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WO2014004270A2 - Downhole jet pump - Google Patents

Downhole jet pump Download PDF

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Publication number
WO2014004270A2
WO2014004270A2 PCT/US2013/046967 US2013046967W WO2014004270A2 WO 2014004270 A2 WO2014004270 A2 WO 2014004270A2 US 2013046967 W US2013046967 W US 2013046967W WO 2014004270 A2 WO2014004270 A2 WO 2014004270A2
Authority
WO
WIPO (PCT)
Prior art keywords
pump housing
jet
jet nozzle
pump
mixing tube
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/US2013/046967
Other languages
French (fr)
Other versions
WO2014004270A4 (en
WO2014004270A3 (en
Inventor
Matthew A. JAMES
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
J&J Technical Services LLC
Original Assignee
J&J Technical Services LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by J&J Technical Services LLC filed Critical J&J Technical Services LLC
Publication of WO2014004270A2 publication Critical patent/WO2014004270A2/en
Publication of WO2014004270A3 publication Critical patent/WO2014004270A3/en
Publication of WO2014004270A4 publication Critical patent/WO2014004270A4/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04FPUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
    • F04F5/00Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04FPUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
    • F04F5/00Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow
    • F04F5/44Component parts, details, or accessories not provided for in, or of interest apart from, groups F04F5/02 - F04F5/42
    • F04F5/46Arrangements of nozzles
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04FPUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
    • F04F5/00Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow
    • F04F5/44Component parts, details, or accessories not provided for in, or of interest apart from, groups F04F5/02 - F04F5/42
    • F04F5/48Control

Definitions

  • the present invention relates to jet pumps and, more particularly, to jet pumps commonly used downhole in wells to pump formation .fluids or other fluids to the surface.
  • the downhole jet pump as disclosed herein has a comparatively high efficiency and may be operated in either the direct flow or reverse flow modes.
  • Jet pumps have long been used for recovering hydrocarbons from, downhole formations.
  • the potential for jet primps is enhanced by its relatively low cost compared to artificial lift systems that use reciprocating on rotating rod strings to pump fluids to the surface.
  • Jet pumps may be operated in a direct flow mode, ere the driving fluid is pumped down the tubing string and to the jet pump, and fluid is pumped by the jet pump to the surface in an annulus between the tubing string and the casing.
  • jet pumps may be operating in the reverse flow mode, wherein the driving fluid is pumped down the annulus to the jet pump, and the formation fluid and driving fluid are pumped to the surface through the tubing string.
  • direct pump flow is more common than reverse pump flow, the ability to pump in either direction is desired by many operators, and the costs of the jet pumps for accomplishing these goals is unfortunately increased by the large number of different parts conventionally used to maintain both direct flow jet pumps and reverse flow jet pomps.
  • a downhole jet pump for positioning in a well on tubular string to pump formation fluids from the well.
  • the jet pump includes an exterior pump bousing defining an elongate passageway therein.
  • a jet nozzle has an exterior sealed to the pom housing and increases the fluid velocity of the power fluid transmitted downhole to the jet nozzle.
  • a mixing tube positioned downstream from the jet nozzle has an elongate mixing tube passageway for receiving fluid from the jet nozzle and fluid from the formation.
  • a drffuser is provided downstream from the jet nozzle and has a lower end passing through a side port in the pump housing,
  • FIG. 1 is a cross-sectional view of one embodiment of a downhole jet pump according to the present invention.
  • J 1 Figure 2 is a cross-sectional view of a downhole jet pump similar to that shown in Figure 1 , with the nozzle and mixing tube reversed for flow to the surface through a tubing string.
  • FIG. 3 is a detailed view of pump components configured for a reverse flow.
  • Figure 5 illustrates temperature and/or pressure probe connected to the jet pump, with a standing valve positioned below the probe.
  • Figure i depicts one embodiment of a downhole jet pump 10 for positioning within a well from a tubular string to pump formation fluid from the well to an annulus surrounding the tubing siring, and then from that annulus up to the surface.
  • a downhoie jet pump may be used for pumping liquid hydrocarbons from a well., but may also be used for pumping other fluids, such as water, to enhance the production of gas or other valuable fluids.
