• 专利附录
  • 专利说明
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    • 专利摘要:
    A system for variably resisting the flow of a fluid composition in an underground well A system for varyingly resisting the flow of a fluid composition may include a flow passageway and a set of one or more rarified passageways that intercept the passageway. flow ratio, whereby a proportion of the fluid composition shifted from the passage to the set of rarified passageways varies based on at least one of: a) viscosity of the fluid composition and b) velocity of the fluid composition in the flow passage. Another variable flow resistance system may include a flow path selection device that selects which of the multiple flow paths through which a majority of fluid flows from the device, based on an unwanted fluid to ratio in the desired fluid composition. fluid. However, another variable flow resistance system may include a flow chamber, with most of the fluid composition entering the chamber in a direction that changes based on a desired fluid to unwanted fluid ratio in the fluid composition.
    公开号:BR112012003672B1
    申请号:R112012003672-6
    申请日:2010-08-04
    公开日:2019-05-28
    发明作者:Jason D. Dykstra；Michael L. Fripp；Syed Hamid
    申请人:Halliburton Energy Services , Inc；
    IPC主号:
    专利说明:

    1/41
    SYSTEM FOR VARIABLE RESISTANCE TO THE FLOW OF A FLUID COMPOSITION IN AN UNDERGROUND WELL [0001] This disclosure generally relates to the equipment used and operations carried out in conjunction with an underground well and, in an example described below, more particularly provides the control of the flow path based on the characteristics of the fluid, thus, to resist variably the flow in an underground well.
    [0002] In a hydrocarbon production well, it is often beneficial to have the ability to regulate the flow of fluids from a land formation into an oil well. A variety of effects can be met by this regulation, including preventing water or gas cone, minimizing sand production, minimizing gas and / or water production, maximizing gas and / or oil production, balance between production areas, etc.
    [0003]
    In an injection well, it is usually desirable to uniformly inject water, steam, gas, etc., into multiple zones, so that the hydrocarbons are displaced uniformly through a formation of earth, without the fluid injected prematurely breaking through a well. production oil. Thus, the ability to regulate the flow of fluids from an oil well in a land formation can also be beneficial for injection wells.
    [0004] Therefore, it will be appreciated that advances in the art of varying fluid flow in a well are desirable in the circumstances mentioned above, and such advances would also be beneficial in a wide variety of other circumstances.
    Summary of the invention
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    2/41 [0005] In the following disclosure, a variable flow resistance system, which brings improvements to the art of regulating the flow of fluids in a well, is provided.
    An example described below, in which a fluid composition flows along a more resistant flow path if the fluid composition has a threshold level (or more than the threshold level) of an undesired characteristic. Another example described in which a resistance to flow through the system increases as the ratio of desired fluid to unwanted fluid in the fluid composition decreases.
    [0006] In one aspect, a system for varying resistance to the flow of a fluid composition in an underground well is provided by the disclosure. The system may include a flow passage and a set of one or more passages that intercept the flow passage. In this way, a proportion of the fluid composition deviated from the flow passage to the set of branched passages varies according to at least one factor among a) viscosity of the fluid composition and, b) the speed of the fluid composition in the flow passage .
    [0007] In another aspect, a system for variablely resisting the flow of a fluid composition in an underground well is described. The system may include a flow path selection device which selects which of the multiple flow paths through which a majority of the fluid flows from the device based on a desired fluid to unwanted fluid ratio in the fluid composition.
    [0008] In yet another aspect, a system for variablely resisting the flow of a fluid composition can
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    3/41 include a flow chamber. Most of the fluid composition enters the chamber in a direction that changes based on the ratio of desired fluid to unwanted fluid in the fluid composition.
    [0009] Still in an additional aspect, the present disclosure provides a system for resisting the flow of a fluid composition in an underground well in a variable way. The system can include a flow chamber, and a majority of the fluid composition can enter the chamber in a direction that changes based on a speed of the fluid composition.
    [0010] In an even further aspect, a variable flow resistance system for use in an underground well may include a flow chamber having an outlet, and at least first and second inlets. A fluid composition entering the flow chamber through the second inlet may oppose the flow of the fluid composition entering the flow chamber through the first inlet, in which a resistance to the flow of the fluid composition through the flow chamber may vary according to a flow rate through the first and second entries.
    [0011] These and other characteristics, advantages and benefits will become apparent to a person skilled in the art upon careful consideration of the detailed description of the representative examples below and the accompanying drawings, in which similar elements are indicated in the various figures using the same numbers of reference. Brief description of the drawings [0012] Figure 1 is a schematic partial cross-sectional view of a well system that can incorporate the
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    4/41 principles of this disclosure;
    [0013] Figure 2 is a schematic cross-sectional view on an enlarged scale of a well screen and a variable flow resistance system that can be used in the well system of figure 1;
    [0014] Figure 3 is a schematic plan view taken from a configuration of the variable flow resistance system taken along line 3-3 of figure 2;
    [0015] Figure 4 is a schematic plan view of another configuration of the variable flow resistance system;
    [0016] Figure 5 is a schematic plan view on an enlarged scale of a portion of the variable flow resistance system of Figure 4;
    [0017] Figure 6 is a schematic plan view of another configuration of the variable flow resistance system;
    [0018] Figures 7A and B are schematic plan views of an additional configuration of the variable flow resistance system; and [0019] Figures 8A and B are schematic plan views of another configuration of the variable flow resistance system.
    Detailed description of the invention [0020] Representatively illustrated in figure 1 is a well system 10, which can incorporate the principles of the present disclosure. As shown in figure 1, an oil well 12 has a generally uncoated vertical section 14 extending below the box 16, as well as a generally uncoated horizontal section 18 extending through a land formation 20.
    [0021] A column of piping 22 (such as a column of
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    5/41 production pipe) is installed in oil well 12. Interconnected to pipe column 22 are multiple well screens 24, variable flow resistance systems 25 and packers 26.
    [0022] The packers 26 seal an annular space 28 formed radially between the pipe column 22 and the oil well section 18. In this way, fluids 30 can be produced from multiple intervals or zones of formation through 20 through isolated portions of the annular space 28 between adjacent pairs of packers 26.
    [0023] Positioned between each adjacent pair of packers 26, a well screen 24 and a variable flow resistance system 25 are interconnected in the pipe column 22. The well screen 24 filters the fluids 30 that flow in the pipe column 22 annular space 28. The variable flow resistance system 25 restricts the flow of fluids 30 in the pipe column 22, based on certain fluid characteristics.
    [0024] At this point, it should be noted that the well system 10 is illustrated in the drawings and is described here as a mere example of a wide variety of well systems in which the principles of the present disclosure can be used. It should be made clear that the principles of the present disclosure are not generally limited to any of the details of the well system 10, or its components, represented in the drawings or described in this document.
    [0025] For example, it is not necessary in line with the principles of this disclosure that oil well 12 includes a generally vertical oil well section 14 or a generally horizontal oil well section 18. It is not
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    6/41 it is necessary for fluids 30 to be produced only from formation 20, since, in other examples, fluids can be injected into one formation, fluids can be injected into both and produced from one formation, etc. ..
