US20050123414A1 - Pumping apparatus - Google Patents
Pumping apparatus Download PDFInfo
- Publication number
- US20050123414A1 US20050123414A1 US11/004,259 US425904A US2005123414A1 US 20050123414 A1 US20050123414 A1 US 20050123414A1 US 425904 A US425904 A US 425904A US 2005123414 A1 US2005123414 A1 US 2005123414A1
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- US
- United States
- Prior art keywords
- fluid
- impedance
- pumping apparatus
- pressure
- flow
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01C—ROTARY-PISTON OR OSCILLATING-PISTON MACHINES OR ENGINES
- F01C21/00—Component parts, details or accessories not provided for in groups F01C1/00 - F01C20/00
- F01C21/10—Outer members for co-operation with rotary pistons; Casings
- F01C21/104—Stators; Members defining the outer boundaries of the working chamber
- F01C21/108—Stators; Members defining the outer boundaries of the working chamber with an axial surface, e.g. side plates
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C15/00—Component parts, details or accessories of machines, pumps or pumping installations, not provided for in groups F04C2/00 - F04C14/00
- F04C15/0003—Sealing arrangements in rotary-piston machines or pumps
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C18/00—Rotary-piston pumps specially adapted for elastic fluids
- F04C18/08—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing
- F04C18/082—Details specially related to intermeshing engagement type pumps
- F04C18/086—Carter
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C18/00—Rotary-piston pumps specially adapted for elastic fluids
- F04C18/08—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing
- F04C18/12—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing of other than internal-axis type
- F04C18/126—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing of other than internal-axis type with radially from the rotor body extending elements, not necessarily co-operating with corresponding recesses in the other rotor, e.g. lobes, Roots type
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C18/00—Rotary-piston pumps specially adapted for elastic fluids
- F04C18/08—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing
- F04C18/12—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing of other than internal-axis type
- F04C18/123—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing of other than internal-axis type with radially or approximately radially from the rotor body extending tooth-like elements, co-operating with recesses in the other rotor, e.g. one tooth
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C18/00—Rotary-piston pumps specially adapted for elastic fluids
- F04C18/08—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing
- F04C18/12—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing of other than internal-axis type
- F04C18/14—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing of other than internal-axis type with toothed rotary pistons
- F04C18/16—Rotary-piston pumps specially adapted for elastic fluids of intermeshing-engagement type, i.e. with engagement of co-operating members similar to that of toothed gearing of other than internal-axis type with toothed rotary pistons with helical teeth, e.g. chevron-shaped, screw type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C2220/00—Application
- F04C2220/10—Vacuum
- F04C2220/12—Dry running
Definitions
- the present invention relates to pumping apparatus.
- Vacuum pumps are known which are oil-free in their vacuum chambers and which are therefore useful in clean environments such as those found in the semiconductor manufacturing industry. In such an environment, if lubricant materials were present in the vacuum chamber, such materials could potentially back migrate into the semiconductor process chamber and, in so doing, may cause contamination of the product under manufacture.
- Such “dry” vacuum pumps are commonly multi-stage positive displacement pumps employing intermeshing rotors in the vacuum chamber of each stage of the pump. The rotors may have the same type of profile in each chamber, or the profile may change from chamber to chamber.
- each chamber is typically defined by two separately machined stator components of the pump, with rotor components of the pump being located in the cavity defined between the stator components. It is necessary to provide a seal between the stator components in order both to prevent leakage of pumped process gas from the cavity and to prevent any ambient air from entering the cavity.
- An O-ring seal is typically provided to perform this sealing function.
- Such seals are typically formed from fluoroelastomeric material, such as VitonTM (Du Pont de Nemours, E. I & Co.)
- Dry vacuum pumps are frequently deployed in applications where they are required to pump substantial quantities of corrosive fluids, particularly halogen gases and solvents. Such materials attack O-ring seals, with the result that these seals may become excessively plastic or very brittle, which can badly affect the integrity of the seal provided between the stator components.
- the intensity of the attack on the seal is dependant on a number of variables including, for example, the nature of the pumped fluid, the material from which the O-ring seal is formed, and the temperature of the pump. In view of this, it is very difficult to predict the appropriate interval for replacing the seals and thus maintaining pump integrity. External inspection of the seals is seldom practical.
