Not applicable.
1. Field of the Invention
The invention relates generally to the field of hydrocarbon production. More particularly, the invention relates to systems, methods, and apparatus for deliquifying a well to enhance production.
2. Background of the Technology
Geological structures that yield gas typically produce water and other liquids that accumulate at the bottom of the wellbore. The liquids typically comprise hydrocarbon condensate (e.g., relatively light gravity oil) and interstitial water in the reservoir. The liquids accumulate in the wellbore in two forms, both as single phase liquid entering from the reservoir and as condensing liquids, falling back in the wellbore. The condensing liquids actually enter the wellbore as a vapor and as they travel up the wellbore, they drop below dew point and condense. In either case, the higher density liquid-phase, being essentially discontinuous, must be transported to the surface by the gas.
In some hydrocarbon producing wells that produce both gas and liquid, the formation gas pressure and volumetric flow rate are sufficient to lift the produced liquids to the surface. In such wells, accumulation of liquids in the wellbore generally does not hinder gas production. However, in the event the gas phase does not provide sufficient transport energy to lift the liquids out of the well (i.e. the formation gas pressure and volumetric flow rate are not sufficient to lift the produced liquids to the surface), the liquid will accumulate in the well bore.
In many cases, the hydrocarbon well may initially produce gas with sufficient pressure and volumetric flow to lift produced liquids to the surface, however, over time, the produced gas pressure and volumetric flow rate decrease until they are no longer capable of lifting the produced liquids to the surface. Specifically, as the life of a natural gas well matures, reservoir pressures that drive gas production to surface decline, resulting in lower production. At some point, the gas velocities drop below the “Critical Velocity” (CV), which is the minimum velocity required to carry a droplet of water to the surface. As time progresses these droplets accumulate in the bottom of the wellbore. The accumulation of liquids in the well impose an additional back-pressure on the formation and may begin to cover the gas producing portion of the formation, thereby restricting the flow of gas, thereby restricting the flow of gas and detrimentally affecting the production capacity of the well. Once the liquid will no longer flow with the produced gas to the surface, the well will eventually become “loaded” as the liquid hydrostatic head begins to overcome the lifting action of the gas flow, at which point the well is “killed” or “shuts itself in.” Thus, the accumulation of liquids such as water in a natural gas well tends to reduce the quantity of natural gas which can be produced from a given well. Consequently, it may become necessary to use artificial lift techniques to remove the accumulated liquid from the wellbore to restore the flow of gas from the formation. The process for removing such accumulated liquids from a wellbore is commonly referred to as deliquification.
For oil wells that primarily produce single phase liquids (oil and water) with a minimal amount of entrained gas, there are numerous artificial lift techniques. The most commonly employed type of artificial lift requires pulling 30 foot tubing joints from the well, attaching a fluid pump to the lowermost joint, and running the pump downhole on the string of tubing joints. The fluid pump may be driven by jointed rods attached to a beam pump, a downhole electric motor supplied with electrical power from the surface via wires banded to the outside of the tubing string, or a surface hydraulic pump displacing a power fluid to the downhole fluid pump via multiple hydraulic lines. Although there are several types of artificial lift used in lifting oil, they usually require an expensive method of deployment consisting of workover rigs, coiled tubing units, cable spoolers, and multiple personnel on-site.
Initially, artificial lift techniques employed with oil producing wells were used to deliquify gas producing wells (i.e., remove liquids from gas producing wells). However, the adaptation of existing oilfield artificial lift technologies for gas producing wells generated a whole new set of challenges. The first challenge was commercial. When employing artificial lift techniques in an oil well, revenue is immediately generated—valuable oil is lifted to the surface. In contrast, when deliquifying a gas well, additional expense is generated mostly from non-revenue generating liquids—typically, water and small amounts of condensed light hydrocarbons are lifted to the surface. The benefit, however, is the ability to maintain and potentially increasing the production of gas for extended time, thereby creating additional recoverable reserves. Typically, at 100 psi downhole pressure, the critical velocity, and hence need for artificial lift, occurs at less than 300 mcfd. The typical gas well in the United States averages about 110 mcfd, and about 90% of all U.S. gas wells (˜480,000 wells) are liquid loaded. The challenge is that large remaining reserve potential with lower per well revenue stream are needed to justify the price of installing traditional artificial lift technologies.
The second major shortcoming of the existing artificial lift technologies is the lack of design for dealing with three phase flow, with the largest percentage being the gas phase. For example, many conventional artificial lift pumps gas lock or cavitate when pumping fluids comprising more than about 30% gas by volume. However, in may gas wells, the pump may experience churn fluid flow where the pump intake may experience transitions between 100% gas and 100% liquid over a few seconds. In general, the goal of a downhole fluid pump is to physically lower the fluid level or hydrostatic in the wellbore as close to the pump intake as possible. Unfortunately, most conventional artificial lift technologies cannot achieve this goal and thus are not fit for purpose.
With well economics driving limited choices for deliquification, one lower cost option that has been investigated is called “plunger lift.” In a plunger lift system, a solid round metal plug is placed inside the tubing at the bottom of the well, and liquids are allowed to accumulate on top of the plug. Then a controller shuts in the well via a shutoff valve and allows pressure to build and then releases the plunger to come to surface, pushing the fluids above it. When the shutoff valve is closed, the pressure at the bottom of the well usually builds up slowly over time as fluids and gas pass from the formation into the well. When the shutoff valve is opened, the pressure at the well head is lower than the bottomhole pressure, so that the pressure differential causes the plunger to travel to the surface. Plunger lift is basically a cyclic “bucketing” of fluids to surface. Since the driver is the wellbore pressure it is directly proportional to the amount of liquid it can lift. Also, the older the well, the longer shut-in times are required to build pressure. Besides the safety risks of launching a metal plug to surface at velocities around 1,000 feet per minute, the plunger requires high manual intervention and only removes a small fraction of the liquid column to surface.
Accordingly, there remains a need in the art for economical methods and systems for deliquifying wells having low volume of liquid.
These and other needs in the art are addressed in one embodiment by a deliquification pump for deliquifying a well. In an embodiment, the deliquification pump comprises a fluid end pump adapted to pump a fluid from a wellbore. In addition, the deliquification pump comprises a hydraulic pump adapted to drive the fluid end pump. The hydraulic pump having a central axis and including a housing having a first internal pump chamber and a first pump assembly disposed in the first chamber. The first pump assembly includes a piston adapted to reciprocate axially relative to the housing. The piston has a first end, a second end opposite the first end, and a throughbore extending between the first end and the second end. Further, the first pump assembly includes a first wobble plate including a planar end face axially adjacent the second end of the piston and a slot extending axially through the first wobble plate. The slot is disposed at a uniform radius from the central axis and the end face is oriented at an acute angle relative to the central axis. The first wobble plate is adapted to rotate about the central axis relative to the housing to axially reciprocate the piston and cyclically place the throughbore of the piston in fluid communication with the slot.
These and other needs in the art are addressed in another embodiment by a system for deliquifying a wellbore. In an embodiment, the system comprises a downhole deliquification pump coupled to a lower end of a tubing string. The downhole deliquification pump has a longitudinal axis and includes a pump inlet and a pump outlet. In addition, the deliquification pump includes a fluid end pump adapted to pump a fluid through the pump outlet to the surface through the tubing string. Further, the deliquification pump includes a hydraulic pump coupled to the fluid end pump and adapted to power the fluid end pump. Still further, the deliquification pump includes an electric motor coupled to the hydraulic pump and adapted to power the hydraulic pump. The system also includes a conduit in fluid communication with the pump inlet and extending axially through the electric motor and the hydraulic pump to the fluid end pump. The conduit is adapted to supply the fluid to the fluid end pump.
These and other needs in the art are addressed in another embodiment by a method for deliquifying a well. In an embodiment, the method comprises (a) positioning a deliquification pump into a wellbore with a tubing string. The deliquification pump comprises a fluid end pump, a hydraulic pump coupled to the fluid end pump, and an electric motor coupled to the hydraulic pump. In addition, the method comprises (b) powering the fluid end pump with the hydraulic pump. Further, the method comprises (c) powering the hydraulic pump with the electric motor. Still further, the method comprises (d) sucking well fluids into the separator. The well fluids include a liquid phase and a plurality of solid particles disposed in the liquid phase. Moreover, the method comprises (e) separating at least a portion of the solid particles from the liquid phase to generate processed well fluids. The method also comprises (f) flowing the processed well fluids to the fluid end pump. In addition, the method comprises (g) pumping the processed well fluids to the surface with the fluid end pump.
