Information
-
Patent Grant
-
6564874
-
Patent Number
6,564,874
-
Date Filed
Wednesday, July 11, 200123 years ago
-
Date Issued
Tuesday, May 20, 200321 years ago
-
Inventors
-
Original Assignees
-
Examiners
- Neuder; William
- Jones; Robert D
Agents
- Fletcher, Yoder & Van Someren
- Griffin; Jeffery E.
- Jeffery; Brigitte L.
-
CPC
-
US Classifications
Field of Search
US
- 166 302
- 166 60
- 166 61
- 166 62
- 166 664
- 166 685
- 166 372
- 417 14
- 417 216
- 417 4101
- 417 4233
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International Classifications
-
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)