- the present invention seeks to solve these and other problems.
- the present invention relates to a pumping apparatus comprising a pump adapted to from a swept volume further and a sealed chamber surrounding the swept volume, the apparatus for other comprising a conduit for supplying fluid to the chamber, the conduit comprising a flow impedance for limiting the rate of flow of fluid to the chamber, and means for determining a pressure difference across the flow impedance.
- Another aspect of the present invention relates to a method of detecting a leak of fluid from a chamber surrounding a swept volume of a pump, the method comprising the steps of supplying the fluid to the chamber through a flow impedance, and monitoring a pressure difference across the flow impedance.
- FIG. 1 is a front view of a stator component showing a seal assembly
- FIG. 2 is a side view of the seal assembly of FIG. 1 ;
- FIG. 3 illustrates apparatus for monitoring the integrity of the seal assembly
- FIG. 4 is a graph indicating the variation of pressure of a gas within the seal assembly with time.
- FIG. 1 illustrates the surface 3 of a stator component 1 from an exhaust stage of a dry pump.
- a corresponding surface of a second stator component (not shown) is brought into contact with the surface 3 of the stator component 1 and a cavity 2 is formed between the adjacent stator components.
- Cavity 2 accommodates the rotor component (not shown) of the pump when the pump is assembled, and is generally referred to as a pump swept volume.
- a dry pump typically comprises several such cavities, each cavity 2 communicating with an adjacent cavity through a port 4 .
- a first O-ring seal 5 is provided around the periphery of the cavity 2 .
- This O-ring seal 5 is preferably formed from a fluoroelastomeric material, such as VitonTM, and provides a fluid tight seal between adjacent stator components so that, when the pump is in use, process or cleaning gases being pumped through the cavity 2 are prevented from leaking from the cavity 2 , and ambient air is prevented from entering the cavity 2 .
- a fluoroelastomeric material such as VitonTM
- first O-ring seal 5 is the first component to fail in such circumstances.
- a second O-ring seal 6 similar to first O-ring seal 5 , is provided between first O-ring seal 5 and the periphery of cavity 2 .
- First and second O-ring seals 5 , 6 are separated by a shallow channel or groove 7 ( FIG. 1 ) which is formed between grooves 8 , 9 used to locate first O-ring seal 5 and second O-ring seal 6 between the adjacent stator components, as shown in FIG. 2 .
- the channel 7 allows a small quantity of fluid, for example a gas such as nitrogen, to be trapped between the two adjacent stator components and the O-ring seals 5 , 6 , which together define a sealed chamber for the gas.
- the gas enters the channel 7 through port 7 a from a gas reservoir 16 via a conduit 9 as indicated in FIG. 3 schematically showing an apparatus for monitoring the integrity of the seal assembly.
- conduit 9 includes a flow impedance 10 and a one-way valve 11 .
- Pressure transducers 12 , 13 are provided in fluid communication upstream and downstream of flow impedance 10 .
- Flow impedance 10 may be formed from slightly porous, sintered material that inhibits a flow of gas such that, when the flow impedance 10 is placed in conduit 9 , it acts to allow only a trickle of gas to pass therethrough.
- Flow impedance 10 could alternatively be provided by a fine metering valve, or by creating a fine capillary hole through solid material.
- One-way valve 11 prevents contamination of the supply reservoir if the pressure in the pump rises above that of the gas supply. Valve 11 also serves to minimise fluctuations in pressure in conduit 9 downstream from valve 11 in the event that the gas supply was to be temporarily interrupted or otherwise affected.
- Pressure transducers 12 , 13 measure the pressure P 2 and P 1 respectively in the conduit 9 on the upstream and the downstream side of flow impedance 10 , and pass signals indicating the measured pressure to a controller 14 .
- gas module 15 is an active manifold that regulates the supply of gas from the reservoir into conduit 9 .
- Gas module 15 is configured to send a signal to controller 14 to indicate one or more characteristics, such as flow rate and pressure, of the gas being fed into conduit 9 .
- Such a gas module may be used to distribute gas to different locations within the pump, for example where the gas is to be used as a purge gas for flushing impurities from the pump.