Thus, embodiments described herein comprise a combination of features and advantages intended to address various shortcomings associated with certain prior devices, systems, and methods. The various characteristics described above, as well as other features, will be readily apparent to those skilled in the art upon reading the following detailed description, and by referring to the accompanying drawings.
For a detailed description of the preferred embodiments of the invention, reference will now be made to the accompanying drawings in which:
The following discussion is directed to various embodiments of the invention. Although one or more of these embodiments may be preferred, the embodiments disclosed should not be interpreted, or otherwise used, as limiting the scope of the disclosure, including the claims. In addition, one skilled in the art will understand that the following description has broad application, and the discussion of any embodiment is meant only to be exemplary of that embodiment, and not intended to intimate that the scope of the disclosure, including the claims, is limited to that embodiment.
Certain terms are used throughout the following description and claims to refer to particular features or components. As one skilled in the art will appreciate, different persons may refer to the same feature or component by different names. This document does not intend to distinguish between components or features that differ in name but not function. 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 following discussion 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, or through an indirect connection via other devices, components, and connections. In addition, as used herein, the terms “axial” and “axially” generally mean along or parallel to a central axis (e.g., central axis of a body or a port), while the terms “radial” and “radially” generally mean perpendicular to the central axis. For instance, an axial distance refers to a distance measured along or parallel to the central axis, and a radial distance means a distance measured perpendicular to the central axis.
Referring now to
Wellbore 20 traverses an earthen formation 12 comprising a production zone 13. Casing 21 lines wellbore 20 and includes perforations 22 that allow fluids 14 (e.g., water, gas, etc.) to pass from production zone 13 into wellbore 20. In this embodiment, production tubing 23 extends from a wellhead 24 through wellbore casing 21. System 10 extends into wellbore 20 through an injector head 50 coupled to a wellhead 24 and production tubing 23. In this embodiment, a blowout preventer 25 sits atop wellhead 24, and thus, system 10 extends through injector head 50, blowout preventer 25, and wellhead 24 into production tubing 23.
As shown in
During deliquification operations, fluids 14 in the bottom of wellbore 20 are pumped through tubing 40 to the surface 11 with pump 100. In general, system 10 may be employed to lift and remove fluids from any type of well including, without limitation, oil producing wells, natural gas producing wells, methane producing wells, propane producing wells, or combinations thereof. However, embodiments of system 10 described herein are particularly suited for deliquification of gas wells. In this embodiment, wellbore 20 is gas well, and thus, fluids 14 include water, hydrocarbon condensate, gas, and possibly small amounts of oil. Pump 100 may remain deployed in well 20 for the life of the well 20, or alternatively, be removed from well 20 once production of well 20 has been re-established.
It should be appreciated that deployment of system 10 and deliquification pump 100 via vehicle 30 eliminates the need for construction and/or use of a rig. In other words, system 10 and pump 100 may be deployed in a “rigless” manner. As used herein, the term “rigless” is used to refer to an operation, process, apparatus or system that does not require the construction or use of a workover rig that includes the derrick or mast, and the drawworks. By eliminating the need for a workover rig for deployment, system 10 offers the potential to provide a more economically feasible means for deliquifying relatively low production gas wells.
Referring still to
As previously described, spoolable tubing 40 is used to deploy and position pump 100 downhole. In general, tubing 40 may comprise any suitable tubing capable of being spooled and stored on reel 31 including, without limitation, coiled steel tubing or spoolable composite tubing. As best shown in
In this embodiment, inner layer 42 and intermediate layer 44 are melt fused together to form a virtually seamless bond therebetween. Thus, inner layer 42 and intermediate layer 44 are preferably made from polymeric materials capable of being melt fused together to form a seamless bond. Examples of suitable polymeric materials for layers 42, 44 include, without limitation, polyethylene, polypropylene, high density polyethylene (HDPE), low density polyethylene (LDPE), copolymers, block copolymers, polyolefins, polycarbonates, polystyrene, or combinations thereof. Although inner layer 42 and intermediate layer 44 are made from the same polymeric material in this embodiment, in other embodiments, inner layer 42 and intermediate layer 44 may be made of different polymeric materials. Further, inner layer 42 may be fiber reinforced.
Intermediate layer 44 may comprise fiber impregnated polymeric tape that is repeatedly wrapped around and melt fused to inner layer 42. In general, the fibers impregnated within the polymeric tape may be made of any suitable material including, without limitation, glass fibers, polymer fibers, carbon fibers, combinations thereof, and the like. The fiber impregnated tape may be wrapped at different angles to modulate or adjust the tensile strength of composite coiled tubing 40.
Since inner layer 42 and intermediate layer 44 are melt fused together, no epoxy or additional compounds are necessary to secure or bond layers, 42, 44 together. As a result, layered composite tubing 40 is solid wall tubing with a relatively high collapse pressure rating. The solid wall technology offers the potential to eliminate gas migration as compared to epoxy based tubing that often develops micro cracks from bending. In particular, composite coiled tubing (e.g., tubing 40) offers the potential for enhanced ductility as compared to epoxy bonded tubing. For example, embodiments of coiled tubing 40 may withstand over 18,000 bend cycles. For use in harsh downhole conditions, spoolable tubing 40 is preferably capable of withstanding temperatures (i.e. temperature rated) of at least about 200° F., and more preferably capable of withstanding temperatures of at least about 250 to 300° F.
As previously described, in this embodiment, spoolable tubing 40 comprises inner layer 42 and intermediate layer 44 preferably made from polymeric that are melt fused together. However, in general, the spoolable tubing (e.g., tubing 40) may be made from any suitable type of spoolable tubing including steel coiled tubing, composite reinforced spoolable tubing, etc. For example, the spoolable tubing may comprise an inner layer (e.g., layer 42) and an intermediate layer (e.g., layer 44) made of high temperature flexible epoxy. Moreover, although this embodiment of system 10 includes spoolable tubing 40, pump 100 may also be delivered downhole with conventional jointed oilfield tubing or pipe joints with one or more conductors strapped to the string or integral with the string (e.g., wire pipe).
Referring now to
Due to the length of deliquification pump 100, it is illustrated in seven longitudinally broken sectional views, vis-à-vis
Although components of deliquification pump 100 may be configured differently, the basic operation of pump 100 remains the same. In particular, fluid 14 in wellbore 20 enters separator 400, which separates solids (e.g., sand, rock chips, etc.) from well fluid 14 to form a solids-free or substantially solids-free fluid 15, which may also be referred to as “clean” fluid 15. Clean fluid 15 output from separator 400 is sucked into fluid end pump 110 and pumped to the surface 11 through coupling 45 and tubing 40. Fluid end pump 110 is driven by hydraulic pump 200, which is driven by electric motor 300. Conductors 46 provide electrical power downhole to motor 300. Compensator 350 provides a reservoir for hydraulic fluid, which can flow to and from hydraulic pump 200 and motor 300 as needed. Deliquification pump 100 is particularly designed to lift substantially solids-free fluid 15, which may include liquid and gaseous phases (e.g., water and gas), in wellbore 20 to the surface 11 in the event the gas pressure in wellbore 20 is insufficient to remove the liquids in fluid 14 to the surface 11 (i.e., wellbore 20 is a relatively low pressure well). As will be described in more detail below, use of hydraulic pump 200 in conjunction with fluid end pump 110 offers the potential to generate the relatively high fluid pressures necessary to force or eject relatively low volumes of well fluids 15 to the surface 11.
Referring now to
Fluid end pump 110 also includes a first or upper piston 122 slidingly disposed in first chamber 121 and a second or lower piston 126 slidingly disposed in second chamber 122. Pistons 122, 126 are connected by an elongate connecting rod 125 that extends axially through shuttle valve assembly 130. A first or upper well fluids control valve assembly 500 is coupled to end 110a of housing 110, and a second or lower well fluids control valve assembly 500′ is coupled to end 110b of housing 110. As will be described in more detail below, valve assemblies 500, 500′ are substantially the same. In particular, each valve assembly 500, 500′ includes a valve body 510, a well fluids inlet valve 520, and a well fluids outlet valve 560.
Piston 122 divides upper chamber 121 into two sections or subchambers—a well fluids section 121a axially positioned between upper valve assembly 500 and piston 122, and a hydraulic fluid chamber 121b axially positioned between piston 122 and shuttle valve assembly 130. Likewise, piston 126 divides lower chamber 125 into two sections or subchambers—a well fluids section 125a axially positioned between lower valve assembly 500′ and piston 126, and a hydraulic fluid chamber 125b axially positioned between piston 125 and shuttle valve assembly 130. Together, housing 110, piston 122, and valve assembly 500 define section 121a, and together, housing 110, piston 126, and valve assembly 500′ define section 125a. In general, inlet valve 520 of valve assemblies 500, 500′ control the flow of well fluids 15 into chamber sections 121a, 125a, respectively, and outlet valve 560 of valve assemblies 500, 500′ control the flow of well fluids out of chamber sections 121a, 125a, respectively.
