The present invention relates to a scroll compressor.
A prior art scroll compressor, or pump, 100 is shown in
The fixed scroll 112 comprises a scroll wall 118 which extends perpendicularly to a generally circular base plate 120. The orbiting scroll 110 comprises a scroll wall 124 which extends perpendicularly to a generally circular base plate 126. The orbiting scroll wall 124 co-operates, or meshes, with the fixed scroll wall 118 during orbiting movement of the orbiting scroll. Relative orbital movement of the scrolls causes a volume of gas to be trapped between the scrolls and pumped from the inlet to the outlet.
The specific scroll arrangement shown in
As indicated above, in some applications it is desirable to increase a capacity of a scroll pump, and the arrangement shown in
The present invention seeks to provide a scroll compressor having increased capacity and yet does not suffer, at least to the same extent, from one or more of the problems associated with prior art arrangements.
The present invention provides a scroll compressor comprising a scroll pumping arrangement comprising two scrolls each having a scroll wall with inner and outer scroll wall surfaces which co-operate with respective outer and inner scroll wall surfaces of the other scroll wall providing two pairs of co-operating surfaces which, on relative orbiting motion of the scrolls, pump fluid from an inlet to an outlet of the arrangement, the scroll walls having a respective plurality of wraps between the inlet and the outlet and wherein the co-operating scroll wall surfaces of one of said pairs of at least one wrap are generally circular.
The present invention also provides a scroll compressor comprising a scroll pumping arrangement comprising two scrolls each having a scroll wall with inner and outer scroll wall surfaces which co-operate with respective outer and inner scroll wall surfaces of the other scroll wall providing two pairs of co-operating surfaces which, on relative orbiting motion of the scrolls, pump fluid from an inlet to an outlet of the arrangement, the scroll walls having a respective plurality of wraps between the inlet and the outlet and wherein the co-operating scroll wall surfaces of one of said pairs of at least one wrap have a rate of change of radius with respect to the angle which is less than said rate of change of the other wraps so that the compression ratio of said one of said pairs is less than for the other wraps.
Other preferred and/or optional aspects of the invention are defined in the accompanying claims.
In order that the present invention may be well understood, an embodiment thereof, which is given by way of example only, will now be described with reference to the accompanying drawings, in which:
A scroll compressor, or pump, 10 is shown in
The fixed scroll 22 comprises a scroll wall 28 which extends perpendicularly to a generally circular base plate 30. The orbiting scroll 20 comprises a scroll wall 34 which extends perpendicularly to a generally circular base plate 36. The orbiting scroll wall 34 co-operates, or meshes, with the fixed scroll wall 28 during orbiting movement of the orbiting scroll. Relative orbital movement of the scrolls causes a volume of gas to be trapped between the scrolls and pumped from the inlet to the outlet.
As shown in
Typically, the co-operating scroll wall surfaces of a scroll pump are involute, or spiral. Since the volume of fluid trapped by each pair of co-operating surfaces reduces as the volume approaches the outlet 26 the pump compresses the fluid. As indicated above with reference to the prior art, many attempts have been made to increase pumping capacity, or the amount of fluid that can be pumped. These attempts have produced increased capacity but suffer from disadvantages such as reduced compression or increased back leakage. In the present invention, one pair of scroll wall surfaces is not involute but instead is substantially circular.
For Archimedean spirals and large angles of an involute, the geometry of a spiral in prior art pumps is such that the rate of change of the radius is generally constant with respect to the change in the angle. Where r is the radius and θ is the angle about the centre of the spiral, for an Archimedean spiral (r=aθ), dr/dθ=a, which is constant. For an involute, dr/dθ is not constant but changes a lot over the first 1/2 turn and then it tends to a single value. In other words, for large angles, it becomes reasonable constant. For a circle, dr/dθ=0. That is, dr/dθ is a constant.
In the present invention, dr/dθ for at least one of the pairs of scroll surfaces 38, 42; 40, 44 for at least one wrap I, II, II, IV, V is reduced such that the spiral tends towards a circular path and departs from a geometrical spiral or involute as defined above. That is, if dr/dθ equals ‘a’ for a spiral and 0 for a circle, then for embodiments of the invention dr/dθ equals a value between ‘a’ and 0, preferably approaching 0. In its most preferred example therefore, the scroll wall surfaces are circular, although benefits of the invention can be achieved by decreasing dr/dθ thereby increasing the trapped volume between the scroll wall surfaces. Therefore, decreasing dr/dθ increases pumping capacity and decreases compression. The circular or generally circular scroll wall surfaces may be located at any one of the wraps I, II, III, IV, V, or may be located at more than one wrap or at all of the wraps, the latter of which is shown in the example described in more detail below with reference to
In the first example as shown in
Typically, as shown in
It will be appreciated that a single circular wrap does not achieve compression since the trapped volume between co-operating scroll wall surfaces is not reduced by pumping along a circular surface. However, capacity is increased because the circular scroll wall surfaces are inherently able to trap more volume than spiral surfaces at the same radius and hence greater capacity is achieved. Furthermore, if the co-operating surfaces of the outer scroll wrap are circular, a previously unused region of the pump is brought within the pumping volume.
