Page 32 - Standard Handbook Petroleum Natural Gas Engineering VOLUME2
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40    Reservoir Engineering


                    where y is a constant that depends on temperature, gas gravity and oil gravity.
                    Values of  y  are provided in Table 5-4.
                      Additional  correlations suitable for  use  with  programmable calculators are
                    discussed in a later section of  this chapter.
                    Water  Formation Volume  Factor. The factors discussed that  affected Bo also
                    affect the water formation volume factor, Bw. However, gas is only slightly soluble
                    in water so  evolution of gas from water has a negligible effect on Bw. Expansion
                    and contraction of water due to reduction of pressure and temperature are slight
                    and offsetting. Hence, Bw is seldom greater than  1.06 [18] and is  usually near
                    unity (see Table 5-5).
                      Several correlations for Bw are available, including the effect of gas saturation
                    in pure water and the  effect of  salinity [23], and the effect of  natural gas on
                    Bw as  a  function of  pressure  and  temperature  [24]. However, since Bw is  not
                    greatly affected by  these variables, only a simplified correction is presented [MI:
                      Bw = (1 + AVT)(l  + AVWJ                                     (5-1 1)
                    where AVwp and AVwT are the volume changes caused by  reduction in pressure
                    and temperature, respectively. Values of  these corrections are given in Figures
                    5-16 and 5-17.

                    Fluid Compresslbilitles
                    Gas Compresslbility. The compressibility of  a gas, which is the coefficient of
                    expansion  at  constant  temperature,  should  not  be  confused  with  the  com-
                    pressibility factor, z,  which refers to the deviation from ideal gas behavior. From
                    the basic gas equation (see Equation 5-2), Muskat [25] provided an expression
                    €or the coefficient of  isothermal compressibility:




                                                  Table 5-4
                                     Values of  Constant for  Equation 5-10
                    Oil gravity                   T = 120°F              T = 140°F
                       "API    Gas gravity:   0.7    0.8     0.9    0.7     0.8     0.9
                        26                  0.0494   0.0577   0.0645   0.0481   0.0563   0.0632
                        30                  0.0568   0.0660   0.0737   0.0550   0.0635   0.0721
                        34                  0.0654   0.0755   0.0842   0.0630   0.0736   0.0823
                        38                  0.0752   0.0864   0.0962   0.0720   0.0841   0.0939
                        42                  0.0865   0.0989   0.1099   0.0824   0.0961   0.1071
                    Oil gravlty                   T = 160°F              T = 180°F
                       "API    Gas gravity:   0.7    0.8     0.9    0.7     0.8     0.9
                        26                  0.0453   0.0519   0.0591   0.0426   0.0481   0.0543
                        30                  0.0522   0.0597   0.0677   0.0492   0.0557   0.0629
                        34                  0.0601   0.0686   0.0775   0.0567   0.0645   0.0728
                        38                  0.0692   0.0788   0.0887   0.0654   0.0747   0.0842
                        42                  0.0797   0.0906   0.1 01 6   0.0755   0.0865   0.0975
                    From Reference 21.
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