VACUUM PUMP WITH REDUCED SEAL REQUIREMENTS

Abstract

The present disclosure relates to vacuum pump 10 comprising a substantially hermetically sealed enclosure 40, a core pump assembly located within the enclosure 40, and an inert purge gas inlet 70 fluidly connected to the enclosure 40 for supplying inert purge gas to an interior of the enclosure 40 surrounding the core pump assembly. By providing a sealed enclosure 40 around the core pump assembly and supplying inert purge gas thereto via the inlet 70, an inert positive pressure can be applied to the core pump assembly that reduces leakage of process gas from the core pump assembly such that seals therein can be removed or reduced. In particular, the need for elastomer seals that may be expensive and not be suited to high temperature or corrosive process gas conditions can be removed.

Claims

1. A vacuum pump comprising: a substantially hermetically sealed enclosure; a core pump assembly located within the enclosure and comprising two stator halves that are joined to define a plurality of pump chambers therein; and an inert purge gas inlet fluidly connected to the enclosure for supplying inert purge gas to an interior of the enclosure surrounding the core pump assembly.

2. The vacuum pump of claim 1, further comprising a thermal spacer positioned between the core pump assembly and the enclosure to thermally isolate the core pump assembly from the enclosure.

3. The vacuum pump of claim 2, wherein the thermal spacer comprises a ceramic material.

4. The vacuum pump of claim 1, wherein: the plurality of pump chambers include an inlet pump chamber configured to receive process gas from a vacuum system; the two stator halves extend between a first axial end face at a high vacuum, inlet side of the vacuum pump and a second, opposing axial end face at a low vacuum, outlet side of the vacuum pump and each define a radially inner face along which they are joined together; and at least one stator half includes a purge gas leakage channel that fluidly connects the first axial end face to a pump chamber downstream of the inlet pump chamber.

5. The vacuum pump of claim 4, wherein the at least one stator half comprises a plurality of purge gas leakage channels that fluidly connect the first axial end face to different pump chambers downstream of the inlet pump chamber.

6. The vacuum pump of claim 5, wherein the plurality of purge gas leakage channels are spaced radially apart, and a radially outward one of the purge gas leakage channels is fluidly connected to a pump chamber that is of a smaller volume than a pump chamber that a radially inward one of the purge gas leakage channels is fluidly connected to.

7. The vacuum pump of claim 4, wherein the purge gas leakage channel extends axially from the first axial end face and is substantially Z-shaped in cross-section.

8. The vacuum pump of claim 4, wherein the purge gas leakage channel further includes a portion of the channel that extends across the first axial end face.

9. The vacuum pump of claim 8, wherein the portion of the channel extending across the first axial end face fluidly connects opposing radial sides of the radially inner face.

10. The vacuum pump of claim 8, wherein the portion of the purge gas leakage channel on the first axial end face comprises a groove defined into the first axial end face.

11. The vacuum pump of claim 4, wherein the purge gas leakage channel comprises a pair of grooves defined into the radially inner face on opposing radial sides of the radially inner face.

12. The vacuum pump of claim 4, wherein the core pump assembly further comprises end pieces joined to the opposed first and second axial end faces.

13. The vacuum pump of claim 1, wherein the core pump assembly does not comprise any elastomer seals.

14. The vacuum pump of claim 1, further comprising: a motor; a gear cover; and an end cover; wherein each of the motor, the gear cover and the end cover are located outside of the enclosure.

15. The vacuum pump of claim 1, further comprising a pair of head plates for supporting a rotor assembly of the vacuum pump, wherein the pair of head plates are spaced apart from the core pump assembly.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0045] Various examples will now be described, by way of example only, and with reference to the accompanying drawings.

[0046] FIG. 1a shows an exemplary pump assembly in accordance with an example of this disclosure.

[0047] FIG. 1b shows another exemplary pump assembly in accordance with an example of this disclosure.

[0048] FIG. 2 shows an exemplary cross-section of a core pump assembly stator in accordance with an example of this disclosure taken across line X-X in FIG. 1a.

[0049] FIG. 3 shows another exemplary stator in accordance with an example of this disclosure.

[0050] FIG. 4 shows another exemplary cross-section of a core pump assembly stator in accordance with an example of this disclosure taken across line Y-Y in FIG. 1a.

DETAILED DESCRIPTION

[0051] With reference to FIGS. 1a and 1b, a multi-stage vacuum pump 10 comprises a first stator component 12 and a second stator component 14, between which a rotor assembly (not shown) is mounted.

