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Guo, Boyun / Computer Assited Petroleum Production Engg 0750682701_chap13 Final Proof page 193  3.1.2007 9:07pm Compositor Name: SJoearun




                                                                                           GAS LIFT  13/193
                       Table 13.3 Result Given by the Computer Program CentrifugalCompressorPower.xls
                       CentrifugalCompressorPower.xls
                       Description: This spreadsheet calculates stage power of reciprocating compressor.
                       Instruction: (1) Update parameter valves in the ‘‘Input data’’ in blue; (2) click ‘‘Solution’’ button; (3) view result in the
                       Solution section.
                       Input data
                       Gas flow rate (q g ):         32 MMscf/day
                       Inlet temperature (T 1 ):     70 8F
                       Inlet pressure ( p 1 ):       100 psia
                       Gas-specific gravity (g g ):  0:65 (air ¼ 1)
                       Discharge pressure ( p 2 ):   341 psia
                       Gas-specific heat ratio (k):  1.25
                       Base temperature (T b ):      60 8F
                       Base pressure ( p b ):        14.7 psia
                       Solution
                          p 2
                       r ¼                           ¼ 3:41
                          p 1
                           q MM
                       q ¼                           ¼ 22,222 scfm
                          (24)(60)
                           p b T 1
                       q 1 ¼   q                     ¼ 3,329 scfm
                           p 1 T b
                       E p ¼ 0:61 þ 0:03 log (q 1 )  ¼ 0:7192
                           n   1  k   1  1
                       R p ¼   ¼                     ¼ 0:2781
                             n    k   E p

                       T 2 ¼ T 1 r R p               ¼ 285 F
                       z 1 by Hall–Yarborogh Method  ¼ 1:0891
                       z 2 by Hall–Yarborogh Method  ¼ 0:9869
                           z 1 p b T 1
                       q 1 ¼    q                    ¼ 3,674
                           z 2 p 1 T b
                       E p ¼ 0:61 þ 0:03 log (q 1 )  ¼ 0:7205
                           n   1  k   1  1
                       R p ¼   ¼                     ¼ 0:2776
                             n    k   E p

                       T 2 ¼ T 1 r R p               ¼ 285 F

                             q 1 p 1  z 1 þ z 2  r R p    1
                       Hp g ¼                        ¼ 3,102 hp
                            229E p  2z 1  R p
                       Hp b ¼ Hp g þ 50              ¼ 3,152 hp
                                                     ¼ 18:85
                       MW a ¼ 29g g
                       R ¼  1,544                    ¼ 81:91
                           MW a
                               z 1 þz 2  r Rp  1
                       H g ¼ RT 1  2  R p            ¼ 65,853 lbf-ft=lbm
                                                                       1          R
                         There are different types of unloading valves, namely casing  P vo ¼  P d þ S t    P t ,  (13:42)
                       pressure-operated valve (usually called a pressure valve), throt-  1   R  1   R
                       tling pressure valve (also called a proportional valve or continu-  where
                       ous flow valve), fluid-operated valve (also called a fluid valve),
                                                                   P vo ¼ valve opening pressure, psig
                       and combination valve (also called a fluid open-pressure closed
                                                                   P d ¼ pressure in the dome, psig
                       valve). Different gas lift design methods have been developed
                                                                   S t ¼ equivalent pressure caused by spring tension, psig
                       and used in the oil industry for applications of these valves.
                                                                   P t ¼ tubing pressure at valve depth when the
                                                                       valve opens, psi
                       13.5.2.1 Pressure Valve                      R ¼ area ratio A p =A b
                       Pressure valves are further classified as unbalanced bellow  A p ¼ valve seat area, in: 2
                                                                                            2
                       valves, balanced pressure valves, and pilot valves. Tubing  A b ¼ total effective bellows area, in: .
                       pressure affects the opening action of the unbalanced  R                        R
                       valves, but it does not affect the opening or closing of  The term  1 R P t is called tubing effect (T.E.) and  1 R
                       balanced valves. Pilot valves were developed for intermit-  is called tubing effect factor (T.E.F.). With other parameters
                       tent gas lift with large ports.           given, Eq. (13.42) is used for determining the required dome
                                                                 pressure at depth, that is, P d ¼ (1   R)P vo   S t þ RP t ,in
                       13.5.2.1.1 Unbalanced Bellow Valve As shown in  valve selection.
                       Fig. 13.9, an unbalanced bellow valve has a pressure-  When a valve is at its open condition (as shown in
                       charged nitrogen dome and an optional spring loading  Fig. 13.10), the maximum pressure under the ball (assumed
                       element. While the forces from the dome pressure and spring  to be casing pressure) required to close the valve is called
                       act to cause closing of the valve, the forces due to casing and  the valve closing pressure and is expressed as
                       tubing pressures act to cause opening of the valve. Detailed  P vc ¼ P d þ S t 1   Rð  Þ,  (13:43)
                       discussions of valve mechanics can be found in Brown (1980).
                       When a valve is at its closed condition (as shown in  where P vc ¼ valve closing pressure, psig.
                       Fig. 13.9), the minimum casing pressure required to open  The difference between the valve opening and closing
                       the valve is called the valve opening pressure and is expressed as  pressures,P vo   P vc ,iscalledspread.Spreadcanbeimportant
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