AXIAL FLOW VACUUM PUMP WITH CURVED ROTOR AND STATOR BLADES
20230109154 · 2023-04-06
Inventors
Cpc classification
F04D19/048
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04D19/042
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F05D2250/71
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04D29/384
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04D29/542
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04D29/38
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04D29/32
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04D29/324
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F04D19/04
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04D29/32
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04D29/38
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
An axial flow vacuum pump for evacuating a chamber in a semiconductor manufacturing process comprises a rotor having a plurality of rotor blades and a stator having a plurality of stator blades, wherein the rotor blades and stator blades have a curved shape.
Claims
1. An axial flow vacuum pump for evacuating a chamber in a semiconductor manufacturing process, the axial flow vacuum pump comprising: a rotor having a plurality of rotor blades; and a stator having a plurality of stator blades, wherein the rotor blades and stator blades have a curved cross-sectional shape.
2. The axial flow vacuum pump of claim 1, wherein the rotor is supported for rotation relative to the stator by magnetic bearings.
3. The axial flow vacuum pump of claim 1, wherein the rotor is formed from stainless steel.
4. The axial flow vacuum pump of claim 1, wherein an inlet stage of the pump comprises blades having a first radial length and an adjacent downstream stage of the pump comprises blades having a second radial length, wherein the ratio of first radial length to second radial length is 2:1 or greater.
5. The axial flow vacuum pump of claim 1, comprising between 4 and 10 pumping stages, each pumping stage comprising a row of rotor blades and a row of stator blades.
6. The axial flow vacuum pump of claim 1, comprising a bypass conduit for directing a portion of the gas from the outlet of the pump towards the inlet of the pump.
7. The axial flow vacuum pump of claim 6, wherein the bypass conduit comprises a pressure relief valve.
8. An apparatus for manufacturing semiconductor equipment comprising: a chamber for manufacturing semiconductor equipment in; a backing pump system positioned remote from the chamber and configured to evacuate gas from the chamber; a foreline for fluidly connecting the backing pump system to the chamber; and an axial flow vacuum pump according to claim 1 configured to evacuate gas from the chamber, wherein the axial flow vacuum pump is connected between the chamber and foreline.
9. The apparatus of claim 8, wherein the axial flow vacuum pump is positioned less than 2 meters from the chamber.
10. The apparatus of claim 8, wherein the backing pump system is positioned more than 8 meters from the chamber.
11. A method of evacuating a semiconductor fabrication chamber comprising: using an axial flow vacuum pump as described in claim 1 to evacuate gas from the chamber; operating the axial flow vacuum pump to pump gas with a pressure of 1 mbar or higher; operating the axial flow vacuum pump to pump gas with a pressure of between 1 mbar and 10-3 mbar; and operating the axial flow vacuum pump to pump gas with a pressure of 10-3 mbar or lower.
12. The method of claim 11, comprising using a backing pump system to evacuate gas from the chamber, the backing pump system being positioned remotely from the chamber and axial flow vacuum pump.
13. The method of claim 11, wherein the axial flow vacuum pump is positioned less than 2 meters from the chamber.
14. The method of claim 11, comprising operating the axial flow vacuum pump to pump gas at a temperature of 130° C. or higher.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0040] Embodiments of the present invention will now be described further, with reference to the accompanying drawings, in which:
[0041]
[0042]
[0043]
[0044]
[0045]
[0046]
DETAILED DESCRIPTION
[0047]
[0048] In use, semiconductor equipment is manufactured within the chamber 16 using one or more tools (not shown). In order to effectively manufacture semiconductor equipment, the gas pressure in the chamber should be very low. For example, in many semiconductor processes, the pressure in the chamber 16 needs to be 10.sup.-2 mbar or lower. As such the axial flow vacuum pump 18 and backing pump system 20 are configured to evacuate gas from the chamber 16 to achieve such pressures.
[0049] The backing pump system 20 comprises a roots blower and primary pump or other similar arrangement for backing the axial flow vacuum pump 18. Such a backing pump system can be very bulky and create considerable noise, as such it is positioned separately from the main manufacturing processes in the chamber 16, in the illustrated example, the backing pump system 20 is positioned on a floor below the chamber 16 in a so called ‛subfab’ area of the manufacturing facility. As the chamber 16 and backing pump system 20 are on separate floors there is a considerable distance between the chamber 16 and backing pump system 20. As such the foreline 22 is eight meters long or greater. A long gas flow path between the backing pump system 20 and chamber 16 reduces pumping effectiveness of the backing pump system 20 particularly at low pressures.
[0050] An axial flow vacuum pump 18 is attached directly to the chamber 16. It will be appreciated that the axial flow vacuum pump 18 may also be positioned close to the chamber 16 such that a short conduit, less than 2 meters, runs between the chamber 16 and axial flow vacuum pump 18.
