CENTRIFUGAL COMPRESSOR

Abstract

A centrifugal compressor is shown, comprising: an impeller; a rotatably mounted diffuser surrounding the impeller; and a driving arrangement configured to drive the impeller and diffuser to rotate in opposing directions.

Claims

1. A centrifugal compressor comprising: a first impeller; a first rotatably mounted diffuser surrounding the impeller; and a driving arrangement configured to drive the first impeller and first diffuser to rotate in opposing directions, the driving arrangement comprising a motor and a first epicyclic gearbox comprising a sun gear, a planetary gear and a ring gear, the first impeller being connected to the sun gear and the first diffuser being connected to the ring gear, the compressor further comprising: a second epicyclic gearbox comprising a sun gear, a planetary gear and a ring gear; a second impeller connected to the sun gear of the second epicyclic gearbox and to a second opposing end of the rotor; and a second diffuser connected to the ring gear of the second epicyclic gearbox; wherein a first end of a rotor of the motor is connected to the sun gear of the first epicyclic gearbox and a second end of the rotor of the motor is connected to the sun gear of the second epicyclic gearbox and a stator of the motor is fixed relative to the planetary gear.

2. The centrifugal compressor of claim 1, wherein the first and second impeller each comprises vanes angled towards a direction of rotation of the respective impeller.

3. The centrifugal compressor of claim 1, wherein the first and second diffuser each comprises vanes angled towards a direction of rotation of the respective diffuser.

4. The centrifugal compressor of claim 1, further comprising an inlet inducer in an inlet gas path of the compressor.

5. The centrifugal compressor of claim 1 further comprising a housing surrounding the first and second diffuser and a seal between the housing and the diffusers.

6. The centrifugal compressor of claim 5, wherein the seal is a labyrinth seal.

7. A method of compressing a gas, the method comprising: rotating a first impeller with a first sun gear of a first epicyclic gearbox, the first sun gear driven by a first end of a rotor of a motor; rotating a first diffuser surrounding the first impeller in an opposite direction to the first impeller using a first ring gear driven by a first planetary gear in the first epicyclic gearbox; passing gas through the first impeller and the first diffuser.

8. The method of claim 7, wherein the gas is neon, hydrogen, or helium.

9. The method of claim 7, wherein the method further comprises: rotating a second impeller with a second sun gear of a second epicyclic gearbox, the second sun gear driven by a second end of the rotor of the motor; rotating a second diffuser surrounding the second impeller in an opposite direction to the second impeller using a second ring gear driven by a second planetary gear in the second epicyclic gearbox; and passing gas through the second impeller and the second diffuser.

10. The method of claim 9, wherein the gas is neon, hydrogen, or helium.

Description

DESCRIPTION OF THE DRAWINGS

[0019] Embodiments will now be described by way of example only with reference to the accompanying drawings, which are purely schematic and not to scale, and in which:

[0020] FIG. 1 is a schematic diagram illustrating example impeller designs with rearward-facing, perpendicular and forward-facing impeller vanes;

[0021] FIG. 2 is a schematic sectional diagram of an impeller and diffuser arrangement of an example centrifugal compressor; and

[0022] FIG. 3 is a schematic sectional diagram of an example centrifugal compressor.

DETAILED DESCRIPTION

[0023] FIG. 1 illustrates three different example impeller designs for a centrifugal compressor. In each case the impeller 101a-c has a central hub 102a-c and a plurality of radially extending vanes 103a-c. In a first example, the impeller 101a has backward-swept vanes 103a, in which the vanes 103a extend radially from the hub 102a angling against the direction of rotation R, with an angle β between the vanes 103a and a tangent of an outer circumference 104 being less than 90 degrees. In a second example, the impeller 101b has radial vanes 103b that remain in line with a radial direction from the hub 102b, with each vane 103b being perpendicular to the outer circumference 104 such that the angle β is 90 degrees. In a third example, the impeller 101c has forward-swept vanes 103c, in which the vanes 103c extend radially from the hub 102c angling towards the direction of rotation R, with the angle β being greater than 90 degrees. The corresponding velocity triangles below each example indicate the impeller gas exit velocity v.sub.2, which increases as the blade angle β increases. Forward-swept vanes 103c therefore allow for a more rapid acceleration of gas flow and consequently a more rapid pressure increase. This results in an increased compression ratio, allowing for more efficient compression in a single stage. In example embodiments having forward-swept vanes, the angle β may be between around 100 and 170 degrees.

