This application is a 371 U.S. National Phase Application of and claims the benefit of priority to International Application Serial No. PCT/US2013/035433, filed on Apr. 5, 2013 and entitled “Controlling Flow in a Wellbore”, the contents of which are hereby incorporated by reference.
The present disclosure relates to well systems, and more particularly to controlling flow in well systems.
It is often desirable to control fluid flow into the completion string of a well system, for example, to balance inflow of fluids along the length of the well. For instance, some horizontal wells have issues with the heel-toe effect, where gas or water cones in the heel of the well and causes a difference in fluid influx along the length of the well. The differences in fluid influx can lead to premature gas or water break through, significantly reducing the production from the reservoir. Inflow control devices (ICD) can be positioned in the completion string at heel of the well to stimulate inflow at the toe and balance fluid inflow along the length of the well. In another example, different zones of the formation accessed by the well can produce at different rates. ICDs can be placed in the completion string to reduce production from high producing zones, and thus stimulate production from low or non-producing zones. Finally, ICDs can be used in other circumstances to balance or otherwise control fluid inflow.
In one general implementation, a wellbore flow control apparatus includes a plurality of inflow control assemblies engageable with a pipe joint that includes a proximal end engageable with a first downhole tool and a distal end engageable with a second downhole tool; and at least one inflow control device (ICD) mounted in each of the plurality of inflow control assemblies, each of the inflow control devices including an inlet adapted to receive a flow of a wellbore fluid at a flow velocity that is less than a transport velocity of fines in the wellbore fluid, and an outlet adapted to transmit a flow of the wellbore fluid to the pipe joint.
In a first aspect combinable with the general implementation, each of the plurality of inflow control assemblies includes a housing engageable with the pipe joint, the at least one ICD mounted at least partially within the housing.
In a second aspect combinable with any of the previous aspects, the housing is threadingly engageable with one of the proximal or distal ends of the pipe joint.
In a third aspect combinable with any of the previous aspects, at least one of the plurality of inflow control assemblies includes an end inflow control assembly.
In a fourth aspect combinable with any of the previous aspects, the end inflow control assembly includes a wellbore fluid inlet positioned on only one axial surface of the end inflow control assembly.
In a fifth aspect combinable with any of the previous aspects, at least one of the plurality of inflow control assemblies includes a middle inflow control assembly engageable with the pipe joint between the end inflow control assembly and one of the proximal or distal ends of the pipe joint.
In a sixth aspect combinable with any of the previous aspects, the middle inflow control assembly includes wellbore fluid inlets positioned on respective axial surfaces of the middle inflow control assembly.
In a seventh aspect combinable with any of the previous aspects, the middle inflow control assembly includes another wellbore fluid inlet positioned on a radial surface of the middle inflow control assembly.
An eighth aspect combinable with any of the previous aspects further includes a filter that extends between the end inflow control assembly and another end flow control assembly such that a radial gap is defined between an outer surface of the pipe joint and the filter.
In a ninth aspect combinable with any of the previous aspects, the middle inflow control assembly is engageable with the pipe joint in the gap and between the filter and the outer surface of the pipe joint.
In a tenth aspect combinable with any of the previous aspects, the middle inflow control assembly is engageable with the pipe joint and the screen and is positioned in the gap with an outer radial surface of the middle inflow control assembly spaced apart from the outer surface of the pipe joint an equidistant as the filter.
In an eleventh aspect combinable with any of the previous aspects, a porosity of the filter is selected so that fines in the wellbore fluid flow through the filter with the wellbore fluid.
In a twelfth aspect combinable with any of the previous aspects, the filter includes at least one of a wire wrap, a mesh screen, a slotted liner, a perforated shroud, or a prepack screen.
In a thirteenth aspect combinable with any of the previous aspects, the housing includes a filter that extends to enclose at least a portion of the ICD.
In a fourteenth aspect combinable with any of the previous aspects, the filter extends to enclose the plurality of ICDs.
In a fifteenth aspect combinable with any of the previous aspects, the filter includes a plurality of filter sections, each filter section enclosing at least a portion of one of the plurality of ICDs.
A sixteenth aspect combinable with any of the previous aspects further includes a divider positioned in a gap between adjacent filter sections.
In a seventeenth aspect combinable with any of the previous aspects, the divider includes swell rubber.