    [0026] It is not necessary that each of the well screens 24 and the variable flow resistance system 25 be positioned between each adjacent pair of packers 26. It is not necessary that a single variable flow resistance system 25 be used together with a single well screen 24. Any number, arrangement and / or combination of these components can be used.
    [0027] It is not necessary that any variable flow resistance system 25 be used with a well screen 24. For example, in injection operations, the injected fluid can be fluid through a variable flow resistance system 25, without also flow through a well screen 24.
    [0028] It is not necessary for the well screen 24, the variable flow resistance system 25, packers 26 or any other component of the pipe column 22 to be positioned in the uncoated sections 14, 18 of the oil well 12. Any section of the oil well 12 can be coated or uncoated, and any portion of the pipe column 22 can be positioned in an uncoated or coated section of the well, in line with the principles of this disclosure.
    [0029] It should be clearly understood, therefore, that this disclosure describes how to make and use some examples, but the principles of the disclosure are not limited to any details of those examples. Instead, the principles of this
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    7/41 disclosure can be applied to a variety of other examples, using the knowledge gained from this disclosure.
    [0030] It will be appreciated by those skilled in the art that it would be beneficial to have the ability to regulate the flow of fluids 30 in the pipe column 22 of each zone of formation 20, for example, to avoid cone and water 32 or gas cone 34 in training. Other uses for regulating flow in a well include, but are not limited to, balancing the production (or injection) of multiple zones, minimizing the production or injection of unwanted fluids, maximizing the production or injection of desired fluids, etc.
    [0031] Examples of variable flow resistance systems 25 described in more detail below can provide these benefits by increasing flow resistance if a fluid velocity increases beyond a selected level (for example, in order to balance the flow between zones , avoid water or gas cone, etc.), increase in flow resistance if fluid viscosity decreases below a selected level or if fluid density increases above a selected level (for example, to thereby restrict the flow of an unwanted fluid, such as water or gas, into an oil-producing well), and / or increase flow resistance if a fluid's viscosity or density increases above a selected level (for example, to minimize injection water in a steam injection well).
    [0032] Whether a fluid is a desired or unwanted fluid will depend on the purpose of the production or the injection operation to be performed. For example, if you want to produce oil
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    8/41 of a well, but does not produce water or gas, so oil is a desired fluid and water and gas are unwanted fluids. If it is desired to produce gas from a well, but does not produce water or oil, gas is a desired fluid, water and oil are unwanted 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 unwanted fluid in a fluid composition.
    [0033]
    Note that, at temperatures and pressures inside the well, the hydrocarbon gas may actually be completely or partially in the liquid phase. Thus, it should be understood that when the term “gas is used here, the supercritical, liquid and / or gas phases are included in the scope of that term.
    [0034] With reference now further to figure 2, an enlarged cross-sectional view of one of the variable flow resistance systems 25 and a portion of one of the well screens 24 is represented illustrated. In this example, a fluid composition 36 (which may include one or more fluids, such as water and oil, liquid water and steam, oil and gas, gas and water, oil, water and gas, etc.) flows into the well 24, is thus filtered, and then flows to an inlet 38 of the variable flow resistance system 25.
    [0035] A fluid composition can include one or more unwanted or desired fluids. Steam and water can be combined into a fluid composition. As another example, oil, water, and / or gas can be combined into a fluid composition.
    [0036] The flow of fluid composition 36 through the
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    9/41 variable flow resistance system 25 is resisted based on one or more characteristics (such as density, viscosity, speed, etc.) of the fluid composition. The fluid composition 36 is then discharged from the variable flow resistance system 25 into an interior of the pipe column 22 via an outlet 40.
    [0037] In other examples, the well screen 24 cannot be used in conjunction with the variable flow resistance system 25 (for example, in injection operations), fluid composition 36 could flow in an opposite direction through the various elements of the well system 10 (for example, in injection operations), a single 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 or discharged into regions of a well other than an annular space or a pipe column, the fluid composition could flow through the variable flow resistance system before flowing through the screen well, other components could be interconnected upstream or downstream of the well screen and / or variable flow resistance system, etc. and it will be appreciated that the principles of disclosure are not, in general, limited to all the details of the example presented in figure 2 and described here.
    Although the well screen shown in figure 2 is of the type known to those skilled in the art as a coiled wire well screen, any other types or combinations of well screens (such as sintered, expanded, prepackaged, wire mesh, etc.) can be
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    10/41 used in other examples. Additional components (such as reinforcement rings, bypass tubes, lines, instrumentation, sensors, flow control devices, etc.) can also be used, if desired.
    [0039] The variable flow resistance system 25 is represented in a simplified way in figure 2, but in a preferred example, the system can include several passages and devices to perform various functions, as described more fully below. In addition, the system 25 preferably extends at least partially circumferentially around the pipe column 22, or the system can be formed in a wall of an interconnected tubular structure as part of the pipe column.
    [0040] In other examples, the system 25 cannot extend circumferentially around a pipe column or be formed in a wall of a tubular structure. For example, the system 25 can be formed in a flat structure, etc. The system 25 could be in a separate housing that is fixed to the pipe column 22, or it could be oriented so that the axis of the outlet 40 is parallel to the pipe column axis. System 25 could be in a registration column or attached to a device that is not tubular in shape. Any orientation or configuration of the system 25 can be used in accordance with the principles of this disclosure.
    [0041] With reference now to figure 3, a more detailed cross-sectional view of an example of system 25 is represented illustratively. System 25 is represented in figure 3, if it were “unfolded from its configuration that extends
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    11/41 circumferentially for a generally planar configuration. [0042] As described above, fluid composition 36 enters system 25 through inlet 38, and exits the system through outlet 40. Resistance to flow fluid composition 36 through system 25 varies based on one or more characteristics of the fluid composition. The system 25 shown in figure 3 is similar in many respects to that illustrated in figure 23 of previous application no. 12 / 700.685 standard here incorporated by reference above.
    [0043] In the example of figure 3, fluid composition 36 initially flows in multiple flow passages 42, 44, 46, 48. Flow passages 42, 44, 46, 48 direct fluid composition 36 to two flow devices flow path selection 50, 52. Device 50 selects which of the two flow paths 54, 56 most of the flow from passages 44, 46, 48 will enter, and the other device 52 selects which of the two flow paths 58, 60 most of the flow of passages 42, 44, 46, 48 will enter.
    [0044] Flow passage 44 is configured to be more restrictive to the flow of fluids having higher viscosity. The flow of fluids of increased viscosity will be increasingly restricted through the flow passage 44.
    [0045] As used here, the term “viscosity is used to encompass both Newtonian and non-Newtonian rheological behaviors. Related rheological properties include kinematic viscosity, flow resistance, viscoplasticity, surface tension, wetting capacity, etc. For example, a desired fluid may have a desired range of kinematic viscosity, resistance to
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    12/41 flow, viscoplasticity, surface tension, wetting capacity, etc.
    [0046] The flow passage 44 may have a relatively small flow area, the flow passage may require that the fluid flowing through it follow a tortuous path, rough surface or flow preventing structures from being used to provide a increased resistance to high viscosity fluid flow, etc. The fluid of relatively low viscosity, however, can flow through flow passage 44 with relatively low resistance to this flow.