Referring still to
Outlet passage 112 is in fluid communication with tubing 40 (via coupling 45), outlet valve 560 of upper valve assembly 500, and outlet valve of lower valve assembly 500′. Thus, outlet passage 112 places both outlet valves 560 in fluid communication with tubing 40. Outlet valves 560 of valve assemblies 500, 500′ control the flow of well fluids out of chamber sections 121a, 125a, respectively. As will be described in more detail below, well fluids 15 are pumped by fluid end pump 110 from chamber sections 121a, 125a through outlet valves 560, outlet passage 112, and tubing 40 to the surface 11.
Hydraulic fluid passage 113 is in fluid communication with hydraulic pump 200 and shuttle valve assembly 130. In particular, hydraulic pump 200 provides compressed hydraulic fluid to shuttle valve assembly 130 via passage 113. Shuttle valve assembly 130 includes a stroke sensor and plurality of valves and associated flow passages that reciprocally distribute the flow of the compressed hydraulic fluid to hydraulic fluid chambers 121b, 125b, thereby driving the axial, reciprocal motion of pistons 122, 126. The stroke sensor ensures controlled switching of the supply of hydraulic fluid among the valves and flow passages. In general, shuttle valve assembly 130 may comprise any suitable shuttle valve that reciprocally alternates the flow of compressed hydraulic fluid between two distinct and separate chambers. Examples of suitable shuttle valves are disclosed in U.S. Pat. No. 4,597,722 which is hereby incorporated herein by reference in its entirety for all purposes.
A pair of annular seals 123, 127 are disposed about each piston 122, 126, respectively, and sealingly engages piston 122, 126, respectively, and housing 120. In particular, each seal 123, 127 forms a dynamic seal with housing 120 and a static seal with piston 122, 126, respectively. Seals 123, 127 restrict and/or prevent fluid communication between well fluids 15 in chambers 121a, 125a, respectively, and hydraulic fluid in sections 121b, 125b, respectively. It should be appreciated that over time, small amounts of hydraulic fluid may leak or seep past seals 123, 127 from sections 121b, 125b, respectively, to sections 121a, 125a, respectively. However, as will be described in more detail below, compensator 350 functions as a hydraulic fluid reservoir to compensate for any lost hydraulic fluid.
During pumping operations, hydraulic pump 200 provides compressed hydraulic fluid to shuttle valve assembly 130 via fluid passage 113. Shuttle valve assembly 130 controls the flow of compressed hydraulic fluid into chambers 121b, 125b to drive the axial reciprocal motion of pistons 122, 126 in chambers 121, 125, respectively. Namely, shuttle valve assembly 130 provides compressed hydraulic fluid to sections 121b, 125b in a reciprocating or alternating fashion, and allows fluid to exit sections 125b, 121b, respectively, in a reciprocating or alternating fashion. As shuttle valve assembly 130 supplies compressed hydraulic fluid to chamber 121b, piston 122 is urged axially upward within chamber 121 towards upper valve assembly 500, thereby increasing the volume of section 121b and decreasing the volume of section 121a. Since pistons 122, 126 are connected by connecting rod 125, pistons 122, 126 move axially together. Thus, when piston 122 is urged axially upward within chamber 121, piston 126 is also urged axially upward within chamber 125, thereby decreasing the volume of section 125b and increasing the volume of section 125a. Simultaneous with directing compressed hydraulic fluid to chamber 121b, shuttle valve assembly 130 allows hydraulic fluid to exit section 125b, thereby allowing the volume of section 125b to decrease without restricting the axial movement of pistons 122, 126.
The upward axial movement of pistons 122, 126 continues as compressed hydraulic fluid is supplied to chamber 121b until piston 122 is proximal upper valve assembly 500 and the volume of section 121a is at its minimum. At this point, piston 122 may be described as being at the axially outermost end of its stroke relative to shuttle valve assembly 130 (i.e., its furthest axial position from shuttle valve assembly 130), and piston 126 may be described as being at the axially innermost end of its stroke relative to shuttle valve assembly 130 (i.e., its closest axial position to shuttle valve assembly 130). In this embodiment, fluid end pump 110 and upper valve assembly 500 are sized and configured to minimize the dead or unswept volume in section 121a when piston 122 is at the outermost end of its stroke. In embodiments, described herein, the volume of section 121a when piston 122 is at the outermost end of its stroke (i.e., the unswept volume of section 121a) is close to zero.
Referring still to
The downward axial movement of pistons 122, 126 continues as compressed hydraulic fluid is supplied to chamber 125b until piston 126 is proximal lower valve assembly 500′ and the volume of section 125a is at its minimum. At this point, piston 126 may be described as being at the axially outermost end of its stroke relative to shuttle valve assembly 130 (i.e., its furthest axial position from shuttle valve assembly 130), and piston 122 may be described as being at the axially innermost end of its stroke relative to shuttle valve assembly 130 (i.e., its closest axial position to shuttle valve assembly 130). In this embodiment, fluid end pump 110 and lower valve assembly 500′ are sized and configured to minimize the dead or unswept volume in section 125a when piston 126 is at the outermost end of its stroke. In embodiments, described herein, the volume of section 125a when piston 126 is at the outermost end of its stroke (i.e., the unswept volume of section 125a) is close to zero. Simultaneous with piston 126 achieving the axially outermost end of its stroke (i.e., its closest position to upper valve assembly 500), shuttle valve assembly 130 stops supplying compressed hydraulic fluid to chamber 125b, begins supplying compressed hydraulic fluid to chamber 121b, and the process repeats. In the manner previously described, pistons 122, 126 are axially reciprocated within chambers 121, 125 by reciprocating the flow of compressed hydraulic fluid into sections 121b, 125b.
As previously described, as pistons 122, 126 move axially upward within chambers 121, 125, respectively, the volume of section 121a decreases, and the volume of section 125a increases. As the volume of section 121a decreases, the pressure of well fluids 15 therein increases, and as the volume of section 125a increases, the pressure of well fluids 15 therein decreases. When the pressure in section 121a is sufficiently large, outlet valve 560 of upper valve assembly 500 transitions to an “open position,” thereby allowing well fluids to flow from section 121a to tubing 40 via outlet passage 112 and coupling 45; and when the pressure in section 125a is sufficiently low, inlet valve 520 of lower valve assembly 500′ transitions to an “open position,” thereby allowing well fluids to flow into section 125a from well fluids conduit 116. As will be described in more detail below, each valve assembly 500, 500′ is designed such that outlet valve 560 is closed when its corresponding inlet valve 520 is open, and inlet valve 520 is closed when its corresponding outlet valve 560 is open.
Conversely, as pistons 122, 126 move axially downward within chambers 121, 125, respectively, the volume of section 121a increases, and the volume of section 125a decreases. As the volume of section 121a increases, the pressure of well fluids 15 therein decreases, and as the volume of section 125a decreases, the pressure of well fluids 15 therein increases. When the pressure in section 121a is sufficiently low, inlet valve 520 of upper valve assembly 500 transitions to an “open position,” thereby allowing well fluids to flow into section 121a from inlet passage 111; and when the pressure in section 125a is sufficiently high, outlet valve 560 of lower valve assembly 500′ transitions to an “open position,” thereby allowing well fluids to flow from section 125a to tubing 40 via outlet passage 112 and coupling 45.
As pistons 122, 126 reciprocate within chambers 121, 125, well fluids 15 are sucked into sections 121a, 125a from well fluids conduit 116 and inlet passage 111, respectively, in an alternating fashion, and pumped from sections 125a, 121a, respectively, to outlet passage 112 and tubing 40 in an alternating fashion. In this manner, fluid end pump 110 pumps well fluids 15 through tubing 40 to the surface 11. Since fluid end pump 110 is a double acting reciprocating pump, well fluids 15 are pumped from fluid end pump 110 to the surface 11 when pistons 122, 126 move axially downward and when pistons 122, 126 move axially upward, and well fluids 15 are sucked from separator 400 into fluid end pump 110 when pistons 122, 126 move axially downward and when pistons 122, 126 move axially upward.