  • the jet pump is adapted for receiving power fluid from a. tubular, and pumping both the power fluid and the formation fluid to the surface.
  • Various functional, components of a jet pump may alternatively he arranged for reverse flow, as explained subsequently,, so that the power fluid is transmitted down the annulus and the formation fluid and power fluid are recovered at the surface through the tubing string.
  • the jet pump 10 includes an exterior pump housing 12 which defines an elongate housing passageway 14 therein extending from an upper portion to a lower portion of the pump housing.
  • the exterior pump housing 12 preferably has a generally outer cylindrical surface 16 and a generally cylindrical inner surface I S which defines the passageway in the pump housing.
  • Ported sub 62 surrounds pump housing 12, and is threaded to upper seal sub 60, which is threaded to the tubing string.
  • the pump housing is thus generally tube or sleeve shaped, with its ends secured to both a top pin 20 and a bottom pin 24, respectively.
  • the top pin 20 is adapted for sealing engagement with the tubular string.
  • a lower seal sub 22 ma be provided at the lower end of the pin 24, and is threaded to tubular 62.
  • Pin 24 has a passageway 28 providing an inlet for hydrocarbons into the pump housing when pumping in the direct flow mode.
  • FIG. 1 depicts a power fluid jet nozzle 30 with a passageway 31 which becomes axialiy restrictive in the downward direction, thereby increasing the velocity of power fluid transmitted through the jet nozzle.
  • the jet nozzle 30 is supported on and has an exterior sealed to the carrier 40, which includes cireumferentia!ly spaced ports 41.
  • a mixing tube 32 within carrier 40 is provided fluidly downstream from the jet nozzle, and has an elongate mixing tube passageway 34 receiving power fluid from the jet nozzle 30.
  • A. plurality of venturi ports 41 or an axial spacing 38 between the lower end of the nozzle and an upper end of the mixing tube provided immediately below the nozzle 30 allow for entry of formation fluids from within the housing 1.2 and into the mixing tube 32.
  • the mixing tube 32 preferably may be formed from a tungsten carbide allo material to define the mixing tube passageway 34.
  • the pump as shown in FIG. 1 also includes a diffuser 46.
  • the lower portion 50 of the dif&ser includes a substantially circular curved bore 56, Diffuser 46 has a -significant advantage over a cross-over sub, which is used in other jet pumps.
  • a cross-over sub typically has a plurality of relatively small diameter flow paths to pass formation .fluid to the jet nozzle, while the diffuser provides a relatively large circumferential flow path 14 between the pump housing and both the dif&ser and the mixing tube.
  • An inlet or standing valve 100 as shown in FIG. 5 is provided at the lower end of the pump housing, and is retrievable by a wire line.
  • the jet pump .10 as shown in Figure 1 is thus configured for direc t fluid flow, wherein fluid is pumped down the tubing string and passes through the top pin 20 to the nozzle 30. which increases fluid velocity tor the fluid exiting the nozzle 30 and drawing fluid from the annulus 1 -, thus drawing in formation fluid so that both the drive fluid and the formation fluid pass through the mixing tube 32 and exit the pump through the outlet from the diffuser 46 and into the annulus between the pum housing 12 and the outer housing 62. Formation fluid thus enters interior the housing through the flow path provided in the pin 24 and passes upward in the annulus 14 to the surface. Fluid discharged by the pump thus passes upward i « the well in the annulus between the casing and the tubing string,
  • FIG. 4 shows in greater detail the nozzle 30 and mixing tube 32.
  • Sub 76 may be tht eadably connected to carrier 40, so thai nozzle 30 is sandwiched between the lower end of sub 76 and shoulder 75 on the carrier.
  • Carrier 40 includes the circumferential ' ly spaced ports 41 discussed above.
  • the upper end of sleeve 76 includes conventional seals 72 for sealing with the top sub 60.
  • Lower sub 78 is also threaded to carrier 40, and includes O-ring seals 76 for sealing with the diffiiser 46.
  • Figure 3 discloses the same nozzle 30 and mixing tube 32.
