Technique for facilitating the pumping of fluids by lowering fluid viscosity

Information

  • Patent Grant
  • 6564874
  • Patent Number
    6,564,874
  • Date Filed
    Wednesday, July 11, 2001
    23 years ago
  • Date Issued
    Tuesday, May 20, 2003
    21 years ago
Abstract
A viscosity handling system for facilitating the movement of certain fluids. The system utilizes kinetic energy in the form of a rapidly and repetitively moving component that imparts energy in the form of heat to surrounding fluid. The system is particularly useful in applications, such as downhole pumping systems, used to produce hydrocarbon-based fluids from beneath the surface of the earth.
Description




FIELD OF THE INVENTION




The present invention relates generally to movement of fluids, such as wellbore fluids, and particularly to a technique for lowering the viscosity of a fluid to permit more efficient production of the fluid.




BACKGROUND OF THE INVENTION




When pumping viscous fluids, the performance of certain pumps, such as centrifugal pumps, is considerably degraded. For example, the pump head and rate of production are decreased while the horsepower requirement increases drastically. This leads to substantially reduced efficiency of the pump. In certain pumping applications, such as in the production of oil, this low efficiency can add considerably to the cost of oil production or even inhibit the ability to produce from the region.




Attempts have been made to lower the fluid viscosity prior to pumping. For example, electric heaters have been used in combination with electric submersible pumping systems to heat the oil prior to being drawn into the submersible pump of the overall system. With electric heaters, however, electricity must be supplied downhole by, for example, a power cable. Other attempts to lower viscosity have included the injection of relatively hot vapor or the use of downhole combustion to generate heat. Each of these approaches can add undesirable cost and complexity depending on the particular environment and application.




SUMMARY OF THE INVENTION




The present invention relates generally to a technique for lowering the viscosity of a fluid prior to pumping the fluid. The technique is particularly amenable for use in a downhole environment for the production of oil. The viscous fluid is passed through a viscosity handler prior to being drawn into the production pump which moves a desired fluid from one location to another. The viscosity handler utilizes a movable component that is rapidly and repetitively moved through the fluid. Part of this kinetic energy is translated to the surrounding oil in the form of heat. The heat, in turn, lowers the viscosity of the fluid to permit more efficient production of the fluid by the production pump.











BRIEF DESCRIPTION OF THE DRAWINGS




The invention will hereafter be described with reference to the accompanying drawings, wherein like reference numerals denote like elements, and:





FIG. 1

is a front elevational view of an exemplary pumping system, according to one embodiment of the present invention;





FIG. 2

is a front elevational view of an exemplary pumping system disposed within a wellbore;





FIG. 3

is a front elevational view of an exemplary electric submersible pumping system that may be used to pump fluids within a wellbore;





FIG. 4

is an enlarged view of the production pump and viscosity handler illustrated in

FIG. 3

;





FIG. 5

is an enlarged cross-sectional view of a radial flow type impeller that may be utilized within the viscosity handler illustrated in

FIG. 4

;





FIG. 6

is an enlarged cross-sectional view of a mixed flow type impeller that may be used with the production pump illustrated in

FIG. 4

; and





FIG. 7

is a front elevational view of an alternate embodiment of the pumping system disposed in a wellbore.











DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS




Referring generally to

FIG. 1

, a system


10


for facilitating the movement of a viscous fluid is illustrated. Generally, system


10


comprises a production pump


12


that produces a fluid


14


from a reservoir


16


to a desired location, such as holding tank


18


. Production pump


12


draws fluid


14


along an intake pathway


20


and discharges the fluid along an outflow pathway


22


to tank


18


. A viscosity handler


24


is disposed upstream from production pump


12


and is utilized to lower the viscosity of fluid


14


prior to entering the production pump.




Viscosity handler


24


is designed as an energy translator in which kinetic energy is transferred to fluid


14


in the form of heat. The heat energy lowers the viscosity of fluid


14


to promote better efficiency and greater production from production pump


12


. Viscosity handler


24


comprises a movable component


26


that rapidly and repetitively moves through fluid


14


as it flows through viscosity handler


24


to production pump


12


. For example, movable component


26


may be a rotatable component rotated through fluid


14


. In this example, the rotation of movable component


26


is the action that causes fluid


14


to rise in temperature, consequently lowering its viscosity.




An exemplary application of system


10


is illustrated in FIG.


