EP1441128B1 - Vacuum pump system - Google Patents
Vacuum pump system Download PDFInfo
- Publication number
- EP1441128B1 EP1441128B1 EP03028333A EP03028333A EP1441128B1 EP 1441128 B1 EP1441128 B1 EP 1441128B1 EP 03028333 A EP03028333 A EP 03028333A EP 03028333 A EP03028333 A EP 03028333A EP 1441128 B1 EP1441128 B1 EP 1441128B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pump
- vacuum pump
- vacuum
- pumps
- pumping
- 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.)
- Expired - Lifetime
Links
- 239000007789 gas Substances 0.000 claims description 29
- 238000006073 displacement reaction Methods 0.000 claims 2
- 239000000203 mixture Substances 0.000 claims 1
- 238000005086 pumping Methods 0.000 description 29
- 230000006835 compression Effects 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 239000012159 carrier gas Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D19/00—Axial-flow pumps
- F04D19/02—Multi-stage pumps
- F04D19/04—Multi-stage pumps specially adapted to the production of a high vacuum, e.g. molecular pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D25/00—Pumping installations or systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
Definitions
- the invention relates to a vacuum pumping system for conveying light gases with at least one high vacuum pump.
- Pump systems for evacuating a recipient consist, for example, of a turbomolecular pump on the high-vacuum side and of one or more backing pumps for further conveying and for compressing to atmospheric pressure of the gases compressed by the turbomolecular pump.
- These backing pumps may be, for example, a combination of a Roots pump and a rotary vane pump or a dry-compressing, anti-atmosphere pump.
- the DE-OS 38 28 608 shows such a vacuum pumping station, which is composed of a molecular pump, a Roots pump and a mechanical, the atmosphere-compressing vacuum pump. In order to control the pumping speed of the arrangement, it is proposed to equip the Roots pump with means for controlling the speed.
- Such pumping systems are suitable for conveying and compressing medium and high molecular weight gases (for example, N 2 , O 2 , Ar).
- medium and high molecular weight gases for example, N 2 , O 2 , Ar.
- they are less suitable for pumping light gases (eg H 2 , He), especially when it comes to conveying large quantities of gas.
- light gases eg H 2 , He
- several high-vacuum pumps are often used for sucking up the resulting gases on the high-vacuum side.
- the conventional pre-vacuum systems are incapable of absorbing the large amounts of gas accumulating on the gas discharge side of the high vacuum pump.
- the forepumps used since are extremely bad for the Pumps of light gases suitable. Roots pumps have little compression and rotary vane pumps are not oil free. You would have to be equipped with a cold trap in which condense the oil parts. This means a lot of effort and complicates the pumping system.
- Vorvakuumsystem is mounted at a greater distance from the gas connection part of the high vacuum pump, so that at this point still a large Leitwert theme added.
- the invention has for its object to design a pumping system, which is suitable to pump large amounts of gas whose main components are light gases.
- Existing pumping systems should be able to be converted by simple measures in suitable for the task pumping systems.
- the solution is an increase in compression and pumping speed in the fore-vacuum range.
- This increase is made by providing an additional Pump, hereinafter called intermediate pump, reached between the gas discharge side of the high vacuum pump and the suction side of the backing system. It is important according to the invention that this intermediate pump is connected directly to the discharge side of the high-vacuum pump without a large loss of conductance.
- the pumping speed of the at least one intermediate pump should advantageously be of the order of magnitude of the pumping speed of the at least one high-vacuum pump or at least 50% thereof.
- one or more intermediate pumps may be provided. If several intermediate pumps are provided, these are connected in series and / or in parallel.
- a molecular pump including a side channel pump, which operates in the same pressure range to count.
- the molecular pump is formed with a preferred embodiment as a turbomolecular pump.
- the compression for light gases of such a pump is sufficiently high to ensure that the amount of gas produced at the discharge of the high vacuum pump can be compressed and conveyed further without loss.
- a further improvement in conductance and thus an increase in the gas throughput takes place in that the at least one intermediate pump is connected directly to the discharge side of the high-vacuum pump.
