Page 267 - Fundamentals of The Finite Element Method for Heat and Fluid Flow
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                        CONVECTION IN POROUS MEDIA



















                        Figure 8.8 Buoyancy-driven flow in a fluid-saturated porous medium. Finite element
                        mesh. Nodes: 2601, elements: 5000


                        the non-Darcy effects. It is clearly obvious that the maximum velocity in the Darcy flow
                        regime, at a Darcy number of 10 −6 , is located very close to the solid walls. The non-Darcy
                        velocity profile, at a Darcy number of 10 −2 , on the other hand, looks very similar to that
                        of a single-phase fluid, and the maximum velocity is located away from the solid walls. At
                        a Darcy number of 10 −4 , the flow undergoes a transition from a Darcy flow regime to a
                        non-Darcy flow regime. The temperature contours also undergo noticeable changes as the
                        Darcy number increases from 10 −6  to 10 −2 .
                           Both the scheme and the model implementation have been designed in such a way that
                        as the Darcy number increases, the flow approaches a single-phase fluid flow, which is
                        evident from Figure 8.9
                           In Table 8.2, the quantitative results obtained from the above analysis (only for the
                        Darcy flow regime, Da < 10 −5 ) are compared with other available analytical and numerical


                                 Table 8.2 Average Nusselt number comparison with analytical
                                 and numerical results

                                     ∗
                                  Ra = RaDa                   Nu
                                                Analytical  Numerical1  Numerical2  CBS
                                       10          –         1.07          –       1.08
                                       50         1.98         –         2.02      1.96
                                      100         3.09       3.09        3.27      3.02
                                      500         8.40         –           –       8.38
                                     1000        12.49      13.41       18.38     12.52
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