During a hydraulic fracturing operation, a pressurized fracturing fluid is injected into a subterranean formation via a wellbore or multiple wellbores. The injected fracturing fluid is at a higher pressure than the fracture pressure of the subterranean formation such that the fluid creates fractures therein. The fractures increase a permeability of the subterranean formation so that formation fluids (such as oil, gas, water, etc.) may more easily escape the subterranean formation and flow to the surface via the wellbore(s). Proppant (such as sand or other solids) may be mixed with the fracturing fluid prior to injecting the fracturing fluid downhole. The proppant may flow into the fractures in the subterranean formation to hold the fractures open after the hydraulic fracturing operation has ended.
Various fluid conveyance devices and systems are positioned at the surface to route the fracturing fluids into and out of the wellbore(s) during the hydraulic fracturing operation. The fluid conveyance devices may include various combinations of pipes, hoses, conduits, manifolds, tanks, pumps, etc. At least some of these devices transport the fracturing fluid after it has been pressurized into the wellbore(s). Thus, the fluid conveyance devices (or some of the fluid conveyance devices) are configured to withstand relatively high differential pressures during operations. However, due to the severe conditions of a hydraulic fracturing operation, failures of these fluid conveyance devices are common.
As previously described, during a hydraulic fracturing operation, various fluid conveyance devices may be used to route and contain relatively high-pressure fracturing fluid during operations. For instance, one such fluid conveyance device includes a fluid manifold for receiving the pressurized fluid from one or more pumps. Such manifolds are sometimes referred to as “missiles.” The manifold may include one or more flow cross junctions having one or more fluid inlets for receiving the pressurized fluid output from the one or more pumps. Each inlet may include a fluid coupling that connects to an output of a corresponding pump via a suitable conduit. Conventionally, the fluid couplings are attached to the flow cross junctions of the manifold via large, flanged connections. In order to accommodate these flanged connections and maintain a sufficient wall thickness around the internal flow bores (or passages) of the flow cross junction (for withstanding the high pressures of the fracturing fluid), the body of the flow cross junction may be substantial in both dimension and weight. This, in turn, greatly increases the size and weight of the manifold (which may employ a number of flow cross junctions as previously described) such that the manifold occupies a relatively large percentage of the limited available space at the wellsite, and the use of larger (and therefore expensive) lifting and support equipment is necessitated for construction, deconstruction, and repair of the manifold and its components.
In addition, the fluid couplings represent a weak point in the manifold and routinely experience failure due to the high pressures of the fracturing fluid, the vibrations within the system (such as vibrations caused by operation of the pump(s)), and the erosive nature of the proppant entrained within the high-pressure fracturing fluid. However, removal and replacement of these fluid couplings can be cumbersome and time consuming especially when a conventional flanged connection is employed. Thus, a failure of a fluid coupling on the high-pressure manifold can lead to a significant delay in the hydraulic fracturing operation and an associated increase in the cost and time associated with the hydraulic fracturing operation.
Accordingly, some embodiments disclosed herein include flow cross junctions for a manifold of a hydraulic fracturing system that include a streamlined shape and design so as to allow for a significant reduction in size and weight for the flow cross junctions and manifold overall. In addition, some embodiments disclosed herein include fluid coupling assemblies for a manifold of a hydraulic fracturing system that facilitate quick replacement in the event of a failure so as to minimize stoppage time. In some embodiments, the embodiments disclosed herein include a fluid coupling assembly having a removable coupling adapter that is inserted directly within an inlet flow bore of the flow cross junction. Thus, by configuring the coupling adapter so that it may be easily removed and replaced, the downtime associated with the replacement of a failed fluid coupling on the manifold may be reduced. As a result, through use of the embodiments disclosed herein, a hydraulic fracturing operation may be conducted more safely and efficiently.
