Page 399 - Fundamentals of Reservoir Engineering
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NATURAL WATER INFLUX                                   334


                               2k h p −   p wf,n )
                                π
                                     ( n
                                   o
                           q =           r                                                          (9.38)
                            n
                                    µ  ln  h
                                     oh
                                         r w
                     which is a re-formulation of the steady state inflow equation presented in table 6.1. The
                     oil viscosity, µ oh is a function of the average temperature in the hot zone during the n th
                     time interval. The temperature will decline continuously during production as heat is
                     lost by conduction to the cap and base rock and by convection through the produced
                     fluids. A simple method for predicting the temperature decline allowing for both effects
                                                             9
                     has been presented by Boburg and Lantz . The pressure p  in equ. (9.38) is the
                                                                              n
                     average pressure during the time step at r h, the outer boundary of the hot zone, and
                     p wf,n  the average wellbore pressure during the same period. If it is assumed that the
                     pressure declines at r h and r w can be approximated by a series of discrete pressure
                     steps then, in accordance with equ. (9.15), p  and p wf,n   can be expressed as
                                                                n

                           p =  1 2 (p n 1  + p n )                                                 (9.39)
                            n
                                    −
                     and

                           p wf,n  =  1 2 (p wf,n 1  + p wf,n )                                     (9.40)
                                       −

                                                                                                  th
                     where p n and p wf,n are the pressures at r h and r w respectively at the end of the n  time
                     step. The cumulative oil influx across the boundary r h by the end of the time step will be

                           N p,n  = N p,n 1  + q . t
                                          ∆
                                        n
                                    −
                                                                           th
                     in which N p,n-l is the known influx at the end of the (n - 1)  time step. Using equs. (9.39)
                     and (9.40), the influx can be expressed as

                                       α
                           N p,n  = N p,n 1  +  (p n 1  +  p − p wf,n 1  − p wf,n )                 (9.41)
                                                 n
                                    −
                                        2   −           −
                     where

                               2k h t
                                π
                                    ∆
                           α =    o  r
                               µ oh ln r w h

                     An expression for the cumulative oil influx can also be obtained using the unsteady
                     state influx theory of Hurst and van Everdingen in the manner similar to that of
                     equ. (9.34)

                                  n2
                                   −
                           N p,n  = U    ∆ p W T − t  j D  )  +  U p W T −  t D n 1 )               (9.42)
                                                       ∆
                                                         n 1
                                                               ( D
                                                             D
                                           ( D
                                       j
                                          D
                                                          −
                                  j0                                  −
                                   =
                     in which T = n. ∆t and W D is the dimensionless influx function of Hurst and van
                     Everdingen, figs. 9.3-9.7. U is the aquifer constant defined in equ. (9.6), only in this
                     case applied to the oil reservoir for which f = 1, and the radius r o is replaced by r h.
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