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OILWELL TESTING                                    173

                                                                        r
                                   2t           3     ∞   e − α n 2t D  J 1 2  (α n eD )
                              t
                           p D  () =  D  + lnr eD  −  + 2                                           (7.34)
                               D
                                    2
                                                                         ( ))
                                    r eD        4    n1 α n 2  ( 1 2  (α n eD  ) J α n
                                                                        2
                                                            J
                                                                 r
                                                                     −
                                                                        1
                                                      =
                     in which r eD = r e/r w and α n are the roots of
                           J 1  (α n  r )  Y 1  (α n ) − J 1  (α n )  Y 1  (α n  r ) =  0
                                  eD
                                                            eD
                     and J 1 and Y 1, are Bessel functions of the first and second kind. Equation (7.34) is the
                     full Hurst and Van Everdingen constant terminal rate solution referred to in sec. 7.2, the
                                                                                  1
                     detailed derivation of which can be found in their original paper , or in a concise form in
                                                                        6
                     Appendix A of the Matthews and Russell monograph . One thing that can be observed
                     immediately from this equation is that it is extremely complex, to say the least, and yet
                     this is the expression for the case of simple radial symmetry. In fact, as already noted
                     in sec. 7.4 and demonstrated in exercise 7.4, for a well producing from the centre of a
                     regular shaped drainage area there is a fairly abrupt change from transient to semi-
                     steady state flow so that equ. (7.34) need never be used in its entirity to generate p D
                     functions. Instead, equ. (7.23) can be used for small values of the flowing time and
                     equ. (7.27) for large values, with the transition occurring at t DA ≈ 0.1.

                     Problems arise when trying to evaluate p D functions for wells producing from
                     asymmetrical positions with respect to irregular shaped drainage boundaries. In this
                     case a similar although more complex version of equ. (7.34) could be derived which
                     again would reduce to equ. (7.23) for small t D and to equ. (7.27) for large t D.

                     Now, however, there would be a significant late transient period during which there
                     would be no alternative but to use the full solution to express the p D function.

                     Due to the complexity of equations such as equ. (7.34) engineers have always tried to
                     analyse well tests using either transient or semi-steady state analysis methods and in
                     certain cases this approach is quite valid, such analyses having already been
                     presented in exercise 7.2 for a single rate drawdown test. Sometimes, however,
                     serious errors can arise through using this simplified approach and some of these will
                     be described in detail in the following sections. It first remains, however, to describe an
                     extremely simple method of generating p D functions for any value of the dimensionless
                     time and for any areal geometry and well asymmetry. The method requires an
                     understanding of the Matthews, Brons and Hazebroek pressure buildup analysis
                     technique which is described in the following section.


              7.6    THE MATTHEWS, BRONS, HAZEBROEK PRESSURE BUILDUP THEORY

                     In this section the MBH pressure buildup analysis technique will be examined from a
                     purely theoretical standpoint, the main aim being to illustrate a simple method of
                     evaluating the p D function for a variety of drainage shapes and for any value of the
                     dimensionless flowing time.


                     The theoretical buildup equation was presented in the previous section as
                           2kh
                            π
                                  (p −  p ) =  p (t + ∆ t ) −  p D  ( t ∆  D )                      (7.32)
                                              D
                                                      D
                                                 D
                                   i
                                       ws
                            qµ
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