[0052] The two stator components 12, 14 are fixed together to form the pump chambers 80a-g therein (shown in FIGS. 2 and 3 discussed below). In this manner, the two stator components 12, 14 are known as stator halves 12, 14 (i.e., stator clamshell halves 12, 14), and are joined together along an interface 13 defined by radially inner faces 13a, 13b of the stator halves 12, 14.

[0053] The pump 10 defines a central longitudinal axis L along which the stator halves 12, 14 extend and a radial direction R perpendicular thereto. The interface 13 is provided along the longitudinal axis L.

[0054] The rotor assembly can be any suitable type of rotor assembly and in the depicted examples will generally include two counter-rotating shafts with rotors mounted on each shaft (not shown). The rotors interact within the chambers 80a-g to pump working/process gas through the pump from an inlet at high-vac chamber 80a to an outlet at low-vac chamber 80g. The rotor assembly can be any suitable type of rotor assembly, and may form, for example, a Claw type vacuum pump, a Roots type vacuum, or a combination thereof. As such rotor assemblies are generally known and not the focus of the present disclosure, they will not be discussed further in detail.

[0055] End pieces 50, 52 are mounted on opposed axial ends of the two stator components 12, 14 to complete a core pump assembly. It will be appreciated that the core pump assembly is thus the part of the vacuum pump 10 within which the compression and pumping of process gas between chambers 80a-g is to take place.

[0056] Notably, whereas traditional vacuum pumps would comprise longitudinal seals between the two stator components 12, 14 and annular seals between the stator components 12, 14 and the end pieces 50, 52, these are not required in the vacuum pump 10 of the present disclosure.

[0057] The core pump assembly (defined by the two stator components 12, 14 and the two end plates 50, 52) is located within a sealed enclosure 40, which in the depicted example is defined by enclosure covers 16 and head plates 18. The two head plates 18 are located axially on either side of the core pump assembly and comprise bearings and seals for the shafts (not shown) of the rotor assembly. The two enclosure covers 16 are located radially on either side of the core pump assembly (i.e., above and below the core pump assembly) and extend axially between the two head plates 18 to form the enclosure 40. Seals 42 are provided between the enclosure covers 16 and the head plates 18 to ensure that the enclosure 40 is substantially hermetically sealed. In other words, the enclosure 40 is sealed in a substantially gas-tight manner, such that a pressure difference between the interior of the enclosure 40 and the surrounding atmosphere can be maintained when the pump 10 is operational. The placement of the enclosure covers 16 and seals 42 may be such that the enclosure 40 is hermetically sealed from the environment whilst allowing for differential thermal expansion between the head plates 18 and the enclosure covers 16 is formed. For example, a piston seal arrangement, as shown in FIG. 1a, and/or a face seal arrangement, as shown in FIG. 1b. Unlike the core pump assembly, the seals 42 may comprise elastomer seals or any other suitable type of seal (e.g., non-elastomer).

[0058] Outside of the enclosure 40, the vacuum pump 10 further comprises a motor 20 and an end cover 30, between which the shafts of the rotor assembly extend, and a gear cover 22 located axially between the motor 20 and the head plate 18 (nearest the end piece 50), which houses gearing (not shown) for the rotor assembly. Each of the motor 20, the gear cover 22, and the end cover 30 comprise seals 24, 26, 32 to maintain a seal between these components, and to help further seal the enclosure 40 from the environment. In alternative examples, the enclosure covers 16 may extend axially between any element of the pump 10, for example, the gear cover 22 and the end cover 30, such that the enclosure 40 includes these components therein. In such examples, additional plates would be placed axially outboard of these components and placed in sealing connection with the covers 16, instead of using head plates 18. In further alternative examples, the enclosure 40 may enclose components of the pump 10.

[0059] During operation of the vacuum pump 10, the operating temperature of the core pump assembly can typically be between 200-400 C. (e.g., to avoid process gas condensation therein), whilst the suitable temperature for the bearings, gearing, motor and elastomer seals can typically be less than 150 C. To help maintain the appropriate temperatures for each component during operation, thermal spacers 60 are provided between the end pieces 50, 52 and their respective head plates 18. In this manner, the thermal spacers 60 can be used to reduce the conduction of heat from the core pump assembly to the head plate 18 and other lower operating temperature pump components. Accordingly, the thermal spacers 60 may comprise any material with a suitably low thermal conductivity, e.g., a ceramic material, and may have a relatively small cross sectional area to further minimise the heat transfer between the end pieces 50, 52 and the head plates 18. The shafts of the rotor assembly may also comprise thermal breaks to help prevent heat being transferred outside of the core pump assembly via the shafts.

