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                        CONVECTION HEAT TRANSFER
                        7.11.3 Mixed convection heat transfer
                        A mixed convection heat transfer mode has features of both forced and natural convection.
                        The mixed convection solution to a heat transfer problem is necessary if the Reynolds num-
                        ber is small and the importance of the buoyancy contribution is significant. The equations
                        solved are those of forced convection with the addition of a source term (Equation 7.70)
                        in the gravitational direction. If the direction of gravity is not aligned with either of the
                        coordinate directions (x 1 and x 2 ), then appropriate components of the source term need to
                        be added to the momentum equations. The effect of mixed convection can be measured by
                        calculating the source term of Equation 7.70. If this term is close to zero, then the buoyancy
                        effects can be ignored and a forced convection solution is sufficient. However, if the value
                        of the source term is far from being zero (either in the negative or positive sense), then a
                        mixed convection solution is essential.
                           Here we consider a simple mixed convection problem in a rectangular vertical channel
                        as shown in Figure 7.29. In order to compare the results with the analytical solution for


                                                            Flow reversal
                                                               p = 0













                                          Cold wall            Hot wall
                                          u 1 = u 2 = 0  g    u 1 = u 2 = 0  3
                                           T c = 0              T h = 1

                                                     x 2

                                                          x 1





                                                   Cold fluid in
                                                     u 2 = 1
                                                     u 1 = 0
                                                     T a = 0

                                                       1
                        Figure 7.29  Mixed convection in a vertical channel. Geometry and boundary conditions
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