2


. In this application, an electric submersible pumping system


28


utilizes production pump


12


and viscosity handler


24


. Typically, production pump


12


and viscosity handler


24


are powered by a submersible motor


30


. Also, a variety of other components may be utilized as part of electric submersible pumping system


28


as known to those of ordinary skill in the art.




System


28


is designed for deployment in a well


32


within a geological formation containing fluid


14


, typically a desirable production fluid such as petroleum. In this application, a wellbore


36


is drilled and lined with a wellbore casing


38


. Fluid passes through wellbore casing


38


into wellbore


36


through a plurality of openings


40


, often referred to as perforations. Then, the fluid is drawn into electric submersible pumping system


28


, the viscosity is lowered by viscosity handler


24


, and the lower viscosity fluid is discharged to a desired location, such as holding tank


18


.




System


28


is deployed in wellbore


36


by a deployment system


42


that may have a variety of forms and configurations. For example, deployment system


42


may comprise tubing


44


through which fluid


14


is discharged as it flows from electric submersible pumping system


28


through a wellhead


46


to a desired location. Various flow control and pressure control devices


48


may be utilized along the flow path.




A more detailed illustration of electric submersible pumping system


28


is provided in FIG.


3


. In this embodiment, tubing


44


is coupled directly to production pump


12


by a connector


50


. Viscosity handler


24


is coupled to production pump


12


on an end opposite connector


50


. A fluid intake


52


is mounted to viscosity handler


24


at an upstream end to draw fluid


14


into viscosity handler


24


from wellbore


36


. Submersible motor


30


is mounted below fluid intake


52


and typically is coupled to a motor protector


54


. Furthermore, submersible motor


30


receives electrical power via a power cable


56


.




In the example illustrated, submersible motor


30


is deployed between perforations


40


and fluid intake


52


. Thus, as fluid is drawn into wellbore


36


through perforations


40


, it passes submersible motor


30


to fluid intake


52


. Heat generated by motor


30


is used to begin lowering the viscosity of fluid


14


prior to entering viscosity handler


24


.




Referring generally to

FIG. 4

, an exemplary combination of viscosity handler


24


and production pump


12


is illustrated. In this embodiment, production pump


12


is a centrifugal pump having a plurality of stages


58


. Each stage includes an impeller


60


and a diffuser


62


. The impellers


60


drive fluid upwardly through subsequent diffusers and impellers until the fluid is produced or discharged through connector


50


and tubing


44


.




In this exemplary application, movable component


26


of viscosity handler


24


comprises a plurality of rotatable members


64


, such as impellers. The movable members


64


are separated by a plurality of diffusers


66


to form multiple stages


68


. Movable members


64


cooperate to translate substantial kinetic energy into heat energy within the fluid passing therethrough. The power for imparting kinetic energy to movable members


64


as well as for powering production pump


12


is provided by submersible motor


30


via a shaft or shaft sections


70


and


72


to which movable member


64


and impellers


60


, respectively, are mounted.




With the particular design illustrated in

FIG. 4

, movable members


64


and diffusers


66


cooperate to allow fluid movement from intake


52


to production pump


12


. Members


64


may even be configured to facilitate movement of fluid through the viscosity handler. For example, viscosity handler


24


may be designed as a poor efficiency pump able to produce a temperature rise in the fluid and therefore a lower viscosity fluid for production by production pump


12


. In this manner, the use of a low efficiency device promotes higher efficiency of the overall system and allows an application engineer to select a production pump able to produce at a relatively high rate with great efficiency.




In the embodiment illustrated, the impellers


60


of production pump


12


comprise mixed flow impellers, but may be radial flow impellers in certain lower flow applications. Mixed flow impellers are beneficial in many environments because of their ability to produce a relatively high flow rate with great efficiency. However, the fluid being produced must have sufficiently low viscosity or the performance curve of the production pump is greatly degraded and may render electric submersible pumping system


28


incapable of production. Accordingly, if impellers are utilized as rotating members in viscosity handler


24


, it is desirable to utilize low efficiency impellers, such as radial flow impellers. Exemplary embodiments of a radial flow impeller and a mixed flow impeller are illustrated in

FIGS. 5 and 6

, respectively.




