Page 34 - Physical Principles of Sedimentary Basin Analysis
P. 34

16                        Properties of porous media

                 where ¯u is the average velocity of the fluid in the pipe, r is the radius of the pipe and μ is
                 the viscosity. The Darcy flux v D , which is the volume rate of fluid per unit time out of a
                 cross-section, is then
                                                              4
                                               Nπr 2      Nπr dp
                                        v D =−      ¯ u =−                          (2.41)
                                                 A        8Aμ dx
                 for a cross-section A with N pipes, when it is assumed that the cross-section A is normal
                 to the tubes. The permeability is then identified as

                                                    Nπr 4
                                                k =      .                          (2.42)
                                                     8A
                 The porosity of the medium of pipes is

                                                     Nπr 2
                                                φ =                                 (2.43)
                                                      A
                 which is used to replace the pore radius in the permeability (2.42). Using the porosity (2.43)
                 in the Darcy flux (2.41) gives that v D = φ ¯u, which is the general relationship (2.30)
                 between the average fluid velocity in the pores and the Darcy flux. The permeability of the
                 medium becomes
                                                      A    2
                                              k(φ) =     φ                          (2.44)
                                                     8π N
                 when the porosity (2.43) replaces the tube radius in expression (2.42). The permeability
                              2
                 decreases as ∼φ with decreasing porosity, and it is proportional to the area of the cross-
                 section (A), and inversely proportional to the number of pipes (N). The permeability can
                 also be written as
                                                  
 2              2
                                                φ                φ A
                                                                  0
                                    k(φ) = k 0 ·       with  k 0 =                  (2.45)
                                                φ 0              8π N
                 where k = k 0 is the permeability at the reference porosity φ = φ 0 . Notice that permeability
                                          2
                 has units of length squared (m ). We have already seen that the specific surface of the
                                                       3
                                                    2
                 pore space has units of inverse length, (m /m ). It is therefore possible to express the
                 permeability k with the inversely of the specific surface squared. A porous medium of
                 tubes has the specific surface area
                                           2π Nr         2   4Nπφ
                                       S =         or   S =                         (2.46)
                                             A                 A
                 when the tube radius is replaced by the porosity. The permeability as a function of porosity
                 can then be written
                                                       φ 3
                                                k(φ) =    .                         (2.47)
                                                      2S 2
                 This form of permeability function becomes the Kozeny–Carman relationship

                                                       φ 3
                                            k(φ) =                                  (2.48)
                                                     2
                                                  CS (1 − φ) 2
                                                     s
   29   30   31   32   33   34   35   36   37   38   39