The present disclosure is directed to a system comprising a fluid end and a plunger configured to reciprocate within the fluid end. The fluid end has an internal cavity formed therein. The plunger comprises a first surface exposed to the cavity. A blind bore is formed in the first surface, and the blind bore may extend at least one-half the length of the plunger.
In another aspect, the present disclosure is directed to a system comprising a plunger configured to reciprocate within a fluid end. The plunger comprises a first surface resident within the fluid end and a blind bore formed in the first surface of the plunger. The system further comprises a heat exchanger situated within the blind bore. The heat exchanger is made of a material having a higher thermal conductivity than the plunger.
In another aspect, the present disclosure is directed to a system comprising a fluid end and an elongate plunger reciprocable (configured to reciprocate) within the fluid end. The fluid end has an internal cavity within which a working fluid is flowable. The plunger has a first end exposed to the cavity and an opposed second end not exposed to the cavity. The plunger comprises a blind bore formed in the first end. The bore may extend at least one-half the length of the plunger.
High pressure reciprocating pumps typically comprise a power end assembly attached to a fluid end assembly. Fluid end assemblies are typically used in oil and gas operations to deliver highly pressurized corrosive and/or abrasive fluids to piping leading to the wellbore. The assemblies are typically attached to power ends run by engines. The engine crankshaft is attached to a transmission input shaft, the transmission output shaft is connected to a gearbox input shaft, and the gearbox output shaft is attached to the power end crankshaft. The power end crankshaft reciprocates plungers within the fluid end assembly to pump fluid through the fluid end.
Fluid may be pumped through the fluid end at pressures that range from 5,000-15,000 pounds per square inch (psi). However, the pressure may reach up to 22,500 psi. Power ends typically have a power output of at least 2,250 horsepower during hydraulic fracturing operations. A single fluid end typically delivers a fluid volume of about 185-690 gallons per minute or 4-16 barrels per minute during a fracking operation. When a plurality of fluid ends are used together, the fluid ends may collectively deliver about 4,200 gallons per minute or 100 barrels per minute to the wellbore.
Because high pressure reciprocating pumps operate at such high pressures and volumes, one common issue is the overheating of parts. Specifically, fluid end assemblies experience overheating in areas where components wear against each other, or where components expand and retract relative to each other. Areas of particular concern are the components that wear against the reciprocating plunger, such as the plunger packing. High rates of reciprocation, along with tight tolerances between components, leads to an increase in temperatures that causes parts to expand. Such expansion, in addition to high temperatures in general, causes parts to experience significant wear. When components or parts wear beyond a certain critical point, they need to be replaced. This costs valuable time and money. There is therefore an existing need to reduce temperatures of internal components within fluid ends which in turn would reduce friction and increase component life.
The present disclosure describes a liquid cooled plunger system designed to reduce temperatures of a plunger which reciprocates within a fluid end. This leads to longer lifespans of the plunger packing and other related components. In this system, a blind bore may be formed in the front surface of the plunger, which is configured to be exposed to the internal chamber or cavity formed within the fluid end. Such bore may extend a depth of at least half of the length of the plunger.
In a preferred embodiment, the bore will extend far enough into the plunger so that the bore is constantly surrounded by the plunger packing when the plunger is in operation. This means that when the plunger is situated in a maximally inserted, or fully extended, position, the plunger packing surrounds the plunger in such a way that the packing also surrounds at least a portion of the bore. Likewise, when the plunger is situated in a minimally inserted, or fully retracted, position, the plunger packing surrounds the plunger in such a way that the packing surrounds at least a portion of the bore. When the plunger is in any position between the maximally and minimally inserted positions, the plunger packing surrounds the plunger so that the packing surrounds at least a portion of the bore.
As discussed herein, the bore within the plunger is configured to reduce the temperature of the plunger. This leads to an extended life of the plunger packing, as well as other parts.
In some embodiments, the plunger's blind bore is filled with a heat exchanger. The heat exchanger may be formed of a different material than the plunger. The heat exchanger may be solid, or may have bores or passages formed therein. The heat exchanger may be made of a material having a higher thermal conductivity than the material used to form the plunger. This allows the heat exchanger to transfer more heat to the surrounding working fluid within the fluid end, and therefore cool the plunger more effectively than if the heat exchanger were made from the same material as the plunger. The heat exchanger may have a plurality of passages surrounding a central passage. Fluid may flow into and out of the end of the blind bore or the plurality of passages.
