This invention relates to turbomolecular vacuum pumps and hybrid vacuum pumps and, more particularly, to vacuum pumps having pumping channel configurations which assist in achieving improved performance in comparison with prior art vacuum pumps.
Conventional turbomolecular vacuum pumps include a housing having an inlet port, an interior chamber containing a plurality of axial pumping stages and an exhaust port. The exhaust port is typically attached to a roughing vacuum pump. Each axial pumping stage includes a stator having inclined blades and a rotor having inclined blades. The rotor and stator blades are inclined in opposite directions. The rotor blades are rotated at high rotational speed by a motor to pump gas between the inlet port and the exhaust port. A typical turbomolecular vacuum pump may include nine to twelve axial pumping stages.
Variations of the conventional turbomolecular vacuum pump, often referred to as hybrid vacuum pumps, have been disclosed in the prior art. In one prior art configuration, one or more of the axial pumping stages are replaced with molecular drag stages, which form a molecular drag compressor. This configuration is disclosed in U.S. Pat. No. 5,238,362, issued Aug. 24, 1993 and assigned to Varian, Inc. sells hybrid vacuum pumps including an axial turbomolecular compressor and a molecular drag compressor in a common housing. Molecular drag stages and regenerative stages for hybrid vacuum pumps are disclosed in Varian, Inc. owned U.S. Pat. No. 5,358,373, issued Oct. 25, 1994. Other hybrid vacuum pumps are disclosed in U.S. Pat. No. 5,221,179 issued Jun. 22, 1993; U.S. Pat. No. 5,848,873, issued Dec. 15, 1998 and U.S. Pat. No. 6,135,709, issued Oct. 24, 2000. Improved impeller configurations for hybrid vacuum pumps are disclosed in Varian, Inc.'s owned U.S. Pat. No. 6,607,351, issued Aug. 19, 2003.
Molecular drag stages include a rotating disk, or impeller, and a stator. The stator defines a tangential flow channel and an inlet and an outlet for the tangential flow channel. A stationary baffle, often called a stripper, disposed in the tangential flow channel separates the inlet and the outlet. The momentum of the rotating disk is transferred to gas molecules within the tangential flow channel, thereby directing the molecules toward the outlet. Molecular drag stages were developed for molecular flow conditions. In molecular flow, pumping action is produced by a fast moving flat surface dragging molecules in the direction of movement.
When viscous flow is approached, the simple momentum transfer does not work as well, because of increased backward flow due to the establishment of a pressure gradient rather than a molecular density gradient. As a result, the molecular drag stage may not achieve the desired pressure difference in viscous flow conditions.
Accordingly, there is a need for improved molecular drag stages for vacuum pumps.
According to a first aspect of the invention, a vacuum pump comprises a housing having an inlet port and an exhaust port, at least one molecular one drag stage located within the housing and disposed between the inlet port and the exhaust port, the molecular drag stage including a rotor comprising a molecular drag disk and a stator that defines a tangential flow channel which opens onto a surface of the disk, the stator further defining at least one obstruction in the channel so as to induce turbulent flow in a selected pressure range, and a motor to rotate the rotor of the molecular drag stage so that gas is pumped from the inlet port to the exhaust port.
According to a second aspect of the invention, a vacuum pump comprises a housing having an inlet port and an exhaust port, at least one molecular drag stage located within the housing and disposed between the inlet port and the exhaust port, the molecular drag stage including a rotor and a stator, the stator defining a tangential flow channel which opens onto a surface of the rotor, a baffle that blocks the channel at a circumferential location, and one or more obstructions in the channel that alter gas flow through the channel, and a motor to rotate the rotor of the molecular drag stage so that gas is pumped from the inlet port to the exhaust port.
For a better understanding of the present invention, reference is made to the accompanying drawings, which are incorporated herein by reference and in which:
A simplified cross-sectional diagram of a high vacuum pump in accordance with an embodiment of the invention is shown in
Located within housing 10 are vacuum pumping stages 30, 32, . . . , 46. Each vacuum pumping stage includes a stationary member, or stator, and a rotating member, also known as an impeller or a rotor. The rotating member of each vacuum pumping stage is coupled by a drive shaft 50 to a motor 52. The shaft 50 is rotated at high speed by motor 52, causing rotation of the rotating members about a central axis 54 and pumping of gas from inlet port 14 to exhaust port 16. The embodiment of
The vacuum pumping stages 30, 32, . . . , 46 may include one or more axial flow vacuum pumping stages and one or more molecular drag stages. In some embodiments, one or more regenerative vacuum pumping stages may be included. The number and types of vacuum pumping stages are selected based on the application of the vacuum pump.