    [0047] A control passage 64 of the flow path selection device 50 receives the fluid that flows through the flow passage 44. A control port 66 at the end of the control passage 64 has a reduced flow area so that way, increase the speed of the fluid that left the control passage.
    [0048] The flow passage 48 is configured to have a resistance to flow that is relatively insensitive to the viscosity of fluids flowing through it, but which can be increasingly resistant to the flow of fluids of greater density, greater or greater speed. The flow of fluids of increased viscosity can be increasingly resisted through flow passage 48, but not to a large extent as the flow of such fluids would be resisted through flow passage 44.
    [0049] In the example shown in figure 3, the fluid flowing through the flow passage 48 must flow through a vortex chamber 62, before being discharged to a control passage 68 of the path selection device
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    13/41 flow 50. Since the chamber 62 in this example has a cylindrical shape with a central outlet, and the fluid composition 36 moves in a spiral around the chamber, increasing the speed as it approaches the outlet, driven by a pressure difference from the inlet to the outlet, the chamber is referred to as a vortex chamber. In other examples, one or more orifices, injectors, nozzles, etc., can be used. [0050] Control passage 68 ends at control port 70. Control port 70 has a reduced flow area in order to increase the speed of the fluid leaving control passage 68.
    [0051] It will be appreciated that, as the viscosity of the fluid composition 36 increases, a greater proportion of the fluid composition will flow through flow passage 48, control passage 68 and control port 70 (due to flow passage 44 resist the flow of fluids with high viscosity more than flow passage 48 and vortex chamber 62). On the other hand, as the viscosity of the fluid composition 36 decreases, a greater proportion of the fluid composition will flow through the flow passage 44, control passage 64 and control port 66.
    [0052] Fluid flowing through the flow passage 46 also flows through a vortex chamber 72, which may be similar to vortex chamber 62 (although vortex chamber 72 in a preferred example offers less resistance to flow through it than the vortex chamber 62), and is discharged into a central passage 74. The vortex chamber 72 is used to “combine resistance to achieve a desired flow balance through the flow passages 44, 46, 48.
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    14/41 [0053] Note that the dimensions and other characteristics of the various components of the system 25 must be properly selected, so that the desired results are achieved. In the example of figure 3, a desired result of the flow path selection device 50 is that the flow of most of the fluid composition 36 which flows through the flow passages 44, 46, 48 is directed in the flow path 54, when the fluid composition has a sufficiently high ratio of desired fluid to undesired fluid therein.
    [0054] In this example, the desired fluid is oil, which has a higher viscosity than water or gas, and so, when a sufficiently high proportion of the fluid composition 36 is oil, the majority (or at least one most) of the fluid composition 36 entering the flow path selection device 50 will be directed to flow to flow path 54, instead of flow path 56. This result is achieved due to the fluid leaving the port control 70 at a higher rate, greater speed and / or a moment greater than the fluid exiting the control port 66, thereby influencing the fluid flowing from passages 64, 68, 74 to flow towards the path of flow 54.
    [0055] If the viscosity of fluid composition 36 is not high enough (and therefore a ratio of desired fluid to unwanted fluid is less than a selected level), most (or at least a major part) of the fluid composition entering the flow path selection device 50 will be directed to flow to flow path 56, instead of flow path 54.
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    15/41
    This will be due to the fluid leaving the control port 66 at a higher rate, greater speed and / or greater kinetics than the fluid leaving the other control port 70, thus influencing the fluid flowing into passages 64, 68, 74 to flow further towards flow path 56.
    [0056] It will be appreciated that, by the appropriate configuration of flow passages 44, 46, 48, control passages 64, 68, control ports 66, 70, vortex chambers 62, 72, etc., the desired fluid ratio for unwanted fluid in the fluid composition 36 in which the device 50, selects flow passage 54 or 56 to flow a majority of fluid from the device can be adjusted to several different levels.
    [0057] Flow paths 54, 56 direct the fluid to the respective control passages 76, 78 of the other flow path selection device 52. Control passages 76, 78 end at the respective control ports 80, 82. A central passage 75 receives the fluid from the flow passage 42.
    [0058] The flow path selection device 52 operates similar to the flow path selection device 50, in that the majority of the fluid flowing into
    the device 52 through the tickets 75, 76, 78 is directed to a of the paths flow 58 , 60, and the selection of the paths of flow depends of a reason in fluid
    discharged from control ports 80, 82. If fluid flows through control port 80 at a higher rate, speed and / or kinetics compared to fluid flowing through control port 82, then most (or at least least a major part) of the fluid composition 36 will be
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    16/41 directed to flow through flow path 60. If fluid flows through control port 82 at a higher rate, speed and / or kinetics compared to fluid flowing through control port 80, then most ( or at least a major part) of the fluid composition 36 will be directed to the flow through the flow path 58.
    [0059] Although two of the flow path selection devices 50, 52 are represented in the example of system 25 in figure 3, it should be appreciated that any number (including one) of the flow path selection devices can be used in concert with the principles of this disclosure. The devices 50, 52 illustrated in figure 3 are of the type known to those skilled in the art such as jet-type fluid ratio amplifiers, but other types of flow path selection devices (e.g., pressure-type fluid ratio amplifiers, switches bistable fluids, proportional fluid ratio amplifiers, etc.) may be used in accordance with the principles of this disclosure.
    [0060] The fluid flowing through the flow path 58 enters a flow chamber 84 through an inlet 86, which directs the fluid to enter the chamber, generally tangentially (for example, the chamber 84 is shaped like a cylinder, and inlet 86 is aligned with a tangent to the circumference of the cylinder). As a result, the fluid will spiral up around chamber 84, until it finally exits through outlet 40, as indicated schematically by arrow 90 in figure 3.
    [0061] The fluid flowing through the flow path 60 enters the flow chamber 84 through an inlet 88,
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    17/41 which directs the fluid to flow more directly towards outlet 40 (for example, in a radial direction, as shown schematically by arrow 92 in figure 3). As will be readily appreciated, much less energy is consumed at the same flow rate when the fluid flows more directly towards outlet 40 compared to when the fluid flows less directly towards outlet.
    [0062] Thus, less resistance to flow is experienced when the composition fluid 36 flows more directly towards outlet 40 and, conversely, greater resistance to flow is experienced when the fluid composition flows less directly towards outlet. Thus, when working upstream of the experienced outlet when most of the composition flows into the chamber from inlet 88, flow path 60.
    [0063]
    A majority of the flow path 60 years when the fluid composition
    40, lower resistance
    to flow is in fluid 36 and through of gone 36 seeps fluid comes out gives
    control port 80 at a higher rate, speed and / or kinetics compared to the fluid that leaves control port 82. More fluid leaves control port 80, when most of the fluid that flows out of passages 64, 68, 74 flows through the flow path 54.
    [0064] A majority of the fluid that flows from the passages 64, 68, 74 flows through the flow path 54, when fluid leaves control port 70 at a higher rate, speed and / or kinetics compared to the fluid that leaves from control port 66. More fluid exits control port 70 when the viscosity of fluid composition 36 is above a selected level.