Some embodiments disclosed herein are directed to a method including (a) inserting a coupling adapter into an inlet flow bore of a flow cross junction of a manifold of a hydraulic fracturing system. In addition, the method includes (b) positioning a connection device of the coupling adapter outside of the inlet flow bore as a result of (a). The connection device to connect to an output of a pump of the hydraulic fracturing system. Further, the method includes (c) compressing a retainer ring against an external shoulder of the coupling adapter.
Some embodiments disclosed herein are directed to a manifold of a hydraulic fracturing system. In some embodiments, the manifold includes a flow cross junction including an inlet flow bore. In addition, the manifold includes a coupling adapter including an external shoulder and a connection device. The connection device is to connect to an output of a pump of the hydraulic fracturing system, and the coupling adapter is removably inserted within the inlet flow bore such that the connection device is positioned outside of the inlet flow bore. Further, the manifold includes a retainer ring connected to the flow cross junction and compressed against the external shoulder.
In some embodiments, the manifold includes a first elongate manifold section. In addition, the manifold includes a second elongate manifold section. Further, the manifold includes a flow cross junction positioned between the first elongate manifold section and the second elongate manifold section along a longitudinal axis. The flow cross junction includes a first end connected to the first elongate manifold section. In addition, the flow cross junction includes a second end connected to the second elongate manifold section. Further, the flow cross junction includes a throughbore extending axially between the first end and the second end. Still further, the flow cross junction includes an outer surface extending axially between the first end and the second end. The outer surface has an outer diameter that is greater than an axial length of the flow cross junction measured from the first end to the second end along the longitudinal axis. Also, the flow cross junction includes an inlet flow bore extending between the outer surface and the throughbore.
Some embodiments disclosed herein are directed to a flow cross junction for a manifold of a hydraulic fracturing system. In some embodiments, the flow cross junction includes an upstream end configured to connect with a first elongate manifold section. In addition, the flow cross junction includes a downstream end spaced from the upstream end along a longitudinal axis to define an axial length of the flow cross junction measured axially from the upstream end to the downstream end. The downstream end is configured to connect to a second elongate manifold section. Further, the flow cross junction includes a throughbore extending axially between the upstream end to the downstream end. Still further, the flow cross junction includes an outer surface extending axially between the upstream end to the downstream end. The outer surface has an outer diameter that is greater than the axial length of the flow cross junction.
Embodiments described herein comprise a combination of features and characteristics intended to address various shortcomings associated with certain prior devices, systems, and methods. The foregoing has outlined rather broadly the features and technical characteristics of the disclosed embodiments in order that the detailed description that follows may be better understood. The various characteristics and features described above, as well as others, will be readily apparent to those having ordinary skill in the art upon reading the following detailed description, and by referring to the accompanying drawings. It should be appreciated that this disclosure may be readily utilized as a basis for modifying or designing other structures for carrying out the same purposes as the disclosed embodiments. It should also be realized that such equivalent constructions do not depart from the spirit and scope of the principles disclosed herein.
For a detailed description of various embodiments, reference will now be made to the accompanying drawings in which:
As previously described, during a hydraulic fracturing operation, various fluid conveyance devices may be used to route and contain relatively high-pressure fracturing fluid during operations. For instance, one such fluid conveyance device includes a fluid manifold for receiving the pressurized fluid from one or more pumps. Such manifolds are sometimes referred to as “missiles.” The manifold may include one or more flow cross junctions that further include one or more fluid inlets (or “inlet flow bores”) for receiving the pressurized fluid output from the one or more pumps. Each fluid inlet may include a fluid coupling that connects to an output of a corresponding pump via a suitable conduit. Such fluid couplings represent a weak point in the manifold and routinely experience failure due to the high pressures of the fracturing fluid, the vibrations within the system (such as vibrations caused by operation of the pump(s)), and the erosive nature of the proppant entrained within the high-pressure fracturing fluid. However, removal and replacement of these fluid couplings can be cumbersome and time consuming. Thus, a failure of a fluid coupling on the high-pressure manifold can lead to a significant delay in the hydraulic fracturing operation and an associated increase in the cost and time associated with the hydraulic fracturing operation.
