Page 406 - Hydrocarbon Exploration and Production Second Edition
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Managing the Producing Field                                          393


                                                             tubing size
                   P i
                                                            2  7/8"
                  Flowing bottom hole pressure (psig)  P 2       5  1/2"


                                                                 3  1/2"








                                                                IPR 1

                                                                             unstable
                                                                             flow
                                                   IPR 2
                                                                             stable
                                   Liquid flow rate (stb/d)                  flow
             Figure 16.8  Tubing size selection.

             to achieve this. The tubing size should maximise the potential of the reservoir.
             The example shown in Figure 16.8 shows that at the beginning of the field life,
                                                                   1
             when the reservoir pressure is P i , the optimum tubing size is 5 in. However, as the
                                                                   2
             reservoir pressure declines, the initial tubing is no longer able to produce to surface,
                                  7
             and a smaller tubing (2 in.) is required. Changing the tubing size would require
                                  8
             a workover. Whether it would be better to install the smaller tubing from the
             beginning (initially choking the flowrate but not requiring the later workover) is an
             economic decision.
                The relationship between the tubing performance and reservoir performance
             is more fully explained in Section 10.5, Chapter 10.
                Artificial lift techniques are discussed in Section 10.8, Chapter 10. During
             production, the operating conditions of any artificial lift technique will be
             optimised with the objective of maximising production. For example, the optimum
             gas–liquid ratio will be applied for gas lifting, possibly using computer assisted
             operations (CAO) as discussed in Section 12.2, Chapter 12. Artificial lift may not be
             installed from the beginning of a development, but at the point where the natural
             drive energy of the reservoir has reduced. The implementation of artificial lift
             will be justified, like any other incremental project, on the basis of a positive NPV
             (see Section 14.4, Chapter 14).
                Sand production from loosely consolidated formations may lead to erosion of
             tubulars and valves and sand-fill in both the sump of the well and surface separators.
             In addition, sand may bridge off in the tubing, severely restricting flow. The
             presence of sand production may be monitored by in-line detectors. If the quantities
             of sand produced become unacceptable then downhole sand exclusion should be
             considered (Section 10.7, Chapter 10).
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