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    18/41
    [0065] Like this, O flow through of system 25 is n it is us resist gone when The composition flowing of 36 features an bigger viscosity (and a bigger reason in fluid wanted for fluid unwanted at same). O flow through system 25 is
    more resistant when fluid composition 36 has a decreased viscosity.
    [0066] More resistance to flow is experienced when fluid composition 36 flows less directly towards outlet 40 (for example, as indicated by arrow 90). Thus, more resistance to flow is experienced when most of the fluid composition 36 flows into chamber 84 from inlet 86, and through flow path 58.
    [0067] A majority of fluid composition 36 flows through flow path 58 when fluid exits control port 82 at a higher rate, speed and / or kinetics compared to the fluid leaving control port 80. More
    fluid leaves from the door control 82 when The most of fluid what seeps from of passages 64, 68 74 drains through of way of flow 56, instead of through the way
    flow rate 54.
    [0068] A majority of the fluid that flows from passages 64, 68, 74 flows through flow path 56, when fluid leaves control port 66 at a higher rate, speed and / or kinetics compared to the fluid that exits control port 70. More fluid exits control port 66 when a viscosity of fluid composition 36 is below a selected level.
    [0069] As described above, system 25 is configured to offer less resistance to flow when fluid composition 36 has increased viscosity, and greater
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    19/41 resistance to flow when the fluid composition has a decreased viscosity. This is beneficial when you want to drain more than one high viscosity fluid, and less than one low viscosity fluid (for example, in order to produce more oil and less water or gas).
    [0070] If it is desired to drain more of a lower viscosity fluid, and less of a higher viscosity fluid (for example, to produce more gas and less water, or to inject more steam and less water), then the system 25 can be easily reconfigured for this purpose. For example, inlets 86, 88 could conveniently be inverted, so that the fluid flowing through flow path 58 is directed to inlet 88, and the fluid flowing through flow path 60 is directed to inlet 86 .
    [0071] With reference now to Figure 4, another configuration of the variable flow resistance system 25 is represented illustratively. The configuration in figure 4 is similar in some respects to the configuration in figure 3, but differs somewhat in that the vortex chambers 62, 72 are not used for flow passages 46, 48, and the separate flow passage 42 connecting input 38 to the flow path selection device 52 is not used in the configuration of FIG. 4. Instead, flow passage 48 connects inlet 38 to central passage 75 of device 52.
    [0072] A series of branched passages spaced apart 94a-c intersects flow passage 48 and provide fluid communication between flow passage and control passage 68. Chambers 96a-c are provided in the respective
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    20/41 intersections between branched passages 94a-c and flow passage 48.
    [0073] A larger proportion of the fluid composition 36 flowing through the flow passage 48 will be deflected in the branched passages 94a-c as the viscosity of the fluid composition increases, or as the speed of the fluid composition decreases. Therefore, the fluid flows at a higher rate, speed and / or kinetics through the control port 70 of the device 50 (in comparison with the rate, speed and / or kinetics of the fluid flow through the control port 66) as that the viscosity of the fluid composition increases, or as the speed of the fluid composition in the flow passage 48 decreases.
    [0074] Preferably, the system 25 of figure 4 is properly configured so that the flow rate through control ports 66, 70 has a linear or monotonous ratio to a proportion of a desired fluid in the fluid composition 36. For example, if the desired fluid is oil, then the ratio of flow through port 70 to flow through control port 66 may vary according to the percentage of oil in the fluid composition 36.
    [0075] The chambers 96a-c are not strictly necessary, but are provided to improve the effect of viscosity on the diversion of fluid in the branched passages 94a-c. The chambers 96a-c can be considered "turbulence chambers", since they provide a volume in which the fluid composition 36 can act on itself, thus increasing the deviation of the fluid as the viscosity increases. Various different shapes, volumes, surface treatments,
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    21/41 surface topographies, etc. can be used for chambers 96a-c to improve the effect of viscosity on fluid bypass in branched passages 94a-c.
    [0076] Although three of the branched passages 94a-c are represented in figure 4, any number (including one) of branched passages can be used in accordance with the principles of this disclosure. The branched passages 94a-c are linearly spaced on one side of the flow passage 48, as shown in Figure 4, but in other examples they could be spaced radially, helically or spaced apart, and they could be on either side (s) of the flow passage 48, in line with the principles of this disclosure.
    [0077] As is more clearly seen in figure 5, the flow passage 48 preferably increases in width (and therefore in the flow area) at each of the intersections between the branched passages 94a-c and the flow passage. Thus, a width w2 of the flow passage 48 is greater than the width w1 of the flow passage, the width w3 is greater than the width w2 and the width w4 is greater than the width w3. Each width increase is preferably on the side of the flow passage 48 intercepted by the respective branched passages 94a-c.
    [0078] The width of the flow passage 48 increases at each intersection with the branched passages 94a-c, in order to compensate for the flow propagation of the fluid composition through the flow passage 36. Preferably, a jet-like flow of the composition fluid 36 is maintained as it passes through each of the intersections. Thus, the higher velocity and lower viscosity of fluids are less influenced to be diverted to branched passages.
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    22/41
    94a-c.
    [0079] The intersections of branched passages 94a-c with flow passage 48 can be uniformly spaced (as shown in figures 4 and 5) or unevenly spaced. The spacing of the branched passages 94a-c is preferably chosen to maintain the jet-like flow of the fluid composition 36 through the flow passage 48, as it travels through each intersection, as mentioned above.
    [0080] In the configuration of figures 4 and 5, the desired fluid has a higher viscosity in comparison to the unwanted fluid, and thus the various elements of the system 25 (for example, flow passages 44, 48, control passages 64, 68, control ports 66, 70, branched passages 94a-c, chambers 96a-c, etc.) are properly configured so that device 50 directs most (or at least a major part) of the fluid that flows through passages 44 , 46, 48 in the flow path 54, when fluid composition 36 has a sufficiently high viscosity. If the viscosity of the fluid composition 36 is not high enough, then the device 50 directs most (or at least a major part) of the fluid to the flow path 56.
    [0081] If the majority of the fluid was directed to the flow path 54 (i.e., if the fluid composition 36 has a sufficiently high viscosity), device 52 will direct the majority of the fluid composition to flow into the flow path. flow 60. Thus, a substantial majority of the fluid composition 36 will flow to chamber 84 through inlet 88, and follow a path
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    Relatively straightforward, less resistant to outflow 40.
    [0082]
    If a majority of the fluid was directed by the device 50 to the flow path 56 (i.e., if the fluid composition has a viscosity
    relatively low), O device 52 go direct The most of the composition of fluid flowing for the way in flow 58. Thus, a substantial majority gives composition in
    fluid 36 will flow into chamber 84 through inlet 86, and
    it will follow a relatively tortuous route, more resistant to exit 40.
    [0083]
    It will therefore be appreciated that the system 25 of figures 4 and 5 increases the flow resistance of fluid compositions with relatively low viscosity and decreases the flow resistance of fluid compositions with relatively high viscosity. The level of viscosity at which the resistance to flow through the system 25 increases or decreases above or below certain levels can be determined by suitably configuring the various elements of the system.
