Page 96 - gas transport in porous media
P. 96

Chapter 6: Conservation Equations
                           in which the column matrix on the right hand side of this result can be expressed as
                              ⎡            ⎤  ⎡                                  ⎤  ⎡     ⎤  89
                                  D Am ∇x A     D Am   0     0   ......  0    0      ∇x A
                              ⎢            ⎥  ⎢   0          0   ......  0    0  ⎥
                                  D Bm ∇x B           D Bm                        ⎢  ∇x B  ⎥
                              ⎢            ⎥  ⎢                                  ⎥
                                                                                  ⎢       ⎥
                              ⎢            ⎥  ⎢   0    0         ......  0    0  ⎥  ⎢     ⎥
                              ⎢   D Cm ∇x C  ⎥  ⎢          D Cm                  ⎥   ∇x C
                                                                                  ⎢       ⎥
                              ⎢            ⎥ = ⎢                                 ⎥
                                    ...           .    .     .   ......  .    .   ⎢   ..  ⎥
                              ⎢            ⎥  ⎢                                  ⎥
                                                                                  ⎢       ⎥
                              ⎢            ⎥  ⎢                                  ⎥
                                                  0    0     0   ......       0   ⎣       ⎦
                              ⎣ D N−1m ∇x N−1  ⎦  ⎣                  D N−1m      ⎦  ∇x N−1
                                     0            0    0     0   ......  0  D Nm      0
                                                                                        (6.107)
                            The diffusivity matrix is now defined by
                                           ⎡                                     ⎤
                                              D Am   0     0   ......  0      0
                                           ⎢   0   D Bm    0   ......  0      0  ⎥
                                           ⎢                                     ⎥
                                           ⎢   0     0   D Cm  ......  0      0  ⎥
                                 [D]=[R]  −1 ⎢                                   ⎥      (6.108)
                                           ⎢   .     .     .   ......  .      .  ⎥
                                           ⎢                                     ⎥
                                           ⎣   0     0     0   ......  D N−1m  0  ⎦
                                               0     0     0   ......  0    D Nm
                           so that Eq. (6.106) takes the form
                                               ⎡     ⎤         ⎡        ⎤
                                                  J A              ∇x A
                                                  J B              ∇x B
                                               ⎢     ⎥         ⎢        ⎥
                                               ⎢     ⎥         ⎢        ⎥
                                                  J C              ∇x C
                                               ⎢     ⎥         ⎢        ⎥
                                               ⎢     ⎥  =−c [D]  ⎢      ⎥               (6.109)
                                               ⎢  ...  ⎥       ⎢   ...  ⎥
                                               ⎢     ⎥         ⎢        ⎥
                                               ⎣ ... ⎦         ⎣ ∇x N−1  ⎦
                                                  J N               0
                           This result can be expressed in a form analogous to that given by Eq. (6.102) leading to
                                                 E=N−1

                                         J A =−c      D AE ∇x E ,  A = 1, 2, ... , N    (6.110)
                                                  E=1
                           In the general case, the elements of the diffusivity matrix, D AE , will depend on the
                           mole fractions in a non-trivial manner. When this result is used in Eq. (6.101), we
                           obtain the non-linear, coupled governing differential equation for given by

                                                   E=N−1
                              ∂c A
                                  +∇ · (c A v) =∇ · c    D AE ∇x E  + R A ,  A = 1, 2, ... , N  (6.111)
                              ∂t
                                                    E=1
                           Use of the transport equations presented in this section to describe transport phenom-
                           ena in porous media requires that we upscale the equations from the so-called point
                           scale to an appropriate larger scale (Cushman, 1990, 1997). This analysis is described
                           in the following section.
   91   92   93   94   95   96   97   98   99   100   101