Compressors and systems incorporating compressors have been developed and are often utilized in a myriad of industrial processes (e.g., petroleum refineries, offshore oil production platforms, and subsea process systems). Conventional compressors may be configured to compress a process fluid by adding energy (e.g., kinetic energy) to the process fluid to transport the process fluid from a low pressure environment to a high pressure environment. The compressed process fluid discharged from the compressors may be utilized to efficiently perform work or operate one or more downstream processes. Improvements in the efficiency of conventional compressors has increased the application of the compressors at various oil production sites. Many of the oil production sites (e.g., offshore), however, may be constrained or limited in weight and space. Accordingly, there is an increased interest and demand for smaller and lighter compressors, or compact compressors. In addition to the foregoing, it is often desirable that compression stages in the compact compressors be capable of achieving higher compression ratios (e.g., 10:1 or greater) for increased production while maintaining a compact footprint. The higher compression ratios may result in a compressor where the flow discharged from an impeller has a velocity in excess of local sonic velocity.
To achieve the higher compression ratios, components (e.g., inlet guide vanes, diffuser vanes, and/or return channel vanes) of the conventional compact compressors may often be adjusted by an operator or user such that the compact compressors may operate at a “design” condition. In addition to achieving the “design” condition, an operator may need to vary or control the performance and efficiency of the compact compressors. However, the adjustment of the components may often be difficult, time-consuming, and/or require the fabrication of new components.
What is needed, then, is an improved system and method for adjusting internal components of a compact compressor to control the performance of the compact compressor.
Embodiments of the disclosure may provide an inlet guide vane assembly for a compressor. The inlet guide vane assembly may include a hub configured to be disposed in an inlet of the compressor, and an inlet guide vane extending from the hub. The inlet guide vane may include a stationary section configured to be coupled with the inlet and a mobile section disposed adjacent the stationary section. The mobile section may include a rod configured to extend through an opening formed in the inlet. The inlet guide vane assembly may also include at least one biasing member disposed about the rod and configured to exert a biasing force on the mobile section to urge the mobile section radially outward.
Embodiments of the disclosure may also provide a compressor. The compressor may include a casing at least partially defining an impeller cavity, an impeller disposed in the impeller cavity, and an inlet coupled or integral with the casing. An inner surface of the inlet may at least partially defining an inlet passageway fluidly coupled with the impeller cavity. The compressor may also include an inlet guide vane assembly. The inlet guide vane assembly may include a hub disposed in the inlet passageway, and at least one inlet guide vane extending between the inner surface and the hub. The at least one inlet guide vane may be configured to control at least one fluid property of a process fluid flowing through the inlet passageway. The inlet guide vane assembly may also include at least one biasing member disposed about a portion of the inlet guide vane. The at least one biasing member may be configured to exert a biasing force on the inlet guide vane to urge the inlet guide vane toward the inner surface of the inlet.
Embodiments of the disclosure may further provide a compression system including a driver and a compressor coupled with and configured to be driven by the driver. The compressor may include a casing and an inlet coupled with or integral with the casing. The inlet and the casing may at least partially define an inlet passageway of the compressor configured to receive a process fluid. The compressor may also include a rotary shaft disposed in the casing, an impeller coupled with the driver via the rotary shaft, and an inlet guide vane assembly. The rotary shaft may be configured to couple the compressor with the driver. The impeller may be configured to be rotated by the driver via the rotary shaft. The inlet guide vane assembly may include a hub disposed in the inlet passageway, at least one inlet guide vane extending radially between the inlet and the hub, and at least one biasing member disposed about a portion of the at least one inlet guide vane. The at least one inlet guide vane may be configured to control at least one fluid property of the process fluid flowing through the inlet passageway, and the at least one biasing member may be configured to urge the at least one inlet guide vane radially outward.
The present disclosure is best understood from the following detailed description when read with the accompanying Figures. It is emphasized that, in accordance with the standard practice in the industry, various features are not drawn to scale. In fact, the dimensions of the various features may be arbitrarily increased or reduced for clarity of discussion.
