In the accompanying drawings:
Referring to
The diffuser 10 is located between the forward 32 and aft 26 annular walls and comprises first 10.1 and second 10.2 annular portions, the former of which is upstream of the latter. The first annular portion 10.1 is concentric with, radially adjacent to, and around, a circumferential discharge boundary 42 of the impeller 14. The second annular portion 10.2 is concentric with, radial adjacent to, and around, a radially outer boundary 44 of the first annular portion 10.1, and a radially outer boundary 46 of the second annular portion 10.2 is concentric with, radial adjacent to, and within the collector 16. Accordingly, compressed gases 18′ from the impeller 14 are first discharged therefrom into the first annular portion 10.1, and after flowing therethough, then flow through the second annular portion 10.2, after which the resulting diffused compressed gases 18″ are discharged therefrom into the collector 16.
The first annular portion 10.1 of the diffuser 10 is vaneless and the second annular portion 10.2 incorporates a plurality of vanes 48, wherein the vaneless first annular portion 10.1 provides for reducing the velocity of the compressed gases 18′ prior to entering the vaned second annular portion 10.2. For example, the radius ratio of the first annular portion 10.1—i.e. the ratio of the radius of the radially outer boundary 44 of the first annular portion 10.1 to the outer radius of the impeller 14—is sufficiently great that the mean velocity of compressed gases 18′ is reduced within the first annular portion 10.1 to Mach 0.7 or less upon entering the second annular portion 10.2. Upon exiting the second annular portion 10.2, the mean velocity of the compressed gases 18′ is reduced to a sufficiently low velocity, for example, less than Mach 0.5, so that the compressed gases 18′ substantially act as an incompressible fluid. For example, in one embodiment, the mean velocity of the compressed gases 18′ is reduced to about Mach 0.45 upon exiting the second annular portion 10.2 of the diffuser 10.
At least one of the forward 32 or aft 26 annular walls abutting the second annular portion 10.2 of the diffuser 10 is sloped so that the axial gap 40′ between the forward 32 and aft 26 annular walls increases with respect to radial distance R from the central axis 38, so as to provide for a meridional divergence of the diffuser 10 within the second annular portion 10.2 thereof, for example, in a range of 1.4 to 2.0, wherein meridional divergence is defined as the ratio of the axial gap 40′ at the exit 10.2″ of the second annular portion 10.2 to the axial gap 40′ at the entrance 10.2′ of the second annular portion 10.2. The axial extent of the vanes 48 within the second annular portion 10.2 also varies with respect to radial distance R from the central axis 38, so as to substantially conform to the axial gap 40′, wherein the vanes 48 provide for substantially preventing wall separation of the compressed gases 18′ flowing therethrough, so that the associated flow of compressed gases 18′ remains attached to the forward 32 and aft 26 annular walls while flowing through the meridionally divergent second annular portion 10.2, so that the meridional divergence provides for further diffusing the compressed gases 18′ flowing therethrough. Referring to
Each of the plurality of vanes 48 of the second annular portion 10.2 of the diffuser 10 is oriented to as to substantially conform to what would be the corresponding direction of the flow field within the second annular portion 10.2 but with the vanes 48 absent. As a result, for each vane 48 of the plurality of vanes 48, an angle of a tangent to a surface of the vane 48 varies with axial position along the vane 48, and the angle of the tangent to the surface of the vane 48 varies with radial position along the vane 48. More particularly, in one set of embodiments, each vane 48 of the plurality of vanes 48 is shaped so a variation of the angle of the tangent of the surface of the vane 48 with respect to axial position along the vane 48 and with respect to radial position along the vane 48 substantially corresponds to simulated directions of flow within regions of the second annular portion 10.2 adjacent to the vane 48 for at least one operating condition when the impeller 14 cooperates with the diffuser 10. Accordingly, each vane 48 is twisted along a length thereof so that the angle of the vane 48 relative to a longitudinal axis thereof varies with position along the vane 48, with the leading-edge (LE) angle of each vane 48 substantially matched to the measured or analytically-or-computationally predicted flow discharge conditions at the exit of the first annular portion 10.1, and with the exit angle of each vane 48 substantially matched to the inlet flow conditions of the collector 16. For example, in one set of embodiments, the shape of the vane 48 is configured to optimize the inlet conditions of the collector 16, for example, so as to safely maximize the loading of the vanes 48 and provide for relatively uniform exit conditions, with the collector 16 similarly designed to match the exit conditions of the vaned second annular portion 10.2 of the diffuser 10.