In an eighteenth aspect combinable with any of the previous aspects, each of the ICDs includes at least one of a nozzle, an orifice, a helix channel, one or more tubulars, or an autonomous ICD.
In another general implementation, a method for controlling flow of a wellbore fluid includes positioning a plurality of inflow control assemblies on a pipe joint in a wellbore, the pipe joint including a proximal end engageable with a first downhole tool and a distal end engageable with a second downhole tool; receiving a flow of a wellbore fluid from a subterranean zone to an inlet of at least one inflow control device (ICD), the at least one ICD mounted in each of the plurality of inflow control assemblies, the flow at a velocity that is less than the transport velocity of fines in the wellbore fluid; and transmitting the flow of the wellbore fluid to the pipe joint from the ICDs to an interior of the pipe joint.
A first aspect combinable with the general implementation further includes receiving the flow of the wellbore fluid at a housing that at least partially encloses the ICD; and distributing the flow of the wellbore fluid through a portion of the housing to the ICD.
In a second aspect combinable with any of the previous aspects, distributing the flow of the wellbore fluid through a portion of the housing to the ICD includes distributing the flow of the wellbore fluid through one or more axially-facing inlets of the housing.
In a third aspect combinable with any of the previous aspects, distributing the flow of the wellbore fluid through a portion of the housing to the ICD further includes distributing the flow of the wellbore fluid through a radially-facing inlet of the housing.
A fourth aspect combinable with any of the previous aspects further includes receiving the flow of the wellbore fluid through a filter that extends at least partially between the proximal and distal ends of the pipe joint and into a radial gap defined between an outer surface of the pipe joint and the filter.
In a fifth aspect combinable with any of the previous aspects, receiving the flow of the wellbore fluid through a filter includes receiving fines in the flow of the wellbore fluid through the filter; and circulating the fines in the flow of the wellbore fluid to the inlet of the at least one ICD.
A sixth aspect combinable with any of the previous aspects further includes receiving the flow of the wellbore fluid through a filter that extends to enclose at least a portion of the ICD.
In a seventh aspect combinable with any of the previous aspects, the filter extends to enclose the plurality of ICDs.
In an eighth aspect combinable with any of the previous aspects, the filter includes a plurality of filter sections, each filter section enclosing at least a portion of one of the plurality of ICDs.
In a ninth aspect combinable with any of the previous aspects, receiving a flow of a wellbore fluid at a velocity that is less than the transport velocity of fines in the wellbore fluid includes restricting a flow rate of the wellbore fluid entering the at least one ICD based on a property of the wellbore fluid; and modifying a velocity of the flow of the wellbore fluid to be less than the transport velocity of fines in the wellbore fluid based on the restriction.
In a tenth aspect combinable with any of the previous aspects, the wellbore fluid includes a hydrocarbon fluid and an aqueous fluid.
In an eleventh aspect combinable with any of the previous aspects, restricting a flow rate of the wellbore fluid entering the at least one ICD based on a property of the wellbore fluid includes restricting a flow rate of the wellbore fluid entering the at least one ICD based on a difference in a property of the hydrocarbon fluid and a property of the aqueous fluid.
In a twelfth aspect combinable with any of the previous aspects, the property includes a viscosity, a velocity, or a density of the wellbore fluid.
In a thirteenth aspect combinable with any of the previous aspects, restricting a flow rate of the wellbore fluid entering the at least one ICD based on a difference in a property of the hydrocarbon fluid and a property of the aqueous fluid includes flowing the hydrocarbon fluid through a first passage of the at least one ICD; flowing the aqueous fluid through a second passage of the at least one ICD that is different than the first passage; and flowing the hydrocarbon fluid and the aqueous fluid together from the first and second passages based at least in part on the difference in the property of the hydrocarbon fluid and the property of the aqueous fluid.
In another general implementation, a wellbore flow control system includes a pipe joint including a tubular that extends between threaded ends; and a plurality of flow control apparatus fixed to the tubular between the threaded ends, each of the flow control apparatus including means for receiving a flow of a wellbore fluid into the flow control apparatus at a flow velocity less than a transport velocity of particulates in the wellbore fluid and transmitting the flow of the wellbore fluid to a volume defined by the tubular.