  • Sub 76 has been replaced with sub 70, which contains O-rings 72
  • Sub 78 is replaced with sub 74, and has similar O-rings as 76.
  • the carrier 40 containing the nozzle 30 and the mixing tube 32 is thus inverted in Figure 3 compared to Figure 4 for reverse fluid flow.
  • the terra "carrier” as used herein includes not only the tube 40 which surrounds the jet nozzle 30 and the mixing tube 32, but also includes the subs 70, 74. 77 and 78 each secured to the tube 40 and retrievable with the tube 40.
  • These subs which may fractionally be considered pari of the carrier, include O ring seals 72, 76 for sealing the carrier to either of the outer subs 60, 22, and are retrieved with the tube 40,
  • the sealing diameter of the subs 70, 76, 77, and 78 are thus substantially the same, so that the carrier with the subs can be inverted from a direct fluid flow configuration as shown in Figure 4 to the reverse fluid flow configuration as shown in Figure 3, while still maintaining sealing engagement between the carrier and the outer subs 60, 22,
  • Figure 2 illustrates the pump as shown in Figure I with the jet nozzle and mixing tube inverted from the Figure 1 embodiment. Except for the inversion of jet nozzle 30 and mixing tube 32 from the Figure 1 embodiment, the primary components of the pump as shown in Figure 2 are substantially identica! to the components shown in Figure 1. Since the jetting force is down for the direct flow Figure 1 configuration, no additional components are required to maintain the jet: nozzle and .mixing tube in the position as shown in Figure 1. For the Figure 2 configuration for everse flow, the jetting force is upward, and accordingly the upper end of the Figure 2 embodiment has components which retain the jet nozzle and mixing tube as shown in Figure 2, and do not allow these components to be pumped upward and instead secure the components in place.
  • Figure 2 shows an upper housing .102 which is adapted for engagement with a tubular string (not shown).
  • Sleeve 100 is positioned radially within housing 102.
  • Leaf spring 108 or other biasing means bias the dogs 104 into engagement with the annular pocket 106, thereby retaining th assembly in place.
  • a. conventional tool may be used to unlatch the dogs 104, so that the sub-assembly including components 102, 110, 108 and 104 may be retrieved to a surface while the seal sub 60 and ported sub 62 remain in place.
  • Figure 5 illustrates a lower end of the pump disclosed above, wherein the pump housing 12 includes sleeve 82, which is sealed to the housing 62.
  • Coupling 86 connects housing 62 with tubular 88 extending down from coupling 86.
  • the temperature and/or pressure probe 90 is supported on base 92, and is supported on the tubular 84.
  • probe 90 is also retrieved with the pump, so a separate operation to retrieve the probe is not required.
  • the standing valve 100 as shown in the bottom of Figure 5 ma subsequently be retrieved by a wire line operation.
  • the pump and the probe may be returned to the surface without pulling the tubular string, so that a work over rig is not required.
  • seals 72, 76 allow for a limited axial movement of the carrier with the nozzle and the mixing tube, while maintaining sealed engagement with the pump housing.
  • the axial length of a sleeve-shaped insert 94 as shown in Figures 3 and 4 may be used to selectively control the axial spacing between the tip of the nozzle 30 and the entrance to the mixing tube 32.
  • the sleeve-shaped insert 94 thus serves as an adjustment mechanism for adjusting the axial space between the jet nozzle and the mixing tube.
  • the carrier tube which houses the jet nozzle and the mixing tube may be reversed end to end when switching from a direct pump mode to a reverse pump mode, or vise versa. Additional end couplings may be manufactured, and may be the only components one needs to use the direct pump configuration or the reverse flow pump configuration.
  • the jet pump as disclosed herein is well suited for a frac flowbaek operation, when the jet pump is used to reduce formation pressure required to recover the fluid, including tracing fluids to the surface.
  • the jet pump may frequently be operated in the direct flow mode, the easy switch to reverse flow mode may be particularly beneficial for certain applications, including the reliable return of formation sand with the recovered fluid to the surface, and sour gas operations wherein the recovered fluid does not contact the casing.
