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EVALUATION OF TREATMENTS AND POSTFRACTURE PERFORMANCE



            EXAMPLE F-7
                                                                   Since a 1000-ft half-length fracture with kJw = 1000 md-ft
            Posttreatment Pressure Transient Test Design
                                                                 was intended, then
            A fracture treatment was successful in an oil reservoir having
            1 md permeability. The fracture design was intended to create                                   (F-24)
            a 1000-ft half-length with a kfw = 1000 md-ft. Using the data
            in Table F-3, predict the length of time that the well should be   and therefore the first foldout type curve can be used for the
            definitely within the bilinear flow. What would be the pressure   calculation.
            drop at that time if the test flow rate is 500 STB/d?   At CDJ=    to be well within the bilinear flow regime,
                                                                 the ratio fDAf/CD, must be equal to 100 (from the type curve).
            Solution (Ref. Section 11-6)                         Thus,.
            This exercise is to give a rough estimate of the required test
            duration to provide meaningful and interpretable data. Often,   tDxf = (ioo)(i x   = iod        (F-25)
            it is necessary to assume plausible values of the variables to be   From the definition of the dimensionless time (Eq. 11-10)
            calculated in order to design a test of appropriate duration. The   and rearrangement,
            foldout curves at the end of Chapter 11 can be used for this
            calculation.                                                (lo- 3)(0.1)(2)(10- s)( 1000~)
              At first, the dimensionless fracture wellbore storage coef-   t=                   = 7.5 hr.   (F-26)
            ficient must be estimated. This is given by Eq.  11-22.           (0.000264) ( 1 )
              The dimensioned wellbore storage coefficient C is simply   The dimensionless pressure at that time is 0.43 (from the
            the well volume multiplied by the fluid compressibility within   type curve). Thus, from Eq.  11-8 and rearrangement,
            the tubing string. Assuming that only oil is produced, the oil
            compressibility can be used. If gas is liberated in the tubing,   Ap =  (0.43) (14 1.2) (500) (1.1) (2)
            which  is often the case,  then  its impact  must be  taken  into         (1) (37)
            account. For the purpose of this exercise, the oil is assumed to
            have a very low bubblepoint pressure. Thus,                     = 1805 psi.                     (F-27)

                c = K,C,,                                        I
                      n( 2.44 1 )’                                 k   =  1md
                  -              (12,000)(6x                     1
                  -
                    (4)( 144)(5.615)
                  = 4.17 x   bbl /psi.                 (F-22)
                                                                           1.1 resbbl/STB
            From Eq.  11-22,                                     I  H   =  12,000ft

                            (5.615)(4.17 x                       I
                                                                                 psi-’
                 CDJ =                                             c,   =  6~10-~
                      (2) (3.14) (0. I ) ( 10- 5, (37) ( 10002)   7
                                                                   dtbg =  2.441 in.
                    = IX  lo-?                         (F-23)



                                                                 Table F-3-Posttreatment  test data for Example F-7.
















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