A first aspect combinable with the general implementation further includes means for filtering the flow of wellbore fluid that encloses at least a portion of the plurality of flow control apparatus.
In a second aspect combinable with any of the previous aspects, the means for filtering includes a specified porosity that includes apertures larger than a majority of the particulates.
In a third aspect combinable with any of the previous aspects, the means for receiving the flow of the wellbore fluid is fluidly coupled to an interior of the tubular that includes the volume.
Various implementations of a system for controlling flow in a wellbore may include none, one, some, or all of the following features. For example, the system for controlling flow in a wellbore may resist (e.g., all or in part) plugging (e.g., by particulates from a subterranean zone) in an unconsolidated geological formation. As another example, production of sands, fines, and other particulates to a terranean surface within a wellbore fluid may be minimized or eliminated. As another example, conventional filtering techniques to reduce or help reduce production of such particulates may be minimized (e.g., by using screens of larger porosity) thereby minimizing installation and/or production costs. As yet another example, “hot spots” of high wellbore fluid flow rates through production equipment may be eliminated or minimized, thereby reducing erosion on such equipment due to production of sand or fines or other particulates in the wellbore fluid. As yet another example, flow rates through production (or injection) equipment may be more uniform (e.g., along a length or lengths of production tubing) as compared to conventional techniques
The details of one or more implementations are set forth in the accompanying drawings and the description below. Other features, objects, and advantages will be apparent from the description and drawings, and from the claims.
According to the present disclosure, a flow control system includes one or more flow control apparatus positioned on a base pipe and in fluid communication with an interior volume of the base pipe. Each flow control apparatus includes one or more ICDs that adjust a flow of a wellbore fluid received at the flow control apparatus from a subterranean zone so that a velocity of the flow of the wellbore fluid provided to the interior volume is less than a transport velocity of sands or fines in the wellbore fluid.
Various implementations of the concepts disclosed herein may be utilized in various orientations and in various configurations. Example orientations include inclined, inverted, horizontal, vertical, and others. The concepts of this patent application are not limited to any of the example implementations disclosed herein.
Directional terms are used to describe the example implementations. Example directional terms include “above,” “below,” “upper,” “lower,” and others. The terms “above,” “upper,” and “upward” may refer to a direction toward the earth's surface along a wellbore. The terms “below,” “lower,” and “downward” may refer to a direction away from the earth's surface along a wellbore.
The packers 18 seal or substantially seal against passage of fluids between a wall of the wellbore 14 and the completion string 12, and thus isolate portions of the wellbore 14 from other portions of the wellbore 14. As illustrated, one or more of the inflow control assemblies 16 may be positioned in an isolated portion of the wellbore 14, for example, between packers 18 set in the wellbore. In addition, or alternatively, many of the inflow control assemblies 16 could be positioned in a long, continuous portion of the wellbore 14, without packers isolating the wellbore between the screens.
Gravel packs could be provided about any or all of the inflow control assemblies 16, if desired. A variety of additional well equipment (such as valves, sensors, pumps, control and actuation devices, etc.) could also be provided in the well system 10.
The well system 10 is merely representative of one well system in which the principles of the present disclosure may be beneficially utilized. However, the invention is not limited in any manner to the details of the well system 10 described herein. For example, the inflow control assemblies 16 could instead be positioned in a cased and perforated portion of a wellbore, the inflow control assemblies 16 could be positioned in a generally vertical portion of a wellbore, the inflow control assemblies 16 could be used in an injection well, rather than in a production well. For example, although shown in the context of a horizontal well system 10, the concepts herein can be applied to other well configurations, including vertical well systems consisting of a vertical or substantial vertical wellbore, multi-lateral well systems having multiple wellbores deviating from a common wellbore and/or other well systems. Also, although described in a production context, concepts herein can are applicable in other contexts, including injection (e.g., with the inflow control assemblies 16 as part of an injection string), well treatment (e.g., with the inflow control assemblies 16 as part of a treatment string) and/or other applications.
