Classifications

• • E—FIXED CONSTRUCTIONS
  • E21—EARTH OR ROCK DRILLING; MINING
  • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
  • E21B34/00—Valve arrangements for boreholes or wells
  • E21B34/06—Valve arrangements for boreholes or wells in wells
  • E21B34/08—Valve arrangements for boreholes or wells in wells responsive to flow or pressure of the fluid obtained
• • E—FIXED CONSTRUCTIONS
  • E21—EARTH OR ROCK DRILLING; MINING
  • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
  • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
  • E21B43/02—Subsoil filtering
  • E21B43/08—Screens or liners
• • E—FIXED CONSTRUCTIONS
  • E21—EARTH OR ROCK DRILLING; MINING
  • E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
  • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
  • E21B43/12—Methods or apparatus for controlling the flow of the obtained fluid to or in wells

Definitions

• This disclosure relates generally to equipment utilized and operations performed in conjunction with a subterranean well and, in an example described below, more particularly provides for preventing flow of undesired fluid through a variable flow resistance system.
• a flow control system which brings improvements to the art of regulating fluid flow in wells.
• a flow control system is used in conjunction with a variable flow resistance system.
• flow through the variable flow resistance system is completely prevented when an unacceptable level of undesired fluid is flowed through the system.
• a flow control system for use with a subterranean well can include a flow chamber through which a fluid composition flows, and a closure device which is biased toward a closed position in which the closure device prevents flow through the flow chamber.
• the closure device can be displaced to the closed position in response to an increase in a ratio of undesired fluid to desired fluid in the fluid composition.
• a flow control system can include a closure device and a structure which prevents the closure device from being displaced to a closed position in which the closure device prevents flow through the flow chamber.
• the fluid composition can flow through the structure to an outlet of the flow chamber.
• FIG. 1 is a representative partially cross-sectional view of a well system which can embody principles of this disclosure .
• FIG. 2 is an enlarged scale representative cross- sectional view of a well screen and a variable flow
• FIGS. 3A & B are representative "unrolled" plan views of one configuration of the variable flow resistance system, taken along line 3-3 of FIG. 2.
• FIGS. 4A & B are representative plan views of another configuration of the variable flow resistance system.
• FIG. 5 is a representative cross-sectional view of a well screen and a flow control system which may be used in the well system of FIG. 1.
• FIG. 6 is a representative cross-sectional view of another example of the flow control system.
• FIG. 7 is a representative perspective view of another example of the flow control system. DETAILED DESCRIPTION
• FIG. 1 Representatively illustrated in FIG. 1 is a well system 10 which can embody principles of this disclosure.
• a wellbore 12 has a generally vertical uncased section 14 extending downwardly from casing 16, as well as a generally horizontal uncased section 18 extending through an earth formation 20.
• a tubular string 22 (such as a production tubing string) is installed in the wellbore 12. Interconnected in the tubular string 22 are multiple well screens 24, variable flow resistance systems 25 and packers 26.
• the packers 26 seal off an annulus 28 formed radially between the tubular string 22 and the wellbore section 18. In this manner, fluids 30 may be produced from multiple intervals or zones of the formation 20 via isolated portions of the annulus 28 between adjacent pairs of the packers 26.
• a well screen 24 and a variable flow resistance system 25 are interconnected in the tubular string 22.
• the well screen 24 filters the fluids 30 flowing into the tubular string 22 from the annulus 28.
• the variable flow resistance system 25 variably restricts flow of the fluids 30 into the tubular string 22, based on certain characteristics of the fluids .
• the wellbore 12 it is not necessary in keeping with the principles of this disclosure for the wellbore 12 to include a generally vertical wellbore section 14 or a generally horizontal wellbore section 18. It is not necessary for fluids 30 to be only produced from the formation 20 since, in other examples, fluids could be injected into a
• fluids could be both injected into and produced from a formation, etc.
• variable flow resistance system 25 It is not necessary for one each of the well screen 24 and variable flow resistance system 25 to be positioned between each adjacent pair of the packers 26. It is not necessary for a single variable flow resistance system 25 to be used in conjunction with a single well screen 24. Any number, arrangement and/or combination of these components may be used.