It is to be understood that the following disclosure describes several exemplary embodiments for implementing different features, structures, or functions of the invention. Exemplary embodiments of components, arrangements, and configurations are described below to simplify the present disclosure; however, these exemplary embodiments are provided merely as examples and are not intended to limit the scope of the invention. Additionally, the present disclosure may repeat reference numerals and/or letters in the various exemplary embodiments and across the Figures provided herein. This repetition is for the purpose of simplicity and clarity and does not in itself dictate a relationship between the various exemplary embodiments and/or configurations discussed in the various Figures. Moreover, the formation of a first feature over or on a second feature in the description that follows may include embodiments in which the first and second features are formed in direct contact, and may also include embodiments in which additional features may be formed interposing the first and second features, such that the first and second features may not be in direct contact. Finally, the exemplary embodiments presented below may be combined in any combination of ways, i.e., any element from one exemplary embodiment may be used in any other exemplary embodiment, without departing from the scope of the disclosure.
Additionally, certain terms are used throughout the following description and claims to refer to particular components. As one skilled in the art will appreciate, various entities may refer to the same component by different names, and as such, the naming convention for the elements described herein is not intended to limit the scope of the invention, unless otherwise specifically defined herein. Further, the naming convention used herein is not intended to distinguish between components that differ in name but not function. Further, in the following discussion and in the claims, the terms “including” and “comprising” are used in an open-ended fashion, and thus should be interpreted to mean “including, but not limited to.” All numerical values in this disclosure may be exact or approximate values unless otherwise specifically stated. Accordingly, various embodiments of the disclosure may deviate from the numbers, values, and ranges disclosed herein without departing from the intended scope. Furthermore, as it is used in the claims or specification, the term “or” is intended to encompass both exclusive and inclusive cases, i.e., “A or B” is intended to be synonymous with “at least one of A and B,” unless otherwise expressly specified herein.
The compressor 102 may be a direct-inlet centrifugal compressor. The direct-inlet centrifugal compressor may be, for example, a version of a Dresser-Rand Pipeline Direct Inlet (PDI) centrifugal compressor manufactured by the Dresser-Rand Company of Olean, New York. The compressor 102 may have a center-hung rotor configuration or an overhung rotor configuration, as illustrated in
The compressor 102 may include one or more stages (not shown). In at least one embodiment, the compressor 102 may be a single-stage compressor. In another embodiment, the compressor 102 may be a multi-stage centrifugal compressor. Each stage (not shown) of the compressor 102 may be a subsonic compressor stage or a supersonic compressor stage. In an exemplary embodiment, the compressor 102 may include a single supersonic compressor stage. In another embodiment, the compressor 102 may include a plurality of subsonic compressor stages. In yet another embodiment, the compressor 102 may include a subsonic compressor stage and a supersonic compressor stage. Any one or more stages of the compressor 102 may have a compression ratio greater than about 1:1. For example, any one or more stages of the compressor 102 may have a compression ratio of about 1.1:1, about 1.2:1, about 1.3:1, about 1.4:1, about 1.5:1, about 1.6:1, about 1.7:1, about 1.8:1, about 1.9:1, about 2:1, about 2.1:1, about 2.2:1, about 2.3:1, about 2.4:1, about 2.5:1, about 2.6:1, about 2.7:1, about 2.8:1, about 2.9:1, about 3:1, about 3.1:1, about 3.2:1, about 3.3:1, about 3.4:1, about 3.5:1, about 3.6:1, about 3.7:1, about 3.8:1, about 3.9:1, about 4:1, about 4.1:1, about 4.2:1, about 4.3:1, about 4.4:1, about 4.5:1, about 4.6:1, about 4.7:1, about 4.8:1, about 4.9:1, about 5:1, about 5.1:1, about 5.2:1, about 5.3:1, about 5.4:1, about 5.5:1, about 5.6:1, about 5.7:1, about 5.8:1, about 5.9:1, about 6:1, about 6.1:1, about 6.2:1, about 6.3:1, about 6.4:1, about 6.5:1, about 6.6:1, about 6.7:1, about 6.8:1, about 6.9:1, about 7:1, about 7.1:1, about 7.2:1, about 7.3:1, about 7.4:1, about 7.5:1, about 7.6:1, about 7.7:1, about 7.8:1, about 7.9:1, about 8.0:1, about 8.1:1, about 8.2:1, about 8.3:1, about 8.4:1, about 8.5:1, about 8.6:1, about 8.7:1, about 8.8:1, about 8.9:1, about 9:1, about 9.1:1, about 9.2:1, about 9.3:1, about 9.4:1, about 9.5:1, about 9.6:1, about 9.7:1, about 9.8:1, about 9.9:1, about 10:1, about 10.1:1, about 10.2:1, about 10.3:1, about 10.4:1, about 10.5:1, about 10.6:1, about 10.7:1, about 10.8:1, about 10.9:1, about 11:1, about 11.1:1, about 11.2:1, about 11.3:1, about 11.4:1, about 11.5:1, 11 3.6:1, about 11.7:1, about 11.8:1, about 11.9:1, about 12:1, about 12.1:1, about 12.2:1, about 12.3:1, about 12.4:1, about 12.5:1, about 12.6:1, about 12.7:1, about 12.8:1, about 12.9:1, about 13:1, about 13.1:1, about 13.2:1, about 13.3:1, about 13.4:1, about 13.5:1, about 13.6:1, about 13.7:1, about 13.8:1, about 13.9:1, about 14:1, or greater. In an exemplary embodiment, the compressor 102 may include a plurality of compressor stages, where a first stage (not shown) of the plurality of compressor stages may have a compression ratio of about 1.75:1 and a second stage (not shown) of the plurality of compressor stages may have a compression ratio of about 6.0:1.