In one alternative example, the string 12 can be used to inject stimulating fluids (e.g., acid in an acidizing treatment, steam in a heated fluid injection treatment, and/or other types of stimulating fluid) into a subterranean zone that surrounds the wellbore 14 (e.g., a horizontal portion of the wellbore 14). Thereafter, the string 12 can be used to produce fluids (e.g., hydrocarbons and/or other fluids) from the subterranean zone substantially uniformly, or in some other flow profile, along the length of the production/injection interval. In another example, the string 12 is used for injection of sweeping fluids (e.g., water, brine and/or other fluids) into the subterranean zone substantially uniformly, or in some other flow profile, along the length of the production/injection interval for the purpose of maintaining pressure in the subterranean zone and sweeping the zone's fluids to a specified location in the subterranean zone. The well may be shut-in while the sweeping fluids reside in the subterranean zone. In certain instances, the greater resistance or sealing against inflow into the string 12 can limit cross-flow of fluids from one sub-interval, through the string 12 and out to another sub-interval. Thereafter, the string 12 is used to produce fluids (e.g., hydrocarbons and/or other fluids) from the subterranean zone substantially uniformly, or in some other flow profile, along the length of the production/injection interval.
During the production of fluids from the subterranean zone, each of the illustrated flow control apparatus 16 may receive a wellbore fluid (e.g., a gas or liquid or multiphase hydrocarbon fluid) from the subterranean zone that is produced into the annulus 20. Once received from the annulus 20, the flow control apparatus 16 may transmit the wellbore fluid to an interior of the completion string 12, such as to an interior of a tubular joint, or “pipe joint,” that makes up the completion string 12. In other example embodiments, the flow control apparatus 16 may transmit the wellbore fluid to an interior of a coiled tubing that makes up the completion string 12. Wellbore fluid produced into the completion string 12 may be further produced to the terranean surface.
As described in more detail below, each of the flow control apparatus 16 may include one or more inflow control devices (“ICDs”) that adjust a flow rate and/or flow velocity of the wellbore fluid received into the flow control apparatus 16 from the annulus 20. Examples of ICDs can include, for instance, nozzle type ICDs, orifice-type ICDs, helix channel ICDs, valves, tubings, and autonomous ICDs (e.g., microfluidic or vortex type ICDs). As further examples, ICDs may include flow channels that direct and/or adjust a flow of the wellbore fluid as it is distributed through the flow control apparatus 16. ICDs may include vanes mounted in flow paths that direct and/or adjust a flow of the wellbore fluid as it is distributed through the flow control apparatus 16. ICDs may include posts or other textured surfaces that direct and/or adjust a flow of the wellbore fluid as it is distributed through the flow control apparatus 16.
In example implementations, the ICDs are autonomous ICDs (“AICDs”). AICDs may include an autonomous valve that autonomously (i.e., without human or other interaction) changes between allowing and restricting against flow to the completion string 12 from the annulus 20 in response to a fluid flow characteristic, such as, at least one of fluid flow rate, viscosity or density. For example, an autonomous valve can become more restrictive of fluid flow as the flow rate increases and less restrictive as the flow rate decreases or vice versa. An autonomous valve can become more restrictive of fluid flow as the viscosity fluid increases and less restrictive of viscosity of the fluid decreases or vice versa. An autonomous valve can become more restrictive of fluid flow as the fluid density increases and less restrictive as the fluid density decreases or vice versa. In certain instances, an autonomous valve can automatically be more restrictive to water than oil or vice versa, more restrictive to gas than oil or vice versa, and/or more restrictive to production flow (e.g., flow from the wellbore 14 into the interior of the completion string 12) than to injection flow (e.g., flow from the interior of the completion string 12 into the wellbore 14) or vice versa.
Several examples of autonomous valves that could be used as the autonomous valve are disclosed in U.S. patent Publication Ser. No. 12/700,685, entitled “METHOD AND APPARATUS FOR AUTONOMOUS DOWNHOLE FLUID SELECTION WITH PATHWAY DEPENDENT RESISTANCE SYSTEM,” filed Feb. 4, 2010, the entirety of which is incorporated herein by reference. Still other examples exist. In some examples, autonomous valves (e.g., an AICD) include no moving parts. The autonomous valve includes multiple passages, each having a different resistance to flow in relation to a characteristic of the fluid flow. The passages include fluid diodes that provide resistance to flow based on the density, viscosity, and/or velocity of the fluid they receive. The multiple passages feed into a fluid amplifier and the flows from the passages act on each other to direct the total flow based on the respective momentum of flow from the passages. The amplifier increases the total fluid flow's tendency to flow towards one direction, and thus directs the flow to preferentially enter one or another of multiple outlets. The result is that the resistance to flow through the autonomous valve as a whole depends on the characteristics of the fluid flow, such as its density, viscosity and/or flow rate.
