Page 116 - Fundamentals of Reservoir Engineering
P. 116

PVT ANALYSIS FOR OIL                                   55


                     gas oil ratio if the pressure in the vicinity of the well is at or above bubble point
                     pressure. If not, the surface gas oil ratio will be too low or too high, depending upon
                     whether the free gas saturation in the reservoir is below or above the critical saturation
                     at which gas will start to flow. In this respect it should be emphasized that PVT samples
                     should be taken as early as possible in the producing life of the field to facilitate the
                     collection of samples in which the oil and gas are combined in the correct ratio.


              2.4    DETERMINATION OF THE BASIC PVT PARAMETERS IN THE LABORATORY AND
                     CONVERSION FOR FIELD OPERATING CONDITIONS


                     Quite apart from the determination of the three primary PVT parameters B o, R s and B g,
                     the full laboratory analysis usually consists of the measurement or calculation of fluid
                     densities, viscosities, composition, etc. These additional measurements will be briefly
                     discussed in section 2.6. For the moment, the essential experiments required to
                     determine the three basic parameters will be detailed, together with the way in which
                     the results of a PVT analysis must be modified to match the field operating conditions.

                     The analysis consists of three parts:

                     −    flash expansion of the fluid sample to determine the bubble point pressure;

                     −    differential expansion of the fluid sample to determine the basic parameters B o,
                          R s and B g;

                     −    flash expansion of fluid samples through various separator combinations to
                          enable the modification of laboratory derived PVT data to match field separator
                          conditions.

                     The apparatus used to perform the above experiments is the PV cell, as shown in
                     fig. 2.8. After recombining the oil and gas in the correct proportions, the fluid is charged
                     to the PV cell which is maintained at constant temperature, the measured reservoir
                     temperature, throughout the experiments. The cell pressure is controlled by a positive
                     displacement mercury pump and recorded on an accurate pressure gauge. The
                     plunger movement is calibrated in terms of volume of mercury injected or withdrawn
                     from the PV cell so that volume changes in the cell can be measured directly.

                     The flash and differential expansion experiments are presented schematically in
                     figs. 2.9(a) and 2.9(b). In the flash experiment the pressure in the PV cell is initially
                     raised to a value far in excess of the bubble point. The pressure is subsequently
                     reduced in stages, and on each occasion the total volume v t of the cell contents is
                     recorded. As soon as the bubble point pressure is reached, gas is liberated from the oil
                     and the overall compressibility of the system increases significantly. Thereafter, small
                     changes in pressure will result in large changes in the total fluid volume contained in
                     the PV cell. In this manner, the flash expansion experiment can be used to "feel" the
                     bubble point. Since the cell used is usually opaque the separate volumes of oil and
                     gas, below bubble point pressure, cannot be measured in the experiment and
                     therefore, only total fluid volumes are recorded. In the laboratory analysis the basic unit
                     of volume, against which all others are compared, is the volume of saturated oil at the
   111   112   113   114   115   116   117   118   119   120   121