Page 273 - Standard Handbook Petroleum Natural Gas Engineering VOLUME2
P. 273

242   Reservoir Engineering


                     pressure. (Note: if  the formation volume factors are expressed in ft5/scf, 7,758
                     should be replaced with 43,560  ft3 per acre-ft.
                       If  Equation 5-145 is rearranged in terms of  the initial gas in place:


                                                                                  (5-170)


                     The recovery efficiency, En, which is the  volume of  gas recovered divided by
                     the volume of  gas initially in place, can be found from:

                            B,  - B,
                       E,  =                                                       (5-1 71)
                              B#

                     For volumetric gas reservoirs (which assumes no change in Sw) recoveries may
                     range from 80% to 90% of  the initial gas in place.
                       For gas reservoirs under water drive, recovery efficiency is:



                                                                                  (5-172)

                     where SBt is the residual gas saturation and the other terms axe as defined above.


                     Recovery of 011
                     Solution-Gas or  Depletion Drlvr.  Oil recovery by  depletion  or  solution-gas
                     drive is:

                                               (I-% -s*>
                                      (l-Sw)
                       N,  = 7,758 Ah@[ -                1                         (5-179)
                                             -
                                        B,         BO
                     where B . is the initial oil formation volume factor and Bo is the oil formation
                     volume &tor  at abandonment, and the other terms are as previously defined.
                     The ultimate free gas saturation is often estimated from the old data of Arps
                     [245] and  Craze and  Buckley [241] in  which  the  average  Sg was  30%  for  a
                     2.2  cp oil with 400 fts/bbl of  solution gas. A general rule suggests that for each
                     doubling of  solution gas, S8 should be increased 3%; and for each doubling of
                     oil viscosity,  Sg should be  decreased  by  3% [14].  As  a first  approximation,
                     Sgr can be taken to be about 0.25 [254]
                       For  a volumetric, undersaturated reservoir,


                                                                                   (5-1 74)

                     where N,  is  the oil produced in stock tank barrels, N  is the initial oil in place
                     in STB and the other terms are as already given. In this case, the oil saturation
                     after any  stage of  primary production, Sa, can be  obtained from:
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