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Guo, Boyun / Computer Assited Petroleum Production Engg 0750682701_chap17 Final Proof page 263  3.1.2007 9:19pm Compositor Name: SJoearun




                                                                                 HYDRAULIC FRACTURING  17/263
                         Simulating controlled height growth with a pseudo-3D  Post-propped Frac Decline. The simulator-generated
                       model can be tricky. Height growth is characterized by  pressure decline is affected by the model of extension
                       a slower rate of pressure increase than in the case of a  recession that is implemented and by the amount of sur-
                       confined fracture. To capture the big picture, a simplifica-  face area that still have leakoff when the simulator cells are
                       tion to a three-layer model can help by reducing the num-  packed with proppant. It is very unlikely that the simula-
                       ber of possible inputs. Pressure-matching slow height  tor matches any of those extreme cases. The lumped solu-
                       growth of a fracture is tedious and lengthy. In the first  tion used in FracProPT does a good job of matching
                       phase, we should adjust the magnitude of the simulated  pressure decline. The analysis methodology was indeed
                       net pressure. The match can be considered excellent if  developed around pressure matching the time to closure.
                       the difference between the recorded pressure and the  The time to closure always relates to the efficiency of the
                       simulated pressure is less than 15% over the length of  fluid regardless of models (Nolte and Smith, 1981).
                       the pad.
                         The pressure matching can be performed using data
                       from real-time measurements (Wright et al., 1996; Burton  17.6.2 Pressure Buildup Test Analysis
                       et al., 2002). Computer simulation of fracturing operations  Fracture and reservoir parameters can be estimated using
                       with recorded job parameters can yield the following frac-  data from pressure transient well tests (Cinco-Ley and
                       ture dimensions:                          Samaniego, 1981; Lee and Holditch, 1981). In the pressure
                                                                 transient well-test analysis, the log-log plot of pressure
                       . Fracture height                         derivative versus time is called a diagnostic plot. Special
                       . Fracture half-length                    slope values of the derivative curve usually are used
                       . Fracture width                          for identification of reservoir and boundary models. The
                                                                 transient behavior of a well with a finite-conductivity
                       A typical pressure matching with a pseudo-3D fracturing  fracture includes several flow periods. Initially, there is a
                       model is shown in Fig. 17.12 (Burton et al., 2002).
                                                                 fracture linear flow characterized by a half-slope straight
                          Efficiency and Leakoff. The first estimate of effi-  line; after a transition flow period, the system may or
                       ciency and leakoff is obtained from the calibration treat-  may not exhibit a bilinear flow period, indicated by a
                       ment decline analysis. The calibration treatment provides  one-fourth–slope straight line. As time increases, a for-
                       a direct measurement of the efficiency using the graphical  mation linear flow period might develop. Eventually,
                                       3
                       G-plot analysis and the ⁄ 4 rules or by using time to closure  the system reaches a pseudo-radial flow period if the drain-
                       with a fracturing simulator. Then calibration with a model  age area is significantly larger than the fracture dimension
                       that estimates the geometry of the fracture provides the  (Fig. 17.13).
                       corresponding leakoff coefficient (Meyer and Jacot, 2000).  During the fracture linear flow period, most of the
                       This leakoff coefficient determination is model dependent.  fluid entering the wellbore comes from the expansion
                          Propped Fracture Geometry.  Once we have obtained  of the system within the fracture. The behavior in the
                       both a reasonable net pressure match, we have an estimate  period occurs at very small amounts of time, normally
                       of length and height. We can then directly calculate the  a few seconds for the fractures created during frac-packing
                       average width expressed in mass/area of the propped frac-  operations. Thus, the data in this period, even if not
                       ture from mass balance. The propped geometry given by  distorted by wellbore storage effect, are still not of prac-
                       any simulator after closure should not be any different.  tical use.

                             4,000                                                            30
                                                                                              28
                                                                                              26

                             3,500                                                            24
                                                                                              22
                                                                                              20
                                                                                              18
                             3,000                                   BHP (Job data)           16
                           BHP(psi)                                  BHP (PropFRAC)           14  Slurry Rate(bbl/min)  &  Prop Conc(PPA)

                                                                     Slurry Rate (bbl/min)
                                                                     Prop Conc  (PPA)         12
                             2,500
                                                                                              10
                                                                                              8
                                                                                              6
                             2,000
                                                                                              4
                                                                                              2
                                                                                              0
                             1,500                                                            −2
                                 0      5      10      15     20     25      30     35      40
                                                        Treatment Time(min)
                              Figure 17.12 Bottom-hole pressure match with three-dimensional fracturing model PropFRAC.
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