• variable flow resistance system 25 it is not necessary for any variable flow resistance system 25 to be used with a well screen 24.
• the injected fluid could be flowed through a variable flow resistance system 25, without also flowing through a well screen 24.
• tubular string 22 components of the tubular string 22 to be positioned in uncased sections 14, 18 of the wellbore 12. Any section of the wellbore 12 may be cased or uncased, and any portion of the tubular string 22 may be positioned in an uncased or cased section of the wellbore, in keeping with the
• variable flow resistance systems 25 can provide these benefits by increasing resistance to flow if a fluid velocity increases beyond a selected level (e.g., to thereby balance flow among zones, prevent water or gas coning, etc.), and/or increasing resistance to flow if a fluid viscosity decreases below a selected level (e.g., to thereby restrict flow of an
• undesired fluid such as water or gas, in an oil producing well
• Whether a fluid is a desired or an undesired fluid depends on the purpose of the production or injection operation being conducted. For example, if it is desired to produce oil from a well, but not to produce water or gas, then oil is a desired fluid and water and gas are undesired fluids. If it is desired to produce gas from a well, but not to produce water or oil, the gas is a desired fluid, and water and oil are undesired fluids. If it is desired to inject steam into a formation, but not to inject water, then steam is a desired fluid and water is an undesired fluid.
• a fluid composition 36 (which can include one or more fluids, such as oil and water, liquid water and steam, oil and gas, gas and water, oil, water and gas, etc.) flows into the well screen 24, is thereby filtered, and then flows into an inlet 38 of the variable flow resistance system 25.
• a fluid composition can include one or more undesired or desired fluids. Both steam and water can be combined in a fluid composition. As another example, oil, water and/or gas can be combined in a fluid composition.
• Flow of the fluid composition 36 through the variable flow resistance system 25 is resisted based on one or more characteristics (such as viscosity, velocity, etc.) of the fluid composition.
• the fluid composition 36 is then
• variable flow resistance system 25 discharged from the variable flow resistance system 25 to an interior of the tubular string 22 via an outlet 40.
• the well screen 24 may not be used in conjunction with the variable flow resistance system 25 (e.g., in injection operations), the fluid composition 36 could flow in an opposite direction through the various elements of the well system 10 (e.g., in injection
• variable flow resistance system could be used in conjunction with multiple well screens, multiple variable flow resistance systems could be used with one or more well screens, the fluid composition could be received from or discharged into regions of a well other than an annulus or a tubular string, the fluid composition could flow through the variable flow resistance system prior to flowing through the well screen, any other components could be interconnected upstream or downstream of the well screen and/or variable flow resistance system, etc.
• well screen 24 depicted in FIG. 2 is of the type known to those skilled in the art as a wire-wrapped well screen, any other types or combinations of well screens (such as sintered, expanded, pre-packed, wire mesh, etc.) may be used in other examples. Additional components (such as shrouds, shunt tubes, lines, instrumentation, sensors, inflow control devices, etc.) may also be used, if desired.
• variable flow resistance system 25 is depicted in simplified form in FIG. 2, but in a preferred example the system can include various passages and devices for
• system 25 preferably at least partially extends circumferentially about the tubular string 22, and/or the system may be formed in a wall of a tubular structure interconnected as part of the tubular string.
• system 25 may not extend
• the system 25 could be formed in a flat structure, etc.
• the system 25 could be in a separate housing that is attached to the tubular string 22, or it could be oriented so that the axis of the outlet 40 is parallel to the axis of the tubular string.
• the system 25 could be on a logging string or attached to a device that is not tubular in shape. Any orientation or configuration of the system 25 may be used in keeping with the principles of this disclosure.
• FIGS. 3A & B a more detailed cross-sectional view of one example of the system 25 is representatively illustrated.
• the system 25 is
• FIGS. 3A & B depicted in FIGS. 3A & B as if it is "unrolled" from its circumferentially extending configuration to a generally planar configuration.
• the fluid composition 36 enters the system 25 via the inlet 38, and exits the system via the outlet 40.