[0060] The vacuum pump 10 further comprises an inert purge gas inlet 70 fluidly connected to the enclosure 40. In the depicted example, the inert purge gas inlet 70 passes through the top housing cover 16. The inert gas inlet 70 allows for an inert gas, such as nitrogen, to be fed into and fill the interior of the enclosure 40. The inert gas will be supplied to the inlet 70 via an inert purge gas line (not shown). The temperature of the purge gas may be chosen to be any temperature suitable for the application. For example, the purge gas may be heated to help the core pump assembly get up to and maintain the correct operating temperature (e.g., to avoid process gas condensation).

[0061] Purge gas being inert may prevent the purge gas from having any negative or unwanted effects with the pump 10 and the process gas therein. Although nitrogen is exemplified, any other suitable inert gas could be used, e.g., argon.

[0062] It is to be appreciated that the inert purge gas inlet 70 is separate and distinct from a process gas inlet (not shown) that is fluidly connected to the core pump assembly for communicating process gas thereto (i.e., to the inlet (high-vac) stage 80a). Such a process gas inlet will also pass through the enclosure 40, but it will be fluidly connected to the pump inlet (not shown) defined through the stator components 12, 14, and will not be fluidly connected with the interior space of the enclosure 40 such that it can be filled with purge gas, as is the case for inert purge gas inlet 70.

[0063] Inert purge gas enters the enclosure 40 through the inlet 70 and is subsequently removed through an exhaust 72. The exhaust 72 is a duct or pipe that passes through the enclosure 40, and in the depicted example, is fluidly connected to the exhaust of the core pump assembly. In other words, it is connected to the outlet of the low-vac (i.e., outlet) stage 80g, and is not fluidly open to the interior of the enclosure 40.

[0064] In this example, an inert purge gas removal passage 90 is defined through the stator component 14 (see FIGS. 2 and 3) and is in fluid communication with the inlet of the low-vac stage 80g. In this manner, the purge gas in the enclosure 40 is removed by feeding it into the inlet of the low-vac stage 80g via the passage 90, where it will travel through the low-vac stage 80g and be communicated to the exhaust 72, along with the process gas also passing through the low-vac stage 80g. In alternative examples, the purge gas can be fed into the outlet of the low-vac stage 80g rather than its inlet, or fed into the exhaust 72 directly. In other examples, any other suitable arrangement (e.g., pipe and/or passage) can be used to achieve the removal of purge gas from the enclosure 40 via the exhaust 72.

[0065] A pressure and/or temperature sensor may be incorporated into the pump 10 for monitoring the pressure and/or temperature of the purge gas inside the enclosure 40. The sensors can communicate with a purge gas flow rate controller (e.g., a flow control valve placed in the inlet 70 and/or passage 90) to maintain a desired pressure and/or temperature inside the enclosure 40 by controlling the flow of the inert purge gas in and/or out of the enclosure 40. Any appropriate pressure and/or temperature sensor may be employed, and any suitable flow controller, such as a flow control valve or pressure control valve (pressure regulator) can be used.

[0066] It is to be appreciated that having the enclosure 40 sealed around the core pump assembly and providing and maintaining a desired amount of inert gas therein (e.g., via inlet 70 and exhaust 72) allows a positive pressure differential to be maintained around the core pump assembly. This helps minimise leakage of process gas from the core pump assembly despite it not being provided with any seals, as well as prevent the ingress of atmospheric gases from the environment entering the enclosure 40. It is also to be appreciated that this sealing configuration may also be more resilient to changes in operating temperature and corrosive process gas than applications which use seals, as well as removing the potential outgassing, permeability and cost issues associated with employing several elastomer seals in the core pump assembly instead.

[0067] Moreover, the enclosure 40 in combination with the thermal spacers 60 can permit the separation of different components that have different operating temperature limits. For example, the shaft bearings and seals in the head plates 18 can be maintained at lower operating temperatures than that of the core pump assembly. This can help improve the lifetime and running characteristics of the different pump components.

[0068] Referring now to FIG. 2, a cross-section along line X-X in the core pump assembly in FIG. 1a is shown. This cross-section shows the radially inner face 13b of the second stator component 14, which allows the pump chambers 80a-g to be visible. Whilst the following example will be described in relation to the second stator component 14, it should be understood that the same can also (though not necessarily) apply to the first stator component 12, which will have a corresponding radially inner face 13a (not shown).

[0069] The stator components 12, 14 are joined across the interface 13 defined by respective radially inner faces 13a, 13b to form the core pump assembly. Accordingly, each stator component 12, 14 comprises half of each pump chamber 80a-g, such that when joined together to form the core pump assembly, the pump chambers 80a-g are formed. As discussed above, in the example shown, the inert purge gas is removed from the enclosure 40 using the passage 90 that is fluidly connected to the inlet of the outlet (or low-vac) chamber 80g.

