Page 190 - Fundamentals of Reservoir Engineering
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RADIAL DIFFERENTIAL EQUATION FOR FLUID FLOW                         128

                                                                           dr




                                        h                             qρ |  r  qρ |  r + dr


                                           r e                r w
                                                                      r

                     Fig. 5.1   Radial flow of a single phase fluid in the vicinity of a producing well.


                     Consider the flow through a volume element of thickness dr situated at a distance r
                     from the centre of the radial cell. Then applying the principle of mass conservation
                        Mass flow rate     −    Mass flow rate   =    Rate of change of mass in
                              IN                    OUT               the volume element


                            qρ  rdr        −         qρ  r       =    2rh dr  ∂ ρ
                                                                       πφ
                                +
                                                                                t ∂
                     where 2πrhφdr is the volume of the small element of thickness dr. The left hand side of
                     this equation can be expanded as

                                   ∂ (q )                     ∂ ρ
                                      ρ
                                                       π φ
                              qρ  r  +   dr −  qρ  r    =  2 rh dr
                                      r ∂                       t ∂
                     which simplifies to


                              ρ
                           ∂ (q )         ∂ ρ
                                 =  2rh                                                              (5.2)
                                    πφ
                              r ∂          t ∂
                     By applying Darcy's Law for radial, horizontal flow it is possible to substitute for the flow
                     rate q in equ. (5.2) since


                                π
                               2 khr ∂  p
                           q =
                                 µ      r ∂
                     giving

                           ∂     2khr   ∂ p          ∂ ρ
                                π
                                                π
                                      ρ       =  2rhφ
                            r ∂     µ    r ∂          t ∂
                     or

                           1 ∂     kρ  ∂ p    ∂ ρ
                                   ρ       =  φ                                                      (5.3)
                           rr ∂     µ  r ∂     t ∂

                     The time derivative of the density appearing on the right hand side of equ. (5.3) can be
                     expressed in terms of a time derivative of the pressure by using the basic
                     thermodynamic definition of isothermal compressibility
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