- pressurised gas (typically at approximately 6 psi) is passed along conduit 9 , through flow impedance 10 , and into channel 7 until a pressure equilibrium is established between the gas downstream from flow impedance 10 , and the gas upstream of flow impedance 10 . Due to the presence of pressurised gas in channel 7 downstream from flow impedance 10 , during use of the pump a significant pressure difference will be experienced across second O-ring seal 6 , as the pumped gas in cavity 2 (the swept volume of the pump) will be sub-atmospheric (typically 800 mbar) when the pump is under normal steady state operating conditions.
- sub-atmospheric typically 800 mbar
- controller 14 which receives the signals output from the pressure transducers 12 , 13 , to output an alarm, for example, via a display, indicating the failure of the second O-ring seal 6 if the pressure difference exceeds a predetermined value.
- the apparatus described above can thus provide a reliable indication of the state of critical seals inside a pump. Such an indication can allow maintenance intervals to be lengthened and costs of operation to be reduced without intrusive intervention. Since the predictability of deterioration of these critical components can be improved the probability of potentially hazardous leaks is consequently reduced.
- a conduit supplies a flow of gas to a sealed chamber surrounding the swept volume of a pump.
- the conduit comprises a flow impedance for limiting the rate of flow of the gas to the sealed chamber. Signals output from pressure transducers provided on either side of the flow impedance are used to detect leakage of gas from the sealed chamber into the pump swept volume, thus indicating the state of the seal surrounding the swept volume.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Examining Or Testing Airtightness (AREA)
- Non-Positive Displacement Air Blowers (AREA)
- Structures Of Non-Positive Displacement Pumps (AREA)
Abstract
Description
- The present invention relates to pumping apparatus.
- Vacuum pumps are known which are oil-free in their vacuum chambers and which are therefore useful in clean environments such as those found in the semiconductor manufacturing industry. In such an environment, if lubricant materials were present in the vacuum chamber, such materials could potentially back migrate into the semiconductor process chamber and, in so doing, may cause contamination of the product under manufacture. Such “dry” vacuum pumps are commonly multi-stage positive displacement pumps employing intermeshing rotors in the vacuum chamber of each stage of the pump. The rotors may have the same type of profile in each chamber, or the profile may change from chamber to chamber.
- In either a Roots, screw or Northey (“claw”) type device, each chamber is typically defined by two separately machined stator components of the pump, with rotor components of the pump being located in the cavity defined between the stator components. It is necessary to provide a seal between the stator components in order both to prevent leakage of pumped process gas from the cavity and to prevent any ambient air from entering the cavity. An O-ring seal is typically provided to perform this sealing function. Such seals are typically formed from fluoroelastomeric material, such as Viton™ (Du Pont de Nemours, E. I & Co.)
- Dry vacuum pumps are frequently deployed in applications where they are required to pump substantial quantities of corrosive fluids, particularly halogen gases and solvents. Such materials attack O-ring seals, with the result that these seals may become excessively plastic or very brittle, which can badly affect the integrity of the seal provided between the stator components.
- The intensity of the attack on the seal is dependant on a number of variables including, for example, the nature of the pumped fluid, the material from which the O-ring seal is formed, and the temperature of the pump. In view of this, it is very difficult to predict the appropriate interval for replacing the seals and thus maintaining pump integrity. External inspection of the seals is seldom practical.
- These problems are particularly acute when pumping reactive gases such as fluorine from semiconductor processing equipment, where gas compositions are varied by reactions in the equipment. Here, even precise knowledge regarding the gas flows admitted to the process chamber is a very poor predictor of the quantity or nature of the reactive gas entering the pump and hence the anticipated useful seal life. Recommended maintenance often includes frequent seal leak checks but this is expensive, inconvenient to do and consequently is sometimes omitted.
- In principle, other types of sensor could be used to attempt to measure the integrated exposure level of the seals and hence the state of the seals. For example, a spectroscopic or chemical technique could be employed to measure gas composition. However, such techniques would require complex calibration procedures and be costly to implement.
- In at least its preferred embodiment, the present invention seeks to solve these and other problems.
- The present invention relates to a pumping apparatus comprising a pump adapted to from a swept volume further and a sealed chamber surrounding the swept volume, the apparatus for other comprising a conduit for supplying fluid to the chamber, the conduit comprising a flow impedance for limiting the rate of flow of fluid to the chamber, and means for determining a pressure difference across the flow impedance.