[0070] As can be seen from FIG. 2, the pump chambers 80a-g successively decrease in size in the axial direction with the largest volume, inlet (or high-vac) pump chamber 80a being closest to the motor 20 and the smallest volume, outlet (or low-vac) pump chamber 80g being closest to the end cover 30. The inlet pump chamber 80a is configured to receive process gas from a vacuum system via a process gas inlet and the outlet pump chamber 80g is configured to exhaust process gas from the core pump assembly via an outlet (discussed above). The gradual decrease in volume from chambers 80a-80g corresponds to an equivalent gradual increase in pressure from the desired operating pressure of the vacuum to atmospheric pressure. By employing multiple pump chambers, and thus multiple stages of compression, pumping efficiency is improved and higher vacuum pressures may be maintained.

[0071] As also shown, the stator components 12, 14 extend axially between opposed axial end faces 15a, 15b to which end pieces 50, 52 are joined. In this manner, the end pieces 50, 52 can be said to provide an interface with the stator components 12, 14 along faces 15a, 15b, respectively. Moreover, given their positioning relative to the chambers 80a-80g, the first axial end face 15a is at the high vacuum, inlet side of the pump 10 and the second, opposing axial end face 15b is at the low vacuum, outlet side of the pump 10.

[0072] Due to the lack of seals between the first and second stator components 12, 14 and between the stator components 12, 14 and the end pieces 50, 52, inert purge gas from the enclosure 40 can leak into the core pump assembly. If no measures are implemented to prevent this, the efficiency of the pump 10 may be reduced, as leaked purge gas 110 can enter the pump chambers 80a-g and be compressed along with the process gas therein, increasing the compressive work.

[0073] To combat this effect, the present example further comprises purge gas leakage channels 100a and 100b in the stator component 14 that extend from the first axial end 15a that interfaces with the end piece 50 at the high vacuum, inlet side of the pump 10 to the third and fifth pump chambers 80c, 80e, respectively. Whilst the present example depicts two purge gas leakage channels 100a, 100b, examples comprising between 1 and n1 purge leakage channels are envisaged, with n being the number of pump stages 80. Furthermore, whilst the channels 100a, 100b are shown connected to the third and fifth pump chambers 80c, 80e, the channels 100 may be connected to any of the pump chambers 80, as long as it excludes the inlet (high-vac) pump stage 80a.

[0074] The purge gas leakage channels 100a, 100b serve to capture purge gas 110 that leaks into the core pump assembly. As the channels 100a, 100b are connected to the pump chambers 80c, 80e respectively, this means that the leaked gas 110 entering the channels 100a, 100b is pumped by the pump stage 80c, 80e along with the process gas. For example, the leaked gas 110 at the high-vac inlet end of the pump 10, i.e. closer to the end piece 50, will first come into contact with the channel 100b. Channel 100b is connected to the pump chamber 80e, which may be pressurised at, for example, around 100 mbar. Therefore, the leaked gas 110 is driven into the pump chamber 80e until the pressure in the channel 100b is also 100 mbar. The leaked gas 110, now at a pressure of 100 mbar, may continue to flow radially inwards. In doing so, it will then come into contact with the channel 100a. Channel 100a is connected to the pump chamber 80c, which is pressurised at a lower pressure of, for example, around 10 mbar. As with the channel 100b, this means that the flow of leaked gas 110 is reduced to a pressure of 10 mbar. As such, assuming the leaked gas 110 was initially at atmospheric pressure (1 bar), the amount of leakage has been reduced to 1/100.sup.th of its original pressure. By reducing the pressure of the leaked gas 110 in this way, this ensures that when the leaked gas 110 comes into contact with the lowest-pressure pump stages 80a, 80b, the additional work by these stages 80a, 80b to compress the leaked gas 110 is significantly reduced.

[0075] It will be appreciated that in the depicted configuration, owing to the relative gas pressures present, a radially inner channel 100 may be connected to a larger volume pump chamber 80 than a channel 100 that is radially outwards thereof in order for the inner channel 100 to provide a benefit.

[0076] The channels 100a, 100b depicted resemble substantially a Z-shape in cross-section such that they each comprise two turns 102, 104. These turns 102, 104 may help prevent leakage out of the core pump assembly via the channels 100a, 100b. However, the channels 100a, 100b can have any suitable shape for capturing and transporting the leaked gas 110 to the corresponding pump chamber 80.