• a resistance to flow of the fluid composition 36 through the system 25 varies based on one or more
• a relatively high velocity and/or low viscosity fluid composition 36 flows through a flow passage 42 from the system inlet 38 to an inlet 44 of a flow chamber 46.
• the flow passage 42 has an abrupt change in direction 48 just upstream of the inlet 44. The abrupt change in
• direction 48 is illustrated as a relatively small radius ninety degree curve in the flow passage 42, but other types of direction changes may be used, if desired.
• the chamber 46 is generally cylindrical-shaped and, prior to the abrupt change in direction 48, the flow passage 42 directs the fluid
• composition 36 to flow generally tangentially relative to the chamber. Because of the relatively high velocity and/or low viscosity of the fluid composition 36, it does not closely follow the abrupt change in direction 48, but instead continues into the chamber 46 via the inlet 44 in a direction which is substantially angled (see angle A in FIG. 3A) relative to a straight direction 50 from the inlet 44 to the outlet 40. The fluid composition 36 will, thus, flow circuitously from the inlet 44 to the outlet 40, eventually spiraling inward to the outlet.
• a relatively low velocity and/or high viscosity fluid composition 36 flows through the flow passage 42 to the chamber inlet 44 in FIG. 3B.
• the fluid composition 36 in this example more closely follows the abrupt change in direction 48 of the flow passage 42 and, therefore, flows through the inlet 44 into the chamber 46 in a direction which is only slightly angled (see angle a in FIG. 3B) relative to the straight direction 50 from the inlet 44 to the outlet 40.
• the fluid composition 36 in this example will, thus, flow much more directly from the inlet 44 to the outlet 40.
• composition 36 also exits the chamber 46 via the outlet 40 in a direction which is only slightly angled relative to the straight direction 50 from the inlet 44 to the outlet 40.
• the fluid composition 36 exits the chamber 46 in a direction which changes based on velocity, viscosity, and/or the ratio of desired fluid to undesired fluid in the fluid composition .
• the much more circuitous flow path taken by the fluid composition 36 in the example of FIG. 3A dissipates more of the fluid composition's energy at the same flow rate and, thus, results in more resistance to flow, as compared to the much more direct flow path taken by the fluid composition in the example of FIG. 3B.
• the variable flow resistance system 25 of FIGS. 3A & B will provide less resistance to flow of the fluid composition 36 when it has an increased ratio of desired to undesired fluid therein, and will provide greater resistance to flow when the fluid composition has a decreased ratio of desired to undesired fluid therein.
• the straight direction 50 from the inlet 44 to the outlet 40 is in a radial direction.
• the flow passage 42 upstream of the abrupt change in direction 48 is directed generally tangential relative to the chamber 46 (i.e., perpendicular to a line extending radially from the center of the chamber) .
• the chamber 46 is not necessarily cylindrical-shaped and the straight direction 50 from the inlet 44 to the outlet 40 is not necessarily in a radial direction, in keeping with the principles of this disclosure.
• the chamber 46 in this example has a cylindrical shape with a central outlet 40, and the fluid composition 36 (at least in FIG. 3A) spirals about the chamber, increasing in velocity as it nears the outlet, driven by a pressure differential from the inlet 44 to the outlet, the chamber may be referred to as a "vortex" chamber.
• FIGS. 4A & B another configuration of the variable flow resistance system 25 is representatively illustrated.
• the configuration of FIGS. 4A & B is similar in many respects to the configuration of FIGS. 3A & B, but differs at least in that the flow passage 42 extends much more in a radial direction relative to the chamber 46 upstream of the abrupt change in direction 48, and the abrupt change in direction influences the fluid composition 36 to flow away from the straight direction 50 from the inlet 44 to the outlet 40.
• a relatively high viscosity and/or low velocity fluid composition 36 is influenced by the abrupt change in direction 48 to flow into the chamber 46 in a direction away from the straight direction 50 (e.g., at a relatively large angle A to the straight direction).
• the fluid composition 36 will flow circuitously about the chamber 46 prior to exiting via the outlet 40.