The driver 104 may be configured to provide the drive shaft 106 with rotational energy. The drive shaft 106 may be integral or coupled with a rotary shaft 108 of the compressor 102 such that the rotational energy of the drive shaft 106 may be transmitted to the rotary shaft 108. The drive shaft 106 of the driver 104 may be coupled with the rotary shaft 108 via a gearbox (not shown) having a plurality of gears configured to transmit the rotational energy of the drive shaft 106 to the rotary shaft 108 of the compressor 102. Accordingly, the drive shaft 106 and the rotary shaft 108 may spin at the same speed, substantially similar speeds, or differing speeds and rotational directions via the gearbox. The driver 104 may be a motor, such as a permanent magnetic electric motor, and may include a stator (not shown) and a rotor (not shown). It should be appreciated, however, that other embodiments may employ other types of motors including, but not limited to, synchronous motors, induction motors, and brushed DC motors, or the like. The driver 104 may also be a hydraulic motor, an internal combustion engine, a steam turbine, a gas turbine, or any other device capable of driving or rotating the rotary shaft 108 of the compressor 102.
The compression system 100 may include one or more radial bearings 110 directly or indirectly supported by a housing 112 of the compression system 100. The radial bearings 110 may be configured to support the drive shaft 106 and/or the rotary shaft 108. The radial bearings 110 may be oil film bearings. The radial bearings 110 may also be magnetic bearings, such as active magnetic bearings, passive magnetic bearings, or the like. The compression system 100 may also include one or more axial thrust bearings 114 disposed adjacent the rotary shaft 108 and configured to control the axial movement of the rotary shaft 108. The axial thrust bearings 114 may be magnetic bearings configured to at least partially support and/or counter thrust loads or forces generated by the compressor 102.
The process fluid pressurized, circulated, contained, or otherwise utilized in the compression system 100 may be a fluid in a liquid phase, a gas phase, a supercritical state, a subcritical state, or any combination thereof. The process fluid may be a mixture, or process fluid mixture. The process fluid may include one or more high molecular weight process fluids, one or more low molecular weight process fluids, or any mixture or combination thereof. As used herein, the term “high molecular weight process fluids” refers to process fluids having a molecular weight of about 30 grams per mole (g/mol) or greater. Illustrative high molecular weight process fluids may include, but are not limited to, hydrocarbons, such as ethane, propane, butanes, pentanes, and hexanes. Illustrative high molecular weight process fluids may also include, but are not limited to, carbon dioxide (CO2) or process fluid mixtures containing carbon dioxide. As used herein, the term “low molecular weight process fluids” refers to process fluids having a molecular weight less than about 30 g/mol. Illustrative low molecular weight process fluids may include, but are not limited to, air, hydrogen, methane, or any combination or mixtures thereof.
In an exemplary embodiment, the process fluid or the process fluid mixture may be or include carbon dioxide. The amount of carbon dioxide in the process fluid or the process fluid mixture may be at least about 80%, at least about 85%, at least about 90%, at least about 95%, at least about 96%, at least about 97%, at least about 98%, at least about 99%, or greater by volume. Utilizing carbon dioxide as the process fluid or as a component or part of the process fluid mixture in the compression system 100 may provide one or more advantages. For example, carbon dioxide may provide a readily available, inexpensive, non-toxic, and non-flammable process fluid. In another example, the relatively high working pressure of applications utilizing carbon dioxide may allow the compression system 100 incorporating carbon dioxide (e.g., as the process fluid or as part of the process fluid mixture) to be relatively more compact than compression systems incorporating other process fluids (e.g., process fluids not including carbon dioxide). Additionally, the high density and high heat capacity or volumetric heat capacity of carbon dioxide with respect to other process fluids may make carbon dioxide more “energy dense.” Accordingly, a relative size of the compression system 100 and/or the components thereof may be reduced without reducing the performance of the compression system 100.