Referring now to
In this embodiment, both inlet valve 520 and outlet valve 560 are double poppet valves. Inlet valve 520 includes a seating assembly 521 disposed in bore 511 at end 510b, a retention assembly 530 disposed in bore 511 at end 510b, a primary poppet valve member 540, and a backup or secondary poppet valve member 550 telescopically coupled to primary poppet valve member 540. Retention assembly 521, seating assembly 530, and valve members 540, 550 are coaxially aligned with bore axis 513.
Seating assembly 521 includes a seating member 522 threaded into bore 511 at end 510b, an end cap 526, and a biasing member 529. Seating member 522 has a first end 522a proximal body end 510b, a second end 522b disposed in bore 511 opposite end 522a, and a central through passage 523 extending axially between ends 522a, b. In addition, the radially inner surface of seating member 522 includes an annular recess 524 proximal end 522a, a first annular shoulder 525a axially spaced from recess 524, and a second annular shoulder 525b axially spaced from shoulder 525a. First annular shoulder 525a is axially disposed between recess 524 and shoulder 525b. As will be described in more detail below, valve members 540, 550 move into and out of engagement with shoulders 525a, b, respectively, to transition between closed and opened positions. Thus, annular shoulders 525a, b may also be referred as valve seats 525a, b, respectively.
End cap 526 is disposed in passage 523 at end 522a and is maintained within passage 523 with a snap ring 527 that extends radially into retention member recess 524. As best shown in
Referring again to
Referring still to
Secondary valve member 550 extends axially into passage 532. In particular, secondary valve member 550 slidingly engages retention member 531 between end 531a and shoulder 533, but is radially spaced from retention member 531 between shoulder 533 and end 531b. A retention ring 534 disposed about secondary valve member 550 is axially positioned between shoulder 533 and end 531b. A snap ring 535 disposed about secondary valve member 550 prevents retention ring 534 from sliding axially off of secondary valve member 550. Thus, biasing member 539 biases secondary valve member 550 axially towards end 510b and into engagement with valve seat 525b. In other words, biasing member 539 biases secondary valve member 550 to a “closed” position. Specifically, when secondary valve member 550 is seated in valve seat 525b, axial fluid flow through inlet valve 520 between inlet passage 111 and section 121a is restricted and/or prevented. Although biasing member 539 is a coil spring in this embodiment, in general, biasing member (e.g., biasing member 539) may comprise any suitable device for biasing the primary valve member (e.g., valve member 550) to the closed position.
Referring still to
Stem 551 of secondary valve member 550 extends axially into passage 532 and includes an annular recess in which snap ring 535 is seated. Secondary valve member 550 also includes a central counterbore 554 extending axially from end 550a through head 552 and into stem 551. Stem 541 of primary valve member 540 is slidingly received by counterbore 554. Further, head 542 of primary valve member 540 includes a cylindrical recess 546. Biasing member 529 is seated in recess 546, which restricts and/or prevents biasing member 529 from moving radially relative to valve head 542.
As previously described, during pumping operations, inlet valve 520 of upper valve assembly 500 controls the supply of well fluids 15 to section 121a. In particular, valve members 540, 550 are biased to closed positions engaging seats 525a, b, respectively, and valve heads 542, 552, are axially positioned between seats 525a, b, respectively, and section 121a. Thus, when the pressure in chamber 121a is equal to or greater than the pressure in passage 111, valves heads 542, 552 sealingly engage valve seats 525a, b, respectively, thereby restricting and/or preventing fluid flow between passage 111 and section 121a. However, as piston 122 begins to move axially downward within chamber 121, the volume of section 121a increases and the pressure therein decreases. As the pressure in section 121a drops below the pressure in passage 111, the pressure differential seeks to urge valves members 540, 550 axially downward and out of engagement with seats 525a, b, respectively. Biasing members 529, 539 bias valve members 540, 550, respectively, in the opposite axial direction and seek to maintain sealing engagement between biasing members valve heads 542, 552 and valve seats 525a, b, respectively. However, once the pressure in section 121a is sufficiently low (i.e., low enough that the pressure differential between section 121a and passage 111 is sufficient to overcome biasing member 529), valve member 540 unseats from seat 525a and compresses biasing member 529. Then, almost instantaneously, the combination of the relatively low pressure in section 121a and relatively high pressure of well fluids in passage 111 overcomes biasing member 539, valve member 550 unseats from seat 525b and compresses biasing member 539, thereby transitioning inlet valve 520 to an “opened” position allowing fluid communication between passage 111 and section 121a. Since the pressure in section 121a is less than the pressure of well fluids 15 in passage 111, well fluids 15 will flow through inlet valve 520 into section 121a from passage 111. In this embodiment, biasing members 529, 539 provide different biasing forces. In particular, biasing member 529 provides a lower biasing force than biasing member 539 (e.g., biasing member 529 is a lighter duty coil spring than biasing member 539).
After piston 122 reaches its axially innermost stroke end proximal shuttle valve assembly 130 and begins to move axially upward within chamber 121, the volume of chamber 121a decreases and the pressure therein increases. Once the pressure in section 121a in conjunction with the biasing forces provided by biasing members 529, 539 are sufficient to overcome the pressure in passage 111, valve members 540, 550 move axially upward and seat against valve seats 525a, b, respectively, thereby transitioning back to the closed positions restricting and/or preventing fluid communication between section 121a and passage 111.
Referring again to
Seating member 561 is threaded into counterbore 512 at end 510b and has a first end 561a flush with body end 510b, a second end 561b disposed in counterbore 512 opposite end 561a, and a central through passage 562 extending axially between ends 561a, b. In addition, the radially inner surface of seating member 561 includes an annular shoulder 563 proximal end 561a. As will be described in more detail below, valve members 580, 590 move into and out of engagement with shoulder 563 and end 561b, respectively, to transition between closed and opened positions. Thus, annular shoulder 563 and seat member end 561b may also be referred as valve seats 563, 561b, respectively.
Valve member 580 is disposed in passage 562 and has a first end 580a and a second end 580b opposite end 580a. End 580a comprises a radially enlarged valve head 581 that mates with and sealingly engages valve seat 563. In this embodiment, valve head 581 includes a frustoconical sealing surface 582 that sealingly engages a mating frustoconical surface of valve seat 563. A biasing member 569 is axially compressed between valve members 580, 590. Thus, biasing member 569 biases primary valve member 580 axially away from valve member 590 and into engagement with valve seat 563. In other words, biasing member 569 biases primary valve member 580 to a “closed” position. Specifically, when primary valve member 580 is seated in valve seat 563, fluid communication between outlet passage 113 and section 121a is restricted and/or prevented. In this embodiment, biasing member 569 is seated in a cylindrical counterbore 583 extending axially from end 580b, thereby restricting and/or preventing biasing member 569 from moving radially relative to valve member 580. Although biasing member 569 is a coil spring in this embodiment, in general, biasing member (e.g., biasing member 569) may comprise any suitable device for biasing the primary valve member (e.g., valve member 580) to the closed position.
Referring still to
Valve member 590 is disposed in passage 562 and has a first end 590a and a second end 590b opposite end 590a. End 590a comprises a radially enlarged valve head 591 that mates with and sealingly engages valve seat 561b. In this embodiment, valve head 591 includes a frustoconical sealing surface 592 that sealingly engages a mating frustoconical surface of valve seat 561b. As previously described, biasing member 579 biases valve member 590 into sealing engagement with seat 561b. In addition, in this embodiment, end 590b comprises a cylindrical tip 593 that extends axially into biasing member 579, thereby restricting and/or preventing biasing member 579 and valve member 590 from moving radially relative to each other.
As previously described, during pumping operations, outlet valve 560 of upper valve assembly 500 controls the flow of well fluids 15 from section 121a into tubing 40. In particular, valve members 580, 590 are biased to closed positions engaging seats 563, 561b, respectively, and valve seats 563, 561b are axially positioned between valve heads 581, 591, respectively, and section 121a. Thus, when the pressure in chamber 121a is less than to or greater than the pressure in passage 113 and coupling 45, valves heads 581, 591 sealingly engage valve seats 563, 561b, respectively, thereby restricting and/or preventing fluid flow between coupling 45 and section 121a. However, as piston 122 begins to move axially upward within chamber 121, the volume of section 121a decreases and the pressure therein increases. As the pressure in section 121a increases above the pressure in passage 112 and coupling 45, the pressure differential seeks to urge valves members 580, 590 axially upward and out of engagement with seats 563, 561b, respectively. Biasing members 569, 579 bias valve members 580, 590, respectively, in the opposite axial direction and seek to maintain sealing engagement between biasing members valve heads 581, 591 and valve seats 563, 561b, respectively. However, once the pressure in section 121a is sufficiently high (i.e., high enough that the pressure differential between section 121a and passage 112 is sufficient to overcome biasing members 569), valve member 580 will unseat from seat 563 and compresses biasing member 569. Then, almost instantaneously, the combination of the relatively high pressure in section 121a and relatively lower pressure in passage 112 overcome biasing member 579, valve member 590 unseats from seat 561b, thereby transitioning outlet valve 560 to an “opened” position allowing fluid communication between passage 112 and section 121a. Since the pressure in section 121a is greater than the pressure of well fluids 15 in passage 112, well fluids 15 will flow through outlet valve 560 from section 121a into passage 112, coupling 45, and tubing 40. In this embodiment, biasing members 569, 579 provide different biasing forces. In particular, biasing member 569 provides a lower biasing force than biasing member 579 (e.g., biasing member 569 is a lighter duty coil spring than biasing member 579).
