Page 489 - Petrophysics
P. 489

TURBULENT FLOW OF GAS            457



                                C(kifi)2 (35.6 x 0.40)2 + (155 x 0.60)2
                                         =
                                         = 8851.77

                                     kifi  = k = 35.6 x 0.40 + 155 x 0.60

                                         = 107.24mD

                                From Equation 7.1 16d, the average non-Darcy  flow coefficient is:

                                -      93.2 x 10l2
                                                      = 9.82 x 10'ft-I
                                  = 8851.77 x 107.24
                             2.  The  arithmetic  average  porosity  of  the  two  layers  is  (0.166  +

                                0.138)/2  = 0.152,  and  the  average  permeability  is  107.24 mD.
                                Substituting these  values  into  Equations  7.116a  and  b,  we  find,
                                respectively:

                                    4.11 x 10"'
                                  = ( 107.24)4/3  = 8 x lo7 ft-'
                                        4.8s x io4
                                P=  0.1525.5 x Jm
                                                       = 14.8 x  10'  ft-I

                                The value of p obtained from Equation 7.116a compares well with the
                                lab-derived p.



                             EXAMPLE

                               A  consolidated  sand  core  2cm  in  diameter  and  5cm  long  has  a
                             permeability of 225 mD and a porosity of 20%. Air at 75°F is injected into
                             this core. The inlet pressure is 100 psia and the outlet pressure 14.7 psia.
                             The viscosity of air is 0.02 cP, and the compressibility is assumed to be
                             equal to 1 .O. Calculate the mass flow rate.


                             SOLUTION

                               The mass flow rate for air can be calculated from Equation 7.1 13. Let
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