The carbon dioxide may be of any particular type, source, purity, or grade. For example, industrial grade carbon dioxide may be utilized as the process fluid without departing from the scope of the disclosure. Further, as previously discussed, the process fluids may be a mixture, or process fluid mixture. The process fluid mixture may be selected for one or more desirable properties of the process fluid mixture within the compression system 100. For example, the process fluid mixture may include a mixture of a liquid absorbent and carbon dioxide (or a process fluid containing carbon dioxide) that may enable the process fluid mixture to be compressed to a relatively higher pressure with less energy input than compressing carbon dioxide (or a process fluid containing carbon dioxide) alone.
As illustrated in
The inlet guide vanes 216 may extend through at least a portion of the inlet passageway 206 from an inner surface 218 (i.e., inner radial surface) of the inlet 204 to an outer radial surface of a hub 220 of the inlet guide vane assembly 214. As illustrated in
As previously discussed, respective portions of the inlet guide vanes 216 may be moveable (e.g., adjustable) to vary the one or more fluid properties and/or fluid flow attributes (e.g., swirl, velocity, mass flowrate, etc.) of the process fluid flowing through the inlet passageway 206. In an exemplary embodiment, the inlet guide vanes 216 may be configured to move or adjust within the inlet passageway 206, as disclosed in U.S. Pat. No. 8,632,302, the subject matter of which is incorporated herein to the extent consistent with the present disclosure. In another embodiment, illustrated in
The mobile section 228 of the inlet guide vane 216 may be configured to rotate or pivot about an axis 232 disposed proximal a second end portion 234 of the stationary section 226. For example, as illustrated in
The inlet guide vane assembly 214 may include one or more bushings or bearings (three are shown 246, 248, 250) configured to facilitate the rotation of the mobile section 228 about the axis 232. For example, as illustrated in
The inlet guide vane 216 may include one or more flanges 254 (e.g., cylindrical flanges) coupled or integrally formed with the mobile section 228 and configured to at least partially position the mobile section 228 in the inlet passageway 206 and/or control the rotation of the mobile section 228 about the axis 232. For example, as illustrated in
The compressor 200 may include an actuating assembly 258 configured to rotate the respective mobile sections 228 of the inlet guide vanes 216 within the inlet passageway 206.
As illustrated in
As previously discussed, the actuating member 260 may be configured to rotate about the longitudinal axis 262 relative to the casing 202 or the inlet 204. In an exemplary embodiment, illustrated in
As previously discussed, the actuating member 260 may be configured to rotate the mobile section 228 of the inlet guide vanes 216. As illustrated in
As illustrated in
In an exemplary embodiment, illustrated in
The biasing members 290 may exert the biasing forces 294, 296 on the pivoting member 280 and/or the bearings 246, 248, 250 directly or indirectly. For example, the biasing members 290 may directly engage the pivoting member 280 and/or the first bearing 246 to apply the biasing forces 294, 296 thereto. In another example, one or more spacers 298 (two are shown) may be interposed between the biasing members 290 and the pivoting members 280 and/or the first bearing 246 such that the biasing members 290 may indirectly engage the pivoting members 280 and/or the first bearing 246 via the spacers 298. The spacers 298 may be configured to facilitate the alignment of the biasing members 290 and/or adjust the load applied to the mobile section 228 of the inlet guide vanes 216.
As previously discussed, the biasing members 290 may be configured to apply the biasing loads 294, 296 or preload to the mobile section 228 of the inlet guide vanes 216 to at least partially hold or urge the mobile section 228 radially outward or radially inward. The biasing members 290 may also be configured to reduce unintentional motions or deflections of the mobile section 228 of the inlet guide vanes 216. For example, during one or more modes of operating the compressor 200, unintentional forces (e.g., vibrational forces, unsteady fluid dynamic forces, etc.) may be exerted on the mobile section 228 of the inlet guide vanes 216 to thereby cause unintentional motions (e.g., fluttering, vibrational motion, rotational motion, axial motion, and/or radial motion) of the mobile section 228. The biasing loads 294, 296 applied by the biasing members 290 may increase frictional forces between the mobile section 228 of the inlet guide vanes 216 and one or more adjacent components (e.g., the casing 202, the spacers 298, the bearings 246, 248, 280, etc.) to counter or resist the unintentional forces and thereby reduce the unintentional motions of the mobile section 228 of the inlet guide vanes 216. The increased frictional forces may advantageously increase frictional damping to thereby minimize unintentional motion of the mobile section 228. The biasing members 290 may also be configured to maintain clearances about the inlet guide vanes 216. For example, the biasing members 290 may be configured to urge the mobile section 228 of the inlet guide vanes 216 radially outward or radially inward to maintain the outer radial clearance 222 and/or the inner radial clearance 224.