- a pumping system which is suitable for pumping large amounts of gas, which mainly consist of light gases, more effectively and compressing them to atmospheric pressure. It even results in a disproportionate increase in the pumping speed on the high-vacuum side.
- a particular advantage of the vacuum pumping system according to the invention is that the pumping system is compatible with conventional systems, that is, these can be retrofitted for pumping larger amounts of light gases without much effort.
- the intake system and the entire backing system can continue to be used unchanged.
- the use of a molecular pump as an intermediate pump takes up little space, so that a compact system is created which can be used effectively by simple modification in a wide pressure range for all gases.
- the Fig. 1 shows a vacuum pumping system (1).
- two high-vacuum pumps (3, 4) preferably turbomolecular pumps, arranged.
- a backing system consisting of two backing pumps (8, 9), conveys and compresses the pumped gases to atmospheric pressure.
- a further intermediate pump (6) which is connected directly to the gas outlet (7) of the high-vacuum pumps (3, 4), is located between the high-vacuum pumps (3, 4) and the backing system (8, 9).
- the intermediate pump (6) serves to supply the gas quantity delivered by the high-vacuum pumps (3, 4) to the fore-vacuum system (8, 9) without losses.
- the backing pump system (8, 9) On an outlet side (5) of the intermediate pump (6), the backing pump system (8, 9) is arranged. Between the intermediate pump (6) and the backing pump (8, 9) may be a greater distance.
- Fig. 2 shows a vacuum pumping system (10).
- two turbomolecular pumps (3, 4) are arranged.
- two intermediate pumps (12, 13) are arranged downstream of the turbomolecular pumps (3, 4) on an outlet side (11).
- the intermediate pumps (12, 13) are connected in parallel to increase the pumping speed.
- the pre-vacuum system (8, 9) is as in Fig. 1 downstream of the intermediate pumps (12, 13).
- Fig. 3 shows a vacuum pumping system (14) with a recipient (2) on which two turbomolecular pumps (3, 4) are arranged.
- the turbomolecular pumps (3, 4) are connected directly downstream without any significant conductance losses intermediate pumps (16, 17).
- the intermediate pumps (16, 17) connected in series.
- the system of the intermediate pumps (16, 17), the backing system (8, 9) connected downstream.
Abstract
Description
Die Erfindung betrifft ein Vakuumpumpsystem zur Förderung leichter Gase mit wenigstens einer Hochvakuumpumpe.The invention relates to a vacuum pumping system for conveying light gases with at least one high vacuum pump.
Pumpsysteme zur Evakuierung eines Rezipienten bestehen zum Beispiel aus einer Turbomolekularpumpe auf der Hochvakuumseite und aus einer oder mehreren Vorvakuumpumpen zur Weiterförderung und zum Verdichten auf Atmosphärendruck der von der Turbomolekularpumpe komprimierten Gase. Diese Vorvakuumpumpen können zum Beispiel eine Kombination aus einer Wälzkolbenpumpe und einer Drehschieberpumpe oder einer trocken verdichtenden, gegen Atmosphäre ausstoßenden Pumpe bestehen. Die
Die herkömmlichen Vorvakuumsysteme sind nicht in der Lage, die auf der Gasausstoßseite der Hochvakuumpumpe anfallenden großen Gasmengen aufzunehmen. Die seither verwendeten Vorpumpen sind äußerst schlecht für das Pumpen von leichten Gasen geeignet. Wälzkolbenpumpen haben nur eine geringe Kompression, und Drehschieberpumpen sind nicht ölfrei. Sie müssten mit einer Kühlfalle ausgestattet sein, in welcher die Ölteile kondensieren. Dies bedeutet einen großen Aufwand und kompliziert das Pumpsystem.The conventional pre-vacuum systems are incapable of absorbing the large amounts of gas accumulating on the gas discharge side of the high vacuum pump. The forepumps used since are extremely bad for the Pumps of light gases suitable. Roots pumps have little compression and rotary vane pumps are not oil free. You would have to be equipped with a cold trap in which condense the oil parts. This means a lot of effort and complicates the pumping system.