    [0084] Likewise, if the fluid flowing through the flow passage 48 has a relatively low velocity, proportionally more of the fluid will be diverted to the flow passage and in the branched passages 94a-c, resulting in a higher fluid ratio flowing through control port 70 to the fluid flowing through control port 66. As a result, most (or at least a major part) of the fluid composition will flow through inlet 88 to chamber 84, and the composition fluid flow will follow a relatively direct, less resistant path to outlet 40.
    Petition 870190008860, of 01/28/2019, p. 29/59
    24/41 [0085] On the other hand, if the fluid flowing through the flow passage 48 has a relatively high velocity, proportionally less of the fluid will be diverted from the flow passage and in the branched passages 94a-c, resulting in a decreased ratio from the fluid flowing through the control port 70 to the fluid flowing through the control port 66.
    As a result, most (or at least a major part) of the fluid composition 36 will flow through inlet 86 to chamber 84 and the fluid composition will follow a relatively tortuous, more resistant path to outlet 40.
    [0086] It will therefore be appreciated that the system 25 of figures 4 and 5 increases the resistance to the flow of fluid compositions with relatively high speed, and decreases the resistance to the flow of fluid compositions with relatively low speed. The level of speed at which resistance to flow through the system 25 increases or decreases above or below a certain level can be determined by appropriately configuring the various elements of the system. [0087] In a preferred example of system 25, the flow of a fluid of relatively low viscosity (such as fluid composition 36 having a high proportion of gas in it) is resisted by the system, no matter its speed (above a minimum speed limit). However, the flow of a relatively high viscosity fluid (such as fluid composition 36 with a high proportion of oil in it) is resisted by the system only when the speed is above a selected level. Again, these characteristics of system 25 can be determined by properly configuring the various
    Petition 870190008860, of 01/28/2019, p. 30/59
    25/41 elements of the system.
    With reference now further to Figure 6, another configuration of the system 25 is represented illustratively. The configuration of figure 6 is similar in many ways to the configuration of figures and 5, but differs somewhat in that the fluid from both flow passages
    44, is communicated to the central passage 75 of the device
    52, and a separate series of branched passages spaced 98a-c intersects flow passage 44, with chambers 100 a-c at intersections. Any number (including one), spacing, size, configuration, etc., of the branched passages 98 a-c and chambers 100 a-c may be used in accordance with the principles of this disclosure.
    Similar to the branched passages 94 ac and chambers 96 ac described above, the branched passages 98ac and chambers 100 ac function to proportionally divert more fluid from the flow passage 44 (and to the central passage 75 of the device 52) in that the viscosity of the fluid velocity composition 36 increases, or as the fluid composition decreases in the flow passage. Therefore, proportionally less fluid is released to the control port 66, as the viscosity of the fluid composition 36 increases, or as the speed of the fluid composition decreases in the flow passage 44.
    [0090] As more fluid is released to the control port 70, as the viscosity of the fluid composition 36 increases, or as the speed of the fluid composition decreases in flow passage 48 (as described above regarding the configuration of
    Petition 870190008860, of 01/28/2019, p. 31/59
    26/41 figures 4 and 5), the ratio of fluid flow through control port 70 to fluid flow through control port 66 increases substantially more when the viscosity of fluid composition 36 increases, or when the speed of fluid composition decreases in the configuration of figure 6, compared to the configuration of figures 4 and 5. [0091] On the other hand, the ratio of fluid flow through the control port 70 to fluid flow through the control port 66 decreases substantially more when the viscosity of the fluid composition 36 decreases, or when the speed of the fluid composition increases in the configuration of figure 6, compared to the configuration of figures 4 and 5. Thus, the system 25 of figure 6 is more responsive changes in viscosity or speed of fluid composition 36, compared to the system of figures 4 and 5.
    [0092] Another difference in the configuration of figure 6 is that chambers 96 ac and chambers 100 ac gradually decrease in volume downstream along the respective flow passages 48, 44. Thus, chamber 96b has a smaller volume than that of chamber 96a, and chamber 96c has a smaller volume than that of chamber 96b. Likewise, chamber 100b has a smaller volume than chamber 100a, and chamber 100c has a lower volume than chamber 100b.
    [0093] Changes in volume of chambers 96a-c and 100a-c can help compensate for changes in flow rate, speed, etc. of fluid composition 36 through respective passages 48, 44. For example, at each successive intersection between branched passages 94a-c and flow passage 48, the velocity of the fluid through the passage of
    Petition 870190008860, of 01/28/2019, p. 32/59
    The flow 48 will decrease, and the volume of the respective one of the chambers 96a-c decreases accordingly. Likewise, at each successive intersection between the branched passages 98a-c and the flow passage 44, the velocity of the fluid through the flow passage 44 will decrease, and the volume of the respective one of the chambers 100 a-c decreases accordingly.
    [0094] An advantage of the configurations in figures 4-6 around the configuration in figure 3 is that all
    flow, paths in flow, passages control, tickets branched, etc . in the settings figures 4-6 are of preferably, in a single plan (such as visa we
    drawings). Of course, when system 25 extends circumferentially over, or in, a tubular structure, passages, flow paths, etc. they should preferably be at the same radial distance, or around the tubular structure. This makes the system 25 less difficult and expensive to build.
    [0095] With reference now to figures 7A & B, another configuration of the variable flow resistance system 25 is represented illustratively. The system 25 of figures 7A & B is much less complex when compared to the systems of figures 3-5, at least in part because it does not include flow path selection devices 50, 52.
    [0096] The flow chamber 84 of figures 7A & B is also slightly different, in that the two inlets 116, 110 of the chamber are provided with the flow of fluid composition 36 through the two flow passages 110, 112, which direct the fluid composition to flow in opposite directions with respect to outlet 40. As
    Petition 870190008860, of 01/28/2019, p. 33/59
    28/41 was shown in figures 7A & B, the fluid entering the chamber 84 through inlet 116 is directed to flow clockwise in relation to outlet 40, and the fluid entering the chamber through inlet 110 is directed to flow counterclockwise from the exit.
    [0097] In figure 7A, system 25 is represented in a situation where an increase in speed and / or a reduction in viscosity of the fluid composition 36 results in the majority of the fluid composition flowing to chamber 84 through inlet 116. A fluid composition 36, thus it spirals around outlet 40 in chamber 84, and resistance to flow through system 25 increases. The reduced viscosity could result from a relatively low ratio of desired fluid to unwanted fluid in the fluid composition 36.
    [0098] Relatively little gives composition in fluid 36 seep to the camera 84 through gives entry 110 at figure 7A, why the passing in flow 114 it's on at tickets
    branched 102-c that branch from the flow passage 112 of the swirl chambers 104-c. At relatively high speeds and / or low viscosity, the fluid composition 36 tends to flow past the swirl chambers 104c, without a substantial amount of the fluid composition flowing through the swirl chambers and branched passages 102-c for the passage of flow 114.
