Page 191 - Fundamentals of Reservoir Engineering
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RADIAL DIFFERENTIAL EQUATION FOR FLUID FLOW                         129

                                 1 ∂ V
                           c =−
                                 V ∂ p

                     and since

                               m
                           ρ =
                               V


                     then the compressibility can be alternatively expressed as

                                       m
                                   ∂
                                 ρ      ρ    1 ρ∂
                           c =−           =                                                          (5.4)
                                 m   ∂ ρ    ρ ∂ p

                     and differentiating with respect to time gives

                              ∂ p  ∂ ρ
                           cρ    =                                                                   (5.5)
                               t ∂   t ∂


                     Finally, substituting equ. (5.5) in equ. (5.3) reduces the latter to

                           1 ∂     kρ  r  ∂ p    =  φρ ∂ p                                           (5.1)
                                             c
                           r ∂ r       µ  r ∂       t ∂

                     This is the basic, partial differential equation for the radial flow of any single phase fluid
                     in a porous medium. The equation is referred to as non-linear because of the implicit
                     pressure dependence of the density, compressibility and viscosity appearing in the
                     coefficients kρ /µ and φ cρ. Because of this, it is not possible to find simple analytical
                     solutions of the equation without first linearizing it so that the coefficients somehow
                     lose their pressure dependence. A simple form of linearization applicable to the flow of
                     liquids of small and constant compressibility (undersaturated oil) will be considered in
                     sec. 5.4, while a more rigorous method, using the Kirchhoff integral transformation, will
                     be presented in Chapter 8 for the more complex case of linearization for the flow of a
                     real gas.


              5.3    CONDITIONS OF SOLUTION

                     In principle, an infinite number of solutions of equ. (5.1 ) can be obtained depending on
                     the initial and boundary conditions imposed. The most common and useful of these is
                     called the constant terminal rate solution for which the initial condition is that at some
                     fixed time, at which the reservoir is at equilibrium pressure p i, the well is produced at a
                     constant rate q at the wellbore, r = r w. This type of solution will be examined in detail in
                     Chapters 7 and 8 but it is appropriate, at this stage, to describe the three most
                     common, although not exclusive, conditions for which the constant terminal rate
                     solution is sought. These conditions are called transient, semi-steady state and steady
                     state and are each applicable at different times after the start of production and for
                     different, assumed boundary conditions.

                     a)   Transient condition
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