This section is intended to introduce the reader to various aspects of art that may be related to various aspects of the present invention, which are described and/or claimed below. This discussion is believed to be helpful in providing the reader with background information to facilitate a better understanding of the various aspects of the present invention. Accordingly, it should be understood that these statements are to be read in this light, and not as admissions of prior art.
As will be appreciated, fluids, such as natural gas and air, have a wide array of uses in industrial and commercial applications. For instance, natural gas may be used to provide power to a range of vehicles, to heat homes during winter, and to operate various consumer appliances, such as ovens or clothes dryers. Further, natural gas may be used to generate electricity for distribution over a power grid, and may be used in the manufacture of an array of products and materials, including glass, steel, and plastics, for example.
In order to meet the demand for natural gas, companies may spend a significant amount of time and resources searching for, extracting, and transporting natural gas. It will be appreciated that natural gas may be produced from oil fields, in which case the gas may be referred to as casinghead gas, or from natural gas fields. As may also be appreciated, transportation of such natural gas, such as through a pipeline from the production site to a consumer, is often facilitated by compression of the gas via a compressor.
One common type of compressor for such applications is the reciprocating compressor. Such reciprocating compressors are positive-displacement devices that generally utilize a crankshaft that is coupled to pistons, via connecting rods and crossheads, to reciprocally drive the pistons and compress a fluid within attached compression cylinders. As may be appreciated by one skilled in the art, natural gas (or some other fluid) is generally introduced into compression chambers of the cylinders through one or more inlet or suction valve assemblies and, following compression, the fluid generally exits the cylinders via one or more outlet or discharge valve assemblies. Unfortunately, existing arrangements may inefficiently route fluids to and from a compressor causing compression losses.
Various features, aspects, and advantages of the present invention will become better understood when the following detailed description is read with reference to the accompanying figures in which like characters represent like parts throughout the figures, wherein:
One or more specific embodiments of the present invention will be described below. In an effort to provide a concise description of these embodiments, all features of an actual implementation may not be described in the specification. It should be appreciated that in the development of any such actual implementation, as in any engineering or design project, numerous implementation-specific decisions must be made to achieve the developers' specific goals, such as compliance with system-related and business-related constraints, which may vary from one implementation to another. Moreover, it should be appreciated that such a development effort might be complex and time consuming, but would nevertheless be a routine undertaking of design, fabrication, and manufacture for those of ordinary skill having the benefit of this disclosure.
When introducing elements of various embodiments of the present invention, the articles “a,” “an,” “the,” and “said” are intended to mean that there are one or more of the elements. The terms “comprising,” “including,” and “having” are intended to be inclusive and mean that there may be additional elements other than the listed elements. Moreover, the use of “top,” “bottom,” “above,” “below,” and variations of these terms is made for convenience, but does not require any particular orientation of the components.
The disclosed embodiments include a co-axial flow device (e.g., toroidal volute) that increases efficiency, and facilitates valve exchange or substitution in a compression system. The co-axial flow device (e.g., toroidal volute) improves the efficiency in the compression system by effectively routing fluid and by reducing unused cylinder space. When a fluid abruptly changes direction or encounters sharply angled surfaces, the fluid loses momentum/energy. The loss in momentum/energy may therefore cause a system to work more to compensate for the losses and to continue moving the fluid. The additional work increases a system's energy consumption/input, thereby reducing the system's overall efficiency. As will be discussed in more detail below, the co-axial flow device (e.g., toroidal volute) reduces resistance to fluid flow by reducing obstacles (i.e., the number of sharp turns and angles that resist fluid flow into and out of the compression system). Moreover, the co-axial flow device (e.g., toroidal volute) routes fluid into and out of one end of a compression cylinder, enabling a piston to extend the length of the cylinder. This reduces unused cylinder space, thereby compressing more fluid per piston stroke. Furthermore, the co-axial flow device (e.g., toroidal volute) enables easy substitution or exchange of valves, to include different kinds of valves. For example, the co-axial flow device (e.g., toroidal volute) enables the system to switch between using a single valve (e.g., concentric valve) and multiple valves (e.g., suction valves, discharge valves, a plate with poppet valves, etc.).