Oft wird ein Trägergas eingesetzt, um den Transport von leichten Gasen zu verbessern. Auch diese Lösung ist mit großem Aufwand verbunden. Zudem müssen in diesen Fällen Maßnahmen ergriffen werden, um die Gase wieder zu trennen. Dazu kommt, dass der Vorvakuumdruck und damit die Pumpeigenschaften des gesamten Systems durch das Trägergas wieder verschlechtert werden.Often a carrier gas is used to enhance the transport of light gases. This solution is associated with great effort. In addition, measures must be taken in these cases to separate the gases again. In addition, the prevacuum pressure and thus the pumping properties of the entire system are again degraded by the carrier gas.
In vielen Fällen ist das Vorvakuumsystem in größerer Entfernung vom Gasanschlussteil der Hochvakuumpumpe angebracht, so dass an dieser Stelle noch ein großer Leitwertverlust hinzukommt.In many cases, the Vorvakuumsystem is mounted at a greater distance from the gas connection part of the high vacuum pump, so that at this point still a large Leitwertverlust added.
Der Erfindung liegt die Aufgabe zugrunde, ein Pumpsystem zu entwerfen, welches geeignet ist, große Gasmengen zu pumpen, deren Hauptbestandteile leichte Gase sind. Bestehende Pumpsysteme sollen durch einfache Maßnahmen in für die Aufgabe geeignete Pumpsysteme umgewandelt werden können.The invention has for its object to design a pumping system, which is suitable to pump large amounts of gas whose main components are light gases. Existing pumping systems should be able to be converted by simple measures in suitable for the task pumping systems.
Diese Aufgabe wird durch ein Vakuumpumpsystem mit den Merkmalen gemäß Anspruch 1 gelöst.This object is achieved by a vacuum pumping system having the features according to claim 1.
Die Lösung besteht in einer Erhöhung von Kompression und Saugvermögen im Vorvakuumbereich. Diese Erhöhung wird durch Vorsehen einer zusätzlichen Pumpe, im Folgenden Zwischenpumpe genannt, zwischen der Gasausstoßseite der Hochvakuumpumpe und der Ansaugseite des Vorvakuumsystems erreicht. Dabei ist es erfindungsgemäß wichtig, dass diese Zwischenpumpe direkt ohne großen Leitwertverlust an die Ausstoßseite der Hochvakuumpumpe angeschlossen wird. Das Saugvermögen der wenigstens einen Zwischenpumpe soll vorteilhaft in der Größenordnung des Saugvermögens der wenigstens einen Hochvakuumpumpe liegen oder mindestens 50 % davon betragen.The solution is an increase in compression and pumping speed in the fore-vacuum range. This increase is made by providing an additional Pump, hereinafter called intermediate pump, reached between the gas discharge side of the high vacuum pump and the suction side of the backing system. It is important according to the invention that this intermediate pump is connected directly to the discharge side of the high-vacuum pump without a large loss of conductance. The pumping speed of the at least one intermediate pump should advantageously be of the order of magnitude of the pumping speed of the at least one high-vacuum pump or at least 50% thereof.
Gemäß der Erfindung können eine oder mehrere Zwischenpumpen vorgesehen sein. Sind mehrere Zwischenpumpen vorgesehen, werden diese in Serie und/oder parallel geschaltet.According to the invention, one or more intermediate pumps may be provided. If several intermediate pumps are provided, these are connected in series and / or in parallel.
Als Pumpentyp wird eine Molekularpumpe vorgeschlagen, wozu auch eine Seitenkanalpumpe, welche im gleichen Druckbereich arbeitet, zu zählen ist. Die Molekularpumpe ist mit einer bevorzugten Ausführungsform als Turbomolekularpumpe ausgebildet.As a pump type, a molecular pump is proposed, including a side channel pump, which operates in the same pressure range to count. The molecular pump is formed with a preferred embodiment as a turbomolecular pump.
