1. Field of the Invention
This invention relates in general to electric submersible pumps (ESPs) and, in particular, to a high efficiency impeller for use in an ESP.
2. Brief Description of Related Art
Electric submersible pump (ESP) assemblies are disposed within wellbores and operate immersed in wellbore fluids. ESP assemblies generally include a pump portion and a motor portion. Generally, the motor portion is downhole from the pump portion, and a rotatable shaft connects the motor and the pump. The rotatable shaft is usually one or more shafts operationally coupled together. The motor rotates the shaft that, in turn, rotates components within the pump to lift fluid through a production tubing string to the surface. ESP assemblies may also include one or more seal sections coupled to the shaft between the motor and pump. In some embodiments, the seal section connects the motor shaft to the pump intake shaft. Some ESP assemblies include one or more gas separators. The gas separators couple to the shaft at the pump intake and separate gas from the wellbore fluid prior to the entry of the fluid into the pump.
The pump portion includes a stack of impellers and diffusers. The impellers and diffusers are alternatingly positioned in the stack so that fluid leaving an impeller will flow into an adjacent diffuser and so on. Generally, the diffusers direct fluid from a radially outward location of the pump back toward the shaft, while the impellers accelerate fluid from an area proximate to the shaft to the radially outward location of the pump. Each impeller and diffuser may be referred to as a pump stage.
The shaft couples to the impeller to rotate the impeller within the non-rotating diffuser. In this manner, the stage may lift the fluid. The impeller includes vanes circumferentially spaced around the impeller. The vanes may be straight or curved. The vanes will define passages through which fluid may move within the impeller. The vanes may push fluid from the radially inward fluid inlet to the radially outward location, pressurizing the fluid. Maximum pump efficiency generally occurs at a particular flow rate or along a range of flow rates, where the range is typically significantly less than the operating range of flow rates. Pumps are usually designed to operate at or close to a maximum efficiency. However, fluid flow rates through a pump may change, such as due to depletion of fluids in a reservoir, so that over time a pump may not be operating at its maximum efficiency. A key factor in pump efficiency is the prevention of fluid boundary separation from the impeller vane. Fluid boundary separation may occur as the speed of the impeller rotation increases. When the fluid boundary separates from the surface of the impeller vane, turbulent flow is introduced, increasing drag and thus, decreasing the acceleration imparted to the fluid from the impeller vane. This decreases pump efficiency and leads to an increase in pump energy requirements. Therefore, an impeller vane that could decrease the instances of fluid boundary separation from the impeller vane and consequently increase efficiency would be desired.
These and other problems are generally solved or circumvented, and technical advantages are generally achieved, by preferred embodiments of the present invention that provide a high efficiency impeller.
In accordance with an embodiment of the present invention, an electric submersible pump (ESP) impeller is disclosed. The impeller includes a curved vane interposed between an upper shroud and a lower shroud, the vane extending radially outward from an area proximate to a cylindrical hub. A groove is formed on a convex surface of the vane, the groove extending substantially parallel with an elongate direction of the vane. A pair of ridges are formed on lateral sides of the groove.
In accordance with another embodiment of the present invention, an electric submersible pump (ESP) system is disclosed. The ESP includes a pump having an impeller for moving fluid, and a motor coupled to the submersible pump so that the motor may variably rotate the impeller in the pump. The impeller is positioned within the pump so that the impeller will accelerate fluid from a fluid inlet in the impeller toward an outer area of the pump, the impeller having at least one vane with a groove fanned on a surface of the vane.
In accordance with yet another embodiment of the present invention, a method for improving pumping efficiency in an electric submersible pump assembly having a motor portion coupled to a pump portion to rotate an impeller of the pump portion in a diffuser of the pump portion is disclosed. The method rotates the impeller within the diffuser and fauns a boundary layer along a vane of the impeller in response to the rotation of the impeller. The method then induces oppositely rotating vortices along the vane as the boundary layer separates from the vane, and mixes the oppositely rotating vortices along the vane to accelerate fluid flow along the vane.
An advantage of the disclosed embodiments is that they provide for higher fluid flow rates through the impeller with decreased separation from the high pressure or working surface of the impeller vane. In addition, the disclosed embodiments provide for pumps with decreased power requirements, allowing for a similar volume of fluid to be lifted from a wellbore using less energy over similar pumps having impeller vanes without the disclosed embodiments.
So that the manner in which the features, advantages and objects of the invention, as well as others which will become apparent, are attained, and can be understood in more detail, more particular description of the invention briefly summarized above may be had by reference to the embodiments thereof which are illustrated in the appended drawings that form a part of this specification. It is to be noted, however, that the drawings illustrate only a preferred embodiment of the invention and are therefore not to be considered limiting of its scope as the invention may admit to other equally effective embodiments.
The present invention will now be described more fully hereinafter with reference to the accompanying drawings which illustrate embodiments of the invention. This invention may, however, be embodied in many different forms and should not be construed as limited to the illustrated embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the invention to those skilled in the art. Like numbers refer to like elements throughout, and the prime notation, if used, indicates similar elements in alternative embodiments.
In the following discussion, numerous specific details are set forth to provide a thorough understanding of the present invention. However, it will be obvious to those skilled in the art that the present invention may be practiced without such specific details. Additionally, for the most part, details concerning ESP operation, construction, and the like have been omitted inasmuch as such details are not considered necessary to obtain a complete understanding of the present invention, and are considered to be within the skills of persons skilled in the relevant art.