After piston 122 reaches its axially outermost stroke end distal shuttle valve assembly 130 and begins to move axially downward within chamber 121, the volume of chamber 121a increases and the pressure therein decreases. Once the pressure in coupling 45 in conjunction with the biasing forces provided by biasing members 569, 579 are sufficient to overcome the pressure in section 121a, valve members 580, 590 move axially downward and seat against valve seats 563, 561b, respectively, thereby transitioning back to the closed positions restricting and/or preventing fluid communication between section 121a and coupling 45.
Referring now to
As previously described, during pumping operations, inlet valve 520 of lower valve assembly 500′ controls the supply of well fluids 15 to section 125a. In particular, valve members 540, 550 are biased to closed positions engaging seats 525a, b, respectively, and valve heads 542, 552, are axially positioned between seats 525a, b, respectively, and section 121a. Thus, when the pressure in chamber 125a is equal to or greater than the pressure in well fluids conduit 116, valves heads 542, 552 sealingly engage valve seats 525a, b, respectively, thereby restricting and/or preventing fluid flow between well fluids conduit 116 and section 125a. However, as piston 126 begins to move axially upward within chamber 125, the volume of section 125a increases and the pressure therein decreases. As the pressure in section 125a drops below the pressure in well fluids conduit 116, the pressure differential seeks to urge valves members 540, 550 axially downward and out of engagement with seats 525a, b, respectively. Biasing members 529, 539 bias valve members 540, 550, respectively, in the opposite axial direction and seek to maintain sealing engagement between biasing members valve heads 542, 552 and valve seats 525a, b, respectively. However, once the pressure in section 125a is sufficiently low (i.e., low enough that the pressure differential between section 1251a and well fluids conduit 116 is sufficient to overcome biasing members 529, 539), valve members 540, 550 will unseat from seats 525a, b, respectively, thereby transitioning inlet valve 520 of lower valve assembly 500′ to an “opened” position allowing fluid communication between well fluids conduit 116 and section 125a. Since the pressure in section 125a is less than the pressure of well fluids 15 in well fluids conduit 116, well fluids 15 will flow through inlet valve 520 into section 125a from well fluids conduit 116. In this embodiment, biasing members 529, 539 provide different biasing forces. In particular, biasing member 529 provides a lower biasing force than biasing member 539 (e.g., biasing member 529 is a lighter duty coil spring than biasing member 539). Thus, valve member 540 of lower valve assembly 500′ will unseat just before valve member 550 of lower valve assembly 500′.
After piston 126 reaches its axially innermost stroke end proximal shuttle valve assembly 130 and begins to move axially downward within chamber 125, the volume of chamber 125a decreases and the pressure therein increases. Once the pressure in section 125a in conjunction with the biasing forces provided by biasing members 529, 539 are sufficient to overcome the pressure in well fluids conduit 116, valve members 540, 550 move axially upward and seat against valve seats 525a, b, respectively, thereby transitioning back to the closed positions restricting and/or preventing fluid communication between section 125a and well fluids conduit 116.
Referring still to
After piston 126 reaches its axially outermost stroke end distal shuttle valve assembly 130 and begins to move axially upward within chamber 125, the volume of chamber 125a increases and the pressure therein decreases. Once the pressure in passage 113 in conjunction with the biasing forces provided by biasing members 569, 579 are sufficient to overcome the pressure in section 125a, valve members 580, 590 move axially downward and seat against valve seats 563, 561b, respectively, thereby transitioning back to the closed positions restricting and/or preventing fluid communication between section 125a and passage 113.
In the manner described, inlet valve 520 and outlet valve 560 of upper valve assembly 500 control the flow of well fluids 15 into and out of section 121a, and inlet valve 520 and outlet valve 560 of lower valve assembly 500′ control the flow of well fluids 15 into and out of section 125a. Each valve 520, 560 includes two poppet valve members adapted to move into and out of engagement with mating valve seats. Namely, inlet valve 520 includes poppet valve members 540, 550, and outlet valve 560 includes poppet valve members 580, 590. Valve members 540, 550 are capable of operating independent of one another. Thus, valve member 540 may seat against valve seat 525a even if valve member 550 is not seated against valve seat 525b, and vice versa. Likewise, valve members 580, 590 are capable of operating independent of one another. Thus, valve member 580 may seat against valve seat 563 even if valve member 590 is not seated against valve seat 561b, and vice versa. Inclusion of multiple, serial, operationally independent valve members 540, 550 in inlet valve 520 offers the potential to enhance the reliability and sealing of inlet valve 520 in harsh downhole conditions. For example, even if valve member 540 gets stuck in the opened position (e.g., solids get jammed between valve member 540 and seat 525a), valve member 550 can still sealingly engage valve seat 525b, thereby closing inlet valve 520. Likewise, inclusion of multiple, serial, operationally independent valve members 580, 590 in outlet valve 560 offers the potential to enhance the reliability and sealing of inlet valve 560 in harsh downhole conditions. For example, even if valve member 590 gets stuck in the opened position (e.g., solids get jammed between valve member 590 and seat 561b), valve member 580 can still sealingly engage valve seat 563, thereby closing outlet valve 560.
Referring now to
A tubular well fluids conduit 205 extends coaxially through hydraulic pump 200 and is in fluid communication with conduit 116 of distributor 115. As will be described in more detail below, conduit 205 supplies well fluids 15 from separator 400 to fluid end pump 110 via distributor conduit 116. Although conduit 205 extends through hydraulic pump 200, it is not in fluid communication with any of chambers 220, 230, 240.
Referring now to
Passage 214 is in fluid communication with hydraulic fluid passage 113 of fluid end pump 110 via hydraulic fluid conduit 117 extending through distributor 115. Thus, hydraulic pump 200 supplies compressed hydraulic fluid to shuttle valve assembly 130 previously described via branches 215, 216 and passages 214, 117, 113. A hydraulic fluid return passage (not shown) allows hydraulic fluid from shuttle valve assembly 130 to return to chambers 220, 230, 240 of hydraulic pump 200. End caps 212, 213 include throughbores 218, 219, respectively, through which conduit 205 extends.
Referring still to
Guide member 251 axially abuts end cap 212 and includes a central throughbore 252, a plurality of circumferentially spaced piston guide bores 253 radially spaced from central throughbore 252, and an axially extending counterbore 254 coaxially aligned with throughbore 252 and facing the remainder of assembly 250. Biasing member 260 is seated in counterbore 254, and biasing sleeve 261 is disposed about biasing member 260 and slidingly engages counterbore 254. As will be described in more detail below, biasing member 260 is compressed between guide member 251 and biasing sleeve 261, and thus, biases biasing sleeve 261 axially away from guide member 251. Each guide bore 253 is aligned with and in fluid communication with one of the branches 215 in end cap 212. In addition, one piston 255 is telescopically received by and extends axially from each of the piston guide bores 253.
Biasing sleeve 261 has a first or upper end 261a disposed in counterbore 254, a second end 261b opposite end 261a, and a radially inner surface including an annular shoulder 262 between ends 261a, b and a frustoconical seat 263 at end 261b. Biasing member 260 axially abuts annular shoulder 262 and guide member 251, and swivel plate 265 is pivotally seated in seat 263.
Each piston 255 is disposed at the same radial distance from axis 105 and has a first end 255a disposed in one bore 253, a second end 255b axially positioned between swivel plate 265 and wobble plate 270, and a throughbore 256 extending axially between ends 255a, b. Throughbore 256 of each piston 255 is in fluid communication with its corresponding bore 253. In this embodiment, end 255b of each piston 255 comprises a spherical head 257.