Die Kompression für leichte Gase einer solchen Pumpe ist ausreichend hoch, um zu gewährleisten, dass die am Ausstoß der Hochvakuumpumpe anfallende Gasmenge verdichtet und ohne Verlust weiter gefördert werden kann. Eine weitere Leitwertverbesserung und damit eine Steigerung des Gasdurchsatzes erfolgt dadurch, dass die wenigstens eine Zwischenpumpe direkt an der Austoßseite der Hochvakuumpumpe angeschlossen ist.The compression for light gases of such a pump is sufficiently high to ensure that the amount of gas produced at the discharge of the high vacuum pump can be compressed and conveyed further without loss. A further improvement in conductance and thus an increase in the gas throughput takes place in that the at least one intermediate pump is connected directly to the discharge side of the high-vacuum pump.
Mit der erfindungsgemäßen Anordnung wird ein Pumpsystem bereitgestellt, welches geeignet ist, große Gasmengen, die hauptsächlich aus leichten Gasen bestehen, effektiver zu pumpen und auf Atmosphärendruck zu verdichten. Es ergibt sich sogar eine überproportionale Erhöhung des Saugvermögens auf der Hochvakuumseite.With the arrangement according to the invention, a pumping system is provided, which is suitable for pumping large amounts of gas, which mainly consist of light gases, more effectively and compressing them to atmospheric pressure. It even results in a disproportionate increase in the pumping speed on the high-vacuum side.
Ein besonderer Vorteil des erfindungsgemäßen Vakuumpumpsystems liegt darin, dass das Pumpsystem kompatibel ist mit herkömmlichen Systemen, das heißt, diese können zum Pumpen von größeren Mengen leichter Gase ohne großen Aufwand umgerüstet werden. Dabei kann das Ansaugsystem und das gesamte Vorvakuumsystem unverändert weiterverwendet werden. Die Vewendung einer Molekularpumpe als Zwischenpumpe beansprucht darüber hinaus wenig Platz, so dass ein kompaktes System entsteht, welches durch einfache Modifikation in weitem Druckbereich für alle Gase wirkungsvoll einsetzbar ist.A particular advantage of the vacuum pumping system according to the invention is that the pumping system is compatible with conventional systems, that is, these can be retrofitted for pumping larger amounts of light gases without much effort. In this case, the intake system and the entire backing system can continue to be used unchanged. In addition, the use of a molecular pump as an intermediate pump takes up little space, so that a compact system is created which can be used effectively by simple modification in a wide pressure range for all gases.
In der Zeichnung ist ein Ausführungsbeispiel der Erfindung dargestellt, und zwar zeigen:
- Fig. 1
- ein erfindungsgemäßes Vakuumpumpsystem mit einer Zwischenpumpe;
- Fig. 2
- ein Vakuumpumpsystem mit zwei parallel geschalteten Zwischenpumpen;
- Fig. 3
- ein Vakuumpumpsystem mit zwei in Serie geschalteten Zwischenpumpen.
- Fig. 1
- a vacuum pump system according to the invention with an intermediate pump;
- Fig. 2
- a vacuum pumping system with two intermediate pumps connected in parallel;
- Fig. 3
- a vacuum pumping system with two intermediate pumps connected in series.
Die
An einer Auslassseite (5) der Zwischenpumpe (6) ist das Vorvakuumpumpsystem (8, 9) angeordnet. Zwischen der Zwischenpumpe (6) und den Vorvakuumpumpen (8, 9) kann eine größere Wegstrecke liegen.On an outlet side (5) of the intermediate pump (6), the backing pump system (8, 9) is arranged. Between the intermediate pump (6) and the backing pump (8, 9) may be a greater distance.