The second annular portion 10.2 is relatively compact, and the plurality of vanes 48 therein are of relatively high solidity. For example, the second annular portion 10.2 is configured with a radius ratio in the range of 1.08 to 1.20, and the solidity of the plurality of vanes 48 is generally within a range of 1.8 to 4.0, and, in one set of embodiments, within the range of 3.0 to 3.5, wherein solidity is defined as the ratio of the choral length of each vane 48 to the mean circumferential spacing between the vanes 48. Referring to
The orientation and slope of the leading-edge portions 48.1 of the vanes 48 are adapted to match the measured or analytically-or-computationally predicted exit flow conditions of the first annular portion 10.1, and, as described hereinabove, the orientation and slope of the trailing-edge portions 48.2 of the vanes 48 are adapted to match the entrance flow conditions of the collector 16. For example, in one set of embodiments, the trailing-edge portions 48.2 are configured so as to provide for a flow entrance angle 52 of 60 to 80 degrees—relative to the radial direction—with relatively low mean velocities in the range of 0.2 to 0.45 Mach number under substantially all operating conditions of the radial compressor 12. In one set of embodiments, each of the trailing-edge portions 48.2 is oriented at a uniform angle. Alternatively, referring to
Furthermore, referring to
In accordance with a method of diffusing a flow of gases 18 from an impeller 14—provided for as described hereinabove,—the gases 18 are first directed from the impeller 14 into a first annular portion 10.1 of a diffuser 10, wherein the first annular portion 10.1 is bounded by forward 32 and aft 26 annular walls, the first annular portion 10.1 is vaneless, and the first annular portion 10.1 is of sufficient radial extent so that the flow of gases 18 from the impeller 14 is reduced in velocity from a relatively high velocity upon entrance to the first annular portion 10.1 to a mean velocity less than a Mach number threshold upon exiting the first annular portion 10.1, wherein the Mach number threshold is in the range of 0.7 to 0.4. Then, the gases 18 exiting the first annular portion 10.1 are directed into a second annular portion 10.2 of the diffuser 10, wherein the second annular portion 10.2 is bounded by the forward 32 and aft 26 annular walls, and the second annular portion 10.2 is concentric with, radial adjacent to, and around, a radially outer boundary 44 of the first annular portion 10.1. The gases 18 flowing through the second annular portion 10.2 are directed through a plurality of vanes 48 therewithin, wherein a contour of each vane 48 of the plurality of vanes 48 is shaped so as to substantially match a direction of the gas flow adjacent to the vane 48 for at least one operating condition during operation of the diffuser 10; and the gases 18 are also meridionally diverged while flowing through the second annular portion 10.2 of the diffuser 10. The gases flow from the second annular portion 10.2 of the diffuser 10 directly into a collector 16, for example, a plenum 16′ or volute 16″.
The combination of the vaneless first annular portion 10.1 with the twisted vanes 48 or relatively-high solidity within the meridionally-divergent second annular portion 10.2 provides for a relatively-compact diffuser 10, and provides for relatively-improving the efficiency of an associated volute 16″.
In accordance with one embodiment, the radial compressor 12 incorporating the diffuser 10 is incorporated as the compressor of a turbocharger or supercharger (not illustrated), wherein the aft annular wall 26 of the radial compressor 12 is either operatively coupled to or a part of a centerbody 24 of the turbocharger or supercharger, wherein the centerbody 24 incorporates a plurality of bearings that support a rotor shaft that operatively couples the impeller 14 of the radial compressor 12 to a source of shaft power, for example, either an exhaust driven turbine of a turbocharger, a pulley or sprocket of an engine-driven supercharger, or an electric motor of a motor-driven supercharger.
It should be understood that the diffuser 10 is not limited to application either in combination with a radial compressor 12 as illustrated hereinabove, or to diffusing the flow of a gaseous medium. More particularly, it should be understood that the same type of diffuser 10 could also be utilized with either an axial-flow compressor with a significant non-axial—i.e. radial—exit flow region, or a mixed-flow compressor, i.e. wherein the gas flow exits the compressor in a direction other than purely radial or purely axial. Furthermore, it should be understood that the same type of diffuser 10 could also be utilized in cooperation with a pump rather than a compressor, for example, so as to provide for diffusing a flow of a liquid exiting the pump.
The vanes 48 of the diffuser 10 can be manufactured in a variety of ways, including, but not limited to, machining—for example, milling, Electrical Discharge Machining (EDM) or Electro Chemical Machining (ECM),—casting or additive manufacturing, either integral with the aft 26 or forward 32 annular walls of the diffuser 10, or formed individually in accordance with any of the above methods, or by stamping or forging, followed by insertion of or cooperation of the individually manufactured vanes 48 into or with slots or receptacles in the aft 26 or forward 32 annular walls of the diffuser 10. Referring to
While specific embodiments have been described in detail in the foregoing detailed description and illustrated in the accompanying drawings, those with ordinary skill in the art will appreciate that various modifications and alternatives to those details could be developed in light of the overall teachings of the disclosure. It should be understood, that any reference herein to the term “or” is intended to mean an “inclusive or” or what is also known as a “logical OR”, wherein when used as a logic statement, the expression “A or B” is true if either A or B is true, or if both A and B are true, and when used as a list of elements, the expression “A, B or C” is intended to include all combinations of the elements recited in the expression, for example, any of the elements selected from the group consisting of A, B, C, (A, B), (A, C), (B, C), and (A, B, C); and so on if additional elements are listed. Furthermore, it should also be understood that the indefinite articles “a” or “an”, and the corresponding associated definite articles “the’ or “said”, are each intended to mean one or more unless otherwise stated, implied, or physically impossible. Yet further, it should be understood that the expressions “at least one of A and B, etc.”, “at least one of A or B, etc.”, “selected from A and B, etc.” and “selected from A or B, etc.” are each intended to mean either any recited element individually or any combination of two or more elements, for example, any of the elements from the group consisting of “A”, “B”, and “A AND B together”, etc. Yet further, it should be understood that the expressions “one of A and B, etc.” and “one of A or B, etc.” are each intended to mean any of the recited elements individually alone, for example, either A alone or B alone, etc., but not A AND B together. Furthermore, it should also be understood that unless indicated otherwise or unless physically impossible, that the above-described embodiments and aspects can be used in combination with one another and are not mutually exclusive. Accordingly, the particular arrangements disclosed are meant to be illustrative only and not limiting as to the scope of the invention, which is to be given the full breadth of the appended claims, and any and all equivalents thereof.
The instant application claims the benefit of prior U.S. Provisional Application Ser. No. 61/893,518 filed on 21 Oct. 2013, which is incorporated herein by reference.
Filing Document | Filing Date | Country | Kind |
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PCT/US2014/061613 | 10/21/2014 | WO | 00 |
Number | Date | Country | |
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61893518 | Oct 2013 | US |