- Another aspect of the present invention relates to a method of detecting a leak of fluid from a chamber surrounding a swept volume of a pump, the method comprising the steps of supplying the fluid to the chamber through a flow impedance, and monitoring a pressure difference across the flow impedance.
- Preferred features of the present invention will now be described, by way of example only, with reference to the accompanying drawings, in which:
-
FIG. 1 is a front view of a stator component showing a seal assembly; -
FIG. 2 is a side view of the seal assembly ofFIG. 1 ; -
FIG. 3 illustrates apparatus for monitoring the integrity of the seal assembly; and -
FIG. 4 is a graph indicating the variation of pressure of a gas within the seal assembly with time. -
FIG. 1 illustrates thesurface 3 of astator component 1 from an exhaust stage of a dry pump. A corresponding surface of a second stator component (not shown) is brought into contact with thesurface 3 of thestator component 1 and acavity 2 is formed between the adjacent stator components.Cavity 2 accommodates the rotor component (not shown) of the pump when the pump is assembled, and is generally referred to as a pump swept volume. A dry pump typically comprises several such cavities, eachcavity 2 communicating with an adjacent cavity through aport 4. - A first O-
ring seal 5 is provided around the periphery of thecavity 2. This O-ring seal 5 is preferably formed from a fluoroelastomeric material, such as Viton™, and provides a fluid tight seal between adjacent stator components so that, when the pump is in use, process or cleaning gases being pumped through thecavity 2 are prevented from leaking from thecavity 2, and ambient air is prevented from entering thecavity 2. However, as discussed above, such gases can be particularly aggressive and can readily cause damage to many parts of the pump. Typically, first O-ring seal 5 is the first component to fail in such circumstances. In view of this, a second O-ring seal 6, similar to first O-ring seal 5, is provided between first O-ring seal 5 and the periphery ofcavity 2. First and second O-ring seals FIG. 1 ) which is formed betweengrooves ring seal 5 and second O-ring seal 6 between the adjacent stator components, as shown inFIG. 2 . Thechannel 7 allows a small quantity of fluid, for example a gas such as nitrogen, to be trapped between the two adjacent stator components and the O-ring seals channel 7 throughport 7 a from agas reservoir 16 via aconduit 9 as indicated inFIG. 3 schematically showing an apparatus for monitoring the integrity of the seal assembly. - As shown in
FIG. 3 ,conduit 9 includes aflow impedance 10 and a one-way valve 11.Pressure transducers flow impedance 10. -
Flow impedance 10 may be formed from slightly porous, sintered material that inhibits a flow of gas such that, when theflow impedance 10 is placed inconduit 9, it acts to allow only a trickle of gas to pass therethrough.Flow impedance 10 could alternatively be provided by a fine metering valve, or by creating a fine capillary hole through solid material. - One-
way valve 11 prevents contamination of the supply reservoir if the pressure in the pump rises above that of the gas supply. Valve 11 also serves to minimise fluctuations in pressure inconduit 9 downstream fromvalve 11 in the event that the gas supply was to be temporarily interrupted or otherwise affected. -
Pressure transducers conduit 9 on the upstream and the downstream side offlow impedance 10, and pass signals indicating the measured pressure to acontroller 14. - The supply of gas to
conduit 9 is controlled bygas module 15. In this arrangement,gas module 15 is an active manifold that regulates the supply of gas from the reservoir intoconduit 9.Gas module 15 is configured to send a signal to controller 14 to indicate one or more characteristics, such as flow rate and pressure, of the gas being fed intoconduit 9. Such a gas module may be used to distribute gas to different locations within the pump, for example where the gas is to be used as a purge gas for flushing impurities from the pump. - In use, pressurised gas (typically at approximately 6 psi) is passed along