A retaining element may be used to hold the heat exchanger within the bore. This retaining element may be a variety of things, such as a snap ring or plug. If the retaining element is a plug, the plug may be secured within the bore by press fit, or other securing methods. The plug may also be positioned at least partially inside of a heat exchanger. The plug may have an internal cavity, which is in fluid communication with the cavity formed inside of the fluid end.
In some embodiments, the bore within the plunger may receive an element which is not mechanically coupled to the plunger. Such element may be fixed to another component within the fluid end, such as a plug or a valve. The plunger may reciprocate over this element to facilitate circulation of fluid within the bore. This circulation of fluid leads to cooler temperatures within the plunger. The element may also be configured such that a heat exchanger situated within the blind bore may reciprocate over the element. The element may be stationary relative to the plunger. In other embodiments, the element may move relative to the plunger.
In some embodiments, an object may be at least partially resident within the bore of the plunger. Such object may be in a mechanically uncoupled relationship with the plunger. One example of such object is a ball, such as a ball used in ball valves. The ball may have a slightly smaller outer diameter than the diameter of the blind bore, so that the ball can freely roll inside of the bore. The ball may also be positioned within a heat exchanger and operate similarly to what is discussed above. The ball may be restricted from exiting the bore or heat exchanger by a valve seat, or a smaller diameter of the bore or valve seat, as discussed herein.
The liquid cooled plunger systems and components disclosed herein may be used in various types of fluid ends, fluid end sections, fluid end assemblies, and other types of pumps configured to use plungers.
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The fluid end section 200 also comprises a housing 202 having a horizontal bore 204 formed therein. Fluid enters the housing 202 through one or more suction bores 206 and exits the housing 202 through one or more discharge bores 208. Fluid is routed throughout the housing 202 by a fluid routing plug 210. Movement of fluid throughout the fluid routing plug 210 is controlled by a suction valve 212 and a discharge valve 214. The valves 212 and 214 are configured to seat against opposite surfaces of the fluid routing plug 210.
As described herein, multiple embodiments of the liquid cooled plunger system may be used within either the fluid end 10, or the fluid end section 200. Additionally, multiple embodiments of the liquid cooled plunger system may be used within other fluid ends, fluid end sections, or high pressure reciprocating pumps known in the art. In short, the liquid cooled plunger system may be used in many types of pumps.
Turning to
During operation, the plunger 20 reciprocates within housing 12, specifically the horizontal bore 14 and the internal chamber 18, to pressurize fluid within the housing 12. The plunger 20 is reciprocable between a maximally inserted or fully extended position, and a minimally inserted or fully retracted position.
Continuing with
In short, the plunger packing 32 is configured to surround the blind bore 42 while the plunger 20 is in both the maximally and minimally inserted positions, as well as all positions between.
The suction plug 22 also has a blind bore 44 formed therein and opening on a rear surface 46 of the suction plug 22. Installed within the blind bore 44 and projecting out and away from the suction plug 22 is an elongate stem 48. The stem 48 is positioned to extend into the blind bore 42 formed within the plunger 20. During operation, the stem 48 stays in one place and the plunger 20 reciprocates back and forth over the stem 48. Movement of the plunger 20 over the stem 48 causes the stem 48 to force fluid within the blind bore 42 of the plunger 20 to circulate or flow therein. Insertion of the stem 48 within the blind bore 42 forces the fluid to exit the blind bore 42. This allows new fluid to enter the blind bore 42 during operation, cooling the plunger 20.
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The plunger 20 comprises opposed first and second surfaces 88 and 36. The first surface 88 may also be referred to as a front surface. Likewise, the second surface 36 may also be referred to as a rear surface. Further, the first and second surfaces 88 and 36 may also be referred to as first and second ends. The first surface 88 is configured to stay within the fluid end 10 or fluid end section 200 during operation, while the second surface 36 is configured to protrude from the fluid end 10/fluid end section 200 during operation. Likewise, the first surface 88 is configured to be exposed to the internal chamber 18 or horizontal bore 204, while the second surface 36 is not.
The surfaces 88 and 36 are joined by an intermediate outer surface 34. The intermediate outer surface 34 is configured to contact the plunger packing 32/232. As described herein, the blind bore 42 is formed within the first surface 88 of plunger 20. The blind bore 42 may receive various objects or components, as described herein. In some embodiments, the blind bore 42 may be in fluid communication with the internal chamber 18 or horizontal bore 204. In alternative embodiments discussed herein, the blind bore 42 may not be in fluid communication with the internal chamber 18 or horizontal bore 204.
