Page 18 - gas transport in porous media
P. 18

Chapter 2: Gas Transport Mechanisms
                           The term β is defined as
                                                        β = φ S g τ                         11

                           where D ∗  is the effective diffusion coefficient for the AB gas system in a porous
                                  AB
                           media, D AB,CF is the effective diffusion coefficient of the AB gas system in a clear
                           fluid, φ is the porosity, S g is the gas saturation (equal to 1.0 for all-gas conditions),
                           and τ is the tortuosity. The tortuosity factor is discussed in further detail below.
                             Similar to the clear fluid equation, the mole flux through a porous media relative
                           to stationary coordinates is given by


                                           F A − ω A (F A + F B ) =−βρ g D AB,CF ∇ω A
                                                             =−ρ g D ∗ AB  ∇ω A

                           Inclusion of the β term takes into account the effective area for gas flow in the
                           pores (φ S g ) and the porous media tortuosity (τ). The diffusion coefficient D AB,CF
                           can be estimated from correlations as discussed by Reid et al. (1987). The diffusion
                           coefficient for gases is inversely proportional to the absolute pressure and directly
                           proportional to the absolute temperature to the 1.75 power as given by the Fuller et al.
                           correlation discussed in Reid et al. (1987).
                             The tortuosity factor, τ, as defined in this application as the ratio of the length of
                           the “tortuous” path in a porous media divided by a straight line value. The tortuosity
                           factor is evaluated for diffusion, not advection. For clear fluids, the tortuosity is
                           equal to 1.0. Note that sometimes other definitions of the tortuosity factor are used
                           (Dullien, 1992, pg. 311). There are a number of models for the tortuosity factor. The
                           most widely used correlation is that of Millington and Quirk (1961). The tortuosity
                           correlation of Millington and Quirk (1961) is given by

                                                               S
                                                       τ = φ 1/3 7/3
                                                                g
                           which can be rewritten as

                                                                1/3 7/3
                                                            = φ   S
                                                                   g
                                                    τ = τ o τ S g
                                                                                          is the
                           where τ o is the tortuosity due to the structure of the porous medium and τ S g
                           tortuosity due to the partial saturation. For all-gas conditions as discussed in this
                           chapter, the tortuosity factor reduces to the porous medium value, or

                                                  τ(S g = 1.0) = τ o = φ 1/3

                           Costanza-Robinson and Brusseau (Chapter 7 of this book) discuss porous media
                           tortuosity.
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