- 11
- VakuumpumpsystemVacuum pumping system
- 22
- Rezipientrecipient
- 3, 43, 4
- Hochvakuumpumpenhigh vacuum pumps
- 55
- Auslassseiteoutlet
- 66
- Zwischenpumpebetween the pump
- 77
- Gasauslassgas outlet
- 8, 98, 9
- VorvakuumsystemVorvakuumsystem
- 1010
- VakuumpumpsystemVacuum pumping system
- 1111
- Auslassseiteoutlet
- 12, 1312, 13
- Zwischenpumpebetween the pump
- 1414
- VakuumpumpsystemVacuum pumping system
- 16, 1716, 17
- Zwischenpumpenbetween the pump
Claims (3)
- Vacuum pump system for delivering gases, in particular gas mixtures with a high proportion of light gases, having at least one high vacuum pump, wherein at a discharge end (7) of the at least one high vacuum pump (3, 4) at least one intermediate pump (6; 12, 13; 16, 17) is disposed directly and with a low conductance loss, characterized in that the at least one intermediate pump (6; 12, 13; 16, 17) has a displacement capacity corresponding to at least 50% of the displacement capacity of the at least one high vacuum pump (3, 4).
- Vacuum pump system according to claim 1, characterized in that a plurality of intermediate pumps (12, 13; 16, 17) are provided connected in series and/or in parallel.
- Vacuum pump system according to claim 1, characterized in that as an intermediate pump (6; 12, 13; 16, 17) Lhere is provided a molecular pump, in particular a turbomolecular pump.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10302764A DE10302764A1 (en) | 2003-01-24 | 2003-01-24 | Vacuum pumping system |
DE10302764 | 2003-01-24 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1441128A2 EP1441128A2 (en) | 2004-07-28 |
EP1441128A3 EP1441128A3 (en) | 2004-09-01 |
EP1441128B1 true EP1441128B1 (en) | 2008-03-26 |
Family
ID=32520090
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP03028333A Expired - Lifetime EP1441128B1 (en) | 2003-01-24 | 2003-12-10 | Vacuum pump system |
Country Status (4)
Country | Link |
---|---|
US (1) | US7033142B2 (en) |
EP (1) | EP1441128B1 (en) |
AT (1) | ATE390561T1 (en) |
DE (2) | DE10302764A1 (en) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB0214273D0 (en) * | 2002-06-20 | 2002-07-31 | Boc Group Plc | Apparatus for controlling the pressure in a process chamber and method of operating same |
JP4633370B2 (en) * | 2004-02-17 | 2011-02-16 | 財団法人国際科学振興財団 | Vacuum equipment |
US20050186099A1 (en) * | 2004-02-19 | 2005-08-25 | Graeme Huntley | Active vibration reduction |
GB0411426D0 (en) * | 2004-05-21 | 2004-06-23 | Boc Group Plc | Pumping arrangement |
GB0418771D0 (en) * | 2004-08-20 | 2004-09-22 | Boc Group Plc | Evacuation of a load lock enclosure |
GB0505500D0 (en) * | 2005-03-17 | 2005-04-27 | Boc Group Plc | Vacuum pumping arrangement |
US8147222B2 (en) * | 2007-05-15 | 2012-04-03 | Agilent Technologies, Inc. | Vacuum divider for differential pumping of a vacuum system |
DE102007057944A1 (en) * | 2007-12-01 | 2009-06-04 | Inficon Gmbh | Method and device for leak testing |
GB2472638B (en) * | 2009-08-14 | 2014-03-19 | Edwards Ltd | Vacuum system |
DE202012012359U1 (en) * | 2012-12-22 | 2014-03-24 | Oerlikon Leybold Vacuum Gmbh | Pumping station for pumping light gases |
DE102013218506A1 (en) * | 2013-09-16 | 2015-03-19 | Inficon Gmbh | Sniffer leak detector with multi-stage diaphragm pump |
