Page 176 - Percolation Models for Transport in Porous Media With
P. 176

10.2  OPTIMAL TREATMENT REGIME                                       173


         Introduce the following notation
                           X=  {  1n(Raq/r)/1n(Raq/rw),   i = 1
                                                                           {10.26)
                                 (r-  1   - R;;q )/(r;;I - R;;q 1  ),  i =  2
                                          1
         Using {10.16)  and {10.23), we  transform {10.22) to get

                                                                           {10.27)

         Further, based on {10.24), {10.25), and (10.27), we obtain a universal equation for
         both problems               1

                           Qo    K  j            dx                        {10.28)
                           Q =  °  K[we(CJPJQ)- 1 x +  T(Raq)]
                                    0
         If  we assume that at a distance Raq, the temperature of the medium is close to its
         initial value T(Raq)  :::::l  To,  K(T(Raq)) = K(To)  :::::l  Ko,  for  a  specific  dependence
         {10.24), the relationship (10.28) is an equation for  Q  with a fixed We.
            The  relationship  {10.24)  was  obtained  experimentally  for  sandy-argillaceous
         rocks described in  chapter 9 and has the following form

                            Ko+B"(T-To),                   T<Tc
                          {                                                (10.29)
                  K(T) =  Ko + B"(T- To)+ D"(T- Tc) 2 ,  T  >  Tc

         Here Ko  is the permeability at the initial temperature T0 ;  B", D" are the param-
         eters to be  determined  from  experiment;  Tc  is  the critical  temperature, starting
         from  which  the dependence  K(T) becomes nonlinear.  After substituting (10.29)
         in  (10.28)  and  integrating,  we  obtain  a  transcendental equation  that  relates the
         production rate Q to the power of energy release We

                      ln[1 +  We/(E"Q)],                         We< We
            Qowe    {
            Q2 E" =                2         (  w  - L"  E"  Q)F"          (10.30)
                      ln(1 + L") + F" arctan [ ( 2 ~  L")E"  Q +We] ,

         where

                                                    2
                  L" = (T.e  - ,.,o)B"K 0 -  1 ·,   F" =   4E" D"  (1 + L")  -  1  ;
                                                  2  2K
                            .~,
                                                 CJPJ  o
                         We= QoE"L" ln- {1 + L"),  E" = KoCJPJ/B"
                                     2
                                         1
            The experimental dependence  (10.29)  is a good approximation for  describing
         the dependence K(T) in  a large temperature range (from several degrees Celsius
         to the boiling  point of the fluid).  After determining the parameters Te,  Ko,  B",
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