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                        CONVECTION IN POROUS MEDIA
                        Energy equation
                                                                    2
                                               σ  ∂T  ∗  + u ∗ i  ∂T  ∗  = k  ∗    ∂ T  ∗  !  (8.30)
                                                 ∂t  ∗   ∂x  ∗      ∂x ∗2
                                                           i          i
                           Other alternative scales are possible and the appropriate references should be consulted
                        to learn more about scaling. In the above formulation, the buoyancy effects are incorpo-
                        rated by invoking the Boussinesq approximation as discussed in Chapter 7. The kinematic
                        viscosity ν, used in the above scales, is defined as
                                                              µ
                                                          ν =                               (8.31)
                                                              ρ
                        and α is the thermal diffusivity, given as
                                                              k f
                                                       α f =                                (8.32)
                                                            (ρc p ) f
                           It may be observed that the scales and non-dimensional parameters are defined by
                        using the fluid properties. Often, a quantity called the Darcy–Rayleigh number is used in
                        the literature as a governing non-dimensional parameter for Darcy flow. This is the product
                        of the Darcy (Da) and fluid Rayleigh (Ra) numbers as defined previously.


                        8.2.2 Limiting cases

                        The equations discussed above represent a porous medium, which tends to a solid as the
                        porosity,   → 0. Thus, a conjugate problem, in which part of the domain is completely
                        solid, can be dealt with by using the above equations.
                           Another limiting case of these equations is that they approach the incompressible
                        Navier–Stokes equations as   → 1. Again, a very general problem in which the porous
                        medium and a single-phase fluid are part of the domain (porous-fluid interface (Massarotti
                        et al. 2001)) can be solved by using the above equations. Thus, many applications such as
                        alloy solidification (Sinha et al. 1992) and heat exchanger design can be analysed via these
                        equations.


                        8.3 Discretization Procedure

                        The CBS scheme will be employed to solve the porous medium flow equations. In this
                        context, the same four steps, with minor modifications, will be utilized as discussed in the
                        previous chapter.
                           In the following subsections, the temporal and spatial discretization schemes are given,
                        which will then be employed to solve the porous medium equations. Use will be made
                        only of simple, linear triangular elements to study porous medium flow problems.


                        8.3.1 Temporal discretization

                        Before going into the details of the CBS split, let us first consider the temporal discretization
                        of the governing equations. The momentum equation is subjected to the characteristic
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