[0051] The combination of the axial flow vacuum pump 18, with relatively high pumping capacity attached close to the chamber 16, and the backing pump system 20, which can pump effectively at the high pressures of the effective pumping range, provides a set of pumps which pump effectively across the desired pumping range with an increased pumping capacity compared to known systems.
[0052]
[0053] The axial flow vacuum pump 18 comprises a rotor 30 configured to rotate about the pump axis 32 during use and has a plurality of rotor blades 34 mounted on it. The pump 18 further comprises a stator 38 surrounding the rotor 30 and having a plurality of stator blades 36 mounted on it. The rotor 30 and stator 38 define an annular flow path 40 extending from an inlet 42 to an outlet 44 of the pump into which the rotor blades 34 and stator blades 36 extend. The annular flow path 40 has a cross-sectional area that decreases along axial direction from the inlet 42 to the outlet 44.
[0054] The rotor 30 is supported for rotation relative to the stator 38 by magnetic bearings 46. Although the illustrated embodiment shows a single magnetic bearing 46 positioned near the outlet end of the rotor 30, it will be appreciated that other bearing configurations including one or more bearings may be used.
[0055] The rotor 30 is formed from high strength stainless steel which is capable of effectively operating at temperatures between 150 and 180° C., in use.
[0056] The rotors blades 34 and stator blades 36 are arranged in stages 50, 52, 54, 56 as shown in
[0057] Each stage of the pump 18 has an associated volume that decreases from the inlet 42 towards the outlet 44 such that an upstream stage will have a greater volume than stage downstream of. This volume decrease facilitates compression of the gas in the viscous flow regime. The volume decrease may be achieved by decreasing the internal diameter of the stator 38 and/or increasing the external diameter of the rotor 30 along the axis 32 of the pump 18 in a direction from the inlet 42 to the outlet 44. In the illustrated example, the internal diameter of the stator 38 decreases in the inlet stage 50 but remains generally fixed in the further compression stages 52, 54, 56 and the external diameter of the rotor 30 increases throughout all stages. It will be appreciated that other configurations of stator 38 and rotor 30 geometries that achieve the desired volume decrease, as set out in more detail below, are also within the scope of the invention.
[0058] Accordingly, each stage 50, 52, 54, 56 has a compression ratio which is defined as a ratio of the volume of that stage to the volume of the adjacent downstream stage. The compression ratio of the further compression stages 52, 54, 56 (i.e. downstream of the inlet stage) is around 1.2:1. The compression ratio of the stage will directly affect the length of the rotor and stator blades 34, 36 of the stage compared to the length of the rotor and stator blades 34, 36 in the adjacent downstream stage. More specifically, the rotor blades 34 in each row have a radial length 60 extending from the rotor 30 towards the stator 38 and the stator blades 36 each have a radial length 62 extending from the stator 38 towards the rotor 30. Where the compression ratio is around 1.2:1 ratio between radial length of rotor blade (or stator blade) between stages is also around 1.2:1.
[0059] By comparison, the inlet stage 50 comprises blades 34 having a much longer radial length 60 compared to those of adjacent stages, such that the ratio is much higher than would be optimal for achieving desired pressure ratios during viscous flow. More specifically, the inlet stage 50 has a compression ratio of around 3:1 and a rotor and stator blade length 60, 62 such that the ratio of blade length 60, 62 of the inlet stage 50 to the blade length 60 of the adjacent stage 52 of the pump 18 is around 3:1.
[0060] It will be appreciated that more than one inlet stage 50 having longer blades may be provided although the number of inlet stages configured in this way will be fewer than the number of regular compression stages.
[0061] The axial flow vacuum pump of
[0062] The bypass conduit 76 includes a pressure relief valve 78 positioned between the outlet conduit 74 and inlet conduit 72. The pressure relief valve 78 is configured to open at 100 mbar. It will be appreciated that the pressures relief valve may be configured to open at a pressure of 50 mbar or higher, for example at a pressure of between 50 mbar and 200 mbar or between 80 mbar and 120 mbar, depending on the pressure conditions of system.
[0063] The vacuum pump 18 of
[0064]
[0065] In the configuration of
[0066] In the alternative configuration of
[0067]
[0068] Step 1 S1 of the method 100 comprises operating the axial flow vacuum pump to pump gas with a pressure of 1 mbar or higher, step 2 S2 comprises operating the axial flow vacuum pump to pump gas with a pressure of between 1 mbar and 10-3 mbar and step 3 S3 comprises operating the axial flow vacuum pump to pump gas with a pressure of 10-3 mbar or lower. As such the axial flow vacuum pump is used to pump gas over the viscous flow regime and molecular flow regime as well as in the transition between the two regimes.
[0069] Although elements have been shown or described as separate embodiments above, portions of each embodiment may be combined with all or part of other embodiments described above.
[0070] Although the subject matter has been described in language specific to structural features and/or methodological acts, it is to be understood that the subject matter defined in the appended claims is not necessarily limited to the specific features or acts described above. Rather, the specific features and acts described above are described as example forms of implementing the claims.