Page 152 - Fundamentals of The Finite Element Method for Heat and Fluid Flow
P. 152

144
                           The Galerkin formulation and the element equations are similar to those for two-
                        dimensional heat transfer problems, but are different owing to the ring nature of the
                        elements.        STEADY STATE HEAT CONDUCTION IN MULTI-DIMENSIONS
                           The differential equation in a cylindrical coordinate system (r, z) for steady state is
                                                             2
                                             2
                                                                     2
                                            ∂ T   k r ∂T  k θ ∂ T   ∂ T
                                          k r  2  +    +   2  2  + k z  2  + G = 0          (5.57)
                                            ∂r    r ∂r    r ∂θ      ∂z
                           An axisymmetric problem is independent of the angle θ and hence Equation 5.57
                        reduces to
                                                                 2
                                                ∂T  2  k r ∂T   ∂ T
                                              k r  2  +     + k z  2  + G = 0               (5.58)
                                                ∂r     r ∂r     ∂z
                           This can be rewritten, if the thermal conductivity in the radial direction, k r is constant, as
                                                                  2
                                             1     ∂     ∂T      ∂ T
                                                k r   r      + k z   + G = 0                (5.59)
                                             r    ∂r   ∂r        ∂z 2
                           The boundary conditions are

                                                                 T = T b  on  	 1
                                         ∂T      ∂T
                                       k r  l + k z  n + h(T − T a ) + q = 0  on  	 2       (5.60)
                                          ∂r     ∂z
                           The temperature distribution is described as follows:

                                                  T = N i T i + N j T j + N k T k           (5.61)
                        which is similar in form to that of a linear triangular plane element, where

                                                        1
                                                  N i =   (a i + b i r + c i z)
                                                       2A
                                                        1
                                                  N j =   (a j + b j r + c j z)
                                                       2A
                                                        1
                                                  N k =   (a k + b k r + c k z)             (5.62)
                                                       2A
                           The area, A, is calculated from

                                                            &       &
                                                            & 1 r i z i  &
                                                            &       &
                                                    2A = det 1 r j z j  &                   (5.63)
                                                            &
                                                            &       &
                                                             1 r k z k
                                                            &       &
                           Other constants in Equation 5.62 are defined as
                                          a i = r j z k − r k z j ; b i = z j − z k ; c i = r k − r j
                                          a j = r k z i − r i z k ; b j = z k − z i ; c j = r i − r k
                                          a k = r i z j − r j z i ; b k = z i − z j ; c k = r j − r i  (5.64)
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