  • substantially the same pump components may be used for either the direct flow or the reverse flow applications, so that a. large in ventory of direct flow jet pump components and another inventory of reverse flow jet pump components are not required.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Jet Pumps And Other Pumps (AREA)

Description

DOWNHOLE JET PUMP
Statement of Related Applications
[000! ] This application claims priority to and depends from US application no. 13/535,894 filed on 28 June 2012,
Field of th Invention
[ ββ2| The present invention relates to jet pumps and, more particularly, to jet pumps commonly used downhole in wells to pump formation .fluids or other fluids to the surface. The downhole jet pump as disclosed herein has a comparatively high efficiency and may be operated in either the direct flow or reverse flow modes.
Backgrou nd of the Iny enti n
[0003 [ Jet pumps have long been used for recovering hydrocarbons from, downhole formations. The potential for jet primps is enhanced by its relatively low cost compared to artificial lift systems that use reciprocating on rotating rod strings to pump fluids to the surface.
[0004) Various problems have limited the success of jet pumps in the hydrocarbon recovery industry. Jet pumps may be operated in a direct flow mode, ere the driving fluid is pumped down the tubing string and to the jet pump, and fluid is pumped by the jet pump to the surface in an annulus between the tubing string and the casing. Alternatively, jet pumps may be operating in the reverse flow mode, wherein the driving fluid is pumped down the annulus to the jet pump, and the formation fluid and driving fluid are pumped to the surface through the tubing string. While direct pump flow is more common than reverse pump flow, the ability to pump in either direction is desired by many operators, and the costs of the jet pumps for accomplishing these goals is unfortunately increased by the large number of different parts conventionally used to maintain both direct flow jet pumps and reverse flow jet pomps.
{"0005) Other problems with jet pumps relate to their relatively low efficiency compared to other artificial lift, systems for returning hydrocarbons to the surface, the additional costs associated with retrieving pressure or temperature sensors to the surface after the jet pump is retrieved, and techniques which allow adjustment of the axial spacing between the nozzle and the mixing tube which receives fluid from the nozzle.
{0006) Prior art patents directed to jet pumps include U.S. Patents 4,858,893, 5,083,609, 5,055,022, and 7,909,089. Another jet pump is disclosed in a Volcamca website under www.youtube.com watch'^v^nDYFpBUBwic. Some of these patents discuss reverse flow to pump a component to the sin-face, but the pump is not. operating as a jet pump during this component retrieval operation.
0007) The disadvantages of the prior art are overcome by the present invention, and an improved downhole jet pump is hereinafter disclosed.
SUMMARY OF THE INVENTION
[6008] in one embodiment, a downhole jet pump is provided, for positioning in a well on tubular string to pump formation fluids from the well. The jet pump includes an exterior pump bousing defining an elongate passageway therein. A jet nozzle has an exterior sealed to the pom housing and increases the fluid velocity of the power fluid transmitted downhole to the jet nozzle. A mixing tube positioned downstream from the jet nozzle has an elongate mixing tube passageway for receiving fluid from the jet nozzle and fluid from the formation. In one embodiment, a drffuser is provided downstream from the jet nozzle and has a lower end passing through a side port in the pump housing,
[6009] These and further features and advantages of the present invention will become apparent from the fo! lowing detailed description, wherein reference is made to the figures in the accompanying dra wings.
BRIEF DESCRIPTION OF THE DRAWINGS
fOOiOJ Figure 1 is a cross-sectional view of one embodiment of a downhole jet pump according to the present invention.
| J 1 Figure 2 is a cross-sectional view of a downhole jet pump similar to that shown in Figure 1 , with the nozzle and mixing tube reversed for flow to the surface through a tubing string.
[0012} Figure 3 is a detailed view of pump components configured for a reverse flow.
|0G13J Figure 4 is a detailed view of pump components configured for direct flow.
{0014| Figure 5 illustrates temperature and/or pressure probe connected to the jet pump, with a standing valve positioned below the probe.
DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS
[6015 j Figure i depicts one embodiment of a downhole jet pump 10 for positioning within a well from a tubular string to pump formation fluid from the well to an annulus surrounding the tubing siring, and then from that annulus up to the surface. Those skilled in the art wi l appreciate that a downhoie jet pump may be used for pumping liquid hydrocarbons from a well., but may also be used for pumping other fluids, such as water, to enhance the production of gas or other valuable fluids. The jet pump is adapted for receiving power fluid from a. tubular, and pumping both the power fluid and the formation fluid to the surface. Various functional, components of a jet pump may alternatively he arranged for reverse flow, as explained subsequently,, so that the power fluid is transmitted down the annulus and the formation fluid and power fluid are recovered at the surface through the tubing string.
[0016f The jet pump 10 includes an exterior pump housing 12 which defines an elongate housing passageway 14 therein extending from an upper portion to a lower portion of the pump housing. The exterior pump housing 12 preferably has a generally outer cylindrical surface 16 and a generally cylindrical inner surface I S which defines the passageway in the pump housing. Ported sub 62 surrounds pump housing 12, and is threaded to upper seal sub 60, which is threaded to the tubing string. The pump housing is thus generally tube or sleeve shaped, with its ends secured to both a top pin 20 and a bottom pin 24, respectively. The top pin 20 is adapted for sealing engagement with the tubular string. A lower seal sub 22 ma be provided at the lower end of the pin 24, and is threaded to tubular 62. Pin 24 has a passageway 28 providing an inlet for hydrocarbons into the pump housing when pumping in the direct flow mode.
[0017j Figure 1 depicts a power fluid jet nozzle 30 with a passageway 31 which becomes axialiy restrictive in the downward direction, thereby increasing the velocity of power fluid transmitted through the jet nozzle. The jet nozzle 30 is supported on and has an exterior sealed to the carrier 40, which includes cireumferentia!ly spaced ports 41. A mixing tube 32 within carrier 40 is provided fluidly downstream from the jet nozzle, and has an elongate mixing tube passageway 34 receiving power fluid from the jet nozzle 30. A. plurality of venturi ports 41 or an axial spacing 38 between the lower end of the nozzle and an upper end of the mixing tube provided immediately below the nozzle 30 allow for entry of formation fluids from within the housing 1.2 and into the mixing tube 32. The mixing tube 32 preferably may be formed from a tungsten carbide allo material to define the mixing tube passageway 34.
[0018} The pump as shown in FIG. 1 also includes a diffuser 46. The lower portion 50 of the dif&ser includes a substantially circular curved bore 56, Diffuser 46 has a -significant advantage over a cross-over sub, which is used in other jet pumps. A cross-over sub typically has a plurality of relatively small diameter flow paths to pass formation .fluid to the jet nozzle, while the diffuser provides a relatively large circumferential flow path 14 between the pump housing and both the dif&ser and the mixing tube. An inlet or standing valve 100 as shown in FIG. 5 is provided at the lower end of the pump housing, and is retrievable by a wire line.
{0019J The jet pump .10 as shown in Figure 1 is thus configured for direc t fluid flow, wherein fluid is pumped down the tubing string and passes through the top pin 20 to the nozzle 30. which increases fluid velocity tor the fluid exiting the nozzle 30 and drawing fluid from the annulus 1 -, thus drawing in formation fluid so that both the drive fluid and the formation fluid pass through the mixing tube 32 and exit the pump through the outlet from the diffuser 46 and into the annulus between the pum housing 12 and the outer housing 62. Formation fluid thus enters interior the housing through the flow path provided in the pin 24 and passes upward in the annulus 14 to the surface. Fluid discharged by the pump thus passes upward i« the well in the annulus between the casing and the tubing string,
{"0020} Figure 4 shows in greater detail the nozzle 30 and mixing tube 32. Sub 76 may be tht eadably connected to carrier 40, so thai nozzle 30 is sandwiched between the lower end of sub 76 and shoulder 75 on the carrier. Carrier 40 includes the circumferential'ly spaced ports 41 discussed above. The upper end of sleeve 76 includes conventional seals 72 for sealing with the top sub 60. Lower sub 78 is also threaded to carrier 40, and includes O-ring seals 76 for sealing with the diffiiser 46.