In addition, a conventional flow cross junction may be relatively large and bulky so as to accommodate the conventional flanged connections of the fluid couplings and to provide sufficient wall thicknesses for the internal flow bores to contain the high-pressure fracturing fluid during operations. However, these large, conventional flow cross junctions substantially increases the total weight of the high-pressure manifold thereby further increasing the costs of these components and the complexity (and inherent dangers) for moving these components about the wellsite.
Accordingly, embodiments disclosed herein include flow cross junctions for a manifold of a hydraulic fracturing system that include a streamlined shape and design so as to allow for a significant reduction in size and weight for the flow cross junctions and manifold overall. In addition, some embodiments of the flow cross junctions disclosed herein include fluid couplings that facilitate quick replacement in the event of a failure so as to minimize stoppage time. In some embodiments, the embodiments disclosed herein include a fluid coupling assembly having a removable coupling adapter that is inserted directly within the flow cross junction of the manifold so as to omit the large, flanged connections associated with a conventional fluid coupling. As will be described in more detail below, the coupling adapter may be the component of the fluid coupling assembly having the highest likelihood of failure. Thus, by configuring the coupling adapter so that it may be easily removed and replaced, the downtime associated with the replacement of a failed fluid coupling on the manifold may be reduced. As a result, through use of the embodiments disclosed herein, a hydraulic fracturing operation may be conducted more safely and efficiently.
It should be appreciated that the hydraulic fracturing system 10 shown in
System 10 generally includes a plurality of storage vessels 12 that are each configured to hold a volume of fracturing fluid therein. The fracturing fluid stored in the storage vessels 12 may include any liquid or semi-liquid (such as a gel) that is suitable for injection into and fracturing of the subterranean formation 103 as previously described. In some embodiments, the fracturing fluid includes an aqueous solution including substantially pure water or water mixed with one or more additives (such as gels or gelling agents, chemicals, etc.). The storage vessels 12 may include any suitable container for holding a volume of fluids (such as liquids) therein. For instance, in some embodiments, storage vessels may include rigid tanks, flexible tanks (such as bladders), open pits, mobile tanks (that may be pulled by a tractor trailer or other vehicle), or a combination thereof.
A blender 14 is positioned downstream of the storage vessels 12 that is configured to mix a proppant into the fracturing fluid. The proppant may include sand or other suitable solids. As previously described, the proppant is configured to flow into the fractures within the subterranean formation 103 so as to hold the fractures open after the hydraulic fracturing operation has ended. In some embodiments, additives (such as chemical additives) may be mixed into the fracturing fluid within the blender 14 either in addition or alternatively to the proppant. The blender 14 emits the fracturing fluid, now with proppant mixed therein, to a manifold assembly 20 that communicates the fracturing fluid to and from a plurality of pumping units 40.
The manifold assembly 20 includes one or more low-pressure, inlet manifolds 22 and one or more high-pressure, outlet manifolds 100. In the particular embodiment depicted in
Each pumping unit 40 includes a pump 44 driven by a driver 42 (which may be referred to herein as a “prime mover”). Pump 44 may include any suitable fluid pumping device or assembly for pressurizing the fracturing fluid (with or without proppant and/or other additives entrained therein) to the pressures associated with a hydraulic fracturing operation. For instance, in some embodiments, the pump 44 may be configured to pressurize the fracturing fluid (again, with or without proppant and/or other additives entrained therein) to a pressure of about 9000 pounds per square inch (psi) or higher. Thus, pump 44 may be referred to herein as a “hydraulic fracturing pump” 44. In some embodiments, pump 44 may include a positive displacement pump, centrifugal pump, or other suitable pump types. Driver 42 may include any suitable motor or engine that is configured to drive or actuate the corresponding pump 44 during operations. For instance, in some embodiments, driver 42 may include a diesel engine, a turbine (such as a gas turbine, steam turbine, etc.), an electric motor, or some combination thereof. During operations, within each pumping unit 40, the driver 42 may actuate the pump 44 to draw fracturing fluid into the pump 44 via the corresponding inlet conduit 24 and to pressurize and output the fracturing fluid from the pump 44 via the corresponding outlet conduit 26.