Referring still to
It should be appreciated that swivel plate 265 is disposed about conduit 205 but radially spaced from conduit 205 by a radial distance that provides sufficient clearance therebetween as swivel plate 265 pivots relative to biasing sleeve 261. Likewise, each bore 269 in swivel plate 265 has a diameter greater than the outside diameter of the portion of piston 255 extending therethrough to provide sufficient clearance therebetween as swivel plate 265 pivots relative to that piston 255.
Referring now to
As best shown in
A piston interface shoe 295 is disposed about each piston head 257, and is axially positioned between wobble plate 270 and piston head 257. Each interface shoe 295 has a planar surface 296 slidingly engaging planer end face 271 and a spherical concave seat 297 opposite surface 296. Spherical piston head 257 is pivotally seated in mating seat 297.
Referring now to
As wobble plate 270 rotates, the axial distance from each piston guide bore 253 to wobble plate end face 271 cyclically varies. For example, the axial distance from a given guide bore 253 and end face 271 is maximum when the “thin” portion of wobble plate 270 is axially opposed that guide bore 253, and the axial distance from a given guide bore 253 and end face 271 is minimum when the “thick” portion of wobble plate 270 is axially opposed that guide bore 253. However, pistons 255 move axially back and forth within bores 253 to maintain piston head 257 axially adjacent end face 271. Specifically, biasing member 260 biases biasing sleeve 261 axially into swivel plate 265, which in turn, biases retention rings 290 and corresponding piston heads 257 against end face 271. Sliding engagement of swivel plate surface 266a and bias sleeve seat 263 allows simultaneous axial biasing of swivel plate 265 and pivoting of swivel plate 265 relative to biasing sleeve 261. It should also be appreciated that engagement of each spherical piston head 257 with a corresponding spherical retention ring seat 292 and spherical interface shoe seat 297 enables ring 290 and shoe 295 to slidingly engage head 257 and pivot about head 257 while maintaining contact with head 257 and plates 265, 270, respectively.
As wobble plate 270 rotates, pistons 255 reciprocate axially within guide bores 253 and slot 272 cyclically moves into and out of fluid communication with bore 256 of each piston 255. In particular, wobble plate 270 is rotated such that bore 256 of each piston 255 first comes into fluid communication with slot 272 at end 272a (generally aligned with point 271a) and moves out of fluid communication with sot 272 at end 272b (generally aligned with point 271b). Thus, bore 256 of each piston 255 is in fluid communication with slot 272 as corresponding piston head 257 moves axially downward and away from guide member 251 as it is biased against end face 271. Accordingly, bore 256 of each piston 255 is in fluid communication with slot 272 as piston 255 telescopically extends axially from its corresponding bore 253. As previously described, check valve 217 in each branch 215 only allows one-way fluid communication from bore 253 to corresponding branch 215. Thus, as each piston 255 extends from its corresponding guide bore 253, the fluid pressure within associated bores 253, 256 decreases and hydraulic fluid within chamber 220 flows through slot 272 and fills bores 253, 256. As will be described in more detail below, compensator 350 maintains hydraulic fluid in chambers 220, 230, 240 at a fluid pressure sufficient to drive hydraulic fluid flow into pistons 255 when piston bores 256 are in fluid communication with chambers 220, 230, 240 via slot 272.
Conversely, once each piston 256 moves out of fluid communication with slot 272, corresponding piston head 257 moves axially upward and toward guide member 251. Accordingly, bore 256 of each piston 255 is isolated from (i.e., not in fluid communication with) slot 272 as piston 255 is telescopically pushed axially into its corresponding bore 253. As each piston 255 is axially pushed further into its corresponding guide bore 253, the hydraulic fluid in associated bores 253, 256 is compressed. As previously described, check valve 217 in each branch 215 only allows one-way fluid communication from bore 253 to corresponding branch 215. Thus, when the hydraulic fluid in bores 253, 256 is sufficiently compressed (i.e., the pressure differential across check valve 217 exceeds the cracking pressure of check valve 217), corresponding check valve 217 will open and allow the compressed hydraulic fluid in bores 253, 256 to flow into associated branch 215 and passage 214.
Referring again to
Lower pump assembly 280 functions in the same manner as upper pump assembly 280 to supply compressed hydraulic fluid to shuttle valve assembly 130. However, each guide bore 253 of guide member 251 of lower pump assembly 280 is in fluid communication with one branch 216 in lower end cap 213. Thus, lower pump assembly 280 provides compressed hydraulic fluid to shuttle valve assembly 130 via branches 216 and passages 214, 117, 113. In particular, driveshaft 298 drives the rotation of lower wobble plate 270. As lower wobble plate 270 rotates, pistons 255 of lower pump assembly 280 reciprocate axially within guide bores 253 and slot 272 in lower wobble plate 270 cyclically moves into and out of fluid communication with bore 256 of each piston 255. In particular, lower wobble plate 270 is rotated such that bore 256 of each piston 255 first comes into fluid communication with slot 272 at end 272a (generally aligned with point 271a of lower wobble plate 270) and moves out of fluid communication with sot 272 at end 272b (generally aligned with point 271b of lower wobble plate 270). Thus, bore 256 of each piston 255 is in fluid communication with slot 272 as corresponding piston head 257 moves axially upward and away from guide member 251 as it is biased against end face 271 of lower wobble plate 270. Accordingly, bore 256 of each piston 255 is in fluid communication with slot 272 of lower wobble plate as piston 255 telescopically extends axially from its corresponding bore 253. Check valve 217 in each branch 216 only allows one-way fluid communication from bore 253 to corresponding branch 216. Thus, as each piston 255 extends from its corresponding guide bore 253, the fluid pressure within associated bores 253, 256 decreases and hydraulic fluid within chamber 230 flows through slot 272 in lower wobble plate 270 and fills bores 253, 256. Conversely, once each piston 256 of lower pump assembly 280 moves out of fluid communication with slot 272 in lower wobble plate 270, corresponding piston head 257 moves axially downward and toward guide member 251. Accordingly, bore 256 of each piston 255 in lower pump assembly 280 is isolated from (i.e., not in fluid communication with) slot 272 of lower wobble plate as piston 255 is telescopically pushed axially into its corresponding bore 253. As each piston 255 of lower pump assembly 280 is axially pushed further into its corresponding guide bore 253, the hydraulic fluid in associated bores 253, 256 is compressed. As previously described, check valve 217 in each branch 216 only allows one-way fluid communication from bore 253 to corresponding branch 216. Thus, when the hydraulic fluid in bores 253, 256 is sufficiently compressed (i.e., the pressure differential across check valve 217 exceeds the cracking pressure of check valve 217), corresponding check valve 217 will open and allow the compressed hydraulic fluid in bores 253, 256 to flow into associated branch 216 and passage 214.
In the manner described, each piston 255 of upper pump assembly 250 and lower pump assembly 280 axially reciprocates within its corresponding guide bore 253, piston bores 256 move into and out of fluid communication with slots 272, and compressed hydraulic fluid is supplied to shuttle valve assembly 130 via branches 215, 216 and passages 214, 117, 113. Although only one piston 255 is shown in each pump assembly 250, 280, however, as previously described, in this embodiment, each pump assembly 250, 280 includes three identical, uniformly circumferentially spaced pistons 255 that function in the same manner. Thus, at any given time during rotation of wobbles plate 270, at least one piston 255 of each assembly 250, 280 is being filled with hydraulic fluid and at least one piston 255 of each assembly 250, 280 is providing compressed hydraulic fluid to shuttle valve assembly 130. Accordingly, hydraulic pump 200 continuously provides compressed hydraulic fluid to shuttle valve assembly 130 to drive fluid end pump 110.
Referring again to
Referring still to
Referring now to
A controller (not shown), which may be disposed at the surface 11 or downhole, controls the speed of motor 320 in response to sensed pressure at the bottom of wellbore 20. Wires 46 in spoolable tubing 40 provide electricity to power the operation of motor 300.
In general, motor 300 may comprises any suitable type of electric motor that converts electrical energy provided by wires 46 into mechanical energy in the form of rotational torque and rotation of driveshaft 320. Examples of suitable electric motors include, without limitation, DC motors, AC motors, universal motors, brushed motors, permanent magnet motors, or combinations thereof. Due to the potentially high depth applications of deliquification pump 100 (e.g., depths in excess of 10,000 ft.), electric motor 300 is preferably capable of withstanding the relatively high temperatures experienced at such depths. In this embodiment, electric motor 300 is a permanent magnet motor. In addition, in this embodiment, motor housing 310 is filled with hydraulic fluid that can flow to and from hydraulic pump 200 and compensator 350. The hydraulic fluid facilitates heat transfer away from electric motor 300 and lubricates bearings 330. In other embodiments, the electric motor (e.g., motor 300) may include heat dissipation fins extending radially from the motor housing (e.g., housing 310) to enhance the transfer of thermal energy from the electric motor to the surrounding environment.
