Page 75 - Fundamentals of Reservoir Engineering
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SOME BASIC CONCEPTS IN RESERVOIR ENGINEERING                          14

                                 pV
                           Z =
                                14.7V o


                     By varying p and measuring V, the isothermal Z(p) function can be readily obtained.
                     This is the most satisfactory method of determining the function but in the majority of
                     cases the time and expense involved are not warranted since reliable methods of direct
                     calculation are available, as described below.

                     b)   The Z-factor correlation of Standing and Katz

                     This correlation requires a knowledge of the composition of the gas or, at least, the gas
                     gravity. Naturally occurring hydrocarbons are composed primarily of members of the
                     paraffin series (C nH 2n+2) with an admixture of non-hydrocarbon impurities such as
                     carbon dioxide, nitrogen and hydrogen sulphide. Natural gas differs from oil in that it
                     predominantly consists of the lighter members of the paraffin series, methane and
                     ethane, which usually comprise in excess of 90% of the volume. A typical gas
                     composition is listed in table 1.1.
                                                                11
                     In order to use the Standing-Katz correlation  it is first necessary, from a knowledge of
                     the gas composition, to determine the pseudo critical pressure and temperature of the
                     mixture as

                           p pc    n p ci                                                           (1.16)
                               =
                                    i
                                  i
                     and

                           T pc    nT                                                               (1.17)
                               =
                                    i ci
                                 i
                     where the summation is over all the components present in the gas. The parameters p ci
                                                                           th
                     and T ci are the critical pressure and temperature of the i  component, listed in table 1.1,
                     while the n i are the volume fractions or, for a gas, the mole fractions of each
                     component (Avogrado's law). The next step is to calculate the so-called pseudo
                     reduced pressure and temperature

                                p
                           p =                                                                      (1.18)
                            pr
                                p pc

                     and

                                 T
                           T pr  =                                                                  (1.19)
                                 T pc

                     where p and T are the pressure and temperature at which it is required to determine Z.
                     In the majority of reservoir engineering problems, which are isothermal, T pr is constant
                     and p pr variable.

                     With these two parameters the Standing-Katz correlation chart, fig. 1.6, which consists
                     of a set of isotherms giving Z as a function of the pseudo reduced pressure, can be
                     used to determine the Z−factor.
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