The outlet manifold 100 is described in more detail below. However, generally speaking the pressurized fracturing fluid is received by the outlet manifold 100 via the outlet conduits 26. The outlet manifold 100 directs the pressurized fracturing fluid toward the wellhead 102 such that it may access the subterranean formation 103 as previously described. During the hydraulic fracturing operations, fracturing fluid may be emitted from the wellbore via the wellhead 102 and recycled back to the storage vessels 12 through one or more recycle conduits 16. In some embodiments, the fracturing fluid output from the wellhead 102 may be routed through one or more filtering or separation assemblies or devices (not shown) to remove additives, proppant, and/or other fluids or solids (such as, rock chips, formation fluids, etc.) that may be entrained within the fracturing fluid, prior to recycling the fracturing fluid to the storage vessels 12.
In addition, outlet manifold 100 includes a plurality of tubular manifold sections 110 and a plurality of flow cross junctions 130 interleaved between the plurality of manifold sections 110 along the longitudinal axis 105. More particularly, each manifold section 110 extends axially between axially adjacent flow cross junctions 130.
Manifold sections 110 are elongate tubular members that are coaxially aligned along the longitudinal axis 105 (so that the manifold sections 110 may be referred to herein as “elongate manifold sections”). As is best shown in
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In some embodiments, one or more of the flow cross junctions 130 may include a single inlet flow bore (such as inlet flow bore 134 or inlet flow bore 136) or may include more than two inlet flow bores. For instance,
In some embodiments, the first inlet flow bore 134 extends along a first axis 135 and the second inlet flow bore 136 extends along a second axis 137. The first axis 135 and the second axis 137 (and thus also the first inlet flow bore 134 and the second inlet flow bore 136, respectively) are radially opposite one another about the axis 139 (and thus also axis 105), and each axis 135, 137 extends radially with respect to axis 139. Thus, the axes 135, 137 are aligned along a common radially extending plane relative to axis 139. In some embodiments, axes 135, 137 may be axially offset from one another along axis 139 such the axes 135, 137 lie in different radially extending planes relative to axis 139. In addition, in some embodiments, one or both of the axes 135, 137 may not extend radially relative to axis 139. For instance, one or both of the axes 135, 137 (and thus also the inlet flow bores 134, 136, respectively) may extend at an angle (such as at an acute angle) relative to the axis 139. In addition, in some embodiments, one or both of the inlet flow bores 134, 136 may be curved.
In some embodiments, the outer surface 130c is a cylindrical surface that extends axially between the ends 130a, 130b relative to axis 139. However, other shapes are contemplated for outer surface 130c in other embodiments. For instance, in some embodiments, the outer surface 130c may include a polygonal cross-section (such as pentagonal, hexagonal, octagonal, etc.) along a plane passing radially through the central axis 139 so that the radially outer surface 130c may be a polygonal surface. The outer surface 130c may include one or more (such as one or a plurality of) flats or facets 138 formed therein. As will be described in more detail below, the facets 138 may form flat surface areas along the otherwise curved, cylindrical outer surface 130c that may be used to form or machine one or more inlet flow bores (such as, inlet flow bores 134, 136) and/or to provide engagement surfaces for lifting or supporting the flow cross junction 130 during operations. Because the outer surface 130c may be a cylindrical surface in some embodiments, the facets 138 may form or define radially inwardly extending recesses in the outer surface 130c.