    [0099] In figure 7B, the speed of the fluid composition 36 has decreased and / or the viscosity of the fluid composition has increased, and as a result, proportionally more of the fluid composition seeps from passage 112 in branched passages 102 bc and through passage 114 for entry
    Petition 870190008860, of 01/28/2019, p. 34/59
    29/41
    110. Since the flows in chamber 84 of the two inlets 116, 110 are in opposite directions, they oppose each other, resulting in a rupture of vortex 90 in the chamber.
    [0100] As shown in figure 7B, fluid composition 36 flows less spiral around outlet 40, and more directly to outlet, thereby reducing resistance to flow through system 25. Thus, resistance to flow through system 25 is decreased when the speed of the fluid composition 36 decreases, when the viscosity of the fluid composition increases, or when a desired fluid to unwanted fluid ratio in the fluid composition increases.
    [0101] With reference now also to Figures 8A & B, another configuration of the variable flow resistance system 25 is represented illustrated. The system 25 of figures 8A and B is similar in many respects to the system of figures 7A & B, but differs at least in that the branched passages 102 ac and swirl chambers 104 ac are not necessarily used in the configuration of figures 8A and B. Instead, flow passage 114 branches from flow passage 112.
    [0102] Another difference is that the circular flow that induces structures 106 is used in chamber 84, the configuration of figures 8A & B. Structures 106 work to maintain the circular flow of fluid composition 36 around outlet 40, or at least prevent flow into the fluid composition towards the outlet, when the fluid composition flows circularly around the outlet. Openings 108 in structures 106 allow fluid composition 36
    Petition 870190008860, of 01/28/2019, p. 35/59
    30/41 eventually flow into outlet 40.
    [0103] Frames 106 are an example of how the configuration of system 25 can be changed to produce a desired flow resistance (for example, when fluid composition 36 has a predetermined viscosity, speed, density, desired fluid ratio for unwanted in it, etc.). The way in which flow passage 114 is branched from flow passage 112 is yet another example of how the configuration of system 25 can be changed to produce a desired flow resistance.
    [0104] In figure 8A, system 25 is represented in a situation where an increase in speed and / or a reduction in viscosity of the fluid composition 36 results in the majority of the fluid composition flowing into chamber 84 through inlet 116. A fluid composition 36 thus spirals around outlet 40 in chamber 84, and resistance to flow through system 25 increases. The reduced viscosity may be due to a relatively low ratio of desired fluid to unwanted fluid in the fluid composition 36.
    [0105] Relatively little of the fluid composition 36 flows into chamber 84 through inlet 110 in figure 8A, because flow passage 114 is branched from flow passage 112 such that most of the fluid composition remains in the flow passage 112. At relatively high speeds and / or low viscosities, fluid composition 36 tends to flow after flow passage 114.
    [0106] In figure 8B, the speed of the fluid composition 36 has decreased and / or the viscosity of the fluid composition
    Petition 870190008860, of 01/28/2019, p. 36/59
    31/41
    increased, and how result, proportionally more gives composition in fluid seeps at passage 112 and through gives passage 114 for input 110. Increased viscosity gives composition in fluid 36 can to be due to an increased ratio
    of desired fluid to unwanted fluids in the fluid composition.
    [0107] Since flows in chamber 84 of two inlets 116, 110 are oppositely directed (or at least the flow of the fluid composition through inlet 110 is opposed to the flow through inlet 116), oppose each other, resulting in a rupture of the vortex 90 in the chamber. Thus, the fluid composition 36 flows more directly to an outlet 40 and a resistance to flow through the system 25 is decreased.
    [0108] Note that any of the characteristics of any of the system configurations 25 described above can be included in any of the other system configurations and, therefore, it should be understood that these characteristics are not exclusive to any special system configuration. System 25 can be used in any type of well system (for example, not only in well system 10), and for carrying out various purposes in various well operations including, but not limited to, injection,
    stimulation, completion, production, conformity, The drilling operations, etc. [0109] Now it can be fully appreciated that The The above disclosure provides substantial advances to the art in
    control the flow of fluids in a well. Fluid flow can be variably resisted based on several characteristics (eg viscosity, density,
    Petition 870190008860, of 01/28/2019, p. 37/59
    32/41 speed, etc.) of a fluid composition that flows through a variable flow resistance system.
    [0110] In particular, the above disclosure provides the art with a system 25 for variablely resisting the flow of a fluid composition 36 in an underground well. System 25 may include a first flow passage 48, 112 and a first set of one or more branched passages 94a-c, 100, 102 ac that intersect the first flow passage 48, 112. In this way, a proportion of the composition of fluid 36 diverted from the first flow passage 48, 112 to the first set of branched passages 94a-c, 100, 102 ac varies based on at least one factor among: a) fluid composition viscosity 36, and b) composition speed of fluid 36 in the first flow passage 48, 98.
    [0111] The proportion of fluid composition 36 shifted from the first flow passage 48, 112 to the first set of branched passages 94a-c, 100, 102 a-c preferably increases in response to the increased viscosity of the fluid composition 36.
    [0112] The proportion of fluid composition 36 shifted from the first flow passage 48, 112 to the first set of branched passages 94a-c, 100, 102 ac, preferably increases in response to the decreased velocity of the fluid composition 36 in the first flow passage 48, 112.
    [0113] The first set of branched passages 94a-c can direct fluid composition 36 to a first control pass 68 of a flow path selection device 50. The flow path selection device 50 can select which of multiple flow paths
    Petition 870190008860, of 01/28/2019, p. 38/59
    33/41
    54, 56 through which the majority of the fluid flows from the device 50 based at least partially on the proportion of the fluid composition 36 diverted to the first passage of the control 68.
    [0114] System 25 may include a second flow passage 44 with a second set of one or more branched passages 98a-c, which intersect the second flow passage 44. In this configuration, a proportion of the fluid composition 36 deviated from the second flow passage 44 for the second set of branched passages 98a-c preferably increases with increasing viscosity of the fluid composition 36, and increases with decreasing the speed of the fluid composition 36 in the second flow passage 44.
    [0115] The second flow passage 44 can direct the fluid composition 36 to a second control passage 64 of the flow path selection device 50. The flow path selection device 50 can select which of the multiple flow paths 54, 56 through which the majority of fluid flows from device 50, based on a fluid composition flow rate ratio 36 through the first and second control passages 64, 68. The ratio of flow rates through first and second control passages 64, 68 preferably vary with respect to a ratio of desired fluid to unwanted fluid in the fluid composition 36.
    [0116] The first set of branched passages 94a-c, 100, 102-c can include multiple branched passages spaced along the first flow passage 48, 112. Chamber 96a-c, 104-c can be provided in each of
    Petition 870190008860, of 01/28/2019, p. 39/59
    34/41 multiple intersections between the first flow passage 48, 112 and the branched passages 94a-c, 102-c.
    [0117] Each of the chambers 96a-c, 104 ac has a fluid volume, and the volumes can decrease in one flow direction of the fluid composition 36 through the first flow passage 48, 112. The flow area of the first flow passage 48, 112 can increase at each of the multiple intersections between the first flow passage 48, 112 and the first set of branched passages 94a-c, 102a-c.