Turning now to the figures, an exemplary compressor system 10 is provided in
The exemplary cylinders 12 may receive and expel gases through a co-axial flow device (e.g., toroidal volute) 18 configured to increase the efficiency of the compressor system 10 by reducing compression losses. In operation, the co-axial flow device (e.g., toroidal volute) 18 enables gas to enter the cylinder 12, where the gas is compressed and then discharged back out of the co-axial flow device 18. However, the co-axial flow device 18 geometry reduces the number of turns and sharp angles that the fluid flows through. With fewer sharp angles and bends, the co-axial flow device 18 enables the fluid to retain more of its velocity, thus reducing compression losses in the compression system 10 as the fluid is more able to maintain momentum. In addition, the co-axial flow device 18 enables pistons within the compression system 10 to extend farther into the cylinders 12, reducing dead space (i.e., space that the cylinders 12 do not travel through). A reduction in dead space enables the pistons to do more work per stroke (i.e., compress more gas per stroke), thus improving the efficiency of the compression system 10.
Although the exemplary compressor system 10 is illustrated as a two-throw reciprocating compressor, other compressor configurations may also employ and benefit from the presently disclosed techniques. For instance, in other embodiments, the compressor system 10 may include a different number of cylinder throws, such as a four-throw compressor, a six-throw compressor, a couple-free reciprocating compressor, a screw compressor, or the like. Further, other variations are also envisaged, including variations in the length of stroke, the operating speed, and the size, to name but a few.
A cross-sectional view of the exemplary compressor system 10 is provided in
In operation, the driver 16 rotates the crankshaft 26 supported within the interior volume 24 of the frame 14. In one embodiment, the crankshaft 26 is coupled to crossheads 30 via connecting rods 28 and pins 32. The crossheads 30 are disposed within crosshead guides 34, which generally extend from the central body 22 and facilitate connection of the cylinders 12 to the compressor system 10. In one embodiment, the compressor system 10 includes two crosshead guides 34 that extend generally perpendicularly from opposite sides of the central body or housing 22, although other configurations are also envisaged. As may be appreciated, the rotational motion of the crankshaft 26 is translated via the connecting rods 28 to reciprocal linear motion of the crossheads 30 within the crosshead guides 34.
As noted above, gas passes through the co-axial flow device 18 and into the cylinders 12 for compression. The crossheads 32 are coupled to pistons 36 disposed within internal compression chambers of the cylinders 12, and the reciprocating motion of the crossheads allows compression of gas within the compression chambers via the pistons 36. Particularly, as a piston 36 is driven forward (i.e., outwardly from central body 22) into a cylinder 12, the piston 36 forces fluid within the cylinder into a smaller volume, thereby increasing the pressure of the gas. The pressurized gas may then exit the cylinder 12 through a valve and into the co-axial flow device 18. The co-axial flow device 18 enables the compressed gas to exit the compression system 10 with minimal compression losses. The piston 36 may then stroke backward, and additional gas may enter the cylinder 12 through the co-axial flow device 18 and an inlet valve, for compression in the same manner as described above.
The co-axial flow device 60 includes a body 62, a first cavity or flow passage 64 (e.g., a curved annular passage, such as a donut-shaped or toroidal shaped passage), a cylindrical member 66, and a second cavity or flow passage 68. As illustrated, the cylindrical member 66 extends into the first cavity 64 and creates the second cavity or flow passage 68. As illustrated, the passage 68 is a central axial passage, the member 66 is an annular wall disposed around the passage 68, and the passage 64 is an annular passage disposed about the member 66. As discussed below, the member 66 may be described as a curved annular wall, which generally defines a curved perimeter extending circumferentially about the central axis of the device 60 to define both a curved annular outer perimeter of the passage 68 and a curved annular inner perimeter of the passage 64.