The flow cross junction 130 may include a total axial length L130 that is measured axially (with respect to the axis 139) from the upstream end 130a to the downstream end 130b. In addition, the outer surface 130c may have an outer diameter (such as a maximum outer diameter) D130 that extends radially across the flow cross junction 130 with respect to the axis 139. In some embodiments, the outer diameter D130 may be greater than the axial length L130. For instance, in some embodiments, the ratio of the axial length L130 to the outer diameter D130 (L130/D130) may be less than 1.
In some embodiments, one or more parameters or dimensions of the flow cross junction 130 may be selected to minimize a total size and weight of the flow cross junction 130 while still maintaining a sufficient amount of material to contain the high pressures associated with a hydraulic fracturing operation (or other fluid delivery operation as described herein). For instance, in some embodiments, parameters such as the outer diameter D130 and the number of mounting bores 133 may selected to comply with specifications set by trade associations such as, for instance, the American Petroleum Institute (API). In some embodiments, the outer diameter D130 and number of mounting bores 133 (among other parameters) may be selected to comply with API 6A specification for wellhead and tree equipment (see, for instance, Tables E.5 of API specification 6A including specifications for flanges to withstand 15,000 psi pressure).
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First inlet flow bore 134 has a first or outer opening 161 positioned at or along the outer surface 130c (particularly along the corresponding one of the facets 138) and a second or inner opening 163 positioned at the intersection between the first inlet flow bore 134 and the main flow bore 132 (
The outer portion 134a of first inlet flow bore 134 includes a cylindrical surface 169 extending axially from outer opening 161 along axis 135 and internal threads 168 positioned axially between the cylindrical surface 169 and the internal shoulder 166. Internal threads 168 may include one or more grooves that extend radially into first inlet flow bore 134 and helically about the central axis 135.
A radially extending circumferential ledge or seat 165 is formed on the internal shoulder 166 within the outer portion 164a. A gasket 174 (or junk ring) may be positioned on the seat 165 that may sealingly engage both the internal shoulder 166 and the coupling adapter 180 (
Inner portion 134b includes a cylindrical surface 170 extending axially from internal shoulder 166 to the inner opening 163. In some embodiments, the cylindrical surface 170 and inner opening 163 may have an inner diameter that is the same as a minimum inner diameter of the internal shoulder 166. As a result, the cylindrical surface 170 may be flush and continuous with a radially inner surface of the internal shoulder 166. In some embodiments, the inner portion 134b may have a surface (such as a cylindrical surface) that has an inner diameter that is greater than or less than a minimum inner diameter of the internal shoulder 166. Thus, in some embodiments, the inner portion 134b may have one or more surfaces that have a variable (such as increasing or decreasing) inner diameter, such as a frustoconical surface (or chamfer), a curved surface, etc.
The facet 138 along outer surface 130c that is associated with the fluid coupling assembly 150 may be a planar surface that extends radially relative to central axis 135 and circumferentially about the outer opening 161 of first inlet flow bore 134. A plurality of mounting bores 159 extend axially into the flow cross junction 130 from the facet 138 and may be arranged about the outer opening 161. The mounting bores 159 may be threaded (at least partially) such that they may receive one or more threaded mounting members (such as, mounting members 212 described herein) during operations. In some embodiments, mounting bores 159 may be evenly circumferentially spaced about axis 155 along the corresponding facet 138.
Throughbore 182 extends axially through the coupling adapter 180 along central axis 185 from the outer end 180a to the inner end 180b. Thus, the throughbore 182 has a first or outer opening 181 positioned at the outer end 180a and a second or inner opening 183 positioned at the inner end 180b. An internal shoulder 184 is defined within the throughbore 182. In some embodiments, the internal shoulder 184 may be positioned axially closer (and more proximate) to the outer end 180a and outer opening 181 than the inner end 180b and inner opening 183. The internal shoulder 184 extends radially inward toward the central axis 185 within throughbore 182.