With reference now to
In an example of operation, pump motor 15 is energized via a power cable 17. Motor 15 rotates an attached shaft assembly 35 (shown in dashed outline). Although shaft 35 is illustrated as a single member, it should be pointed out that shaft 35 may comprise multiple shaft segments. Shaft assembly 35 extends from motor 15 through seal section 19 to pump section 13. An impeller stack 25 (also shown in dashed outline) within pump section 13 is coupled to an upper end of shaft 35 and rotates in response to shaft 35 rotation. Impeller stack 25 includes a vertical stack of individual impellers alternatingly interspaced between static diffusers (not shown). Wellbore fluid 31, which may include liquid hydrocarbon, gas hydrocarbon, and/or water, enters wellbore 29 through perforations 33 formed through casing 12. Wellbore fluid 31 is drawn into pump 13 from inlets 23 and is pressurized as rotating impellers 25 urge wellbore fluid 31 through a helical labyrinth upward through pump 13. The pressurized fluid is directed to the surface via production tubing 27 attached to the upper end of pump 13.
In an exemplary embodiment, impeller stack 25 includes one or more impellers 37 illustrated in
As shown in example of
A lower shroud 47 forms an outer edge of impeller 37 and may be attached to or join an edge of each vane 43. Lower shroud 47 defines a planar surfaced intersected by axis 57 and adjacent a lower lateral side of impeller 37. In some embodiments, lower shroud 47 is attached to impeller hub 39, either directly or via vanes 43. In some embodiments, impeller hub 39, vanes 43, and lower shroud 47 are all cast or manufactured as a single piece of material. Lower shroud 47 may have a lower lip for engaging an impeller eye washer on a diffuser. The lower lip may be formed on the bottom surface of lower shroud 47. Lower shroud 47 defines an impeller inlet 51 on a lower side of lower shroud 47. Impeller inlet 51 allows fluid flow from below impeller 37 into passages 45 defined by vanes 43.
Each impeller 37 includes impeller edge 49 that is a surface on an outer radial portion of impeller 37. In an exemplary embodiment, impeller edge 49 is the outermost portion of lower shroud 47. Impeller edge 49 need not be the outermost portion of impeller 37. The diameter of impeller edge 49 is slightly smaller than an inner diameter of a diffuser in which impeller 37 is positioned.
Further in the example of
Within a single pump housing, one or more of the plurality of impellers 37 may have a different design than one or more of the other impellers, such as, for example, impeller vanes having a different pitch. A plurality of impellers 37 may be installed on shaft 35 (
Referring to
Referring to
Referring to
In the illustrated embodiment of
In an exemplary embodiment, vanes 43 having ridges 61 and grooves 67 may have a fluid flowrate that is 15% greater than the fluid flowrate of a similarly sized impeller having vanes without ridges 61 and grooves 67. In addition, an impeller 37 employing vanes 43 having ridges 61 and grooves 67 may require 10% less power to lift a similar volume of fluid than an impeller employing vanes without ridges 61 and grooves 67. A person skilled in the art will understand that alternative methods may be used to mix vortices along high pressure surface 55 and increase pump efficiency. These alternative methods are contemplated and included in the disclosed embodiments. A person skilled in the art will recognize that vane 37 has a short leading edge, internal end 63, such that high pressure surface 55 may have a length that is several times longer than internal end 63. Ridges 61 and grooves 67 may not protrude from a leading edge, or internal end 63, of vane 37. Instead, ridges 61 and grooves 67 extend along a high pressure surface 55 along a length of vane 37 between internal end 63 and trailing end 65. Still further, vane 37 may not be considered a thick object, nor will vane 37 have an airfoil profile adapted to generate lift. In addition, vane 37 may not uniformly taper to a trailing edge or external end.
Referring to
A person skilled in the art will recognize that ridges 61 and grooves 67 may extend only part of a length of vane 43 from internal end 63 to trailing end 65. For example, referring to
Accordingly, the disclosed embodiments provide numerous advantages. For example, the disclosed embodiments provide for higher fluid flow rates through the impeller with decreased separation from the high pressure or working surface of the impeller vane. In addition, the disclosed embodiments provide for pumps with decreased power requirements, allowing for a similar volume of fluid to be lifted from a wellbore using less energy over similar pumps having impeller vanes without the disclosed embodiments.
A person skilled in the art will understand that the disclosed embodiments include alternative mechanisms and apparatuses that increase pump efficiency and decrease pump power requirements by inducing oppositely spinning vortices from a separating boundary layer of a pump impeller vane. These alternative means may mix the oppositely spinning vortices to increase fluid flow rate through the impeller. These alternative means and apparatuses are contemplated and included in the disclosed embodiments.
It is understood that the present invention may take many forms and embodiments. Accordingly, several variations may be made in the foregoing without departing from the spirit or scope of the invention. Having thus described the present invention by reference to certain of its preferred embodiments, it is noted that the embodiments disclosed are illustrative rather than limiting in nature and that a wide range of variations, modifications, changes, and substitutions are contemplated in the foregoing disclosure and, in some instances, some features of the present invention may be employed without a corresponding use of the other features. Many such variations and modifications may be considered obvious and desirable by those skilled in the art based upon a review of the foregoing description of preferred embodiments. Accordingly, it is appropriate that the appended claims be construed broadly and in a manner consistent with the scope of the invention.