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SOME EXAMPLES OF FLUID FLOW AND HEAT TRANSFER PROBLEMS
                        equations in the gravitational direction. In this section, we will consider a forced heat
                        convection problem in the downstream portion of a backward-facing step. For coupled
                        natural and mixed convection problems, the readers are referred to Chapter 7.  281
                        9.3.1 Backward-facing step
                        The problem definition is similar to the isothermal flow past a backward-facing step as
                        discussed in the previous section, the difference being that additional boundary conditions
                        are prescribed for the temperature field. The boundary conditions discussed in reference
                        (Kondoh et al. 1993) will be adopted. The solid downstream bottom wall was assumed to
                        be at a higher temperature than the fluid (results presented here are for air with Pr = 0.71)
                        entering the channel. All other solid walls were assumed to be insulated. All other boundary
                        conditions for the velocity and pressure values are the same as the ones discussed for the
                        isothermal problem in the previous section and are repeated in Figure 9.19.
                           Three different meshes have been employed to make sure that the solutions presented
                        are accurate. The first mesh used was mesh (a) in Figure 9.9. The second and third meshes
                        are finer than the first mesh and are shown in Figure 9.20.
                           A maximum Reynolds number of 500 was studied. All three meshes were employed to
                        study the heat transfer at this Reynolds number. The local Nusselt number distribution on
                        the hot wall downstream of the step is shown in Figure 9.21. As seen, the Nusselt number

                                        Parabolic u and u = 0, T = 0
                                                    2
                                                1
                                  2L                                               p = 0
                                                            u = u = 0
                                                             1
                                                                 2
                                                                    T = 1
                                   L
                                            4L                  36L
                        Figure 9.19 Forced convection heat transfer downstream of a backward-facing step.
                        Geometry and boundary conditions






                                               (a) Mesh2, nodes:8131, elements:15,410






                                               (b) Mesh3, nodes:11,659, elements:22,257

                        Figure 9.20 Forced convection heat transfer downstream of a backward-facing step.
                        Unstructured meshes
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