{002.1 Figure 3 discloses the same nozzle 30 and mixing tube 32. Sub 76 has been replaced with sub 70, which contains O-rings 72, Sub 78 is replaced with sub 74, and has similar O-rings as 76. The carrier 40 containing the nozzle 30 and the mixing tube 32 is thus inverted in Figure 3 compared to Figure 4 for reverse fluid flow.
{"0022J Referring to Figures 3 and 4, the terra "carrier" as used herein includes not only the tube 40 which surrounds the jet nozzle 30 and the mixing tube 32, but also includes the subs 70, 74. 77 and 78 each secured to the tube 40 and retrievable with the tube 40. These subs, which may fractionally be considered pari of the carrier, include O ring seals 72, 76 for sealing the carrier to either of the outer subs 60, 22, and are retrieved with the tube 40, The sealing diameter of the subs 70, 76, 77, and 78 are thus substantially the same, so that the carrier with the subs can be inverted from a direct fluid flow configuration as shown in Figure 4 to the reverse fluid flow configuration as shown in Figure 3, while still maintaining sealing engagement between the carrier and the outer subs 60, 22,
f O023| Figure 2 illustrates the pump as shown in Figure I with the jet nozzle and mixing tube inverted from the Figure 1 embodiment. Except for the inversion of jet nozzle 30 and mixing tube 32 from the Figure 1 embodiment, the primary components of the pump as shown in Figure 2 are substantially identica! to the components shown in Figure 1. Since the jetting force is down for the direct flow Figure 1 configuration, no additional components are required to maintain the jet: nozzle and .mixing tube in the position as shown in Figure 1. For the Figure 2 configuration for everse flow, the jetting force is upward, and accordingly the upper end of the Figure 2 embodiment has components which retain the jet nozzle and mixing tube as shown in Figure 2, and do not allow these components to be pumped upward and instead secure the components in place. More particularly, Figure 2 shows an upper housing .102 which is adapted for engagement with a tubular string (not shown). Sleeve 100 is positioned radially within housing 102. Leaf spring 108 or other biasing means bias the dogs 104 into engagement with the annular pocket 106, thereby retaining th assembly in place. If it is desired to retrieve the inner components in the Figure 2 embodiment, a. conventional tool may be used to unlatch the dogs 104, so that the sub-assembly including components 102, 110, 108 and 104 may be retrieved to a surface while the seal sub 60 and ported sub 62 remain in place.
24| Figure 5 illustrates a lower end of the pump disclosed above, wherein the pump housing 12 includes sleeve 82, which is sealed to the housing 62. Coupling 86 connects housing 62 with tubular 88 extending down from coupling 86. The temperature and/or pressure probe 90 is supported on base 92, and is supported on the tubular 84. When the jet pump is retrieved to the surface, probe 90 is also retrieved with the pump, so a separate operation to retrieve the probe is not required. If desired, the standing valve 100 as shown in the bottom of Figure 5 ma subsequently be retrieved by a wire line operation. As previously stated, the pump and the probe may be returned to the surface without pulling the tubular string, so that a work over rig is not required. |ft025| In both, the direct flow configuration as shown in Figure 4 and the reverse flow configuration as shown in Figure 3, seals 72, 76 allow for a limited axial movement of the carrier with the nozzle and the mixing tube, while maintaining sealed engagement with the pump housing. Also, the axial length of a sleeve-shaped insert 94 as shown in Figures 3 and 4 may be used to selectively control the axial spacing between the tip of the nozzle 30 and the entrance to the mixing tube 32. The sleeve-shaped insert 94 thus serves as an adjustment mechanism for adjusting the axial space between the jet nozzle and the mixing tube.
|0026| Comparing Figures 3 and 4, the carrier tube which houses the jet nozzle and the mixing tube may be reversed end to end when switching from a direct pump mode to a reverse pump mode, or vise versa. Additional end couplings may be manufactured, and may be the only components one needs to use the direct pump configuration or the reverse flow pump configuration.