Each flow control apparatus 16 has an exterior housing that, in some cases, is sealed to the completion string 12. Wellbore fluid can be communicated from the annulus 20 to an interior of the housing and to the one or more ICDs.
In some aspects, a transport velocity of fines may be determined based on a terminal settling velocity of the fines (e.g., sand or other particulates) in the wellbore fluid. The terminal velocity of the fines in a fluid at rest is determined according to the weight of the fines, the cross sectional area of the fines, the density of the fluid, and the drag coefficient. For example, the terminal velocity of a particle is determined according to the equation:
where vt is the terminal settling velocity, m is the mass of the particle, Cd is the drag coefficient, A is the cross-sectional area of the particle, and p is the fluid density.
The transport velocity is related to the terminal settling velocity by a factor which can be, in some instances, about 10. Thus, the transport velocity of the particle (e.g., fines, sand, or otherwise) is about 10 times the determined terminal settling velocity. In some aspects, sand transport velocities, for example, can range from between about 0.001 m/s to 10 m/s and more optimally, between about 0.1 m/s and 0.6 m/s. Thus, the ICDs adjust the flow of a wellbore fluid that includes sand so that a velocity of the flow of the wellbore fluid to the interior of the base pipe is below between about 0.1 and 0.6 m/s in some aspects.
As illustrated, the flow control system 200 includes inflow control assemblies 205 that receive a flow of a wellbore fluid 210 from the annulus 20 and transmit the wellbore fluid 217 through conduits 215 to an interior 220 of a base pipe 212. In some aspects, the base pipe 212 is a single pipe joint that is can be coupled (e.g., threadingly) to additional pipe joints on both ends of the base pipe 212 or other downhole tools. For example, in some aspects the base pipe 212 is one of a Range 1 (e.g., between about 16-25 ft.), Range 2 (e.g., between about 25-34 ft.), or Range 3 pipe joint. In the case of a Range 3 pipe joint, the base pipe 212 may be threaded on both ends and be 34-48 ft. or about 40 ft. long.
In the case of the base pipe 212 comprising a single pipe joint, the conduits 215 may be apertures formed in the pipe 212 and, in some cases, multiple apertures from an exterior of the pipe 212 to the interior 220 may be formed around the circumference of the base pipe 212. In other cases, the base pipe 212 may include all or portions of several pipe joints that are coupled together (e.g., threadingly or otherwise). For example, in such implementations, a particular flow control apparatus 205 may act as a coupling between two pipe joints of the base pipe 212 in that the apparatus 205 may be coupled (e.g., threadingly) to an end of two adjacent pipe joints, thereby forming a coupling between the pipe joints. In such aspects, the conduit 215 may simply be a gap between the ends of the pipe joints that form the base pipe 212.
As illustrated in
Turning to
In some example implementations, the flow control system 250 (and other flow control systems described herein) may not include the filter 275. For example, because a flow velocity of the wellbore fluid 210 that enters one or more ICDs in each flow control apparatus 280, 285, and/or 290 is below a transport velocity for fines and/or sand in the fluid 210, a filter may be unnecessary to prevent and/or limit the production of such particles in the wellbore fluid 217 (as well as clogging and other problems). The sand and/or fines would not be transported into the ICDs in such example implementations. In some example aspects, however, the filter 275 may not be configured to prevent and/or limit the passage of sand and/or fines but instead, be configured to, for example, withstand a wellbore collapse or to hold a gravel pack in place to support the wellbore. In some aspects, such a filter 275 may include a screen that uses a relatively larger gauge that, in conventional systems, allows fines and/or sands to pass through. But, in accordance with the present disclosure, the filter 275 may not be exposed to sands and/or fines as the flow velocity through such a filter may be less than the transport velocity of sand and/or fines.
In further implementations, the filter 275 may screen or filter fines and/or sand but in much less of a quantity due to the lower flow velocity of the wellbore fluid 210. The filter 275, therefore, may never or rarely experience plugging or other maintenance issues.