Referring now to
Housing 351 includes an elongate tubular section 352, a first or upper end cap 353 closing off tubular section 352 at end 350a and coupling compensator 350 to motor 300, and a second or lower end cap 354 closing off tubular section 352 at end 350b. Conduit 205 extends axially through throughbores 355, 356 in end caps 353, 354, respectively. In addition, upper end cap 353 includes a hydraulic fluid port 357 in fluid communication with motor housing 310, and lower end cap 354 includes a plurality of well fluids ports 358 in fluid communication with separator 400.
Piston 370 is disposed about conduit 205 within chamber 360. In this embodiment, piston 370 includes a piston body 371 extending radially from conduit 205 to housing 351 and a tubular member 372 extending axially from piston body 371 toward end 350b. Piston body 371 slidingly engages both conduit 205 and housing 351, and divides chamber 360 into a first or upper chamber section 360a extending axially from upper end cap 353 to piston 370 and a second or lower chamber section 360b extending axially from piston 370 to lower end cap 354. In this embodiment, piston body 371 includes two axially spaced radially inner annular seals 373 that sealingly engage conduit 205, and two axially spaced radially outer annular seals 374 that sealingly engage housing tubular section 352. Seals 373, 374 restrict and/or prevent fluid communication between chamber sections 360a, b. Chamber section 360a is filled with hydraulic fluid and chamber section 360b is filled with well fluids 15 from separator 400 via ports 358. Thus, as piston 370 moves axially within chamber 360 and the volume of section 360b changes, well fluids 15 are free to move between section 360b and separator 400 via ports 358. The remainder of well fluids 15 output from separator 400 pass through conduit 205 to fluid end pump 110.
Tubular member 372 is disposed about biasing assembly 380 and defines a minimum axial distance between piston body 371 and lower end cap 354, thereby defining a maximum volume of chamber section 360a. In general, piston 370 is generally free to move axially within chamber 360; when piston 370 moves axially toward end cap 353, the volume of section 360a decreases and the volume of section 360b increases, and when piston 370 moves axially toward end cap 354, the volume of section 360a increases and the volume of section 360b decreases. However, tubular member 372 limits the axial movement of piston 370 toward end cap 354. Specifically, once tubular member 372 axially abuts end cap 354, piston 370 is prevented from moving axially downward. In this embodiment, tubular member 372 is sized to abut end cap 354 when biasing assembly 380 is fully compressed.
Referring still to
Piston 370 is a free floating balance piston that moves in response to differences between the axial force applied by the hydraulic fluid pressure in section 360a, and the axial forces applied by biasing assembly 380 and well fluids pressure in section 360b. Specifically, piston 370 will axially within chamber 360 until these axial forces are balanced. For example, if the pressure of hydraulic fluid in section 360a increases, piston 370 will move axially downward (expanding the volume of section 360a) until the axial forces acting on piston 370 are balanced; and if the pressure of hydraulic fluid in section 360a decreases, piston 370 will move axially upward (decreasing the volume of section 360a) until the axial forces acting on piston 370 are balanced. The hydraulic fluid in chamber section 360a is in fluid communication with motor housing 310 via end cap port 357, and is in fluid communication with hydraulic pump chambers 220, 230, 240 via clearances between pump housing end cap 213 and driveshaft shaft 298. Accordingly, if the volume, and associated pressure, of hydraulic fluid in pump 200, motor 300, and/or compensator 350 increases, it can be accommodated by compensator 350. Conversely, if the volume, and associated pressure, of hydraulic fluid in pump 200, motor 300, and/or compensator decreases (e.g., if any hydraulic fluid is lost due to seal leaks etc.), it can be replenished by hydraulic fluid from compensator 350.
Referring now to
Coupling 410 connects separator 400 to compensator 350 and has a first or upper end 410a coupled to compensator end cap 354 and a second or lower end 410b secured to cyclonic separation assembly 420. In this embodiment, coupling 410 includes a frustoconical recess 411 extending axially from upper end 410a, and a throughbore 412 extending axially from recess 411 to lower end 410b. A vortex tube 413 in fluid communication with bore 412 extends axially downward from lower end 410b into cyclonic separation assembly 420. Recess 411, bore 412, and tube 413 are coaxially aligned with axis 405, and together, define a flow passage 415 that extends axially through coupling 410 and into assembly 420. As will be described in more detail below, processed well fluids 15 flow from separation assembly 420 through passage 415 into device 30. Thus, passage 415 may also be referred to as a processed fluid outlet.
Referring still to
Referring now to FIGS. 4G and 10-13, intake member 430 is coaxially disposed in upper end 421a of housing 421 and extends axially from lower end 410b of coupling 410. In this embodiment, intake member 430 includes a feed tube 431 and an elongate fluid guide member 435 disposed about feed tube 431. Feed tube 431 is coaxially disposed about and radially spaced from vortex tube 413. Consequently, an annulus 434 is formed radially between tubes 413, 431. In addition, feed tube 431 has a first or upper end 431a engaging lower end 410b, a second or lower end 431b distal coupling 410, an outer radius R431, and a length L431 measured axially between ends 431a, b. As best shown in
Guide member 435 has a first or upper end 435a engaging coupling lower end 410b and a second or lower end 435b distal coupling 410. In this embodiment, guide member 435 is an elongate thin-walled structure oriented parallel to feed tube 431. Guide member 435 may be divided into a first section or segment 436 disposed at a uniform radius R436 that is greater than radius R431 of feed tube 431, and a second section or segment 437 that extends from first segment 436 and curves radially inward to feed tube 431. Thus, guide member 435 is disposed about feed tube 431 and generally spirals radially inward to feed tube 431. As best shown in
Referring again to FIGS. 4G and 10-13, second segment 437 has a first end 437a contiguous with second end 436b of first segment 436 and a second end 437b that engages feed tube 431. Thus, first end 437a is disposed at radius R436, however, second end 437b is disposed at radius R431. Consequently, moving from end 437a to end 437b, second segment 437 curves radially inward toward feed tube 431. First end 437a is circumferentially positioned to one side of inlet port 436, and second end 437b is circumferentially positioned on the opposite side of inlet port 436. Thus, second segment 437 extends circumferentially across inlet port 436.
A base member 438 extends radially from guide member 435 to feed tube 431, thereby enclosing guide member 435 at lower end 435b and defining a spiral flow passage 439 within intake member 430. In other words, base 438, lower end 410b of coupling 410, and guide member 435 define spiral flow passage 439, which extends from an inlet 439a at end 436a to feed tube port 432. In
First segment 436 has a uniform height H436 measured axially from end 435a to base member 438, and second segment 437 has a variable height H437 measured axially from end 435a to base member 438. Thus, between ends 436a,b of first segment 436, base member 438 is generally flat, however, moving from end 437a to end 437b of second segment 437, base member 438 curves upward. Height H436 is less than height H431, and thus, feed tube 431 extends axially downward from guide member 435. Further, in this embodiment, height H437 is equal to height H436 at end 437a, but linearly decreases moving from end 437a to end 437b. The decrease in height H437 moving from end 437a to end 437b causes fluid flow through passage 439 to accelerate into port 432.
During operation of separator 400, well fluids 14 enter housing 421 through separator inlet ports 422, and flow axially upward within housing 421 and into passage 439 of cyclone intake member 430 via inlet 439a. Flow passage 439 guides well fluids 14 circumferentially about feed tube 431 toward feed tube port 432. As the radial distance between guide member 435 and feed tube 431 decreases along second segment 437, well fluids 14 in passage 439 are accelerated and directed through feed tube port 432 into feed tube 431. As best shown in
Referring now to
In this embodiment, cyclone body 440 includes an upper converging member 442 extending axially from end 440a, a lower diverging member 443 extending axially from end 440b, and a intermediate tubular member 444 extending axially between members 442, 443. Each member 442, 443, 444 has a first or upper end 442a, 443a, 444a, respectively, and a second or lower end 442b, 443b, 444b, respectively.
Tubular member 444 is an elongate tube having a length L444 measured axially between ends 444a, b, and a constant or uniform inner radius R444 along its entire length L444. Converging member 442 has a frustoconical radially outer surface 445a and a frustoconical radially inner surface 445b that is parallel to surface 445a. In addition, converging member 442 has a length L442 measured axially between ends 442a, b, and an inner radius R445b that decreases linearly moving downward from end 442a to end 442b. In particular, radius R445b is equal to inner radius R431 of feed tube 431 at upper end 442a, and equal to inner radius R444 of tubular member 444 at end 442b.
