Page 272 - Standard Handbook Petroleum Natural Gas Engineering VOLUME2
P. 272

Material Balance and Volumetric Analysis   241


                state compressible flow should be used, and that water encroachment generally
                follows the constant pressure solution to the radial diffusivity equation. Solutions
                to  the  radial  diffusivity equation  have  been  provided  by  van  Everdingen  and
                Hurst [253] in terms of  dimensionless time, t,,  and a dimensionless fluid flow
                function, Qm, which is  determined  at t,:

                       6.323 x loJ kt
                   t,  =                                                     (5-166)
                          @w2

                where k is permeability in md,  t is  time in days,  is the fractional porosity, c
                is the compressibility in psi-l, and r  is the reservoir radius in ft. Values of  Q,
                are given  in  tabular  form  as  a function  of  t,in  the paper  by  van Everdingen
                and  Hurst  [253]  and  have been  reproduced  in  several texts  [17,197].  Because
                of  the  length  of  the  tables,  they  will  not  be  reproduced  in  this  section.  The
                water encroachment, We in barrels,  can be estimated from:

                                                                              (5-167)
                where dp is the pressure  drop is psi, and the constant B  is:

                               8
                   B = 1.12@h~'-                                              (5-168)
                               360
                where h is the reservoir thickness in ft, 0 is the angle subtended by the reservoir
                circumference (e is 360" for a circular reservoir and 8 is  180" for a semicircular
                reservoir  against a fault), and the other  terms are as defined above [17].  From
                the slope of cumulative water influx at various times versus the summation term
                at  those  times,  the  aquifer  constant,  B,  can  be  obtained,  and  the  cumulative
                water influx for any pressure history can be estimated from Equation 5-167. Plots
                of  Qco versus  t,  for  various  dimensionless  reservoir  sizes  are  also  available
                [17,253]  and extensions of  these  data are available as well  11971.

                          Volumetric Calculations for  Recovery of  Gas and Oil

                  The volumetric equations for original oil and gas in place were given earlier.
                In this  section, volumetric equations will  be given for the recovery of  gas and
                oil reservoirs under  several common instances.

                Recovery of  Gas
                  The volume of gas recovered, GP in scf, from a  dry-gas reservoir  is:



                                                                              (5-169)


                where 7,758 is the number of barrels  per acre-ft, A is the areal extent in acres,
                h is the reservoir thickness in ft, @  is the fractional porosity, Sw is the fractional
                water saturation, B,  is the initial gas formation volume factor in reservoir barrels
                per scf, and BB is the gas formation volume factor in RB/scf  at the abandonment
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