As illustrated, the end housing 270 is mounted on or coupled to the base pipe 255 at, for example, an uphole end and may not, in this example, receive a flow of the wellbore fluid 210. The end housing 270, as shown, may simply provide an end connection for the filter 275. At the other end of the filter 275, the end flow control apparatus 290 provides a second connection for the filter 275 and also receives a flow of the wellbore fluid 210 that is transmitted through an ICD to a conduit 295 and exits out as wellbore fluid 217 to the interior 220 of the base pipe 255. As illustrated, the end flow control apparatus 290 may only receive the wellbore fluid 210 at a axially-facing surface.
Inflow control apparatus 280 and 285 are positioned, in this example, between the end housing 270 and the end flow control apparatus 290. In this example, the flow control apparatus 280 is positioned on the base pipe 255 underneath the filter 275, thereby allowing, in some aspects, the wellbore fluid 210 to flow into axially-facing and radially-facing surfaces of the apparatus 280. Further, in this example, the flow control apparatus 285 is positioned and sized (e.g., a housing of the apparatus) to intersect the filter 275. The flow control apparatus 285, therefore, in this example, may receive the wellbore fluid 210 into axially-facing surfaces of the apparatus 285.
As with the system 200, each of the flow control apparatus of system 250 (e.g., apparatus 280, 285, and/or 290) includes one or more ICDs that receive the wellbore fluid 210 from the annulus and adjust the flow so that the velocity of the flow of the wellbore fluid 210 to the ICDs in the apparatuses 280, 285, and 290 is below (e.g., slightly or significantly) a transport velocity of fines (e.g., sand or other particulates) carried in the wellbore fluid 210. In this example, the combination of the end housing 270, inflow control apparatuses 280, 285, and 290, and base pipe 255 comprise an inflow control assembly 265. In some instances, the filter 275 is also part of the inflow control assembly 265. Further, other implementations of system 250 exist. For example, the system 250 may include more flow control apparatus, may only include one or more flow control apparatus 280 or 285, may include two end flow control apparatus 290, or may include multiple pipe joints (e.g., multiple base pipes 255 coupled through connections 260).
In operation, systems 200 and 250 can each be positioned in the wellbore 14 (e.g., in a horizontal portion, a vertical portion, a leg, or otherwise). Wellbore fluid 210 flows from the wellbore 14 into the annulus (e.g., from an open hole completion, from a perforated casing, or otherwise). The fluid 210 flows into the illustrated flow control apparatus (and in some cases through the filter 275 first) and into one or more ICDs positioned in each flow control apparatus. The wellbore fluid 210 flows into the flow control apparatus at a velocity that is less than or significantly less than the transport velocity of the fines or sand and thus, such particulates are not carried along in the fluid 210. The ICDs in the flow control apparatus regulate the flow of the fluid 210 into the housings. The flow 217 exiting the ICDs (e.g., through the conduits 295 and into the interior 220 of the base pipe 255) is above the transport velocity of the sands or fines. The wellbore fluid 217 that enters the interior 220 of the base pipe 255 can be produced to the surface, largely free from (or with a reduced amount of) sand or fines
In some cases, a particular number or type (e.g., end flow control apparatus 290 and/or flow control apparatus 280 or 285) may be selected based on production criteria. For example, criteria such as desired flow profile, desired flow rate, formation characteristics, and otherwise may determine the number, as well as the type, of flow control apparatus in the inflow control assembly 265.
For example, in this implementation, the filters 310 are depicted as a wire wrapped screen, having a wire helically wrapped around the base pipe 314. The space between adjacent wraps of the wire is closely controlled to be smaller than a specified size of particulate filtered by the filters 310. For example, in some aspects, the filters 310 may be designed to prevent particulates larger than fines or sand from passing through while allowing fines and sands to pass through (thereby decreasing the cost and complexity of the filters 310). Although depicted as a wire wrapped screen, other configurations of screens, including screens having one or more layers of wire wrap, mesh and/or other filtration structures, could be used.