A fluid is able to enter and exit the co-axial flow device 60 through as series of openings. In the present embodiment, the co-axial flow device 60 includes a first opening 70, a second opening 72, a third opening 74, and a fourth opening 76. These openings 70, 72, 74, and 76 function as inlets and outlets for fluid moving through the co-axial flow device 60 and the compression system 10. The openings 70, 72, 74, and 76 may be inlets or outlets depending on how the fluid flows through the compression system 10. As illustrated, the opening 70 is a radial opening, while openings 72, 74, and 76 are axial openings. Furthermore, the openings 74 and 76 are central axial openings, and opening 72 is an annular axial opening concentric with the central axial opening 74. In operation, a fluid at a first pressure may enter the compressions system 10 and the co-axial flow device 60 through the first opening 70 in a radial direction, as indicated by arrow 69. As the fluid passes through the first opening 70, the fluid enters the first cavity or flow passage 64 and flows around the cylindrical member 66 in a circumferential direction 71 and/or axial direction 73. The first cavity or flow passage 64 turns (e.g., gradually curves or bends) and directs the fluid toward valve(s) 80 resting in the opening 72. The fluid passes through the valve(s) 80 and opening 72, such that the fluid is compressed by the compressor 10. After the fluid is compressed to a second pressure, the fluid flows back through the valve(s) 80 and the third opening 74 and into the cylindrical member 66, i.e., into passage 68. The fluid then passes through the cylindrical member 66 (i.e., passage 68) in the axial direction 75, before exiting the co-axial flow device 60 through the fourth opening or outlet 76.
In another embodiment, the fluid may flow into and out of the compression system 10 in the opposite manner as that described above. For example, fluid at a first pressure may enter the co-axial flow device 60 and the compression system 10 through the opening 76. The fluid may then travel through the second cavity or flow passage 68 of the cylindrical member 66, where the fluid exits the passage 68 through opening 74. As the fluid exits the opening 74, the fluid enters the valve(s) 80 resting in the opening 72. After compression, the valve(s) 80 routes the fluid, now at a second pressure, into the first cavity or flow passage 64. The first cavity or flow passage 64 then turns and directs the fluid out of the system 10 through the opening 70.
As explained above, the co-axial flow device 60 increases the efficiency of the compression system 10 by efficient routing of the fluid into and out of the system 10. A fluid loses momentum/energy when it encounters an obstacle that changes its direction of travel. Accordingly, a system may therefore work more to compensate for losses in fluid momentum as the fluid moves around obstacles (e.g., turns and bends through pipes). The additional work increases a system's energy consumption/input reducing the system's overall efficiency. As seen in
In addition, the co-axial flow device 60 increases system 10 efficiency by reducing sharp angles. As illustrated, the co-axial flow device 60 includes an outer wall 81 (e.g., annular wall) with an interior surface 82 surrounding the first cavity or flow passage 64. The interior surface 82 improves fluid movement with the annular scooped base 84 (e.g., curved annular surface) and the annular sloping surface 86 (e.g., curved annular surface). As illustrated the scooped base 84 has a u-shaped or concave cross-section, which extends circumferentially about the cylindrical member 66 between the member 66 and the outer wall 81. The sloping surface 82 also extends circumferentially about the cylindrical member 66, and generally increases in diameter in the axial direction 73. In operation, as fluid enters the co-axial flow device 60 through the first opening 70, the annular scooped base 84 scoops and turns (e.g., gradually turning) the fluid towards the valve(s) 80, as indicated by arrows 83. As the fluid travels towards the valve(s) 80, the sloping surface 86 gradually channels the fluid into the valve(s) 80. Accordingly, the fluid does not encounter sharp angles or surfaces that might abruptly decrease or stop fluid momentum. Likewise, in embodiments where the fluid flow is in the opposite direction (i.e., from the valve(s) 80 to the opening 70), the