10027) The jet pump as disclosed herein is well suited for a frac flowbaek operation, when the jet pump is used to reduce formation pressure required to recover the fluid, including tracing fluids to the surface. Although the jet pump may frequently be operated in the direct flow mode, the easy switch to reverse flow mode may be particularly beneficial for certain applications, including the reliable return of formation sand with the recovered fluid to the surface, and sour gas operations wherein the recovered fluid does not contact the casing. Also, substantially the same pump components may be used for either the direct flow or the reverse flow applications, so that a. large in ventory of direct flow jet pump components and another inventory of reverse flow jet pump components are not required.
[0028 j The entire jet pum as disclosed herein is retrievable to the surface without pullin the tubing string, which may remain in the well during retrieval and reinsertion of a jet pump. Recovery of the jet pump thus need not eatail the substantial expense and time of the orkover rig to pull the tubing string with the jet pump.
{"0029} Although specific embodiments of the invention have been described herein in some detail, this has been done solely for the purposes of explaining the various aspects of the invention, and is not intended to limit the scope of the invention as defined in die claims which follow. Those skilled in the art will understand that the embodiment shown and described is exemplary, and various other substitutions, alterations and modifications, including but not limited to those design alternatives specifically discussed herein, may be made in the practice of the invention without departing from its scope.

Claims

WHAT IS CLAIMED IS:
1. A dowri olejet pomp for positioning in a well on a tubular string to pump fluids from the well to the surface, comprising;
an exterior pump housing defining an elongate housing passageway therein having a central axis and extending from an upper portion to a lower portion of the pump housing;
a power fluid jet nozzle having an exterior sealed to the pomp housing, the jet nozzle having a jet passageway therein for increasing fluid velocity of power fluid transmitted through the jet nozzle;
a mixing tube fluidly downstream from the jet nozzle and having an elongate mixing tube passageway receivin fluid from the jet nozzle;
a diffuser fluidly downstream from the mixing tube and having a curved flow path therein, the diffuser sealed to the exterior pomp homing and the flow path in the diffuses' being in communication with a throughport in the pump housing, a circumferential spacing betwee an exterior surface of the diffuser and an interior surface of the pump housing defining a flow path for formation fluid flowing to the jet nozzle; and
a carrier in the pump housing and supporting the jet nozzle and the mixing tube, the carrier including one or more ports for passing formation fluid radially inward to the jet nozzle, the carrier having a first end for sealing with either the pump housing and the diffuser, and an axiaily opposing second end for sealing with the other of the pump housing and the diffuser, such that the carrier, the jet nozzle, and the mixing tube may be arranged for direct flow or may be inverted in the pump housing for reverse flow.
The jet pump as defined in Claim I, further comprising: an adjustment mechanism for adjusting an axial position between the jet nozzle with respect to the mixing tube,
3 , The jet pump as defined in Claim 1 , wherein the adjustment mechanism, is a selected axial length sleeve supporting the jet nozzle,
4. The jet pump as defined in Claim I, further comprising:
a temperature and/or pressure probe supported in the well from the jet pump housing, such that retrieval of the jet pump housing to the surface retrieves the probe.
5. The jet pump as defined in Claim 1„ wherein the carrier is scaled to the pump housing and. to the diffuser., such that there is limited axial movement of the carrier with respect to the pump housing and the diffuser.
6. The jet pump as defined in Claim I , further comprising:
an inlet valve below the pump housing for controlling 'formation iluid .flow to the pump housing,
7. A downhole jet pump for positioning in a well on a tubular siring to pump fluids f om the well to the surface, comprising:
an exterior pump housing defining an elongate housing passageway therein having a central axis and extending from an upper portion to a lower portion of the pump housing; a power fluid jet nozzle having an exterior sealed to the pump housing, the jet nozzle having a jet passageway therein for increasing fluid velocity of power fluid transmitted through the jet nozzle;
a mixing tube flu icily downstream from the jet nozzle and having an elongate mixing tube passageway receiving fluid .from the jet nozzle;
a diffuser f!uid!y downstream from the mixing tube and having a curved flow path, therein, the diffuser sealed to the exterior pump housing and the flow path in the diffttser being in communication with a iluoughpori in the pump housing, a circumferential spacing between an exterior surface of the diffuser and an interior surface of the pump housing defining a flow path for formation fluid flowing to the jet nozzle; and
a carrier in the pump housing radialiy exterior of both the jet nozzle and the mixing tube and supporting the jet nozzle and the mixing tube, the carrier including an opening or passing formation fluid radiali inward to the jet nozzle, the carrier having axialiy opposing ends each for sealing with either the pum housing or the diffuser, such that the carrier, the jet nozzle, and the mixing tube may be arranged for direct flow or may be inverted in the pomp housing for reverse flow.