Turning now to
In alternative embodiments, the stem 48 may have a cavity formed therein to reduce any unnecessary weight.
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With reference to
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Continuing with
The seat 86 comprises a central opening 89 sized to be blocked by the ball 84, as shown in
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The liquid cooled plunger system 90 can be used within the fluid end 10, as shown in
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Referring now to
The front surface 308 of the heat exchanger 302 is perpendicular to the longitudinal axis of the heat exchanger 302. The rear surface 309 is perpendicular to the longitudinal axis of the heat exchanger 302 and comprises an outer lip 313 and a countersink 314. The countersink 314 comprises an angled side wall 315 and a base 316. The intermediate outer surface 310 comprises a body 317, a chamfer 318 adjacent the rear surface 309, a nose 319 adjacent the front surface 308 having a smaller diameter than the body 317, and a shoulder 320 adjacent the rear of the nose 319 formed by the diametral difference between the body 317 and nose 319.
Each passage 311 has a circular cross section with a longitudinal axis parallel to the longitudinal axis of the heat exchanger 302. Each passage 311 intersects the front surface 308 at one end and primarily the base 316 of the countersink 314 and partially the angled side wall 315 at the opposite end. The plurality of passages 311 are evenly spaced circumferentially proximate the intermediate outer surface 310. The passages 311 do not intersect the intermediate outer surface 310 of the nose 319. In this embodiment there are eight passages 311 spaced 44-46 degrees apart with 45 degrees preferred. In alternate embodiments there may be greater or fewer passages 311 which may be larger or smaller and have different circumferential spacing that is even or not. The cross section is circular but may have any shape.
The central passage 312 comprises a ball bore 321, a trap bore 322, and a shoulder 323. The longitudinal axes of the central passage 312, ball bore 321, and trap bore 322 are coincident with each other and with the longitudinal axis of the heat exchanger 302. The ball bore 321 has a circular cross section with a diameter that is larger than the diameter of the ball 303 and the diameter of the trap bore 322. The first end of the ball bore 321 intersects the base 316 of the countersink 314. The second end of the ball bore 321 terminates at the second end of the trap bore 322. The trap bore 322 comprises an internal thread 324 and countersink 325. The first end of the trap bore 322 intersects the front surface 308 and the second end of the trap bore 322 terminates at the second end of the ball bore 321. The internal thread 324 is formed in the wall of the trap bore 322. The countersink 325 is formed on the first end of the trap bore 322. The diameter of the trap bore 322 is smaller than the diameter of the ball 303. Shoulder 323 is formed at the intersection of the ball bore 321 and trap bore 322 due to the diametral difference between the ball bore 321 and trap bore 322. In this embodiment the length of the ball bore 321 is approximately ten times the length of the trap bore 322 and the internal thread 324 spans the entire length of the trap bore 322. In alternative embodiments the ratio of the length of the ball bore 321 to the trap bore 322 may be greater or smaller and the internal thread 324 may not span the entire length of the trap bore 322 or may be omitted. Also in alternative embodiments the diameters of the ball bore 321 and trap bore 322 may vary as long as the relationship between the diameters is such that the diameter of the ball bore 321 is always greater than the diameter of the ball 303 and the diameter of the ball 303 is always greater than the diameter of the trap bore 322.
The ball 303 is solid and generally shaped like a sphere. The ball 303 may be made of a relatively dense material such as a lead alloy or a tungsten alloy. The diameter of the ball 303 is smaller than the diameter of the ball bore 321 and larger than the diameter of the trap bore 322. In this embodiment the ball 303 is a sphere but in alternative embodiments may have any shape as long as the shape allows the ball 303 to be retained in the ball bore 321 by the trap bore 322.
The retainer 304 is a standard internal snap ring well known in the art. In this embodiment the retainer 304 is an internal snap ring but in alternative embodiments may not be an internal snap ring.