interior surface 82 improves fluid flow. Specifically, the sloping surface 86 will allow the fluid to gradually expand into the cavity 64, while the rounded base 84 scoops and turns the fluid towards the opening 70 and out of the co-axial flow device 60. Furthermore, and as explained above, the cylindrical member 66 improves fluid flow by providing a direct path for fluid flow (i.e., no turning of the fluid) between the opening 76 and the valve(s) 80. Moreover, the cylindrical member 66 provides transition zones 88 and 90 to improve fluid flow at the openings 74 and 76. Specifically, transition zone 88 improves fluid flow between the diameter 92 at the opening 76 and the smaller diameter 94 in a central portion 98 of the cylindrical member 66. In particular, the transition zone 88 defines a curved annular transition, which may be described as an outwardly curved portion 85 and an inwardly curved portion 87 extending circumferentially about the passage 68. Furthermore, the transition zone 90 provides a smooth transition between the diameter 94 and the larger diameter 96 of the opening 74. Again, the bore 90 defines a curved annular transition, which may be described as an outwardly and/or inwardly curved portion 89 extending circumferentially about the passage 68. Accordingly, as fluid flows through the second cavity or fluid passage 68, the fluid does not encounter abrupt surfaces that could decrease or stop fluid momentum.
The co-axial flow device 60 couples to and seals with fluid carrying conduits and the compression system 10 with flanges 100, 102, and 104. As explained above, the openings 70 and 76 may function as inlets or outlets. Accordingly, the flange 100 may connect to a conduit supplying fluid while the flange 102 connects to a fluid conduit that carries fluid away from the compression system 10. In other embodiments, the flange 102 may connect to a fluid supply, while the flange 100 connects to a conduit that carries fluid away from the compression system 10. The flange 104 connects the co-axial flow device 60 to the compression cylinder 12, enabling the valve(s) 80, resting in the opening 72, to seal between the first cavity 64 and the second cavity 68, to block fluid at a first pressure from mixing with fluid at a second pressure. Specifically, the valve(s) 80 seal against the interior surface 82 of the co-axial flow device 60 and against a gasket 106 resting in a gasket groove 108 surrounding the opening 74. In this manner, the valve(s) 80 block fluid traveling in the first cavity 64 from contacting the fluid traveling in the second cavity 68.
In another embodiment, the fluid may flow in the opposite direction through the volute 130. That is, the fluid may enter through opening 142 and travel through the cavity 140 and the concentric valve 134 into the compression cylinder 132. The compression cylinder 132 may then compress the fluid, forcing the fluid back through the concentric valve 134 and into the second cavity 148 in the cylindrical member 138, where the fluid exits the volute 130 through the opening 144.
In another embodiment, the fluid may flow in the opposite direction through the volute 130. In an embodiment with a reversed flow configuration, the discharge and suction valves are reversed. That is, the fluid may enter through opening 142 and pass through the cavity 140 and suction valve(s) into the compression cylinder 132. The compression cylinder 132 may then compress the fluid, forcing the fluid through discharge valves and into the second cavity 148 in the cylindrical member 138, where the fluid exits the volute 130 through the opening 144.
As explained above,
While the invention may be susceptible to various modifications and alternative forms, specific embodiments have been shown by way of example in the drawings and have been described in detail herein. However, it should be understood that the invention is not intended to be limited to the particular forms disclosed. Rather, the invention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined by the following appended claims.
This application is a Non-Provisional application and claims priority to U.S. Provisional Patent Application No. 61/801,688, entitled “Compression System and Method Having Co-Axial Flow Device”, filed Mar. 15, 2013, which is herein incorporated by reference.
Number | Date | Country | |
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61801688 | Mar 2013 | US |