Page 210 - PVT Property Correlations
P. 210

184  PVT Property Correlations


            The little gas production is usually flared at these quantities for economic
            reasons. Additionally, at these low levels of bubble point pressure, the reser-
            voir pressure may not ever reach the bubble point pressure (the reservoir may
            be abandoned before reaching the bubble point pressure). In some cases (e.g.,
            shallow reservoirs that are developed with the high density of production
            wells), little free gas is generated in the reservoir when the pressure declines
            below the bubble point pressure. Even in those cases, gas production will not
            increase significantly, and the concept of low GOR oils can be justified.
               Low GOR oils usually exist at shallow and medium depths. One can
            argue that oil trapped near the surface may not contain large amounts of gas
            as the volatile components of oil may have escaped the oil and found their
            way to the surface over geologic ages. Low GOR oils are usually discovered
            at low initial reservoir pressures.
               As discussed in Chapter 2, Reservoir-Fluid Classification, many classifi-
            cations for reservoir fluid types have been suggested. The most widely used
            classification is that of McCain (1994). This classification divides oils into
            two types: black and volatile. The low GOR oil is included in the black-oil
            classification of McCain (1994). However, low GOR oils, as a class of fluids
            on their own, differ from typical black oils as follows:
            1. Low GOR oils produce very little gas, which is often ignored in field
               measurements.
            2. Production remains above the bubble point for the entire life of the
               reservoir.
            3. Calculation of PVT properties is reduced to the undersaturated portion of
               the PVT properties curve.
            4. Solution GOR can be neglected for reservoir engineering calculations.
               However, it can be assumed to be a constant value for production engi-
               neering calculations (e.g., vertical-lift performance calculations of pro-
               duction wells).
               A typical phase diagram of low GOR oil is shown in Fig. 8.2.This
            figure shows that at reservoir temperature, bubble point pressure is low and
            may not be reached during reservoir depletion. The oil, therefore, remains in
            the single-phase liquid region for the entire life of the reservoir. The phase
            diagram of low GOR oil also shows that even if the reservoir pressure
            declines below the bubble point pressure, little gas will be formed in the res-
            ervoir. Efficient recovery of the oil from the reservoirs will require a signifi-
            cant number of wells and/or water injection or enhanced oil recovery.
               Fig. 8.3 represents three different phase diagrams plotted using an EOS
            program for three different low GOR oil samples taken from the same
            region. The three samples represent oils that are produced from stacked reser-
            voirs. The depth of the three samples ranges from 5000 to 7000 ft TVDss.
               The composition of the three samples is given in Table 8.1. Although the
            three samples differ in composition (values of C7 1 mole percent range
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