[0077] Furthermore, the channels 100a, 100b are illustrated as connecting axially into the pump chamber 80. In the present example, this is due to the inaccessibility of the inter-stage ports of each pump stage 80, with them being between the two parallel shafts of the rotor assembly. However, in examples where the inlet of the pump stages 80 are not between the two shafts, it is envisaged that the channels 100a, 100b may be connected to the inlet for that pump stage (i.e., the inlet that carries process gas to the pump stage for compression).

[0078] The channels 100a, 100b shown are provided as pairs of grooves on opposing radial sides of the radially inner face 13b of the stator component 14. These grooves can be machined (e.g., milled) into the radially inner face 13b of the stator component 14. However, the channels 100a, 100b can take any other suitable form for capturing and transporting the leaked gas 110 to the corresponding pump chamber 80, and be made in any other suitable manner. For example, they may be cast or drilled into the stator component 14.

[0079] Referring now to FIG. 3, the pump 10 may combine the channels 100 with conventional sealing methods, such as longitudinal seals 120 and/or annular seals 130. The longitudinal seals 120 may extend in a groove in the stator component 12, 14 from the high-vac end piece 50 to the low-vac end piece 52 radially outwards of the channels 100. The longitudinal seals 120 and their grooves may be discontinuous to prevent fluidly connecting the two ends of the core pump assembly. The annular seals 130 are located between the end pieces 50, 52 and the stator components 12, 14 and comprise a diameter that positions them radially outwards of the channels 100. The purpose of these optional seals is to reduce the amount of leaked gas 110 that reaches the radially-outermost channel 100b and thus reduce the amount of work by the pump stage 80e that said channel 100b is connected to, further increasing the efficiency of the pump 10. However, the sealing system 120, 130 of the core pump assembly of this example may not be as accurate or as robust as conventional sealing systems, as any leakage into the core pump assembly through the seals 120, 130 will be reduced by the channels 100 as described above. This means that accurate alignment between the two stator components 12, 14 and between the stator components 12, 14 and the end pieces 50, 52 are not required. Furthermore, this means that the seals 120, 130 may comprise either elastomer or non-elastomer seals as opposed to conventional sealing systems where elastomer seals are a requirement.

[0080] With reference to FIG. 4, a cross-section along line Y-Y in the core pump assembly in FIG. 1a is shown, looking towards the first axial end face 15a of the two stator components 12, 14. The purge gas leakage channels 100a, 100b can be seen to further comprise portions 101a, 101b that extend across the first axial end face 15a of the stator components 12, 14. This can allow additional purge gas leakage to be collected at the interface defined by the first axial end face 15a (i.e., the interface between the stator components 12, 14 and the end piece 50).

[0081] In the depicted example, the portions 101a, 101b are used to fluidly connect opposed radial sides of the radially inner faces 13a, 13b, and thus are fluidly connected to the parts of the channel 100a, 100b in the radially inner faces 13a, 13b. In this manner, the portions 101a, 101b circumscribe portions of the stator components 12, 14 at the first axial end face 15a and collect purge gas leaking to the first axial end face 15a and communicate this to the part of the channel 100a, 100b in the radially inner faces 13a, 13b. This allows the purge gas leakage channels 100a, 100b to collect more leaked gas 110 that may leak into the interface between the stator components 12, 14 and the end piece 50, as the portions 101a, 101b circumscribing the first axial end face 15a extend substantially around 360 degrees at the interface with the end plate 50.

[0082] In this manner, a higher amount of leaked gas 110 may be prevented from entering the lowest-pressure pump stages 80a, 80b and thus the high vacuum efficiency of the pump 10 may be improved further.

[0083] The portions 101a, 101b shown in FIG. 4 are substantially U-shaped but may take any other suitable shape to connect the opposed radial sides of the radially inner faces 13a, 13b, for example, a semi-circular shape. As shown, the portions 101a, 101b comprise different radii such that they are nested radially apart across the first axial end face 15a.

[0084] The portions 101a, 101b shown are provided as grooves connecting the opposing radial sides of the first axial end face 15a of the stator components 12, 14. These grooves can be machined (e.g., milled) into the first axial end face 15a of the stator components 12, 14. However, can take any other suitable form for capturing and transporting the leaked gas 110 across the first axial end face 15a.

[0085] Whilst the present disclosure has been described in the context of a clamshell stator construction with pump chambers defined therein (e.g., Roots and claw type pumps), it is envisaged that the present disclosure could also be applied to other pumps where seal-free designs may be desirable. For example, a screw pump could incorporate similar channels to those described herein, but connecting the channels to different locations along the length of the screw. In the context of a screw pump, different screw length locations are to be seen as an equivalent to the different pump chambers 80a-80g discussed in the present disclosure.