• a relatively high velocity and/or low viscosity fluid composition 36 flows through the flow passage 42 to the chamber inlet 44 in FIG. 4B.
• the fluid composition 36 in this example does not closely follow the abrupt change in direction 48 of the flow passage 42 and, therefore, flows through the inlet 44 into the chamber 46 in a direction which is angled only slightly relative to the straight direction 50 from the inlet 44 to the outlet 40.
• the fluid composition 36 in this example will, thus, flow much more directly from the inlet 44 to the outlet 40. It will be appreciated that the much more circuitous flow path taken by the fluid composition 36 in the example of FIG.
• variable flow resistance system 25 of FIGS. 4A & B will provide less resistance to flow of the fluid composition 36 when it has an increased ratio of desired to undesired fluid therein, and will provide greater resistance to flow when the fluid composition has a decreased ratio of desired to undesired fluid therein.
• variable flow resistance system 25 a configuration is representatively illustrated in which a flow control system 52 is used with the variable flow resistance system 25.
• the control system 52 includes certain elements of the variable flow resistance system 25 (such as, the flow chamber 46, outlet 40, etc.), along with a closure device 54 and a structure 56, to prevent flow into the tubular string 22 when an unacceptable level of undesired fluid has been flowed through the system.
• the structure 56 supports the closure device 54 away from the outlet 40, until sufficient undesired fluid has been flowed through the chamber 46 to degrade the structure.
• the structure 56 resists a biasing force applied to the closure device 54, with the biasing force biasing the closure device toward the outlet 40.
• the closure device 54 depicted in FIG. 5 has a
• closure device cylindrical shape, and is somewhat larger in diameter than the outlet 40, so that when the closure device is released, it will cover and prevent flow through the outlet.
• closure devices e.g., flappers, etc.
• the closure device 54 may be provided with a seal or sealing surface for sealingly engaging a sealing surface (e.g., a seat) about the outlet 40. Any manner of sealing with the closure device 54 may be used, in keeping with the scope of this disclosure.
• the structure 56 may be made of a material which relatively quickly corrodes when contacted by a particular undesired fluid (for example, the structure could be made of cobalt, which corrodes when in contact with salt water) .
• the structure 56 may be made of a material which relatively quickly erodes when a high velocity fluid impinges on the material (for example, the structure could be made of aluminum, etc.).
• any material may be used for the structure 56 in keeping with the principles of this disclosure.
• the structure 56 can degrade (e.g., erode, corrode, break, dissolve, disintegrate, etc.) more rapidly when the fluid composition 36 flows circuitously through the chamber 46.
• the structure 56 could degrade more rapidly in the relatively high velocity and/or low viscosity situation depicted in FIG. 3A, or in the relatively high viscosity and/or low velocity situation depicted in FIG. 4A.
• the chamber 46 is not necessarily a "vortex" chamber.
• the structure 56 can release the closure device 54 for displacement to its closed position when a particular undesired fluid is flowed through the chamber 46, when an increased ratio of undesired to desired fluids is in the fluid composition 36, etc., whether or not the fluid composition 36 flows circuitously through the chamber.
• the structure 56 encircles the outlet 40, and the fluid composition 36 flows through the structure to the outlet. Openings 58 in the wall of the generally tubular structure 56 are provided for this purpose.
• the fluid composition 36 may not flow through the structure 56, or the fluid composition may flow otherwise through the structure (e.g., via grooves or slots in the structure, the structure could be porous, etc . ) .
• FIG. 6 another example of the flow control device 52 is representatively
• a biasing device 60 biases the closure device 54 toward its closed position.
• the structure 56 is interposed between the closure device 54 and a wall of the chamber 46, thereby preventing the closure device from displacing to its closed position.
• the structure 56 is sufficiently degraded (e.g., in response to a ratio of undesired to desired fluids being sufficiently large, in response to a sufficient volume of undesired fluid being flowed through the system, etc.)
• the structure will no longer be able to resist the biasing force exerted by the biasing device, and the closure device 54 will be permitted to displace to its closed position, thereby preventing flow through the chamber 46.
• the biasing device 60 encircles an upper portion of the closure device 54 .
