Page 226 - Fundamentals of Enhanced Oil and Gas Recovery
P. 226

214                                                                    Mohammad Ali Ahmadi


                   Therefore, the correct solution is
                                                 s ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffi

                                                        tq t  df w
                                         r f 5 r e 2  r 2                             (7.39)
                                                   2
                                                   e
                                                       πhφ dS w f
                   In field unit, the expression is
                                               s ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffi

                                                      5:615tq t  df w
                                       r f 5 r e 2  r 2                               (7.40)
                                                  2
                                                  e    πhφ    dS w f
                   There   are  other   extensions,  generalizations,  and  improvements  to
                Buckley Leverett theory developed to obtain and enhance understandings of the
                complicated flow behavior of multiple phases in porous media. In particular, the
                Buckley Leverett fractional flow theory has been generalized and applied by various
                researchers to study enhanced oil recovery (EOR) [7], surfactant flooding [8], polymer
                flooding [9], mechanisms of chemical methods [10], and alkaline flooding [11].
                   More recently, studies have extended the Buckley Leverett solution to flow in a
                composite, one-dimensional heterogeneous, composite-reservoir system [12], to non-
                Newtonian fluid flow [13 17] and the non-Darcy displacement of immiscible fluids
                in porous media [18 22]. Fundamentals of the physics of flow of multiphase fluids in
                porous media have been understood through laboratory experiments, theoretical anal-
                ysis, mathematical modeling, and field studies [23 25]. Analysis of porous medium
                flow processes relies traditionally on Darcy’s law-based approaches, and application of
                such analysis has provided quantitative methodologies and modeling tools for many
                related scientific and engineering disciplines.
                   Fayers and Sheldon [26] described the Frontal advance theory as an application of
                the law of conservation of mass. Flow through a small volume element with length
                Δx and cross-sectional area “A” can be expressed in terms of total flow rate q t as
                                                                                      (7.41)
                                                q t 5 q w 1 q o
                                                q w 5 q t 3 f w                       (7.42)

                                          q o 5 q t 3 f w 5 q t 3 ð1 2 f w Þ          (7.43)
                where q denotes volumetric flow rate at reservoir conditions and subscripts {o,w,t}
                refer to oil, water, and total rate, respectively, and f w and f o are fractional flow to
                water and oil (or water cut and oil cut), respectively.

                                                   kk ro @ AP o Þ
                                                        ð
                                              q o 5                                   (7.44)
                                                   μ    @r
                                                     o
                                                   kk rw @ AP w Þ
                                                        ð
                                              q w 5                                   (7.45)
                                                   μ     @r
                                                    w
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