In addition, throughbore 182 may include a tapered or frustoconical surface 186 (or “chamfer”) that extends from outer end 180a and outer opening 181 and a cylindrical surface 187 extending axially from frustoconical surface 186 to shoulder 184. The frustoconical surface 186 tapers radially inward toward central axis 185 when moving axially from outer end 180a and outer opening 181 toward cylindrical surface 187. Thus, the inner diameter of throughbore 182 may decrease when moving axially from outer end 180a and outer opening 181 toward cylindrical surface 187.
A circumferential or annular groove 189 is positioned along cylindrical surface 187. The annular groove 189 extends both radially into cylindrical surface 187 (and thus radially away from central axis 185) and circumferentially about the central axis 185. In some embodiments (such as the embodiment shown in
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The first set of external threads 188 may be more simply referred to herein as “first threads” 188 and the second set of external threads 190 may be more simply referred to herein as “second threads” 190. The first threads 188 and the second threads 190 may be separate and axially spaced from one another along radially outer surface 180c. In addition, the first threads 188 may be positioned axially closer (and more proximate) to outer end 180a than inner end 180b, and second threads 190 may be positioned more proximate to inner end 180b than outer end 180a. For instance, in some embodiments, the first threads 188 are positioned at (and extend axially from) the outer end 180a and the second threads 190 are positioned at (and extend axially from) the inner end 180b. The first threads 188 and the second threads 190 may include one or more grooves that extend radially into radially outer surface 180c and helically about the central axis 185.
An annular groove or recess 192 is axially positioned between the first threads 188 and the second threads 190. The recess 192 extends radially into the radially outer surface 180c toward central axis 185 and defines a radially extending annular external shoulder 194 that faces axially toward the outer end 180a. The annular external shoulder 194 may be more simply referred to herein as an “external shoulder” 194.
A first or outer cylindrical surface 195 extends axially between first threads 188 and annular recess 192, and a second or inner cylindrical surface 196 extends axially between external shoulder 194 and second threads 190. A plurality of engagement bores 197 extend radially into the outer cylindrical surface 195. In some embodiments, the engagement bores 197 are evenly circumferentially spaced about central axis 185 along outer cylindrical surface 195. As will be described in more detail below, engagement bores 197 may engage with a suitable tool (such as a spanner wrench) to facilitate threaded engagement or disengagement of the coupling adapter 180 from one of the inlet flow bores 134, 136 (
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When installing the coupling adapter 180 into the inlet flow bores 134, 136 of flow cross junction 130, the inner end 180b of coupling adapter 180 is inserted through outer opening 161 such that second threads 190 are threadably engaged with the interior threads 168 within the inlet flow bores 134, 136. More particularly,
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When the metallic seal junk ring 174 is compressed between the coupling adapter 180 and the shoulder 166, the first frustoconical surface 456 may be engaged with a corresponding and complimentary frustoconical surface (or chamfer) 460 formed within the throughbore 182 of coupling adapter 180, and the second frustoconical surface 458 may be engaged with a corresponding and complimentary frustoconical surface (or chamfer) 462 formed on the shoulder 166. Thus, as may be appreciated in
Thus, by threadably engaging the coupling adapter 180 within the first inlet flow bore 134 (or the second inlet flow bore 136), the coupling adapter 180 is axially compressed into the inlet flow bore 134 and against the internal shoulder 166 along the aligned axes 135, 185 (such as along arrows 171 in
As may be appreciated from
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Without being limited to this or any other theory, engaging the retainer ring 204 with the external shoulder 194 of coupling adapter 180 may further secure the coupling adapter 180 within the inlet flow bore 134 or inlet flow bore 136 against the pressure of the fracturing fluid within the outlet manifold 100 during operations as previously described above. In addition, engaging the retainer ring 204 with the external shoulder 194 of coupling adapter 180 may also relieve pressure on the engaged threads 168, 190 during operations. Further, preventing (or restricting) rotation of the coupling adapter 180 about the central axis 185 via the retainer ring 204 may prevent unthreading of the coupling adapter 180 from the outer portion 134a of inlet flow bore 134 (or inlet flow bore 136) (via second threads 190 and interior threads 168) during operations (such as when installing or removing the connector 193 from the coupling adapter 180 via first threads 188).