Continuing with
Once the liquid cooled plunger system 300 is assembled it may be used in fluid end 10 (depicted in
In operation the liquid cooled plunger system 300 reduces the surface temperature of the plunger 301. This reduction in temperature also reduces the temperature of the plunger packing 32/232 thus increasing the life of the plunger packing 32/232. The temperature reduction is accomplished by transferring the heat generated by the friction between the outer surface of the plunger 301 and the plunger packing 32/232 away from the surface of the plunger 301. The close contact of the heat exchanger 302 with the heat exchanger bore 306 and the higher thermal conductivity of the heat exchanger 302 as compared to that of the plunger 301 facilitates the heat flow from the plunger 301 to the heat exchanger 302. Once the heat is transferred to the heat exchanger 302 the heat is then transferred to the fluid being pumped by contact between the fluid and the surfaces of the passages 311, central passage 312, base of the heat exchanger bore 306, and the rear surface 309 of the heat exchanger 302.
The fluid within the passages 311 and central passage 312 is made to flow by the ball 303. Flow is caused by the relative movement of the ball 303 to the heat exchanger 302. Since the ball 303 has a higher density than the fluid, the ball 303 will have a tendency to not move, or not move as much as the heat exchanger 302 while the plunger 301 reciprocates. When the plunger 301 is on the retraction part of its stroke the ball 303 will cause fluid to be drawn into the passages 311. When the plunger 301 is on the insertion part of its stroke the ball 303 will cause fluid to be expelled out of the passages 311. The diameter of the ball 303 is small enough to allow flow around the ball 303 within the central passage 312 as needed. The smaller diameter of the trap bore 322 will keep the ball 303 trapped between the shoulder 320 and the base of the heat exchanger bore 306. The plenum 326 allows fluid to pass between the passages 311 and the central passage 312 as needed. During the time the fluid is drawn into the heat exchanger 302 and expelled out of the heat exchanger 302 the fluid is absorbing heat. Once the fluid is expelled the heat is carried with the fluid away from the pump. Thus each stroke of the plunger 301 carries heat away from the plunger packing 32/232, reducing its temperature and increasing the life of the plunger packing 32/232.
Referring now to
The retainer 404 may be a spanner nut 404 well known in the art. The spanner nut 404 comprises a front surface 427 and a rear surface 428 connected by an intermediate outer surface 429. The intermediate outer surface 429 comprises an external thread 430. The spanner nut 404 further comprises a plurality of spanner wrench holes 431 and a central passage 432. Each spanner wrench hole 431 is a through bore with a bore axis parallel to the longitudinal axis of the spanner nut 404. There are an even number of spanner wrench holes 431 which are diametrically opposed and evenly spaced circumferentially proximate the intermediate outer surface 429. The spanner wrench holes 431 do not intersect the intermediate outer surface 429 or the central passage 432. In this embodiment there are two spanner wrench holes 431 spaced 179-181 degrees apart with 180 degrees preferred. In alternate embodiments there may be greater or fewer spanner wrench holes 431, but only in even numbers, which may be larger or smaller and have different circumferential spacing that is even or not as long as there is always a pair of spanner wrench holes 431 diametrically opposite each other.
In this embodiment the retainer 404 is a spanner nut, but in alternative embodiments the retainer 404 may not be a spanner nut but still have external threads 430.
The liquid cooled plunger system 400 is assembled by first inserting the ball 303 in the ball bore 321. Second, the heat exchanger 302 is inserted in the heat exchanger bore 406 of the plunger 401 until the rear surface 309 of the heat exchanger 302 abuts the base of the heat exchanger bore 406 forming a plenum 426. The fit between the body 317 of the heat exchanger 302 and the inside diameter of the heat exchanger bore 406 is preferably a clearance fit but may be an interference fit or transition fit. Insertion of the heat exchanger 302 may be facilitated by threading a bolt or other assembly aid (not shown) into the internal thread 324 of the trap bore 322. Disassembly will also be facilitated by the use of a bolt or other assembly aid (not shown) threaded in the internal thread 324 of the trap bore 322. Third, the retainer 404, or spanner nut 404, is threaded into the internal thread 407 of the heat exchanger bore 406 until the rear surface 428 of the spanner nut 404 abuts the shoulder 320 of the heat exchanger 302.
Once the liquid cooled plunger system 400 is assembled it may be used in fluid end 10 (depicted in
In operation the liquid cooled plunger system 400 operates exactly the same as liquid cooled plunger system 300.