    [0118] Also described above is a system 25 for variable resistance to the flow of a fluid composition 36 in an underground well, with system 25 including a flow path selection device 50 that selects in which of the multiple flow paths 54, 56 through which the majority of the fluid flows from the device based on a ratio of desired fluid to undesired fluid in the fluid composition 36.
    [0119] The flow path selection device 50 may include a first control port 70. The flow rate of fluid composition 36 through the first control port 70 simulates in which of the multiple flow paths through which the Most of the fluid flows from the device 50. The flow rate of the fluid composition 36, through the first control port 70, preferably varies based on the ratio of desired fluid to unwanted fluid in the fluid composition 36.
    [0120] The flow path selection device 50 can also include a second control port 66. The flow path selection device 50 can select
    Petition 870190008860, of 01/28/2019, p. 40/59
    35/41 which of the multiple flow paths 54, 56 through which the majority of the fluid flows from the device 50, based on a ratio of: a) flow rate of the fluid composition 36 through the first control port 70 to b ) a flow rate of fluid composition 36 through the second control port 66. The ratio of flow rates through the first and second control ports 70, 66 preferably varies with respect to the desired fluid to fluid ratio unwanted in the fluid composition 36.
    [0121] Fluid composition 36 can flow to the first control port 70 at least through a control passage 68, which connects to a flow passage 48 through which the fluid composition 36 flows. The flow rate of fluid composition 36 from flow passage 48 to control passage 68 can vary based on the ratio of desired fluid to unwanted fluid in the fluid composition
    36. A proportion of the fluid composition 36 flowing from the flow passage to the control passage can increase when the viscosity of the fluid composition increases and / or decrease when the speed of the fluid composition 36 in the flow passage increases.
    The flow path selection device may include a second control port 66.
    A flow rate of the fluid composition 36 through the second control port simulates which of the multiple flow paths 54, 56 through which the majority of the fluid flows from the device 50.
    Fluid composition 36 flows from control port 66 through at least the second
    Petition 870190008860, of 01/28/2019, p. 41/59
    36/41 control 64 through which the fluid composition 36 flows. Control passage 64 connects to at least one flow passage 44, and a flow rate of fluid composition 36 from flow passage 44 to control passage 64 can vary based on the desired fluid to unwanted fluid ratio in the fluid composition 36.
    [0124] A proportion of the fluid composition 36 flowing from the flow passage 44 to the control passage 64 may decrease when the viscosity of the fluid composition 36 increases and / or increases when a speed of the fluid composition 36 in the flow passage of 44 increases.
    [0125] The above disclosure also provides the art of a system 25 for variablely resisting the flow of a fluid composition 36 in an underground well, with system 25, including a flow chamber 84. Most of the fluid composition 36 enters chamber 84 in a direction that changes based on a ratio of desired fluid to unwanted fluid in the fluid composition 36.
    [0126] Fluid composition 36 can more directly flow through chamber 84 to an outlet 40 of chamber 84, in response to an increase in the ratio of desired fluid to unwanted fluid in the fluid composition 36.
    [0127] The majority of fluid composition 36 enters chamber 84 through one of multiple inlets 86, 88. The one of multiple inlets 86, 88, which most fluid composition 36 enters is selected based on the fluid ratio desired for unwanted fluid in the fluid composition 36.
    [0128] The first inlet 88 directs fluid composition 36 to flow more directly towards an outlet 40 of chamber 84 compared to a second inlet 86. The
    Petition 870190008860, of 01/28/2019, p. 42/59
    37/41 first inlet 88 can direct fluid composition 36 to flow more radially with respect to outlet 40 compared to second inlet 86. Second inlet 86 can direct fluid composition 36 to spiral more around the outlet 40 compared to the first entry 88.
    [0129] Chamber 84 can generally be cylindrical in shape, and fluid composition 36 may spiral further into chamber 84 as the ratio of desired fluid to unwanted fluid in the fluid composition 36 decreases.
    [0130] System 25 preferably includes a flow path selection device 50 that selects which of the multiple flow paths 54, 56 through which most of the fluid flows from the device, based on the desired fluid ratio for unwanted fluid in the fluid composition 36.
    [0131] The flow path selection device 50 includes a first control port 70. The flow rate of the fluid composition 36 through the first control port 70 simulates in which of the multiple flow paths 54, 56 through which most of the fluid seeps out of the device. The flow rate of the fluid composition 36 through the first control port 70 varies based on the ratio of desired fluid to unwanted fluid in the fluid composition 36.
    [0132] The flow path selection device 50 may also include a second control port 66. The ratio of a) the flow rate of the fluid composition 36 through the first control port 70 to b) a flow rate of fluid composition 36 through second control port 66, simulates which of the multiple paths
    Petition 870190008860, of 01/28/2019, p. 43/59
    38/41 flow rate through which most of the fluid flows from the device. The relationship between flow rates through the first and second control ports 70, 66 preferably varies with respect to the ratio of desired fluid to unwanted fluid in the fluid composition 36.
    [0133] Fluid composition 36 can flow to the first control port 70 at least through a control passage 68, which connects to a flow passage 48 through which fluid composition 36 flows. The flow rate of the fluid composition 36 from the flow passage 48 to the control passage 68 can vary based on the ratio of desired fluid to undesired fluid in the fluid composition 36.
    [0134] The flow path selection device 50 may include a second control port 66. The flow rate of the fluid composition 36 through the second control port 66 simulates which of the multiple flow paths 54, 56 through which most of the fluid flows from the device 50. The fluid composition 36 flows to the second control port 66 through at least one control passage 64 through which the fluid composition 36 flows.
    [0135] Control passage 64 connects to at least one flow passage 44. The flow rate of fluid composition 36 from flow passage 44 to control passage 64 varies based on the desired fluid-to-fluid ratio unwanted in the fluid composition 36.
    [0136] Also described above is the system 25 for variablely resisting the flow of a fluid composition 36 in an underground well, with the system 25 including a
    Petition 870190008860, of 01/28/2019, p. 44/59
    39/41 flow 84. Most of the fluid composition 36 enters the
    chamber 84 in a direction that changes with base in an velocity fluid composition 36. [0137] The fluid composition 36 can more directly drain through camera 84 for an output 40 gives chamber 84,
    in response to a slowdown.
    [0138] Most of the fluid composition 36 can enter chamber 84 through one of multiple inlets 86, 88. One of multiple inlets 86, 88 is selected based on speed. The first of multiple inlets 88 can direct fluid composition 36 to flow more directly towards an outlet 40 of chamber 84 compared to a second of multiple inlets 86.
    [0139] The first inlet 88 can direct fluid composition 36 to flow more radially with respect to outlet 40 compared to the second inlet 86. Second inlet 86 can direct fluid composition 36 to move more in a spiral. around exit 40 compared to first entry 88.
    [0140] Chamber 84 can generally be cylindrical in shape, and fluid composition 36 can move more in
    spiral inside chamber 84 as the speed increases. [0141] System 25 also can include a device in selection flow path 52 that selects in which From several flow paths 58, 60 most of composition in fluid 36 seeps through the device 52, based at fluid composition speed 36. [0142] The above information also describes a system in
    variable flow resistance 25 for use in an underground well, with the variable flow resistance system
    Petition 870190008860, of 01/28/2019, p. 45/59
    40/41 comprising a flow chamber 84 with an outlet 40, and at least first and second inlets 116, 110. A fluid composition 36 that enters the flow chamber 84 through the second inlet 110 is opposed to fluid composition 36 entering the flow chamber 84 through the first inlet 116, whereby a flow resistance of the fluid composition 36 through the flow chamber 84 varies with a ratio of flows through the first and second inlets 116, 110.