Lower diverging member 443 has a frustoconical radially outer surface 446a and a frustoconical radially inner surface 446b that is parallel to surface 446a. In addition, diverging member 443 has a length L443 measured axially between ends 443a, b, and an inner radius R446b that increases linearly moving downward from end 443a to end 443b. In particular, radius R446b is equal to inner radius R431 of feed tube 431 at upper end 443a, and slightly less than inner radius R421 of housing 421 at end 443b. The dimensions of members 442 and 444 are fundamental to strength of the cyclone formed within the device.
Referring now to
Converging member 455 has an upper end 455a that axial abuts annular shoulder 453 and a lower end 455b disposed axially below housing lower end 451b. Thus, member 455 is disposed within and extends axially from housing 451. Converging member 455 has a frustoconical radially inner surface 456 disposed at a radius R456 that decreases moving axially downward from end 455a to end 455b.
Referring now to
As best shown in
Referring again to
Referring again to
Referring now to
Referring now to
Well fluids 14 flow into cyclonic separation assembly 420 via ports 422, and upon entering cyclonic separation assembly 420, flow axially upward within annulus 447 to cyclone intake member 430. At intake member 430, well fluids 14 enter spiral flow passage 439 at inlet 439a. Flow passage 439 guides well fluids 14 circumferentially about feed tube 431 toward feed tube port 432 and accelerates well fluids 14 therein as they approach port 432. Well fluids 14 flow tangentially into feed tube 431 and are partially aided by vortex tube 413 to form a cyclonic or spiral flow pattern within feed tube 431. As well fluids 14 spiral within feed tube 431, they also moves axially downward towards the lower end of vortex tube 413 under the influence of the low pressure region in passage 415.
The solids and particulate matter in well fluids 14 with sufficient inertia, designated as solids 16, begin to separate from the liquid and gaseous phases in well fluids 14 and move radially towards the inner surface of feed tube 431. Eventually solids 16 strike the inner surface of feed tube 431 and fall under the force of gravity into converging member 442. The liquid and gaseous phases in well fluids 14, as well as the relatively low inertia particles remaining therein, (i.e., processed well fluids 15) continue their cyclonic flow in feed tube 431 as they move towards the lower end of vortex tube 413. When processed well fluid 15 reach the lower end of vortex tube 413, they are sucked in passage 415 and are ejected from separator 400 into conduit 205 and flow to fluid end pump 110.
After separation, solids 16 fall through passage 441 of cyclone body 440 under the force of gravity into upper solids collection assembly 450. Trap door assembly 460 is normally biased to the closed position, however, when the accumulation of solids 16 in funnel 455 applies a sufficient load to door 471, trap door assembly 460 will open and allow solids 16 to fall through bore 464 into lower solids collection assembly 450′. Similar to upper solids collection assembly 450, trap door assembly 460 of lower solids collection assembly 450′ is normally biased to the closed position. However, when the accumulation of solids 16 in funnel 455 applies a sufficient load to door 471, trap door assembly 460 opens and allow solids 16 to fall through bore 464 into tubular 481. Solids 16 continue to fall downward and pass through holes 482 in screen 480, thereby exciting separator 400.
Disruption of the cyclonic flow of well fluids 14 in feed tube 431 may negatively impact the ability of separator 400 to separate solids 16 from well fluids 14. However, the use of two trap door assemblies 460 in a serial arrangement offers the potential to minimize the impact on the cyclonic flow within feed tube 431. In particular, the low pressure region in passage 415 has a tendency to pull fluids in passage 441 and housing 451 of upper solids collection assembly 450 upward into vortex tube 413. However, since trap door assembly 460 of upper solids collection assembly 450 is biased closed, upward fluid flow in passage 441 and housing 451 is restricted and/or prevented. Namely, when trap door assembly 460 is closed, passage 441 and housing 451 of upper solids collection assembly 450 function like a sealed tank, if fluid is pulled upward from passage 441 and housing 451a vacuum is created therein which works against such upward fluid flow. As the weight of solids 16 in upper solids collection assembly 450 overcome counterweight 472, trap door assembly 460 opens and allows solids 16 to fall from upper solids collection assembly 450 to lower solids collection assembly 450′. This temporarily allows fluid communication between passage 415 and both housings 451 of assemblies 450, 450′. However, as previously described, trap door assemblies 460 are configured such that each is not opened at the same time. Thus, when trap door assembly 460 of upper assembly 450 is open, trap door assembly 460 of lower assembly 450′ is closed. Consequently, when trap door assembly 460 of upper assembly 450 is temporarily opened to allow solids 16 to pass into lower assembly 450′, upward fluid flow in passage 441 and housings 451 is restricted and/or prevented. Namely, when trap door assembly 460 of upper assembly 450 is open, passage 441 and housings 451 function like a sealed tank.
When trap door assembly 460 of assembly 450 is open, solids 16 fall from upper assembly 450 into lower assembly 450′. Trap door assembly 460 of lower assembly 450′ remains closed as solids 16 fall therewithin. Once a sufficient quantity of the solids in funnel 455 of upper assembly 450 have passed bore 464, trap door assembly 460 of upper assembly 450 will again close. The solids 16 begin to accumulate within funnel 455 of lower assembly 450′ until the load on door 471 of lower assembly 450′ is sufficient to overcome counterweight 472 of lower assembly 450′. In the manner described, upward fluid flow in passage 441 and housings 451 into passage 415 is restricted and/or prevented. As a result, disruption of cyclonic flow of well fluids 14 in feed tube 431 is minimized and/or eliminated.
In this embodiment, separator 400 is designed for substantially vertical deployment. In substantially horizontal deployment of the deliquification pump (e.g., pump 100), separator 400 may be eliminated and replaced with a different type of separator capable of operation in a substantially horizontal orientation, inlet screens or filters, or combinations thereof.
Referring now to
Fluid end pump 110 is driven by hydraulic pump 200, and hydraulic pump 200 is driven by electric motor 300. Conductors 46 in spoolable tubing 40 provide electrical power downhole to motor 300, which powers the rotation of motor driveshaft 320, hydraulic driveshaft 298, and wobble plates 270. As plates 270 rotate, hydraulic fluid in pump chambers 220, 230 is cyclically supplied to pistons 255 via slots 272, compressed in pistons 255, and then passed to shuttle valve assembly 130 of fluid end pump 110 via branches 215, 216 and passages 214, 117, 113. Shuttle valve assembly 130 alternates the supply of compressed hydraulic fluid to chamber sections 121b, 125b, thereby driving the reciprocation of fluid end pump pistons 122, 126. Use of hydraulic pump 200 in conjunction with fluid end pump 110 offers the potential to generate the relatively high fluid pressures necessary to force or eject relatively low volumes of well fluids 15 to the surface 11. In particular, hydraulic pump 200 converts mechanical energy (rotational speed and torque) into hydraulic energy (reciprocating pressure and flow), and is particularly deigned to generate relatively high pressures at relatively low flowrates and at relatively high efficiencies. The addition of fluid end pump 110 allows for an isolated closed loop hydraulic pump system while limiting wellbore fluid exposure to fluid end pump 110. This offers the potential for improved durability and reduced wear. The fluid end pump only has minor hydraulic losses and for the most part is a direct relationship to the pressure output of the hydraulic system. In addition, the variable speed output capability of the system allows for variable pressure and flow output of the fluid end pump.
In general, the various parts and components of deliquification pump 100 may be fabricated from any suitable material(s) including, without limitation, metals and metal alloys (e.g., aluminum, steel, inconel, etc.), non-metals (e.g., polymers, rubbers, ceramics, etc.), composites (e.g., carbon fiber and epoxy matrix composites, etc.), or combinations thereof. However, the components of pump 100 are preferably made from durable, corrosion resistant materials suitable for use in harsh downhole conditions such steel. Although deliquification pump 100 is described in the context of deliquifying gas producing wells, it should be appreciated that embodiments of deliquification pump 100 described herein may also be used in oil wells.
While preferred 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 invention. For example, the relative dimensions of various parts, the materials from which the various parts are made, and other parameters can be varied. 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.
This application claims benefit of U.S. provisional patent application Ser. No. 61/289,440 filed Dec. 23, 2009, and entitled “Rigless Low Volume Pump System,” which is hereby incorporated herein by reference in its entirety.
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