TECHNICAL FIELD
[0001] This disclosure relates to a centrifugal compressor.
BACKGROUND
[0002] Compressors suitable for compressing low density gases such as helium and hydrogen
are typically centrifugal, single-stage, and usually offer low compression ratios.
To achieve higher pressure ratios, compressors may be linked together with multiple
individual compressors in series. This increases weight and cost, as well as increasing
the likelihood of losses. Existing material limits for compressors are generally known
and fixed. A titanium impeller for example is limited to its outer edge periphery
operating at a maximum speed of around 550 metres per second. Since the speed of sound
of helium at atmospheric conditions is over 1000 metres per second, compression is
difficult to achieve in a single stage design. Helium in particular suffers from a
high ratio of specific heats, meaning that more heat is generated through compression
than normal fluids as a result of the molecular degrees of freedom available (three)
compared to diatomic molecules (five or six).
SUMMARY
[0003] In an aspect there is provided a centrifugal compressor 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.
[0004] In an embodiment, the driving arrangement may comprise a motor and a gearbox. The
gearbox may be an epicyclic gearbox comprising a sun gear, a planetary gear and a
ring gear, the impeller being connected to the sun gear and the diffuser connected
to the ring gear.
[0005] In an embodiment, a first end of a rotor of the motor may be connected to the sun
gear and a stator of the motor fixed relative to the planetary gear.
[0006] In an embodiment, where the impeller is a first impeller, the diffuser is a first
diffuser and the epicyclic gearbox a first epicyclic gearbox, the compressor may further
comprise:
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.
[0007] In an embodiment, the driving arrangement may comprise first and second motors, the
impeller and diffuser being connected to respective rotors of the first and second
motors.
[0008] In an embodiment, the impeller may comprise vanes angled towards a direction of rotation
of the impeller. The diffuser may also comprise vanes angled towards a direction of
rotation of the diffuser.
[0009] In an embodiment, the centrifugal compressor may further comprise an inlet inducer
in an inlet gas path of the compressor.
[0010] In an embodiment, the centrifugal compressor may further comprise a housing surrounding
the diffuser and a seal between the housing and the diffuser. The seal may be a labyrinth
seal.
[0011] In an embodiment, the centrifugal compressor may be used for the compression of gas.
The centrifugal compressor may be used for the compression of neon, or hydrogen, or
helium.
BRIEF DESCRIPTION OF THE DRAWINGS
[0012] 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:
Figure 1 is a schematic diagram illustrating example impeller designs with rearward-facing,
perpendicular and forward-facing impeller vanes;
Figure 2 is a schematic sectional diagram of an impeller and diffuser arrangement
of an example centrifugal compressor; and
Figure 3 is a schematic sectional diagram of an example centrifugal compressor.
DETAILED DESCRIPTION
[0013] Figure 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
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.
[0014] An end view of an example centrifugal compressor 200 is illustrated in Figure 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
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
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.
[0015] Figure 3 illustrates an example centrifugal compressor 300 comprising a contra-rotating
impeller and diffuser arrangement. As indicated in the Figure, 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.
[0016] 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.
[0017] 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.
[0018] 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.
[0019] 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.
[0020] 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.
[0021] 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.
[0022] 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.
[0023] 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.
1. A centrifugal compressor (300) comprising:
a first impeller (201a);
a first rotatably mounted diffuser (202a) surrounding the first impeller (201a); and
a driving arrangement (301, 303) configured to drive the first impeller (201a) and
first diffuser (202a) to rotate in opposing directions, the driving arrangement comprising
a motor (301) and a first epicyclic gearbox (303) comprising a sun gear (303a), a
planetary gear (303b) and a ring gear (303c), the first impeller (201) being connected
to the sun gear (303a) and the first diffuser (202) connected to the ring gear (303c),
the compressor (300) further comprising:
a second epicyclic gearbox (304) comprising a sun gear (304a), a planetary gear (304b)
and a ring gear (304c);
a second impeller (201b) connected to the sun gear (304a) of the second epicyclic
gearbox (304) and to a second opposing end of the rotor (301a); and
a second diffuser (202b) connected to the ring gear (304c) of the second epicyclic
gearbox (304); wherein
a first end of a rotor (301a) of the motor (301) is connected to the sun gear (303a)
of the first epicyclic gearbox (303) and a second end of the rotor (301a) of the motor
(301) is connected to the sun gear (304a) of the second epicyclic gearbox (304) and
a stator (301b) of the motor (301) is fixed relative to the planetary gear (303b).
2. The centrifugal compressor (300) of claim 1, wherein the first and second impeller
(201a, 201b) each comprises vanes angled towards a direction of rotation of the respective
impeller.
3. The centrifugal compressor (300) of any preceding claim, wherein the first and second
diffuser (202a, 202b) each comprises vanes angled towards a direction of rotation
of the respective diffuser.
4. The centrifugal compressor (300) of any preceding claim, further comprising an inlet
inducer in an inlet gas path of the compressor (300).
5. The centrifugal compressor (300) of any preceding claim further comprising a housing
(305) surrounding the diffuser (202a) and a seal between the housing and the diffuser
(202a).
6. The centrifugal compressor (300) of claim 10, wherein the seal is a labyrinth seal
(306).
7. Use of the centrifugal compressor (300) of any preceding claim.
8. Use of the centrifugal compressor (300) of any preceding claim for the compression
of neon.
9. Use of the centrifugal compressor (300) of any preceding claim for the compression
of hydrogen.
10. Use of the centrifugal compressor (300) of any preceding claim for the compression
of helium.