In the radial flow design, movable member/impeller


64


is rotationally affixed to shaft section


70


by, for instance, a key (not shown). The impeller comprises an impeller body


74


with a plurality of vanes


76


disposed generally between an upper wall


78


and a lower wall


80


. Walls


78


and


80


as well as vanes


76


define a plurality of flow chambers


82


disposed circumferentially around shaft segment


70


. A recirculation hole


77


extends through upper wall


78


and is helpful in heating the fluid. When impeller body


74


is rotated with shaft segment


70


, fluid is drawn into the flow chamber


82


through an inlet


84


and discharged radially through a radial outlet


86


into adjacent stationary diffuser


66


. The fluid then enters the upper diffuser vanes and is directed through subsequent stages before being drawn into production pump


12


. The inefficient, repetitive motion of members


64


through fluid


14


creates heat and lowers the viscosity of fluid


14


.




In this example, impellers


60


of production pump


12


are mixed flow type impellers, as illustrated best in

FIG. 6. A

mixed flow impeller body


88


comprises a plurality of angled vanes


90


that are spaced circumferentially about shaft segment


72


. Each angled vane


90


defines a flow chamber


92


. As impeller body


88


is rotated with shaft segment


72


, each angled vane


90


draws fluid in through an inlet


94


, and the fluid flows through flow chambers


92


until it is discharged through an impeller outlet


96


to diffuser


62


. With mixed flow impellers, the fluid typically is drawn from a lower location through inlet


94


and moved upwardly and outwardly for discharge at a higher location. The fluid is pumped through consecutive impellers and diffusers as it moves through the plurality of stages


58


for discharge through connector


50


and tubing


44


. (See FIG.


4


).




Viscosity handler


24


may be deployed in a variety of environments and in combination with other components that are used in downhole applications or with electric submersible pumping systems. Additionally, component configurations can be designed to supplement the transfer of energy from the viscosity handler


24


to the fluid being produced by production pump


12


. As illustrated in

FIG. 7

, submersible motor


30


may be located above perforations


40


such that the fluid flows past submersible motor


30


before being drawn into viscosity handler


24


. The heat of the motor assists in lowering the viscosity of the fluid flowing past. Alternatively or in addition to this arrangement of submersible motor


30


, a supplemental heater


98


may be located within the wellbore, as illustrated in FIG.


7


. An exemplary supplemental heater


98


is a resistive type heater powered via a power cable, such as power cable


56


or a separate power cable deployed downhole. Such a supplemental heater


98


may be positioned independently within wellbore


36


or it may be combined with electric submersible pumping system


28


to heat fluid as it flows past and external to the heater. Supplemental heater


98


also may be designed for deployment downstream of fluid intake


52


, such that fluid is drawn through the center of the heater prior to or after entering viscosity handler


24


.




In addition to the components that may be used in combination with the viscosity handler, viscosity handler


24


may use various combinations of stages to facilitate and influence fluid movement through the system. In some environments, a better initiation of fluid movement may be achieved by combining different styles of stages, e.g. at least one mixed flow stage with a plurality of radial flow stages. For example, one combination incorporates mixed flow stages as the lower two stages (as illustrated in

FIG. 4

) with the remainder being radial flow stages. Using mixed flow stages proximate the viscosity handler intake facilitates initial movement of the fluid particularly when the fluid is fairly viscous. Once movement of fluid is initiated, the subsequent radial stages can continue the fluid flow while imparting heat energy to the fluid. Other variations in the order of the flow stages may be used to obtain differing fluid flow efficiencies.




It will be understood that the foregoing description is of exemplary embodiments of this invention, and that the invention is not limited to the specific forms shown. For example, the viscosity handler may be utilized in conjunction with a variety of pumps for producing fluid from one location to another; the system may be utilized in wellbore or other subterranean applications; and a variety of movable components can be used to impart energy in the form of heat to the fluid flowing through the viscosity hander. These and other modifications may be made in the design and arrangement of the elements without departing from the scope of the invention as expressed in the appended claims.