As illustrated by
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Moreover, this reduction in the length L130 relative to the outer diameter D130 when combined with the cylindrical (or polygonal) outer surface 130c may substantially reduce the size and weight of the flow cross junction 130 and the manifold 100 (
Initially, method 300 includes inserting a coupling adapter into an inlet flow bore of a flow cross junction of a manifold of a hydraulic fracturing system at block 302. For instance, as previously described and as may be appreciated from
In addition, method 300 includes positioning a connection device of the coupling adapter outside of the inlet flow bore at block 304, wherein the connection device is to connect to an output of a pump of the hydraulic fracturing system. For instance, as may be appreciated from
Further, method 300 includes compressing a retainer ring against an external shoulder of the coupling adapter at block 306. For instance, as previously described and as may be appreciated from
The embodiments disclosed herein include flow cross junctions for a manifold of a hydraulic fracturing system that include a streamlined shape and design so as to allow for a significant reduction in size and weight for the flow cross junctions and manifold overall. In addition, some embodiments of the flow cross junctions disclosed herein include fluid couplings that facilitate quick replacement in the event of a failure so as to minimize stoppage time. As a result, through use of the embodiments disclosed herein, a hydraulic fracturing operation may be conducted more safely and efficiently.
In some embodiments, the flow cross junction 130 may include one or more fluid ports for pressure and/or fluid communication with the inlet flow bores 134, 136. For instance, during operations, the one or more fluid ports may be used to inject an injectable sealant or packing (such as, polytetrafluoroethylene (PTFE), graphite, grease, polymer-based sealant, etc.) into the inlet flow bore 134, 136 so as to form an additional seal between the coupling adapters 180 and inlet flow bores 134, 136 during operations. For instance, the injectable sealant may be injected (via the one or more fluid flow ports) into the inlet flow bores 134, 136, axially between the annular seal members 199 (
It should be appreciated that embodiments of the flow cross junctions may be utilized in other fluid services other than hydraulic fracturing operations. For instance, embodiments of the flow cross junctions disclosed herein may be utilized in fluid manifolds, lines, or other fluid conveyance systems and devices for transporting pressurized fluids both inside and outside of the oil and gas industry. Some particular examples include the use of embodiments of the flow cross junctions disclosed herein for flowing fluids for other oilfield operations (such as pump down, drilling mud delivery, production operations, etc.). In addition, it is also contemplated that embodiments of the flow cross junctions disclosed herein may be used in other fluid services, including those outside of the oil and gas industry.
The preceding discussion is directed to various exemplary embodiments. However, one of ordinary skill in the art will understand that the examples disclosed herein have broad application, and that the discussion of any embodiment is meant only to be exemplary of that embodiment, and not intended to suggest that the scope of the disclosure, including the claims, is limited to that embodiment.
The drawing figures are not necessarily to scale. Certain features and components herein may be shown exaggerated in scale or in somewhat schematic form and some details of conventional elements may not be shown in interest of clarity and conciseness.