conduit 9, throughflow impedance 10, and intochannel 7 until a pressure equilibrium is established between the gas downstream fromflow impedance 10, and the gas upstream offlow impedance 10. Due to the presence of pressurised gas inchannel 7 downstream fromflow impedance 10, during use of the pump a significant pressure difference will be experienced across second O-ring seal 6, as the pumped gas in cavity 2 (the swept volume of the pump) will be sub-atmospheric (typically 800 mbar) when the pump is under normal steady state operating conditions. In this state, when second O-ring seal 6 is new and has no defects, the signals output frompressure transducers ring seal 6 should become damaged by the pumped gas so that the integrity of second O-ring seal 6 is impaired, pressurised gas can start to leak fromchannel 7 tocavity 2, due to the existence of a relatively higher pressure gas inchannel 7 and a relatively lower pressure gas incavity 2, which leakage will to try to equalise these pressures. Due to the presence offlow impedance 10 inconduit 9, the pressure P2 measured by thepressure transducer 12 will start to fall (as shown inFIG. 4 ), whilst the pressure P1 measured by thepressure transducer 13 will remain at the supply pressure. The difference in the pressures P1 and P2 is therefore indicative of a leak of gas into thecavity 2, and thus is indicative of a failure of the second O-ring seal 6. This can enablecontroller 14, which receives the signals output from thepressure transducers ring seal 6 if the pressure difference exceeds a predetermined value. - The apparatus described above can thus provide a reliable indication of the state of critical seals inside a pump. Such an indication can allow maintenance intervals to be lengthened and costs of operation to be reduced without intrusive intervention. Since the predictability of deterioration of these critical components can be improved the probability of potentially hazardous leaks is consequently reduced.
- In summary, a conduit supplies a flow of gas to a sealed chamber surrounding the swept volume of a pump. The conduit comprises a flow impedance for limiting the rate of flow of the gas to the sealed chamber. Signals output from pressure transducers provided on either side of the flow impedance are used to detect leakage of gas from the sealed chamber into the pump swept volume, thus indicating the state of the seal surrounding the swept volume.
- While the foregoing description and drawings represent the preferred embodiments of the present invention, it will be apparent to those skilled in the art that various changes and modifications may be made therein without departing from the true spirit and scope of the present invention.
Claims (19)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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GB0327964.3 | 2003-12-03 | ||
GB0327964A GB2408801A (en) | 2003-12-03 | 2003-12-03 | Detection of seal leak using differential pressure measurement |
Publications (1)
Publication Number | Publication Date |
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US20050123414A1 true US20050123414A1 (en) | 2005-06-09 |
Family
ID=29764459
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US11/004,259 Abandoned US20050123414A1 (en) | 2003-12-03 | 2004-12-03 | Pumping apparatus |
Country Status (7)
Country | Link |
---|---|
US (1) | US20050123414A1 (en) |
JP (1) | JP3109161U (en) |
CN (1) | CN2844879Y (en) |
DE (1) | DE202004018733U1 (en) |
FR (1) | FR2863322B3 (en) |
GB (1) | GB2408801A (en) |
TW (1) | TWM278782U (en) |
Cited By (8)
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EP1882856A1 (en) * | 2006-07-28 | 2008-01-30 | LOT Vacuum Co., Ltd. | Complex dry vacuum pump having Roots and screw rotors |
WO2009004360A1 (en) * | 2007-07-02 | 2009-01-08 | Edwards Limited | Fkm or ffkm multiple layers seal |
CN102606465A (en) * | 2012-03-06 | 2012-07-25 | 昆山佳铭自动化科技有限公司 | Device for detecting comprehensive performances of electronic vacuum pumps |
US20120260722A1 (en) * | 2011-04-14 | 2012-10-18 | Cincinnati Test Systems, Inc. | Leak testing device and method |
