The invention relates to evacuation devices.
If in a process chamber, or in any other vacuum chamber, pressures are supposed to be generated which lie in the high vacuum range (<=10−3 mbar), it is customary to use evacuation devices with a suction-side vacuum pump and an atmospheric pressure-side vacuum pump (backing vacuum pump). The suction-side vacuum pump is, as a rule, a mechanical, kinetic vacuum pump. Among these are gas ring vacuum pumps and turbo vacuum pumps (axial, radial) as well as molecular and turbomolecular vacuum pumps.
At pressures of said type the gases to be conveyed behave molecularly, that is, in such a way that a directed flow can only be achieved by pump structures which give the individual gas molecules pulses with a preferred direction, the desired direction. Since the gas molecules in the chamber to be evacuated have no preferred direction, only those gas molecules get into the suction nozzles of the connected vacuum pump which randomly have this direction of motion.
From U.S. Pat. No. 4,978,276, an evacuation device of the type relevant here is known. The rotor and stator of the mechanical-kinetic vacuum pump are formed to be cylindrical. In order to achieve the result that as many gas molecules as possible go into the suction nozzles of the vacuum pump connected to the chamber, i.e. the suction-side vacuum pump, the rotor has a conical hub whose diameter increases in the direction of the pressure side. The width of the webs between the hub and the cylindrical inner face of the stator decreases accordingly in the direction of the pressure side. This realization has the advantage that the inlet cross-section for the gases behaving molecularly, i.e. the suction-side annular surface in which the gases to be conveyed enter, is relatively large. An evacuation device of the known type is thus particularly suitable for those applications in which there is a demand for high gas throughputs.
The objective of the present invention is to further improve an evacuation device of the type relevant here with respect to the demand for high gas through puts.
At the suction-side annular surface, gases behaving molecularly enter in the radial direction. An enlargement of the inlet cross-section is achieved, even in the case of a cylindrical structure of the rotor hub, since the inlet cross-section increases quadratically with the radius. Furthermore, the radially outermost edges of the rotor's components (webs) effecting the gas conveyance have, as a consequence, higher circumferential speeds, whereby the gas throughput is further increased.
It is particularly advantageous if the hub is structured conically. In the case of an evacuation device formed in this way the inlet cross-section is greater.
Finally, it is advantageous if the lines, which represent the form of the outer diameter of the rotor as well as the inner diameter of the stator in a longitudinal section through the suction-side vacuum pump, run in the form of a curve arched inwards in such a manner that the slope of the curves increases from the suction side to the pressure side. It is particularly expedient if these lines have essentially the form of a hyperbola. This structure of the suction-side vacuum pump ensures an optimal and, above all, disruption-free flow of the conveyed gases and thus contributes to the improvement of the gas throughput. In all, an improvement of the capacity density is achieved, that is, that the ratio of the capacity of the suction-side vacuum pump to its mass is greater than in the state of the art.
Still further advantages of the present invention will be appreciated to those of ordinary skill in the art upon reading and understand the following detailed description.
The invention may take form in various components and arrangements of components, and in various steps and arrangements of steps. The drawings are only for purposes of illustrating the preferred embodiments and are not to be construed as limiting the invention.
In the Figures, the device is denoted by 1. The suction-side vacuum pump is denoted by 2. The atmospheric pressure-side vacuum pump, only represented symbolically, is denoted by 3. The suction-side pump 2 is a mechanical-kinetic vacuum pump. It comprises a three-part housing 4 with sections 5, 6, and 7. The suction-side section 5 is provided with a flange 8 which forms a suction aperture 9 and serves for the connection to a system to be evacuated. Its inner wall 10 forms the stator component of the mechanical-kinetic vacuum pump 2. The housing section 5 encircles a rotor 11. This comprises a hub 12, which carries on its outer side the structure 13 which effects the gas conveyance. This structure consists of webs 14 (in particular,
The housing section 5, structured, at least on its inner side, conically, is supported on the central, essentially cylindrical housing section 6. A lower end section 18 of the lower part of the housing section 5 projects into the housing section 6, and, in fact, up to the pressure-side end of the rotor 11. The gases conveyed by the rotor 11 and by the stator 10 arrive in an annular chamber 19, to which an outlet nozzle 21 is attached. This is connected to the atmospheric pressure-side vacuum pump 3 via line 22.
The hub 12 is hollow. In the area of the suction side it includes a disk 23 which separates a pressure-side cavity 24 in the hub 12 from the suction side.
The lower housing section 7 is formed to be somewhat vat-shaped and is fastened to the central housing section 6. Together with the pressure-side cavity 24 in the hub 12, it forms a motor and bearing area. In
In the embodiments according to
In the embodiments according to
It is particularly expedient if the stator 10 and the outer contour of the rotor 11 have a hyperbolic curve. The result of this measure is the following calculation:
Following a greatly simplified approach to the description of the mode of function of a threaded pump, one can, ignoring slip effects and gap back-flow, write the following equation:
with
z number of channels
h thread depth
U circumferential speed
a channel width
α thread pitch
s gap between the upper edge of the thread web and the stator
p averaged pressure in a small area dx of the thread
η dyn. viscosity
q gas flow
The first term describes the Cuette flow while the second term describes the channel back-flow arising due to the pressure gradient. All the geometry data, with the exception of the channel depth, can be assumed as essentially constant over the axial length. Furthermore, the denominator in the first term is approximated by 2 since the ratio s/h is rather small. Also, the viscosity is approximated as a quantity independent of pressure.
One can thus write:
This means there is, for a predefined pressure p and gas flow q, a certain channel depth h at which the pressure gradient is maximal. This optimal channel depth can be found by the differentiation of dp/dx by h:
or also
hopt(x)=9q/2ABp(x)
In the case of a linear pressure curve in the pump, in a coordinate system with the axis of rotation 15 as χ-axis, a hyperbolic curve for channel depth over the axial length of the rotor thus results, and, in fact, in such a manner that the slope of the hyperbola decreases from the suction side to the pressure side. The position of the χ-axis and the γ-axis are indicated in
In this calculation the form of the rotor hub 12 was initially not taken into account. It can be formed to be cylindrical, conical, or arched outwards, as represented in
The invention has been described with reference to the preferred embodiments. Modifications and alterations may occur to others upon reading and understanding the preceding detailed description. It is intended that the invention be constructed as including all such modifications and alterations insofar as they come within the scope of the appended claims or the equivalents thereof.
Number | Date | Country | Kind |
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102 24 604 | Jun 2002 | DE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP03/05136 | 5/16/2003 | WO | 00 | 12/3/2004 |
Publishing Document | Publishing Date | Country | Kind |
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WO2004/015272 | 2/19/2004 | WO | A |
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Number | Date | Country | |
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20050220607 A1 | Oct 2005 | US |