Referring now to
In contrast to the other heat exchangers disclosed herein, the heat exchanger 502 does not include any fluid through-bores. Instead, the heat exchanger 502 is solid and made of a material having a higher thermal conductivity than the material forming the plunger 501. For example, if the plunger 501 is made of steel, the heat exchanger 502 may be made of aluminum. During operation, the aluminum heat exchanger 502 absorbs heat from the steel plunger 501, thereby cooling the plunger 501. In alternative embodiments, the heat exchanger 502 may be made of other materials known in the art to have a higher thermal conductivity than that making up the plunger 501.
The liquid cooled plunger system 500 is assembled by inserting the heat exchanger 502, rear surface 509 first, in the heat exchanger bore 506 of the plunger 501 until the rear surface 509 of the heat exchanger 502 abuts the base of the heat exchanger bore 506. The fit between the body 517 of the heat exchanger 502 and the inside diameter of the heat exchanger bore 506 is preferably an interference fit or transition fit. This embodiment is not intended to be disassembled but may be if desired.
Once the liquid cooled plunger system 500 is assembled it may be used in fluid end 10 (shown in
In operation the liquid cooled plunger system 500 reduces the surface temperature of the plunger 501. This reduction in temperature also reduces the temperature of the plunger packing 32/232 thus increasing the life of the plunger packing 32/232. The temperature reduction is accomplished by transferring the heat generated by the friction between the outer surface of the plunger 501 and the plunger packing 32/232 away from the surface of the plunger 501. The close contact of the heat exchanger 502 with the heat exchanger bore 506 and the higher thermal conductivity of the heat exchanger 502 as compared to that of the plunger 501 facilitates the heat flow from the plunger 501 to the heat exchanger 502. Once the heat is transferred to the heat exchanger 502 the heat is then transferred to the fluid being pumped by contact between the fluid and the front surface 508 of the heat exchanger 502.
Referring now to
The front and rear surfaces 608 and 609 of the heat exchanger 602 are perpendicular to the longitudinal axis of the heat exchanger 602. The intermediate outer surface 610 comprises a body 617, a chamfer 618 adjacent the rear surface 609, a nose 619 adjacent the front surface 608 having a smaller diameter than the body 617, and a shoulder 620 adjacent the rear of the nose 619 formed by the diametral difference between the body 617 and nose 619.
The longitudinal axis of the installation bore 622 is coincident with the longitudinal axis of the heat exchanger 602. The installation bore 622 is a blind bore that comprises an internal thread 624 and countersink 625. The installation bore 622 originates from the front surface 608. The internal thread 624 is formed in the wall of the installation bore 622. The countersink 625 is formed on the front surface 608.
Continuing with
Once the liquid cooled plunger system 600 is assembled it may be used in fluid end 10 (shown in
In operation the liquid cooled plunger system 600 operates exactly the same as liquid cooled plunger system 500. The installation bore 622 provides more surface area for the fluid to contact than heat exchanger 502 which may increase the heat transfer rate from the heat exchanger 602 to the fluid.
Referring now to
The liquid cooled plunger system 700 is assembled by first inserting the heat exchanger 602, rear surface 609 first, in the heat exchanger bore 406 of the plunger 401 until the rear surface 609 of the heat exchanger 602 abuts the base of the heat exchanger bore 406. The fit between the body 617 of the heat exchanger 602 and the inside diameter of the heat exchanger bore 406 is preferably a clearance fit but may be an interference fit or transition fit. Insertion of the heat exchanger 602 may be facilitated by threading a bolt or other assembly aid (not shown) into the internal thread 624 of the installation bore 622. Disassembly may also be facilitated by the use of a bolt or other assembly aid (not shown) threaded in the internal thread 624 of the installation bore 622. Next, the retainer 404, or spanner nut 404, is threaded into the internal thread 407 of the heat exchanger bore 406 until the rear surface 428 of the spanner nut 404 abuts the shoulder 620 of the heat exchanger 602.
Once the liquid cooled plunger system 700 is assembled it may be used in fluid end 10 (shown in
In operation the liquid cooled plunger system 700 operates exactly the same as liquid cooled plunger system 500. The installation bore 622 provides more surface area for the fluid to contact than heat exchanger 502 which may increase the heat transfer rate from the heat exchanger 602 to the fluid.
Referring now to
Referring now to
The front surface 808 and rear surface 809 of the heat exchanger 802 are perpendicular to the longitudinal axis of the heat exchanger 802. The intermediate outer surface 810 comprises a chamfer 818 adjacent the rear surface 809.