US20150097339A1 (en) * | 2012-03-02 | 2015-04-09 | Dover Pump Solutions Group (Europe) Gmbh | Sealing arrangement, a conveying device having a sealing arrangement and a method for operating the sealing arrangement |
CN104632614A (en) * | 2013-11-06 | 2015-05-20 | 都福百士吉泵业集团(欧洲)有限公司 | Sealing assembly, a conveyor with the sealing assembly, and a method for operating said sealing assembly |
WO2016017376A1 (en) * | 2014-07-31 | 2016-02-04 | エドワーズ株式会社 | Dry pump and exhaust gas treatment method |
CN114593059A (en) * | 2020-12-07 | 2022-06-07 | 中国科学院沈阳科学仪器股份有限公司 | Stator component of dry vacuum pump |
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GB2442738B (en) * | 2006-10-09 | 2011-08-03 | Boc Group Plc | A sealing system |
DE102008021971A1 (en) * | 2008-05-02 | 2009-11-05 | Oerlikon Leybold Vacuum Gmbh | Vacuum pump and method for cleaning vacuum pumps |
JP2014514538A (en) * | 2011-03-15 | 2014-06-19 | カルクロ テクニカル プラスチックス リミテッド | Liquid flow control in capillaries. |
CN102865219B (en) * | 2012-10-09 | 2014-11-12 | 浙江宇宙智能设备有限公司 | Direct-drive high-pressure pumping seal internal-leakage online monitoring method |
DE102013208614A1 (en) * | 2013-05-10 | 2014-11-13 | Pfeiffer Vacuum Gmbh | Device with at least one channel for guiding a gaseous or liquid operating medium |
CN103422899B (en) * | 2013-08-09 | 2015-06-03 | 华南理工大学 | Process and device for generating power by pressure energy of small natural gas pipeline network |
FR3107575B1 (en) * | 2020-02-20 | 2022-03-25 | Pfeiffer Vacuum Technology AG | Dry vacuum pump |
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- 2004-12-02 JP JP2004007099U patent/JP3109161U/en not_active Expired - Lifetime
- 2004-12-03 DE DE202004018733U patent/DE202004018733U1/en not_active Expired - Lifetime
- 2004-12-03 US US11/004,259 patent/US20050123414A1/en not_active Abandoned
- 2004-12-03 CN CNU2004201174498U patent/CN2844879Y/en not_active Expired - Lifetime
- 2004-12-03 TW TW093219592U patent/TWM278782U/en not_active IP Right Cessation
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1882856A1 (en) * | 2006-07-28 | 2008-01-30 | LOT Vacuum Co., Ltd. | Complex dry vacuum pump having Roots and screw rotors |
WO2009004360A1 (en) * | 2007-07-02 | 2009-01-08 | Edwards Limited | Fkm or ffkm multiple layers seal |
US20100239448A1 (en) * | 2007-07-02 | 2010-09-23 | Emmanuel Uzoma Okoroafor | Fkm or ffkm multiple layers seal |
US20120260722A1 (en) * | 2011-04-14 | 2012-10-18 | Cincinnati Test Systems, Inc. | Leak testing device and method |
US8997553B2 (en) * | 2011-04-14 | 2015-04-07 | Cincinnati Test Systems, Inc. | Leak testing device and method |
US20150097339A1 (en) * | 2012-03-02 | 2015-04-09 | Dover Pump Solutions Group (Europe) Gmbh | Sealing arrangement, a conveying device having a sealing arrangement and a method for operating the sealing arrangement |
US10036385B2 (en) * | 2012-03-02 | 2018-07-31 | Dover Pump Solutions Group (Europe) Gmbh | Sealing arrangement, a conveying device having a sealing arrangement and a method for operating the sealing arrangement |
CN102606465A (en) * | 2012-03-06 | 2012-07-25 | 昆山佳铭自动化科技有限公司 | Device for detecting comprehensive performances of electronic vacuum pumps |
CN104632614A (en) * | 2013-11-06 | 2015-05-20 | 都福百士吉泵业集团(欧洲)有限公司 | Sealing assembly, a conveyor with the sealing assembly, and a method for operating said sealing assembly |
WO2016017376A1 (en) * | 2014-07-31 | 2016-02-04 | エドワーズ株式会社 | Dry pump and exhaust gas treatment method |
US11592025B2 (en) | 2014-07-31 | 2023-02-28 | Edwards Japan Limited | Dry pump and exhaust gas treatment method |
CN114593059A (en) * | 2020-12-07 | 2022-06-07 | 中国科学院沈阳科学仪器股份有限公司 | Stator component of dry vacuum pump |
Also Published As
Publication number | Publication date |
---|---|
DE202004018733U1 (en) | 2005-04-14 |
GB2408801A (en) | 2005-06-08 |
GB0327964D0 (en) | 2004-01-07 |
FR2863322A3 (en) | 2005-06-10 |
JP3109161U (en) | 2005-05-12 |
CN2844879Y (en) | 2006-12-06 |
FR2863322B3 (en) | 2005-12-02 |
TWM278782U (en) | 2005-10-21 |
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