8. The jet pump as defined in Claim 7, further comprising:
an adjustment mechanism for adjusting an axial position between the jet nozzle with respect to the mixing tube.
9. The jet pump as defined in Claim 8, wherein the adjustment mechanism is a selected axial length sleeve supporting the jet nozzle.
10. The jet pump as defined in Claim 7, further comprising;
a temperature and/or pressure probe supported in the well from the jet pump housing, sueh that retrieval of the jet pump housing to the surface retrieves the probe. i 1. The jet pump as defined in Claim 7, farther comprising:
an inlet valve below the pump housing .for controlling formation fluid flow within the pump housing,
12, A method of operating a dewnhole jet pump positioned, in a well on a tubular siring to pump fluids from the well to the surface, comprising:
providing an exterior pump housing defining an elongate housing passageway therein having a centra! axis and extending from an upper portion to a lower portion of the pump housing;
positioning a power fluid jet nozzle having an exterior sealed to the pump housing, the jet nozzle having a jet passageway therein for increasing fluid velocity of power fluid transmitted through the jet nozzle;
positioning a mixing tube fmid!y downsiream from the jet nozzle and having an elongate mixing tube passageway receiving fluid from the jet nozzle;
providing a difftiser fluidly downstream from the mixing tube and having a curved flo path therein, the diffitser sealed to the exterior pump housing and the flow path in the diffuser being in commuaicaiioa with a througaport in the pump housing, a circumferential spacing between an exterior surface of the diffuser and an interior surface of the pump housing defining a flow path for formation fluid flowing to the jet nozzle;
providing a carrier in the pump housing and supporting the jet nozzle and the mixing tube, the carrier including ports for passing formation, .fluid radially inward to the jet nozzle, the carrier having axiaily opposing ends each for sealing with either the pump housing and the diffuser, such that the carrier, the jet nozzle, and the mixing tube may be arranged for direct flow; and
inverting the carrier, the jet nozzle and the mixing tube in the pump housing for reverse flow,
13. The method as defined in Claim 12, further comprising:
adjusting an. axial position between the jet nozzle with respect to the mixing tube,
14, The method as defined in Claim 12, further comprising:
supporting a temperature and/or pressure probe in the well from the jet pump housing, such that retrieval of the jet pump housing to the surface retrieves the probe.
15. The method as defined in Claim 12, wherein the carrier is sealed to the pump housing and to the diffuser. such that there is limited axial movement of the carrier with respect to the pump housing and the diffuser.
16, The method as defined in Claim 12, further comprising; positioning an inlet valve below the pump housing for controlling formation fluid flow within the pump housing.
PCT/US2013/046967 2012-06-28 2013-06-21 Downhole jet pump Ceased WO2014004270A2 (en)

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US20150167697A1 (en) * 2013-12-18 2015-06-18 General Electric Company Annular flow jet pump for solid liquid gas media
WO2016036808A1 (en) 2014-09-02 2016-03-10 Tech Flo Consulting, Llc Flow back jet pump
US10309425B1 (en) 2015-08-20 2019-06-04 Steven P. Burgess High flow capacity well fluid extraction jet pump providing through access
WO2020072393A1 (en) * 2018-10-04 2020-04-09 Harris George E Jet pump
WO2020088732A1 (en) * 2018-10-29 2020-05-07 Othman Ahmed Abdou Abd Elatif Jet pump for the gases self relief of petroleum wells
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WO2014004270A3 (en) 2014-09-25
US20140003965A1 (en) 2014-01-02

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