fluid Flow
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STEADY STATE HEAT CONDUCTION IN ONE DIMENSION




                                                        T o                                   109

                                               T w           T w





                                             x =−L   x = 0  x =+L
                                            Figure 4.6  Plane wall with heat source


                           The boundary conditions are

                                                    at x =±L, T = T w                       (4.28)

                           Integrating twice, we get

                                                        G x 2
                                                  T =−       + C 1 x + C 2                  (4.29)
                                                        k 2
                           From the symmetry of the problem, we find at x = 0, dT/dx = 0. Since T is a maximum
                        at the centre, then C 1 = 0and C 2 = T o . Therefore, Equation 4.29 becomes
                                                           G x 2
                                                     T =−       + T o                       (4.30)
                                                           k 2
                           The temperature, T w , at both ends can be obtained by substituting x =±L,which
                        results in
                                                           G L 2
                                                     T w =−     + T o                       (4.31)
                                                            k 2
                           Similarly, at the centre, that is, x = 0,

                                                               GL 2
                                                      T o = T w +                           (4.32)
                                                                2k
                           From Equations 4.30, 4.31 and 4.32, we can write

                                                                x
                                                                   2
                                                      T − T o
                                                             =                              (4.33)
                                                     T w − T o  L
                        which shows that the temperature distribution is parabolic.
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