The retainer 804 may be a standard spiral retaining ring well known in the art. In this embodiment the retainer 804 is a spiral retaining ring, but in alternative embodiments the retainer 804 may be an internal snap ring.
The plug 833, shown in
The seal 834 is a standard D-ring seal well known in the art. In alternative embodiments the seal 834 may be an O-ring seal or other type of seal.
Continuing with
Once the liquid cooled plunger system 800 is assembled it may be used in fluid end 10 (shown in
In operation the liquid cooled plunger system 800 reduces the surface temperature of the plunger 801. This reduction in temperature also reduces the temperature of the plunger packing 32/232 thus increasing the life of the plunger packing 32/232. The temperature reduction is accomplished by transferring the heat generated by the friction between the outer surface of the plunger 801 and the plunger packing 32/232 away from the surface of the plunger 801. The close contact of the heat exchanger 802 with the heat exchanger bore 806 and the higher thermal conductivity of the heat exchanger 802 as compared to that of the plunger 801 facilitates the heat flow from the plunger 801 to the heat exchanger 802. Once the heat is transferred to the heat exchanger 802 the heat is then transferred to the fluid being pumped by contact between the fluid and the surfaces of the plug 833, base of the heat exchanger bore 806, and the rear surface 809 of the heat exchanger 802. Alternatively, if the pump is only going to be used for a short while, the heat exchanger 802 may absorb the heat produced, cooling the plunger 801 for the period of operation.
Also in operation, the seal 834 prevents fluid from entering the heat exchanger bore 806. Eliminating fluid within the heat exchanger bore 806 also eliminates corrosion within the heat exchanger bore 806 specifically between contacting surfaces of the heat exchanger 802 and plunger 801. Absence of corrosion allows easier removal of the heat exchanger 802 if desired. Absence of corrosion also eliminates the opportunity for stress corrosion cracking of the plunger 801.
Also in operation, the heat exchanger 802, made of aluminum in this embodiment, results in an overall lighter weight of the liquid cooled plunger system 800 than a comparable plunger system made entirely of steel. This reduced weight results in easier field maintenance for operators. The reduced weight also results in less weight on the plunger packing 32/232 during operation. Since the friction force is a function of the normal force, in this case the weight of the liquid cooled plunger system 800, the friction force will be reduced thus reducing the heat caused by the friction force resulting in a longer packing life.
Referring now to
Referring now to
The front surface 908 and rear surface 909 of the heat exchanger 902 are perpendicular to the longitudinal axis of the heat exchanger 902. The intermediate outer surface 910 comprises a chamfer 918 adjacent the rear surface 909. The plug bore 941 is a through bore connecting the front surface 908 and rear surface 909. The plug bore 941 is concentric with the intermediate outer surface 910 and comprises a front chamfer 942, adjacent the front surface 908, and a rear chamfer 943, adjacent the rear surface 909.
The retainer 904 is a standard spiral retaining ring well known in the art. In this embodiment the retainer 904 is a spiral retaining ring but in alternative embodiments may be an internal snap ring.
The plug 933, shown in
The intermediate outer surface 937 comprises a plurality of concentric sections, all of the sections are circular. Beginning at the front surface 908 of the heat exchanger 902 and continuing to the rear surface 909 the sections are a nose 919, a retaining ring shoulder 920, a plunger section 947, a heat exchanger shoulder 948, a transition chamfer 949, a heat exchanger section 950, and a rear chamfer 951. The plunger section 947 comprises a seal groove 938. The seal groove 938 may comprise a base 939 and side walls 940. The base 939 is parallel to the longitudinal axis of the plug 933 and the side walls 940 are perpendicular to the base 939.
The diameter of the plunger section 947 is sized to have a tight transition to light interference fit with the heat exchanger bore 906. The diameter of the nose 919 is smaller than the diameter of the plunger section 947 and is sized to allow the compression and installation of the retainer 904. The seal groove 938 is configured to receive the seal 934. The diameter of the heat exchanger section 950 is sized to have a tight transition to light interference fit with the plug bore 941 of the heat exchanger 902.
The seal 934 is a standard O-ring seal well known in the art. In alternative embodiments the seal 934 may be a D-ring seal or other type of seal.