In the discussion herein and in the claims, the terms “including” and “comprising” are used in an open-ended fashion, and thus should be interpreted to mean “including, but not limited to . . . .” Also, the term “couple” or “couples” is intended to mean either an indirect or direct connection. Thus, if a first device couples to a second device, that connection may be through a direct connection of the two devices, or through an indirect connection that is established via other devices, components, nodes, and connections. In addition, as used herein, the terms “axial” and “axially” generally mean along or parallel to a given axis (e.g., central axis of a body or a port), while the terms “radial” and “radially” generally mean perpendicular to the given axis. For instance, an axial distance refers to a distance measured along or parallel to the axis, and a radial distance means a distance measured perpendicular to the axis. Further, when used herein (including in the claims), the words “about,” “generally,” “substantially,” “approximately,” and the like, when used in reference to a stated value mean within a range of plus or minus 10% of the stated value. This application claims priority to, and the benefit of U.S. Provisional Application No. 63/512,219, filed Jul. 6, 2023, titled “FLUID COUPLING ASSEMBLIES FOR A MANIFOLD OF A HYDRAULIC FRACTURING SYSTEM AND RELATED METHODS,” U.S. Provisional Application No. 63/512,193, filed Jul. 6, 2023, titled “FLOW CROSS JUNCTIONS FOR A MANIFOLD OF A HYDRAULIC FRACTURING SYSTEM AND RELATED METHODS,” U.S. Provisional Application No. 63/491,139, filed Mar. 20, 2023, titled “FLOW CROSS JUNCTIONS FOR A MANIFOLD OF A HYDRAULIC FRACTURING SYSTEM AND RELATED METHODS,” and U.S. Provisional Application No. 63/476,438, filed Dec. 21, 2022, titled “FLUID COUPLING ASSEMBLIES FOR A MANIFOLD OF A HYDRAULIC FRACTURING SYSTEM AND RELATED METHODS,” the disclosures of which are incorporated herein by reference in their entireties. This application is also related to U.S. Non-Provisional application Ser. No. ______, filed Dec. 19, 2023, titled “FLUID COUPLING ASSEMBLIES FOR A MANIFOLD OF A HYDRAULIC FRACTURING SYSTEM AND RELATED METHODS,” the disclosure of which is incorporated herein by reference in its entirety.
While exemplary embodiments have been shown and described, modifications thereof can be made by one skilled in the art without departing from the scope or teachings herein. The embodiments described herein are exemplary only and are not limiting. Many variations and modifications of the systems, apparatus, and processes described herein are possible and are within the scope of the disclosure. Accordingly, the scope of protection is not limited to the embodiments described herein, but is only limited by the claims that follow, the scope of which shall include all equivalents of the subject matter of the claims. Unless expressly stated otherwise, the steps in a method claim may be performed in any order. The recitation of identifiers such as (a), (b), (c) or (1), (2), (3) before steps in a method claim are not intended to and do not specify a particular order to the steps, but rather are used to simplify subsequent reference to such steps.
This application claims priority to, and the benefit of U.S. Provisional Application No. 63/512,219, filed Jul. 6, 2023, titled “FLUID COUPLING ASSEMBLIES FOR A MANIFOLD OF A HYDRAULIC FRACTURING SYSTEM AND RELATED METHODS,” U.S. Provisional Application No. 63/512,193, filed Jul. 6, 2023, titled “FLOW CROSS JUNCTIONS FOR A MANIFOLD OF A HYDRAULIC FRACTURING SYSTEM AND RELATED METHODS,” U.S. Provisional Application No. 63/491,139, filed Mar. 20, 2023, titled “FLOW CROSS JUNCTIONS FOR A MANIFOLD OF A HYDRAULIC FRACTURING SYSTEM AND RELATED METHODS,” and U.S. Provisional Application No. 63/476,438, filed Dec. 21, 2022, titled “FLUID COUPLING ASSEMBLIES FOR A MANIFOLD OF A HYDRAULIC FRACTURING SYSTEM AND RELATED METHODS,” the disclosures of which are incorporated herein by reference in their entireties. This application is also related to U.S. Non-Provisional application Ser. No. ______, filed Dec. 19, 2023, titled “FLUID COUPLING ASSEMBLIES FOR A MANIFOLD OF A HYDRAULIC FRACTURING SYSTEM AND RELATED METHODS,” the disclosure of which is incorporated herein by reference in its entirety.
Number | Date | Country | |
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63512219 | Jul 2023 | US | |
63512193 | Jul 2023 | US | |
63491139 | Mar 2023 | US | |
63476438 | Dec 2022 | US |