An example of an axial flow vacuum pumping stage is shown in
An example of a molecular drag vacuum pumping stage is illustrated in
Referring to
The upper stator portion 202 is provided with an upper channel 210. The channel 210 is located in opposed relationship to the upper surface of disk 200. The lower stator portion 204 is provided with a lower channel 212, which is located in opposed relationship to the lower surface of disk 200. In the embodiment of
In operation, disk 200 is rotated at high speed about shaft 50. Gas is received from the previous stage through conduit 216. The previous stage can be a molecular drag stage, an axial flow stage, or any other suitable vacuum pumping stage. The gas is pumped around the circumference of upper channel 210 by molecular drag produced by rotation of disk 200. The gas then passes through conduit 220 around the outer periphery of disk 200 to lower channel 212. The gas is then pumped around the circumference of lower channel 212 by molecular drag and is exhausted through conduit 224 to the next stage or to the exhaust port of the pump. Thus, upper channel 210 and lower channel 212 are connected such that gas flows through them in series. In other embodiments, the upper and lower channels may be connected in parallel. Two or more concentric pumping channels can be used, connected in series. While the molecular drag stage of
When the pressure level in a molecular drag vacuum pumping stage increases from molecular flow to viscous flow, the compression ratio may decrease significantly, thereby degrading performance. According to an aspect of the invention, the tangential flow channel in the stator of the molecular drag stage is configured to increase the pressure level at which the decrease in compression ratio occurs.
Generally speaking, compression ratios in molecular flow are higher than in viscous flow because the molecules are not subject to a reverse pressure gradient due to the absence of intercollisions. When viscous flow conditions are reached, instability develops. Instead of having reasonably uniform density distributions across the channel and along the length of the channel, the flow may separate, find paths of least resistance and may develop backward streamers, or backward flow. This is the phenomenon which reduces the compression ratio.
Depending on the geometry of the pumping channel and the geometric relationship between the moving and stationary surfaces, the backward streamers may develop in different areas of the cross section. For example, in a tube of circular cross section with a moving wall, the backward streamer may develop in the center. In a configuration where the rotating disk extends into the channel, the backward streamers may develop in corners of the channel farthest from the rotating disk. In a channel that faces a surface of a rotating disk, the backward streamer may develop at the position of lowest peripheral velocity.
It has been recognized that the tendency for backward flow is greater in areas of the channel where the velocity of the adjacent rotating disk is relatively low. In addition, the tendency for backward flow is greater in areas of the channel that are farthest from the rotating disk. Thus, for example, backward flow may develop in an area of the channel, such as a corner of the channel, that is closest to the axis of rotation and that is spaced from the rotating disk. These principles are applied to provide channel configurations having improved performance under viscous or partially viscous flow conditions.
The cross-sectional shape of the channel in a conventional molecular drag stage is rectangular, as shown for example in
According to an aspect of the invention, the circumferential configuration of the channel in the stator is modified to provide improved performance under viscous or partially viscous flow conditions. More particularly, the channel is configured with obstructions which alter gas flow through the channel and which create turbulence in the channel.
A schematic cross-sectional plan view of a molecular drag stage in accordance with a first embodiment of the invention is shown in
As shown in
The obstructions in the channel 306 of stator 300 may have various configurations within the scope of the invention. In the embodiment of
A schematic cross-sectional plan view of a molecular drag stage in accordance with a fourth embodiment of the invention is shown in
In the embodiment of
A schematic cross-sectional plan view of a molecular drag stage in accordance with a fifth embodiment of the invention is shown in
The channel 402 in stator 400 is defined by walls which alternate in direction, but follow a roughly circular path, to define a zigzag channel. Thus, channel 402 includes sections 410, 412, 414, etc. which alternate in direction to define a zigzag channel. The changes in wall direction serve as obstructions to smooth gas flow and thereby reduce the tendency for backward flow in channel 402. The size of the changes in direction of channel 402 and the number of changes in direction are selected depending on the application of the molecular drag stage. Further, the changes in direction of the channel can be produced by variations in the outer wall of channel 402, the inner wall of channel 402, the top wall of channel 402 or some combination of the channel walls. In one example, the inner and outer walls of channel 402 have more or less matching changes of direction.
A schematic cross-sectional plan view of a molecular drag stage in accordance with a sixth embodiment of the invention is shown in
In the embodiment of
A schematic cross-sectional plan view of a molecular drag stage in accordance with a seventh embodiment of the invention is shown in
A schematic cross-sectional plan view of a molecular drag stage in accordance with an eighth embodiment of the invention is shown in
A schematic partial cross-sectional plan view of a molecular drag stage in accordance with a ninth embodiment of the invention is shown in
Various channel configurations have been shown and described to limit the tendency for backward flow in the channel. The shape, dimensions and number of the obstructions in the channel may be selected, depending on the expected operating pressure of the molecular drag stage in the vacuum pump. In a vacuum pump having two or more molecular drag stages, the shape, dimensions and number of obstructions in the channel of each stage may be selected according to the expected operating pressure of the respective stage. Therefore, different stages of the same vacuum pump may have different channel configurations.
Having thus described several aspects of at least one embodiment of this invention, it is to be appreciated various alterations, modifications, and improvements will readily occur to those skilled in the art. Such alterations, modifications, and improvements are intended to be part of this disclosure, and are intended to be within the spirit and scope of the invention. Accordingly, the foregoing description and drawings are by way of example only.
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Number | Date | Country | |
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20080056885 A1 | Mar 2008 | US |