• the structure 56 prevents the closure device 54 from displacing to its closed position.
• the biasing device 60 exerts a biasing force on the closure device 54 , biasing the closure device toward the closed position, but the biasing force is resisted by the structure 56 , until the structure is sufficiently degraded.
• inlet 44 is used for admitting the fluid composition 36 into the chamber 46
• multiple inlets could be provided, if desired.
• the fluid composition 36 could flow into the chamber 46 via multiple inlets 44 simultaneously or separately.
• different inlets 44 could be used for when the fluid composition 36 has corresponding different characteristics (such as different velocities, viscosities, etc.).
• variable flow resistance system 25 and flow control system 52 have been described above, with each configuration having certain features which are different from the other configurations, it should be clearly understood that those features are not mutually exclusive. Instead, any of the features of any of the configurations of the systems 25 , 52 described above may be used with any of the other configurations.
• the flow control system 52 can operate automatically, without human intervention required, to shut off flow of a fluid composition 36 having relatively low viscosity, high velocity and/or a relatively low ratio of desired to undesired fluid.
• the system 52 can include a flow chamber 46 through which a fluid composition 36 flows, and a closure device 54 which is biased toward a closed position in which the closure device 54 prevents flow through the flow chamber 46 .
• the closure device 54 can be displaced to the closed position in
• a biasing device 60 may bias the closure device 54 toward the closed position.
• the closure device 54 may displace automatically in response to the increase in the ratio of undesired to desired fluid.
• the increase in the ratio of undesired to desired fluid may cause degradation of a structure 56 which resists displacement of the closure device 54 .
• the fluid composition 36 may flow through the structure 56 to an outlet 40 of the flow chamber 46 .
• the structure 56 may encircle an outlet 40 of the flow chamber 46 .
• the increase in the ratio of undesired to desired fluid may cause corrosion, erosion and/or breakage of the
• the closure device 56 when released, can prevent flow to an outlet 40 of the flow chamber 46 .
• the increase in the ratio of undesired to desired fluid in the fluid composition 36 may result from an increase in water or gas in the fluid composition 36.
• the increase in the ratio of undesired to desired fluid in the fluid composition 36 may result in an increase in a velocity of the fluid composition 36 in the flow chamber 46.
• a structure 56 prevents a closure device 54 from being displaced to a closed position in which the closure device 54 prevents flow of a fluid composition 36 through a flow chamber 46, and in which the fluid
• composition 36 flows through the structure 56 to an outlet 40 of the flow chamber 46.

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• Geology (AREA)
• Life Sciences & Earth Sciences (AREA)
• Engineering & Computer Science (AREA)
• Mining & Mineral Resources (AREA)
• Environmental & Geological Engineering (AREA)
• Fluid Mechanics (AREA)
• Physics & Mathematics (AREA)
• General Life Sciences & Earth Sciences (AREA)
• Geochemistry & Mineralogy (AREA)
• Pipe Accessories (AREA)
• Pipeline Systems (AREA)
• Physical Or Chemical Processes And Apparatus (AREA)
• Filling Or Discharging Of Gas Storage Vessels (AREA)
• Sliding Valves (AREA)

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Citations (5)

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• 2011
  • 2011-11-14 SG SG11201401978XA patent/SG11201401978XA/en unknown
  • 2011-11-14 EP EP20110875712 patent/EP2766566A4/en not_active Withdrawn
  • 2011-11-14 CN CN201180074708.6A patent/CN103958826A/zh active Pending
  • 2011-11-14 AU AU2011381084A patent/AU2011381084B2/en not_active Ceased
  • 2011-11-14 MX MX2014005845A patent/MX351169B/es active IP Right Grant
  • 2011-11-14 BR BR112014011410A patent/BR112014011410A2/pt not_active IP Right Cessation
  • 2011-11-14 WO PCT/US2011/060606 patent/WO2013074069A1/en active Application Filing
  • 2011-11-14 CA CA2855371A patent/CA2855371C/en not_active Expired - Fee Related
  • 2011-11-14 RU RU2014124165/03A patent/RU2577347C2/ru not_active IP Right Cessation

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