Page 138 - Fundamentals of The Finite Element Method for Heat and Fluid Flow
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STEADY STATE HEAT CONDUCTION IN MULTI-DIMENSIONS
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                        where x o and y o are the coordinates of the point source. In the above equations, all the
                                                                                  ∗
                        shape function values must be evaluated at (x o ,y o ) (note that although G is a point source,
                        in two dimensions, it is a line source in the thickness direction and expressed in units of
                        W/m). The contribution from the point source is then appropriately distributed to the three
                        nodes of the element that contains the point source.
                           In order to demonstrate the characteristics of two-dimensional steady state heat transfer,
                        the temperature distribution in a flat plate having constant temperature boundary conditions
                        is considered in the following example.
                        Example 5.2.1 A square plate of unit thickness, size 100 cm, as shown in Figure 5.4, is
                        subjected to isothermal boundary conditions of 100 C on all sides except the top side, which
                                                                 ◦
                                       ◦
                        is subjected to 500 C. If the thermal conductivity of the material is constant and equal to
                        10 W/m C, determine the temperature distribution using linear triangular finite elements.
                              ◦
                           The square domain is first divided into eight equal-sized linear triangular elements, as
                        shown in Figure 5.5. Two sets of elemental [K] matrices exist because of the orientation of
                        the triangles. For elements 1, 3, 5, and 7, we have the following elements of the [K] matrix:
                                         b 1 = y 2 − y 4 =−0.50;  c 1 = x 4 − x 2 =−0.50
                                         b 2 = y 4 − y 1 = 0.50;  c 2 = x 1 − x 4 = 0.00

                                         b 4 = y 1 − y 2 = 0.00;  c 4 = x 2 − x 1 = 0.50    (5.11)

                                                        500°C




                                                                   100°C   1 m
                                            100°C



                                                        100°C
                                                        1 m
                               Figure 5.4  Square plate with different temperature boundary conditions

                                                   7        8         9

                                                         6        8
                                                      5        7
                                                  4        5          6
                                                         2        4
                                                     1
                                                               3
                                                   1        2        3
                                       Figure 5.5 Discretization using triangular elements
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