Page 202 - Fundamentals of Reservoir Engineering
P. 202

STABILIZED INFLOW EQUATIONS                                140

                                     qµ     r   3
                           pp  wf  =       ln  e  −                                                 (6.14)
                             −
                                   2kh      r′ w  4
                                     π
                     in which

                           r′ = r e −s                                                              (6.15)
                                w
                           w
                     is the effective wellbore radius due to the presence of skin. If the formation is
                     damaged, so that the permeability close to the well is reduced, the skin factor is
                     positive. If, however, the well has been stimulated, for instance by acidising, then the
                     permeability close to the well can exceed the average formation permeability and the
                     skin factor is then negative. In either case the magnitude and sign of the skin factor can
                     be determined from pressure buildup analysis as will be described in Chapter 7, sec. 7.


              6.4    EXAMPLE OF THE APPLICATION OF THE STABILIZED INFLOW EQUATIONS

                     The solution of the diffusivity equation under semi-steady state flow conditions has
                     been described in detail in section 6.2 since the mathematical approach is quite
                     general and can be applied to more complex radial flow problems. Consider, for
                     instance, the case of a well which has been stimulated by steam soaking, refer
                     Chapter 4, sec. 7. In this type of stimulation several thousand tons of steam are
                     injected into the well and, upon re-opening, the well will produce at a greatly increased
                     rate. As a first approximation it will be assumed that, due to the steam injection, the
                                                                                            1
                     temperature distribution can be described by a temperature step function  so that, for
                     r w < r < r h, the temperature T s is uniform and initially equal to the condensing steam
                     temperature at the sandface. During production, T s will decrease due to heat losses by
                     conduction and convection. For r > r h, the temperature is the original reservoir
                     temperature T r. The situation at any time during the production cycle is shown in
                     fig. 6.2,





                                                                                               p e
                              Pressure                    T, µ oh
                                                           s
                                          T, µ oc                             p h
                                           r
                                                                    p wf


                                                                                             r
                                                                  r w        r h              e
                     Fig. 6.2   Pressure profile during the steam soak production phase

                     where µ oh and µ oc are the viscosities of the oil at temperatures T s and T r, respectively. If
                     the inflow equations are formulated under steady state flow conditions, the result will
                     be as follows
   197   198   199   200   201   202   203   204   205   206   207