Continuing with
Once the liquid cooled plunger system 900 is assembled it may be used in fluid end 10 (shown in
In operation the liquid cooled plunger system 900 reduces the surface temperature of the plunger 901. This reduction in temperature also reduces the temperature of the plunger packing 32/232 thus increasing the life of the plunger packing 32/232. The temperature reduction is accomplished by transferring the heat generated by the friction between the outer surface of the plunger 901 and the plunger packing 32/232 away from the surface of the plunger 901. The close contact of the heat exchanger 902 with the heat exchanger bore 906 and the higher thermal conductivity of the heat exchanger 902 as compared to that of the plunger 901 facilitates the heat flow from the plunger 901 to the heat exchanger 902. Once the heat is transferred to the heat exchanger 902 the heat is then primarily transferred to the plug 933, specifically the heat exchanger section 950 of the intermediate outer surface 937. The heat is then transferred to the fluid being pumped by contact between the fluid and the surfaces of the cooling bore 944 of the plug 933. The heat is carried away by the fluid as it flows in and out of the cooling bore 944 during the operation of the plunger 901.
Also in operation the seal 934 prevents fluid from entering the heat exchanger bore 906. Eliminating fluid within the heat exchanger bore 906 also eliminates corrosion within the heat exchanger bore 906 specifically between contacting surfaces of the heat exchanger 902 and plunger 901 and plug 933. Absence of corrosion allows easier removal of the plug 933 and/or heat exchanger 902 if desired. Absence of corrosion also eliminates the opportunity for stress corrosion cracking of the plunger 901.
Also in operation, the heat exchanger 902, made of aluminum in this embodiment, and removal of material from the plug bore 941 and cooling bore 944 result in an overall lighter weight of the liquid cooled plunger system 900 than a comparable plunger system made entirely of steel. This reduced weight results in easier field maintenance for operators. The reduced weight also results in less weight on the plunger packing 32/232 during operation. Since the friction force is a function of the normal force, in this case the weight of the liquid cooled plunger system 900, the friction force will be reduced thus reducing the heat caused by the friction force resulting in a longer packing life.
In all liquid cooled plunger systems comprising the blind bore 42, the blind bore 42 of the plunger 20 extends across the entire length of the plunger packing 32/232 at all times during operation. In other words, during operation, the plunger 20 reciprocates between fully inserted and fully retracted positions. At both the fully inserted and fully retracted positions, as well as all positions between the two, the blind bore 42 of the plunger 20 extends longitudinally across the length of the plunger packing 32/232.
In like manner, in liquid cooled plunger systems 300 and 600 used in fluid end 10, the heat exchanger bore 306 of the plunger 301 extends across the entire length of the plunger packing 32 at all times during operation. If liquid cooled plunger systems 300 and 600 are used in fluid end section 200, the heat exchanger bore 306 of the plunger 301 extends across the entire length of the plunger packing 232 at all times during operation.
Also in like manner, in liquid cooled plunger systems 400 and 700 used in fluid end 10 the heat exchanger bore 406 of the plunger 401 extends across the entire length of the plunger packing 32 at all times during operation. If liquid cooled plunger systems 400 and 700 are used in fluid end section 200, the heat exchanger bore 406 of the plunger 401 extends across the entire length of the plunger packing 232 at all times during operation.
Also in like manner, in liquid cooled plunger system 500 used in fluid end 10, the heat exchanger bore 506 of the plunger 501 extends across the entire length of the plunger packing 32 at all times during operation. If liquid cooled plunger system 500 is used in fluid end section 200, the heat exchanger bore 506 of the plunger 501 extends across the entire length of the plunger packing 232 at all times during operation.
Also in like manner, in liquid cooled plunger systems 800 and 900 used in fluid end 10, the heat exchanger bores 806 and 906 of the plungers 801 and 901 extend across the entire length of the plunger packing 32 at all times during operation. If liquid cooled plunger system 800 or 900 is used in fluid end section 200, the heat exchanger bore 806 or 906 of the plungers 801 or 901 extend across the entire length of the plunger packing 232 at all times during operation.
Similar to blind bore 42, the heat exchanger bores 306, 406, 506, 806, and 906 of the plungers 301, 401, 501, 801, and 901 originate on the front surfaces 305, 405, 505, 805, and 905 of the plungers 301, 401, 501, 801, and 901. The heat exchanger bores 306, 406, 506, 806, and 906 do not intersect any other surface of the plungers 301, 401, 501, 801, and 901.