Referring again to
It will be noted that the transition between circular and spiral pumping surfaces may take place on any of the wraps of the orbiting scroll or any of the wraps of the fixed scroll (except the outer wrap of the fixed scroll).
The inlet 24 to the scroll pumping arrangement shown in
A problem that exists with multi-start arrangements occurs where the pumping channels converge as shown by 150 in
In the embodiment of the invention, the pumping channels 50, 52 converge at 54 and the convergence is a source of some pumping inefficiency as the tip seals are discontinuous thereby reducing the capacity of the pump. However, the increased pumping capacity produced by the circular pumping channel 50 at least partially and preferably fully compensates for the back-leakage at the convergence 54. In this regard, pumping channel 50 has two pairs of co-operating surfaces formed on both sides of the outer wrap V of the orbiting scroll wall 34. Accordingly, the embodiment provides a multi-start scroll pumping arrangement which does not suffer from reduced efficiency.
Whilst a multi-start arrangement is shown in
In an alternative arrangement, a multi-start or single start scroll arrangement comprises one or more circular pumping channels and one or more involute pumping channels and the circular pumping channels are deeper than the involute pumping channels. The transition from deep to shallow channels in prior art pumps can often be a cause of inefficiency because the tip seals are not continuous. In this example of the invention however, the circular nature of the deeper pumping channels compensates for the back-leakage caused at the transition.
In a further scroll pumping arrangement, there are one or more circular pumping channels and one or more involute pumping channels, and a flow intersection between the circular pumping channels and the involute pumping channels is in flow communication with a blow-off valve for releasing over pressure from the scroll arrangement. The intersection is a suitable location for the blow-off valve as it is located at the transition between a high capacity region and a low capacity region and when running at high inlet pressures substantial over-pressure may occur.
A still further scroll arrangement is shown in
As shown in
With regard to the outer pumping channel 68, the fixed scroll wall sections of wraps III and IV form outer 76 and inner 78 scroll wall surfaces respectively. The orbiting scroll wall section of wrap IV forms inner 80 and outer 82 scroll wall surfaces which co-operate with respective outer 76 and inner 78 of the fixed scroll wall surfaces forming two pairs of co-operating surfaces 76, 80; 78, 82 in pumping channel 68. On relative orbiting motion of the scrolls, fluid in the outer pumping channel 68 is trapped between both pairs of co-operating surfaces and pumped from a channel inlet 84 to a channel outlet 86.
Each pumping channel extends through less than 360° (although not substantially less than 360°, e.g. about 350°) so that the pumping channel forms an incomplete circle. The ends of each pumping channel are closed by one or more wall closures 88, 90 thereby separating the inlet from the outlet in a pumping channel. The closures are arcuate so that an end of an orbiting scroll wall section sweeps across its face during orbiting motion. This arrangement allows fluid to be trapped efficiently by the orbiting scroll wall.
The outlet 86 of each channel is connected by a duct (shown by arrows 92) to an inlet 84 of the next inward pumping channel. Trapped fluid in channel 68 is forced along a duct 92 entering channel 70 and so on until fluid is forced through the outlet of the most inward channel 74 to the outlet 66 of the pumping arrangement. As fluid is pumped from one channel to the next it becomes compressed because the trapped volume becomes progressively smaller. Accordingly, compression occurs even though all the pumping channels, and co-operating surfaces are circular.
Circular wall profiles are easier to design, manufacture and inspect. The simple profile allows better tolerances to be achieved. Having all the wraps as circular avoids over compression between any of the stages, which maximises pumping efficiency.
In
In a multi-start pump, one pumping channel at a first start may be circular, a plurality of pumping channels at more than one start may be circular or all of the pumping channels at all of the starts may be circular.
Number | Date | Country | Kind |
---|---|---|---|
1212026.7 | Jul 2012 | GB | national |
This application is a national stage entry under 35 U.S.C. §371 of International Application No. PCT/GB2013/051517, filed Jun. 10, 2013, which claims the benefit of G.B. Application 1212026.7, filed Jul. 6, 2012. The entire contents of International Application No. PCT/GB2013/051517 and G.B. Application 1212026.7 are incorporated herein by reference.
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/GB2013/051517 | 6/10/2013 | WO | 00 |