Claims
  • 1. A system for moving a viscous fluid, comprising:a centrifugal pump; a fluid intake; and a viscosity handler through which fluid flows from the fluid intake to the pump, the viscosity handler comprising a rotatable energy translator having a plurality of radial flow impellers, the rotatable energy translator being disposed in a fluid flow path, wherein rotation of the rotatable energy translator heats fluid as it flows along the fluid flow path prior to entering the centrifugal pump.
  • 2. The system as recited in claim 1, wherein the viscosity handler comprises a plurality of radial flow stages and a plurality of mixed flow stages.
  • 3. The system as recited in claim 1, wherein the radial flow impeller comprises a plurality of recirculation holes.
  • 4. The system as recited in claim 1, further comprising a resistive element heater.
  • 5. The system as recited in claim 1, further comprising a submersible motor to power the centrifugal pump.
  • 6. The system as recited in claim 5, further comprising a motor protector.
  • 7. The system as recited in claim 6, further comprising a wellbore having a wellbore casing, wherein the centrifugal pump, the fluid intake, the viscosity handler, the submersible motor and the motor protector are disposed within the wellbore casing.
  • 8. The system as recited in claim 7, wherein the wellbore casing has a perforation disposed below the submersible motor.
  • 9. The system as recited in claim 8, wherein the fluid intake and the pump are disposed above the submersible motor.
  • 10. A system for producing a viscous fluid from a subterranean reservoir, comprising:a wellbore having a wellbore casing with a perforation to permit ingress of a fluid to be produced; and an electric submersible pumping system having a submersible motor, a submersible pump to produce the fluid to a desired location, and a viscosity handler that converts kinetic energy to heat to lower the viscosity of the fluid; wherein the viscosity handler further comprises a radial flow stage, the radial flow stage including a recirculation path.
  • 11. The system as recited in claim 10, wherein the viscosity handler comprises a rotatable energy translator.
  • 12. The system as recited in claim 11, wherein the rotatable energy translator comprises a plurality of rotating elements to impart energy to the fluid in the form of heat.
  • 13. The system as recited in claim 12, wherein each rotating element comprises a radial flow impeller.
  • 14. The system as recited in claim 13, wherein the electric submersible pumping system further comprises a motor protector.
  • 15. The system as recited in claim 14, wherein the pump comprises a centrifugal pump.
  • 16. The system as recited in claim 15, wherein the centrifugal pump comprises a plurality of stages, each stage having a mixed flow impeller.
  • 17. The system as recited in claim 15, wherein the electric submersible pumping system comprises a fluid intake through which fluid is drawn by the submersible pump, the viscosity handler being positioned in the flow of fluid from the fluid intake to the submersible pump.
  • 18. A method to facilitate production of an oil related fluid from the earth, comprising:operating a production pump in a subterranean environment; drawing a reservoir fluid through a pump intake; and rotating a plurality of radial flow impellers through the reservoir fluid as it passes from the fluid intake to the production pump, the plurality of radial flow impellers being rotated at a rate sufficient to lower the viscosity of the reservoir fluid and raise the efficiency of the production pump.
  • 19. The method as recited in claim 18, further comprising producing the reservoir fluid to a desired location.
  • 20. The method as recited in claim 19, wherein operating comprises powering the production pump with a submersible motor.
  • 21. The method as recited in claim 18, wherein operating comprises operating a centrifugal production pump.
  • 22. The method as recited in claim 21, further comprising placing the production pump and the pump intake within a wellbore.
  • 23. The method as recited in claim 18, wherein operating comprises operating a centrifugal production pump having a plurality of rotatable mixed flow impellers.
  • 24. A system to facilitate production of an oil related fluid from the earth, comprising:means for operating a production pump in a subterranean environment; means for drawing a reservoir fluid through a pump intake; and means for rotating a plurality of radial flow impellers through the reservoir fluid as it passes from the fluid intake to the production pump, the plurality of radial flow impellers being moved at a rate sufficient to lower the viscosity of the reservoir fluid and raise the efficiency of the production pump.
  • 25. The system as recited in claim 24, further comprising means for placing the production pump and the pump intake within a wellbore.
  • 26. The system as recited in claim 24, wherein the plurality of radial flow impellers comprises a plurality of recirculation holes.
  • 27. A viscosity handler for lowering the viscosity of a wellbore fluid, comprising:an outer housing having a fluid flow path therethrough; and an energy translator comprising a plurality of mixed flow impellers and a plurality of radial flow impellers disposed within the outer housing, wherein actuation of the moving element as fluid flows along the fluid flow path heats the fluid.
  • 28. The viscosity handler as recited in claim 27, wherein each radial flow impeller comprises a plurality of recirculation holes.
US Referenced Citations (13)
Number Name Date Kind
3824364 Cachat Jul 1974 A
3841786 Florjancic Oct 1974 A
4401159 Kofahl Aug 1983 A
4790375 Bridges et al. Dec 1988 A
5285846 Mohn Feb 1994 A
5554897 Martin et al. Sep 1996 A
5623576 Deans Apr 1997 A
5845709 Mack et al. Dec 1998 A
6006837 Breit Dec 1999 A
6167965 Bearden et al. Jan 2001 B1
6206093 Lee et al. Mar 2001 B1
6260627 Rivas Jul 2001 B1
6318467 Liu et al. Nov 2001 B1