In certain embodiments disclosed herein containing a ball, the ball may be mechanically uncoupled from the blind bore or heat exchanger bore. In certain embodiments disclosed herein containing a stem, the stem may be mechanically uncoupled from the blind bore or heat exchanger bore, as well as the plunger.
In all embodiments, the plunger comprises a first surface configured to remain within the fluid end or fluid end section. This surface may also be referred to as a front surface or first end. The first surface may also be said to be exposed to the cavity, chamber, or horizontal bore formed within the applicable fluid end or fluid end section. All plungers may also comprise a second surface which is opposed from the first surface, and configured to not remain within the applicable fluid end or fluid end section during operation. This second surface is configured to be attached to a power end. The second surface may also be referred to as a rear surface or second end of the plunger.
In liquid cooled plunger system 40 the fluid enters and exits only through the opening in the front surface 88 of the plunger 20 formed by the blind bore 42.
In liquid cooled plunger system 60 the fluid enters and exits only through the openings adjacent the front surface 88 of the plunger 20 formed by central passage 70 and passages 72 of the heat exchanger 62. If heat exchanger 110 is used in liquid cooled plunger system 60, fluid enters and exits only through the openings adjacent the front surface 88 formed by the central passage 112 and splines 114 of the heat exchanger 110, and blind bore 42 of the plunger 20.
In liquid cooled plunger system 80 the fluid enters and exits only through the opening adjacent the front surface 88 of the plunger 20 formed by the central opening 89 of the seat 86.
In liquid cooled plunger system 90 the fluid enters and exits only through the openings adjacent the front surface 88 of the plunger 20 formed by the central opening 98 and openings 100 of the seat 96. If heat exchanger 110 is used in liquid cooled plunger system 90 and seat 96 is modified to match the splines 114 and channels 120 of the heat exchanger 110, the fluid enters and exits only through the openings adjacent the front surface 88 formed by the central opening 98 and splines 114 of the seat 96, and blind bore 42 of the plunger 20.
In liquid cooled plunger systems 300 and 400 the fluid enters and exits only through the openings adjacent the front surfaces 305 and 405 of the plungers 301 and 401 formed by the trap bore 322 and passages 311 of the heat exchanger 302.
In liquid cooled plunger system 900 the fluid enters and exits only through the opening adjacent the front surface 905 of the plunger 901 formed by the cooling bore 944.
In all embodiments, the fluid referenced is fluid being pumped by the fluid end 10, fluid end section 200, any other pump using a plunger, or any other portion of a pump using a plunger. The fluid is only that fluid within the internal chamber 18 of the fluid end 10, or the horizontal bore 204 of fluid end section 200, or the chamber or reservoir of the pump using a plunger that is always exposed to the instantaneous pressure produced by the pump, or the chamber or reservoir of the portion of a pump using a plunger that is always exposed to the instantaneous pressure produced by the pump.
In no case is fluid flow ever diverted from the above-mentioned internal chamber 18, horizontal bore 204, chamber, or reservoir to cool the plunger. For clarification, while various blind bores, central passages, central openings, installation bores, and openings described herein are not themselves part of the internal chambers 18, horizontal bores 204, chambers, or reservoirs, the combined volume that they encompass shall be considered as a single entity for the purposes of fluid flow and system function. Fluid flow in, through, and/or around these features is not considered diverted.
Additional benefits to the liquid cooled plunger systems disclosed herein include but are not limited to: reduction of weight, reduction of corrosion between parts, and reduction of heat related expansion of parts. The reduced weight leads to easier and quicker installation and repair processes. The reduced weight also leads to less weight riding on the plunger packing and related parts, which in turn extends the lifetime of those components. Finally, the reduced weight leads to less heat being generated due to friction between parts, such as plunger packing and plungers. By introducing plugs made of steel and other materials, corrosion of inserts or heat exchangers may be reduced. Notably, the use of aluminum or like materials having high heat transfer coefficients can result in the plunger being cooler than it would be if it were solid or hollow.
The various features and alternative details of construction of the apparatuses described herein for the practice of the present technology will readily occur to the skilled artisan in view of the foregoing discussion, and it is to be understood that even though numerous characteristics and advantages of various embodiments of the present technology have been set forth in the foregoing description, together with details of the structure and function of various embodiments of the technology, this detailed description is illustrative only, and changes may be made in detail, especially in matters of structure and arrangements of parts within the principles of the present technology to the full extent indicated by the broad general meaning of the terms in which the appended claims are expressed.
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