In operation, wellbore fluid 210 passes through the filters 310 radially and enters the flow control apparatus 305 axially, then flows though the radially-facing openings in a housing of the apparatus 305. The fluid 210 enters an ICD 330 at a particular flow rate and flow velocity. The wellbore fluid 310 passes through the ICD 330 (e.g., a nozzle, orifice, helix channel, tubing, AICD, or otherwise) and into the interior 320 of the base pipe 314 to be produced to the surface. In some aspects, the ICD 330 adjusts the velocity and/or rate of the wellbore fluid 210 so that, as the fluid 217 enters the interior 320 of the base pipe 314, the velocity of the fluid 217 is below a transport velocity of sands or fines in the wellbore fluid 210. Alternatively, the flow 210 of the wellbore fluid that enters the ICD 330 is below a transport velocity of sands or fines in the wellbore fluid 210 and the flow 217 into the interior 320 of the base pipe 314 may be above or below the transport velocity of sands or fines in the wellbore fluid 210. In any event, such flow 217 into the interior may be all or largely free of sand and/or fines.
Turning to
In operation, wellbore fluid 210 flows (e.g., from an annulus through a housing of a flow control apparatus) into the ICD 400 and into the flow paths 410. The wellbore fluid 210 enters the ICD 400 at a particular flow rate and velocity that is less than a transport velocity of sands or fines in the fluid 210. Thus, sands and/or fines in the fluid 210 are not transported through the flow to and, in some cases, into, the ICD 400. Based on the flow paths 405 and vanes 410 (alone or in combination), the velocity of the wellbore fluid 210 is reduced in the ICD 400 to a rate less than the transport velocity of sands or fines contained in the fluid 210. Thus, the fluid 210 entering the apertures 415 may be substantially free of, or have a reduced amount of, fines and sands.
Turning to
In operation, wellbore fluid 210 flows (e.g., from an annulus through a housing of a flow control apparatus) into the ICD 420 and into the flow paths 430. The wellbore fluid 210 enters the ICD 420 at a particular flow rate and velocity that is less than a transport velocity of sands or fines in the fluid 210. Thus, sands and/or fines in the fluid 210 are not transported through the flow to and, in some cases, into, the ICD 420. Based on the flow paths 430, the velocity of the wellbore fluid 210 is reduced in the ICD 420 to a rate less than the transport velocity of sands or fines contained in the fluid 210. Thus, the fluid 210 entering the apertures 430 may be substantially free of, or have a reduced amount of, fines and.
Turning to
In operation, wellbore fluid 210 flows (e.g., from an annulus through a housing of a flow control apparatus) into the ICD 450 and onto the flow surfaces onto which the posts 455 are mounted. The wellbore fluid 210 enters the ICD 450 at a particular flow rate and velocity that is less than a transport velocity of sands or fines in the fluid 210. Thus, sands and/or fines in the fluid 210 are not transported through the flow to and, in some cases, into, the ICD 450. Based on the posts 455 that present flow obstructions to the wellbore fluid 210, the velocity of the wellbore fluid 210 is reduced in the ICD 450 to a rate less than the transport velocity of sands or fines contained in the fluid 210. Thus, the fluid 210 entering the apertures 460 may be substantially free of, or have a reduced amount of, fines and.
Turning particularly to
In operation, flow of the fluid 210 is received through the filters of the flow control apparatus 505 and to the ICDs enclosed within the filters. The ICDs, in some aspects, may be set (e.g., according to a number of flow control apparatus 505 on each base pipe joint, according to a type of ICDs used in the flow control apparatus 505, or otherwise) to provide a maximum velocity of the wellbore fluid 210 to the completion string 212, so as to more uniformly distribute flow from the annulus 20 to the completion string 212. In some aspects, the maximum velocity may be set so as to avoid “hot spots” of high flow of the wellbore fluid 210 to the completion string 212. In some aspects, the maximum velocity may allow for the transport of sands or fines in the wellbore fluid 210 into the completion string 212 but at rates in which a flow distribution among the flow control apparatus is uniform, constant, and/or substantially equal. In some aspects, the maximum velocity may be lower than a transport velocity of sands or fines in the wellbore fluid 210.
Turning now to
Turning now to
A number implementations have been described. Nevertheless, it will be understood that various modifications may be made without departing from the spirit and scope of the disclosure. Accordingly, other implementations are within the scope of the following claims.
Filing Document | Filing Date | Country | Kind |
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PCT/US2013/035433 | 4/5/2013 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
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WO2014/163647 | 10/9/2014 | WO | A |
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Number | Date | Country | |
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20160032694 A1 | Feb 2016 | US |