Page 239 - Fundamentals of Reservoir Engineering
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OILWELL TESTING                                    177

                     array being shown in fig. 7.10, each well producing at the same rate as the real well
                     within the boundary. The constant terminal rate solution for this complex system can
                     then be expressed as

                           2kh                             4t D      ∞      φµ ca 2 j
                            π
                                                 t
                                 (p − p wf  ) =  p D  ( ) =  1 2 ln  +  1 2    ei                   (7.41)
                                   i
                                                 D
                            qµ                              γ        j2      4kt
                                                                     =
                     in which the first term on the right hand side of the equation is the component of the
                     pressure drop due to the production of the well itself, within an infinite reservoir,
                     equ. (7.23), and the infinite summation is the contribution to the wellbore pressure drop
                     due to the presence of the infinite array of image wells which simulate the no-flow
                     boundary. The exponential integral function is the line source solution of the diffusivity
                     equation introduced in sec. 7.2, equ. (7.11), for the constant terminal rate case and is
                     necessitated by the fact that the distance a j between the producing well and the j th
                     image well is large so that the logarithmic expression of the line source solution,
                     equ. (7.10), is an unacceptable approximation and the full exponential integral solution
                     must be used. The infinite summation in equ. (7.41) is therefore an example of
                     superposition in space of the basic constant terminal rate solution of the diffusivity
                     equation. For further details of the mathematical technique the reader should consult
                                                             7
                     the appendices of the original MBH paper .
                     Using this method to determine p D (t D), MBH were able to evaluate equ. (7.40) for a
                     wide variety of boundary conditions and presented their results as plots of

                           4kh   ( p − p vs. t
                            π
                                   *
                                        )
                            qµ                DA
                     where t DA is the dimensionless flowing time. These charts have been included in this
                     text as figs. 7.11-15. The individual plots are for different geometries and different
                     asymmetries of the producing well with respect to the no-flow boundary.

                     The MBH charts were originally designed to facilitate the determination of p from
                                                               *
                     pressure buildup data by first determining p , by the extrapolation of the Horner plot,
                     and k from the slope of the straight line. If an estimate is made of the area being
                     drained, t DA = kt/φµcA can be calculated for the actual flowing time t. Then, using the
                                                               *
                     appropriate MBH chart the value of 4πkh (p −p)/qµ is read off the ordinate from which
                     p can be calculated. The details of this important technique will be described in
                     sec. 7.7. For the moment, the MBH charts will be used in a more general manner to
                     determine p D (t D) functions for the range of geometries covered by the charts and for
                     any value of the flowing time.
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