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Guo, Boyun / Computer Assited Petroleum Production Engg 0750682701_chap13 Final Proof page 185  3.1.2007 9:07pm Compositor Name: SJoearun




                                                                                           GAS LIFT  13/185
                       zone depth, and D v is the depth of the gas injection point.  This example shows that increasing the gas injection rate
                       Based on the oil gravity of 26 8API, G R is calculated to be  from 1 MMscf/day to 1.58 MMscf/day will not make a
                       0.39 psi/ft. D and D v are equal to 5,200 ft and 5,000 ft,  significant difference in the oil production rate.
                       respectively in this problem.
                         The outflow performance curve for the gas injection
                       point can be determined based on 2.259-in. tubing ID,  13.4 Gas Lift Gas Compression Requirements
                       200 psia wellhead pressure, and the GLRs.  The gas compression station should be designed to provide
                                                                 an adequate gas lift gas flow rate at sufficiently high
                       a. Spreadsheet OptimumGLR.xls gives the following:
                                                                 pressure. These gas flow rates and output pressures deter-
                                                                 mine the required power of the compression station.
                                q (stb/d)   GLR opt (scf/stb)
                                                                 13.4.1 Gas Flow Rate Requirement
                                                                 The total gas flow rate of the compression station should
                                 400           4,500
                                 600           3,200             be designed on the basis of gas lift at peak operating
                                 800           2,400             condition for all the wells with a safety factor for system
                                                                 leak consideration, that is,
                                                                          Nw
                                                                         X
                       Using these data to run computer program HagedornBrown-  q g,total ¼ S f  q g,inj i ,  (13:4)
                       Correlation.xls (on the CD attached to this book) gives  i¼1
                                                                 where
                                q (stb/day)      p t (psia)         q g ¼ total output gas flow rate of the compression
                                                                       station, scf/day
                                  400              603              S f ¼ safety factor, 1.05 or higher
                                  600              676             N w ¼ number of wells.
                                  800              752             The procedure for determination of lift gas injection
                                                                 rate q g,inj to each well has been illustrated in Example Prob-
                                                                 lem 13.1.
                       Figure 13.5 shows the system analysis plot given by
                       the computer program GasLiftPotential.xls. It indicates  13.4.2 Output Gas Pressure Requirement
                       an operating point of q ¼ 632 stb=day and p t,v ¼ 698 psia  Kickoff of a dead well (non-natural flowing) requires
                       tubing pressure at the depth of injection.  much higher compressor output pressures than the ulti-
                         The optimum GLR at the operating point is calculated  mate goal of steady production (either by continuous gas
                       with interpolation as                     lift or by intermittent gas lift operations). Mobil compressor
                                         3,200   2,400           trailers are used for the kickoff operations. The output
                            GLR opt,o ¼ 2,400 þ    ð 800   632Þ  pressure of the compression station should be designed
                                          800   600
                                                                 on the basis of the gas distribution pressure under normal
                                  ¼ 3,072 scf=stb:               flow conditions, not the kickoff conditions. It can be
                                                                 expressed as
                       The injection GLR is
                                                                 p out ¼ S f p L ,                   (13:5)
                              GLR inj ¼ 3,072   300 ¼ 2,772 scf=stb:
                                                                 where
                       Then the required gas injection rate to the well can be
                       calculated:                                 p out ¼ output pressure of the compression
                                                                        station, psia
                             q g,inj ¼ (2,772)(632) ¼ 1,720,000 scf=day  S f ¼ safety factor
                                                                    p L ¼ pressure at the inlet of the gas
                       b. For a given amount of lift gas 1 MMscf/day, the GLR  distribution line, psia.
                         can be calculated with Eq. (13.3) as
                                                                   Starting from the tubing pressure at the valve ( p t,v ), the
                                                                 pressure at the inlet of the gas distribution line can be
                                                                 estimated based on the relationships of pressures along
                                q (stb/day)  GLR (scf/stb)
                                                                 the injection path. These relationships are discussed in
                                                                 the following subsections.
                                  400           2,800
                                  600           1,967
                                  800           1,550            13.4.2.1 Injection Pressure at Valve Depth
                                                                 The injection pressure at valve depth in the casing side can
                                                                 be expressed as
                       Using these data to run computer program Hagedorn-
                       BrownCorrelation.xls gives                p c,v ¼ p t,v þ Dp v ,              (13:6)
                                                                 where
                                                                   p c,v ¼ casing pressure at valve depth, psia
                                q (stb/day)      p t (psia)        Dp v ¼ pressure differential across the operating valve
                                                                        (orifice).
                                  400              614
                                  600              694             It is a common practice to use Dp v ¼ 100 psi. The
                                  800              774           required size of the orifice can be determined using the
                                                                 choke-flow equations presented in Subsection 13.4.2.3.
                       Figure 13.6 shows the system analysis plot given by
                       the computer program GasLiftPotential.xls. It indicates  13.4.2.2 Injection Pressure at Surface
                       an operating point of q ¼ 620 stb=day and p t ¼ 702 psia  Accurate determination of the surface injection pressure
                       tubing pressure at the depth of injection.  p c,s requires rigorous methods such as the Cullender and
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