Page 101 - gas transport in porous media
P. 101

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                           We now define the intrinsic interfacial area average according to
                                                                                       Whitaker
                                                            1
                                                   ψ γ   γκ =     ψ γ dA                (6.128)
                                                           A γκ
                                                              A γκ
                           and use this definition with c As and R As so that Eq. (6.127) takes the convenient form
                           given by
                                          γ
                                     ∂ c Aγ                       γ      ∂ c As   γκ
                                   ε γ      +∇ ·  c Aγ v Aγ   =   R Aγ    − a v         (6.129)
                                       ∂t                                   ∂t

                                                transport   homogeneous
                                   accumulation                          adsorption
                                                             reaction
                                                             + a v  R As   γκ

                                                                heterogeneous
                                                                  reaction
                           One must keep in mind that this is a general result based on Eqs. (6.120) and (6.121) ;
                           however, only the first term in Eq. (6.129) is in a form that is ready for applications. On
                           the right hand side of Eq. (6.129) we are confronted with the necessity of chemical
                           kinetic constitutive equations for the reaction rate terms and a suitable connection
                           between the surface concentration, c As , and the bulk concentration, c Aγ . In this
                           development, we will avoid these problems and concentration on a single aspect
                           of Eq. (6.129), the determination of the species velocity, v Aγ .
                             The manner in which v Aγ is determined depends on the particular characteristics
                           of the species momentum equation given by Eq. (6.84). When Eqs. (6.49) and (6.87)
                           are a valid representation of the N species momentum equations, we make use of
                           the total momentum equation to determine the mass average velocity, v γ , and the
                           Stefan-Maxwell equations to determine the N − 1 independent species velocities.
                           Under these circumstances, Eq. (6.129) takes the form
                                             γ
                                        ∂ c Aγ                              γ
                                      ε γ      +∇ · c Aγ v γ   =  ∇ · J Aγ  + R Aγ      (6.130)
                                          ∂t
                                                                 ∂ c As   γκ
                                                             − a v       + a v  R As   γκ
                                                                    ∂t
                           and we are confronted with the average of a product, c Aγ v γ , whereas it is the product
                           of the averages that we desire. Here we follow the approach used in turbulence
                           modeling and decompose the point values of the concentration and velocity into the
                           intrinsic average values and the spatial deviation values. These decompositions are
                           given by
                                                      γ
                                                                       γ
                                            c Aγ = c Aγ   +˜c Aγ ,  v γ = v γ   +˜v γ   (6.131)
                           so that the volume averaged convective transport is described as
                                           +                                     ,
                                               γ    γ         γ      γ
                                   v γ c Aγ  =  v γ    c Aγ   +˜v γ  c Aγ   + v γ   ˜c Aγ +˜v γ ˜c Aγ  (6.132)
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