Referring back to
In one or more embodiments, the process fluid at the tip 306 of the impeller 300 may be subsonic and have an absolute Mach number less than one. For example, the process fluid at the tip 306 of the impeller 300 may have an absolute Mach number less than 1, less than 0.9, less than 0.8, less than 0.7, less than 0.6, less than 0.5, less than 0.4, less than 0.3, less than 0.2, or less than 0.1. Accordingly, in such embodiments, the compressors 102, 200 discussed herein may be “subsonic,” as the impeller 300 may be configured to rotate about the longitudinal axis 262 at a speed sufficient to provide the process fluid at the tip 306 thereof with an absolute Mach number of less than one.
In one or more embodiments, the process fluid at the tip 306 of the impeller 300 may be supersonic and have an absolute Mach number of one or greater. For example, the process fluid at the tip 306 of the impeller 300 may have an absolute Mach number of at least 1, at least 1.1, at least 1.2, at least 1.3, at least 1.4, or at least 1.5. Accordingly, in such embodiments, the compressors 102, 200 discussed herein are said to be “supersonic,” as the impeller 300 may be configured to rotate about the longitudinal axis 262 at a speed sufficient to provide the process fluid at the tip 306 thereof with an absolute Mach number of one or greater or with a fluid velocity greater than the speed of sound. In a supersonic compressor or a stage thereof, the rotational or tip speed of the impeller 300 may be about 500 meters per second (m/s) or greater. For example, the tip speed of the impeller 300 may be about 510 m/s, about 520 m/s, about 530 m/s, about 540 m/s, about 550 m/s, about 560 m/s, or greater.
As illustrated in
The compressor 200 may include a shroud 310 disposed proximal the impeller 300. For example, the shroud 310 may be disposed adjacent the plurality of blades 304 of the impeller 300. As further illustrated in
In an exemplary operation of the compressor 200, with continued reference to
As previously discussed, the biasing members 290 may be configured to apply the biasing loads 294, 296 to the mobile section 228 of the inlet guide vanes 216, and reduce unintentional motions or deflections of the mobile section 228. For example, the process fluid drawn into the compressor 200 via the inlet passageway 206 may be turbulent, or may exert unintentional forces (e.g., vibrational forces, fluid dynamic forces, etc.) on the on the mobile section to thereby cause unintentional motions or deflections (e.g., fluttering, vibrational motion, rotational motion, axial motion, and/or radial motion) of the mobile section 228. The biasing loads 294, 296 applied by the biasing members 290 may increase frictional forces between the mobile section 228 of the inlet guide vanes 216 and one or more adjacent components (e.g., the casing 202, the bearings 246, 248, 280, etc.) to counter or resist the unintentional forces and thereby reduce the unintentional motions of the mobile section 228 of the inlet guide vanes 216. The biasing members 290 may also be configured to maintain clearances about the inlet guide vanes 216. For example, the biasing members 290 may be configured to urge the mobile section 228 of the inlet guide vanes 216 radially outward or radially inward to maintain the outer radial clearance 222 and/or the inner radial clearance 224.
The foregoing has outlined features of several embodiments so that those skilled in the art may better understand the present disclosure. Those skilled in the art should appreciate that they may readily use the present disclosure as a basis for designing or modifying other processes and structures for carrying out the same purposes and/or achieving the same advantages of the embodiments introduced herein. Those skilled in the art should also realize that such equivalent constructions do not depart from the spirit and scope of the present disclosure, and that they may make various changes, substitutions, and alterations herein without departing from the spirit and scope of the present disclosure.
This application claims the benefit of U.S. Provisional Patent Application having Ser. No. 62/139,068, which was filed Mar. 27, 2015. The aforementioned patent application is hereby incorporated by reference in its entirety into the present application to the extent consistent with the present application.
This invention was made with government support under Government Contract No. DOE-DE-FE0000493 awarded by the U.S. Department of Energy. The government has certain rights in the invention.
Number | Date | Country | |
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62139068 | Mar 2015 | US |