    [0143] A flow resistance of the fluid composition 36 through the flow chamber 84 may decrease as the flow through the first and second inlets 116, 110 becomes more equal. The flow through the first and second inlets 116, 110 may become more equal as a viscosity of fluid composition 36 increases, a speed of fluid composition 36 decreases, a density of fluid composition 36 decreases, and / or a ratio of desired fluid to undesired fluid in the fluid composition 36 increases.
    [0144] A flow resistance of the fluid composition 36 through the flow chamber 84 may increase as the flow through the inlets of the first and second inlets 116, 110 becomes less equal.
    [0145] Fluid composition 36 can flow to the first inlet 116 through a first flow passage 112 which is generally oriented tangentially to the flow chamber 84. Fluid composition 36 can flow to the second inlet 110 through a second flow passage 114 which is generally oriented tangentially to the flow chamber 84, and the second passage 114 may receive the
    Petition 870190008860, of 01/28/2019, p. 46/59
    41/41 fluid composition 36 from a branch of the first flow passage 112.
    [0146] It must be understood that the examples described above can be used in various orientations, such as inclined, inverted, horizontal, vertical, etc., and in various configurations, without departing from the present disclosure principles. The modalities illustrated in the drawings are represented and described only as examples of practical applications of the disclosure principles, which are not limited to any specific details of these modalities.
    [0147] Obviously, a person skilled in the art who, after careful consideration of the above description of representative modalities, will easily appreciate that many modifications, additions, substitutions, deletions and other changes can be made to these specific modalities, and those changes are within the scope of the principles of this disclosure. Thus, the foregoing detailed description should be clearly understood to be given by way of illustrations and examples only, the spirit and scope of the present invention being limited only by the appended claims and their equivalents.
    权利要求:
    Claims (3)
    [1]
    1. System for variable resistance to the flow of a fluid composition in an underground well, the system, comprising:
    - a first flow passage (48, 112); and
    - a first set of one or more branched passages (94a-c, 100, 102a-c) that intersect the first flow passage (48, 112), whereby a proportion of the fluid composition (36) deviated from the first flow passage flow (48, 112) for the first set of branched passages (94a-c, 100, 102a-c) varies based on at least one of:
    a) viscosity of the fluid composition (36), and
    b) speed of the fluid composition (36) in the first flow passage (48, 112), characterized by the fact of having
    - a flow path selection device (50) having a first control passage (68), and
    - a pipe column, the first set of branched passages (94a-c, 100, 102a-c) directing the fluid composition (36) to the first control passage (68) of the flow path selection device (50 ) connected to the multiple flow paths (54, 56), and the flow path selection device (50) selects which of the multiple flow paths (54, 56) a majority of fluid flows through the device (50) , based at least partially on the proportion of the fluid composition (36) diverted to the first control passage (68), and the flow path selection device (50) variablely resisting the fluid composition (36) in at least one direction between an interior of the
    Petition 870190008860, of 01/28/2019, p. 48/59
    [2]
    2/2 piping (22), and an earth formation (20) intersected by the underground well.
    System according to claim 1, characterized in that the proportion increases in response to the increased viscosity of the fluid composition (36).
    [3]
    3.
    System according to claim 1, characterized in that the proportion increases in response to the decreased velocity of the fluid composition (36) in the first flow passage (48,
    System according to claim 1, characterized by the fact that it also comprises a second flow passage and a second set of one or more branched passages (98a-c) that intercept the second flow passage (44), whereby a proportion the fluid composition (36) deviated from the second flow passage (44) to the second set of branched passages (98a-c) increases with the increased viscosity of the fluid composition (36) and increases with the decreased speed of the fluid composition (36) in the second flow passage (44).
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    同族专利:
    公开号 | 公开日
    AU2010284478B2|2013-02-07|
    US8327885B2|2012-12-11|
    US8235128B2|2012-08-07|
    RU2519240C2|2014-06-10|
    CO6430486A2|2012-04-30|
    EP2467569B1|2018-11-21|
    MX2012001982A|2012-04-11|
    EP3473800A3|2019-06-26|
    CA2768208A1|2011-02-24|
    MY155208A|2015-09-30|
    CN102472093B|2015-07-22|
    RU2012110214A|2013-09-27|
    CN105134142B|2018-12-14|
    BR112012003672A2|2016-03-22|
    WO2011022210A3|2011-05-12|
    US20130056217A1|2013-03-07|
    CA2768208C|2014-04-08|
    AU2010284478A1|2012-02-02|
    EP3663511A1|2020-06-10|
    US8479831B2|2013-07-09|
    WO2011022210A2|2011-02-24|
    ECSP12011598A|2012-02-29|
    US20110214876A1|2011-09-08|
    CN102472093A|2012-05-23|
    EP3473800A2|2019-04-24|
    EP2467569A4|2017-07-26|
    CN105134142A|2015-12-09|
    SG178471A1|2012-04-27|
    US20110042091A1|2011-02-24|
    EP2467569A2|2012-06-27|
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    法律状态:
    2018-11-27| B06T| Formal requirements before examination|
    2019-01-15| B06F| Objections, documents and/or translations needed after an examination request according art. 34 industrial property law|
    2019-02-05| B15K| Others concerning applications: alteration of classification|Free format text: AS CLASSIFICACOES ANTERIORES ERAM: E21B 43/12 , E21B 43/08 , E21B 43/16 Ipc: E21B 34/08 (1980.01), E21B 43/12 (1968.09) |
    2019-02-19| B06I| Technical and formal requirements: publication cancelled|Free format text: ANULADA A PUBLICACAO CODIGO 6.6.1 NA RPI NO 2506 DE 15/01/2019 POR TER SIDO INDEVIDA. |
    2019-03-26| B09A| Decision: intention to grant|
    2019-05-28| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 04/08/2010, OBSERVADAS AS CONDICOES LEGAIS. (CO) 20 (VINTE) ANOS CONTADOS A PARTIR DE 04/08/2010, OBSERVADAS AS CONDICOES LEGAIS |
    优先权:
    申请号 | 申请日 | 专利标题
    US54269509A| true| 2009-08-18|2009-08-18|
    US12/542,695|2009-08-18|
    US12/700,685|US9109423B2|2009-08-18|2010-02-04|Apparatus for autonomous downhole fluid selection with pathway dependent resistance system|
    US12/700,685|2010-02-04|
    US12/791,993|2010-06-02|
    US12/791,993|US8235128B2|2009-08-18|2010-06-02|Flow path control based on fluid characteristics to thereby variably resist flow in a subterranean well|
    PCT/US2010/044409|WO2011022210A2|2009-08-18|2010-08-04|Flow path control based on fluid characteristics to thereby variably resist flow in a subterranean well|
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