[0024] An end view of an example centrifugal compressor 200 is illustrated in FIG. 2. The compressor 200 comprises an impeller 201 and a diffuser 202. The impeller 201 comprises radially outwardly extending vanes 203 that are angled towards a direction of rotation R.sub.I of the impeller 201, i.e. forward-swept. The diffuser 202 comprises radially inwardly extending vanes 205 that are angled towards a direction of rotation R.sub.D of the diffuser 202, i.e. also forward-swept. In conventional applications, the diffuser 202 will be fixed and the impeller rotatable, the compressor 200 comprising a motor configured to drive the impeller 201. In the present embodiment, however, both the impeller 201 and diffuser 202 are rotatable and the compressor 200 is configured to rotate the impeller 201 and diffuser 202 in opposing directions. An advantage of this arrangement is that there is a higher relative tip speed between the impeller and diffuser. With the above-mentioned material limits providing an upper limit on the tip speed of the impeller vanes, the higher relative speed allows for a relative tip speed to be up to Mach 1 even for low density gases such as helium, compared to traditional impellers where the tip speed may be limited to Mach 0.5 or lower. Using such a contra-rotating impeller-diffuser arrangement, the relative speed between the impeller 201 and diffuser 202 can effectively be doubled, allowing not only more efficient compression in a single stage, but also allowing existing materials to be used.

[0025] FIG. 3 illustrates an example centrifugal compressor 300 comprising a contra-rotating impeller and diffuser arrangement. As indicated in FIG. 3, static parts are non-patterned whilst moving components are patterned. The compressor 300 comprises a first impeller 201a and a first diffuser 202a. Gas G to be compressed enters the compressor 300 through a gas path 302, which passes through the impeller 201a and diffuser 202a and exits the compressor 300 from an outer circumference of the diffuser 202a.

[0026] A driving arrangement is configured to drive the impeller 201a and diffuser 202a in opposing directions. The driving arrangement comprises a motor 301 and a gearbox 303. The motor 301 drives the impeller 201a and diffuser 202a in opposing directions via the gearbox 303. In this example the gearbox 303 is an epicyclic gearbox comprising a sun gear 303a, a plurality of planetary gears 303b and a ring gear 303c. The sun gear 303a is driven by the rotor 301a of the motor 301. In alternative arrangements the motor 301 may drive the ring gear 303c instead. The planetary gears 303b are fixed relative to each other and to the stator 301b of the motor 301, which causes the outer ring gear 303c to rotate in an opposing direction to the sun gear 303a. A ratio between the rotational speeds of the ring gear 303c and sun gear 303a is selectable by selecting the relative sizes of the gears 303a-c. The rotor 301a and sun gear 303a are connected to the impeller 201a, while the ring gear 303c is connected to the diffuser 202a. The ring gear 303c may be integral with the diffuser 202a or may be separate components that are joined to each other.

[0027] A second impeller 201b and a second diffuser 202b is also be driven by the same motor 301 via a second gearbox 304. In this way, axial loads may be balanced. The second gearbox 304 is similar to the first gearbox 303 in having a sun gear 304a connected to the impeller 201b and to an opposing end of the rotor 301a, planetary gears 304b fixed relative to the stator 301b and an outer ring gear 304c connected to the diffuser 202b.

[0028] Alternative examples which are outside the scope of the present application may include separate motors driving the impeller 201a and diffuser 202a. An advantage of using a single motor is that the compressor may be made more compact.

[0029] The compressor 300 comprises a housing 305 surrounding the motor 301 and diffuser 202a. The housing may also define the gas path 302. A seal is required between the housing 305 and the diffuser 202a that prevents gas from leaking away from the gas path 302. The seal may be in the form of a labyrinth seal 306 used between the ring gear 303c and the housing 305. Other ways of sealing against the housing 305 may alternatively be used, such as an air bearing seal.

[0030] In some examples, an inlet inducer may be provided in the gas path 302 leading to the impeller 201a to increase a static pressure of gas entering the compressor 300.

[0031] Using a single motor 301 to drive impellers 201a, 201b and diffusers 202a, 202b at opposing ends of the rotor 301a has a further advantage of allowing high aerodynamic load stresses to be better managed as well as providing improved gas sealing, which is particularly difficult for low density gases such as helium. In alternative examples a single-sided compressor may be sufficient.

[0032] A centrifugal compressor 200 of the type disclosed herein may be particularly useful for compressing gases that are normally more difficult to compress such as neon, hydrogen, and helium. A compressor of the type disclosed herein may also enable smaller and lighter compressors for other gases, particularly where fixed pressure ratios are desired.

[0033] Various examples have been described, each of which comprise various combinations of features. It will be appreciated by those skilled in the art that, except where clearly mutually exclusive, any of the features may be employed separately or in combination with any other features and thus the disclosed subject-matter extends to and includes all such combinations and sub-combinations of the or more features described herein.