KR101979336B1 (en) * | 2015-05-26 | 2019-05-16 | 라스코 게엠베하 | How to handle boats, assemblies, and electronic components |
FR3070489B1 (en) * | 2017-08-29 | 2020-10-23 | Pfeiffer Vacuum | LEAK DETECTOR AND LEAK DETECTION PROCESS FOR THE TIGHTNESS CHECK OF OBJECTS TO BE TESTED |
FR3072774B1 (en) * | 2017-10-19 | 2019-11-15 | Pfeiffer Vacuum | LEAK DETECTOR FOR CONTROLLING THE SEALING OF AN OBJECT TO BE TESTED |
US20220260156A1 (en) * | 2021-02-12 | 2022-08-18 | Kla Corporation | Dual Vacuum Seal |
EP4224015A1 (en) * | 2022-02-07 | 2023-08-09 | Siemens Energy Global GmbH & Co. KG | Hydrogen compressors |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3536418A (en) * | 1969-02-13 | 1970-10-27 | Onezime P Breaux | Cryogenic turbo-molecular vacuum pump |
DD96304A1 (en) * | 1972-02-29 | 1973-03-12 | ||
CH625598A5 (en) * | 1977-12-01 | 1981-09-30 | Balzers Hochvakuum | |
DE3639512A1 (en) * | 1986-11-20 | 1988-06-01 | Alcatel Hochvakuumtechnik Gmbh | Vacuum pump system with a Roots pump |
FR2621141B1 (en) * | 1987-09-25 | 1989-12-01 | Cit Alcatel | METHOD FOR STARTING SERIES COUPLED VACUUM PUMPS, AND DEVICE FOR CARRYING OUT SAID METHOD |
US4850806A (en) * | 1988-05-24 | 1989-07-25 | The Boc Group, Inc. | Controlled by-pass for a booster pump |
DE3865012D1 (en) * | 1988-06-01 | 1991-10-24 | Leybold Ag | PUMP SYSTEM FOR A LEAK DETECTOR. |
DE3828608A1 (en) * | 1988-08-23 | 1990-03-08 | Alcatel Hochvakuumtechnik Gmbh | Vacuum-pump device |
DE4213763B4 (en) * | 1992-04-27 | 2004-11-25 | Unaxis Deutschland Holding Gmbh | Process for evacuating a vacuum chamber and a high vacuum chamber, and high vacuum system for carrying it out |
US5733104A (en) * | 1992-12-24 | 1998-03-31 | Balzers-Pfeiffer Gmbh | Vacuum pump system |
DE4410903A1 (en) * | 1994-03-29 | 1995-10-05 | Leybold Ag | System with vacuum pump, measuring device as well as supply, control, operating and display devices |
DE4442174A1 (en) * | 1994-11-26 | 1996-05-30 | Leybold Ag | Leak detector with vacuum pumps and operating procedures |
DE19639733A1 (en) * | 1996-09-27 | 1998-04-16 | Linde Ag | Process for compressing a gas |
DE19704234B4 (en) * | 1997-02-05 | 2006-05-11 | Pfeiffer Vacuum Gmbh | Method and device for controlling the pumping speed of vacuum pumps |
JP3763193B2 (en) * | 1997-09-22 | 2006-04-05 | アイシン精機株式会社 | Multistage vacuum pump |
DE19821634A1 (en) * | 1998-05-14 | 1999-11-18 | Leybold Vakuum Gmbh | Friction vacuum pump with staged rotor and stator |
-
2003
- 2003-01-24 DE DE10302764A patent/DE10302764A1/en not_active Withdrawn
- 2003-01-24 US US10/350,935 patent/US7033142B2/en not_active Expired - Fee Related
- 2003-12-10 DE DE50309460T patent/DE50309460D1/en not_active Expired - Lifetime
- 2003-12-10 AT AT03028333T patent/ATE390561T1/en not_active IP Right Cessation
- 2003-12-10 EP EP03028333A patent/EP1441128B1/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
EP1441128A2 (en) | 2004-07-28 |
US20040146410A1 (en) | 2004-07-29 |
EP1441128A3 (en) | 2004-09-01 |
DE50309460D1 (en) | 2008-05-08 |
DE10302764A1 (en) | 2004-07-29 |
US7033142B2 (en) | 2006-04-25 |
ATE390561T1 (en) | 2008-04-15 |
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