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3.2  EFFECTS OF PORE SPACE STRUCTURE ON FLOW                          47

         3.2  Effect  of Pore Space  Structure on Laws for
                 Macroscopic Flow


         The foregoing relations (3.13),  (3.14),  (3.15) for flow  types in  the capillaries and
         (3.16)  for  the  pressure  losses  on  the junctions  allow  to specify  the form  of the
         equation (3.7) which relates the flow q through an arbitraryr1-chain (a*~ r1 ~ re)
         to the pressure gradient G in the medium.
            Consider the second term, J(r11 q), in (3.7).  In model I each capillary of radius
         r joins with the pore of size  lp  ~ r  both at its entrance and exit.  After setting
         r' = 0.5lp and passing in  (3.17)  and  (3.18) tor' ~ r(A(r, r'O  ~ Ao, €(r'  fr)  ~ €o),
         we obtain the following from  (3.16) and (3.6)

                                                                            (3.19)

                                 V(rt) = "'( 01  < r1,r- 3 ,a* >,
                                 I'(rt) = d 01  < r1,r-\a* >,               (3.20)
                                   "Ya  = 0.5 o:' l- 1r- Ao,
                                                   1
                                               1
                             da  = o:' z-17r-2€()2[Bi + (1- €o)2 Bi].
            For model II, after averaging (3.16) over r' in accordance with (3.4) with further
         substitution of the averaged result into the second term of (3.5) (and then averaging
         the latter with  respect  to r),  we  shall  arrive  back  at  (3.19),  but  with  different
         functions V ( rt) and I' ( rt)

                                            3
                                                     3
              V(rt) = "Yb  < r1, [< r1, A(r, r')/r' , r >  +r- < r, A(r, r'), a*  >],a* >,
          I'(rt) =db< r11[< r-l,(I(r,r')/r' ,r > +r- < r,({(r,r'),a* >],a*>,  (3.21)
                                          4
                                                   4
                             "Yb  = 0.250: 7r- 1 l- 1 ,  db= 0: 11"- 2 1- 1 .
                                                      1
                                      1
            Introduce the following notations
                                 Tm(q) = d1q,  rd(q) = d2q,                 (3.22)

                              di = (0.511" ReiPt/tL)- ,  i = 1, 2,
                                                 1
                        *d-1          *d-1           d- 1   l       d- 1
                  Qt  =a  2  ,   Qt m  = a  1  1   Qm m  = T1  2   1   Q  m = T1  1  ·
            We shall now specify the form  of equation (3.7),  taking into account the rela-
         tionship  (3.19)  for  various  pressure gradients,  starting with  the interval of large
         g's.
            Turbulent flow.  When rd(q)  ~a*, q ~ Qt·  In  this case, according to (3.22)
         and (3.19), Re(rt) ~ Re(r)  ~ Re(a*)  ~ Re2 , and therefore the flow in all capillaries
         of the r1-chain is turbulent.
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