EP0186776B1 - Dispositif de production d'un vide - Google Patents
Dispositif de production d'un vide Download PDFInfo
- Publication number
- EP0186776B1 EP0186776B1 EP85114893A EP85114893A EP0186776B1 EP 0186776 B1 EP0186776 B1 EP 0186776B1 EP 85114893 A EP85114893 A EP 85114893A EP 85114893 A EP85114893 A EP 85114893A EP 0186776 B1 EP0186776 B1 EP 0186776B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- separator
- gas
- fine separator
- cooler
- vacuum pump
- 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
Links
Images
Classifications
-
- 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
- F04C23/00—Combinations of two or more pumps, each being of rotary-piston or oscillating-piston type, specially adapted for elastic fluids; Pumping installations specially adapted for elastic fluids; Multi-stage pumps specially adapted for elastic fluids
-
- 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
- F04C29/00—Component parts, details or accessories of pumps or pumping installations, not provided for in groups F04C18/00 - F04C28/00
- F04C29/04—Heating; Cooling; Heat insulation
Definitions
- the invention relates to a device for generating a vacuum, which contains a liquid ring pump driven by an electric motor as a vacuum pump, in which device the vacuum pump is followed by a pre-separator provided with a storage space for separating the conveyed gas from the auxiliary liquid carried with the auxiliary liquid from the storage space from a liquid cooler to the liquid ring pump and the gas still loaded with a remainder of the auxiliary liquid is fed to a fine separator downstream of the pre-separator, which is provided with a return line for the auxiliary liquid separated in it.
- a cooler is arranged downstream of a pre-separator for the lubricating oil which serves as a collecting space and via which the compressed air is arranged in a spatially separate manner from the cooler Fine separator is fed.
- the compressed air is cooled in the cooler, so that the lubricating oil particles which are still entrained condense into larger droplets and can thus be better deposited in the fine separator.
- the invention has for its object to improve a device of the type described above in that the liquid separation is significantly improved by appropriate cooling, without condensation of the moisture contained in the sucked gas within the pump and the pre-separator must be accepted. This task should also be solved with the least possible design effort.
- the pre-separator and the fine separator are arranged spatially separate and the gas still loaded with a remainder of the auxiliary liquid is fed to the fine separator via a gas cooler arranged separately from the liquid cooler, the two coolers being dimensioned such that the Gas is cooled to a lower temperature than the outlet temperature of the auxiliary liquid measured at the outlet of the liquid cooler.
- the spatially separated arrangement of the two separators achieves a thermal decoupling of the fine separator from the pre-separator, which is strongly heated by the auxiliary liquid and the compressed gas. Only the auxiliary liquid flowing back to the vacuum pump is cooled via the liquid cooler, it being possible for the liquid cooler to be designed such that a favorable operating temperature of the auxiliary liquid is achieved.
- the liquid cooler can be dimensioned accordingly small.
- the gas cooler arranged between the pre-separator and the fine separator need only apply the smaller cooling capacity necessary for cooling the gas. It can be dimensioned such that a favorable low temperature necessary for separating the auxiliary liquid is reached.
- a separate fan for the liquid cooler and the gas cooler can be avoided by arranging these coolers in the cooling air flow of the electric motor.
- an embodiment of the liquid cooler which does not take up any additional space results from the fact that it is designed as a coiled tube which is arranged concentrically around the electric motor or between it and the vacuum pump. Additional space is also not claimed if a double-walled fan hood is provided as a gas cooler on the electric motor, surrounding the fan, through the cavity of which the gas is passed.
- the described design of the two coolers therefore has the advantage that they are inevitably in the cooling air flow of the fan of the electric motor, the gas cooler being acted upon by the fresh air which has not yet been heated.
- both the pre-separator and the fine separator are each installed in a tubular housing part and the two housing parts are arranged with their longitudinal axes parallel to the longitudinal axis of the electric motor. It is particularly advantageous here that both the inlet and outlet connections of the vacuum pump are directed upwards and the two separators are each attached to one of the two connections lying above the electric motor.
- Such an arrangement of the separators above the engine is particularly favorable for the lateral connection of the gas lines to the fan cover.
- the gas lines led out from the side of the fan hood are led laterally into the pre-separator or fine separator, so that there is a very short and simple pipe guide for the gas lines.
- both the separators and the gas lines are at least partially covered by the cooling air flow from the engine fan.
- the pre-separator and the fine separator each consist of a head part containing the connection points for the lines to be connected and a head part that can be connected to this head part and contains the elements of the respective separator.
- An easily detachable connection of the container parts to the head parts is possible in that the container parts are cylindrical bushings that have a radially outwardly projecting bead on their open side, with which they can be fastened on by means of a clamping lock that overlaps this bead and a corresponding bead formed on the head part Headboard are attached.
- a simple design of the pre-separator is characterized in that a gas guide line connected to the head part runs parallel to the upper boundary wall of the container part, which ends near the bottom of the container part and that the lower region of the container part forms the storage space which has a Opening is connected to a drain opening of the head part connected to the liquid cooler.
- a hollow roller-shaped filter is arranged in the fine separator and its cavity is connected to the gas supply opening of the head part. This means that no further line elements for the gas between the feed opening of the head part and the filter are necessary.
- a return of the auxiliary liquid accumulating in the fine separator to the pump circuit is possible without separate return lines by providing a bore in the head part of the fine separator which is below the level of the surface of the auxiliary liquid collecting in the fine separator and opens into the lateral tube attachment of the suction nozzle of the vacuum pump. If, on the other hand, a return line is provided, it is expedient that this leads into the inlet connection of the vacuum pump or into the sector between the inlet and outlet opening of the working space of the vacuum pump. Due to the higher pressure prevailing in the container part of the fine separator in relation to the mouth into the vacuum pump, the auxiliary liquid is conveyed to the vacuum pump in both cases.
- a condensate separator in it. In this separator, any condensates contained in the auxiliary liquid are separated from the latter.
- the auxiliary liquid can be introduced into the working space of the pump at such a point where the suction process has already been completed.
- the intake volume flow is then only slightly influenced by the evaporating condensate. In such a case, a separate condensate separator is not necessary if the accumulation of condensate is only occasional and limited.
- a return of the auxiliary liquid accumulating in the fan cover without a separate conveying device is possible in that a discharge line of small cross-section is connected at the lowest point of the fan cover and is guided into the fine separator above the level of the auxiliary liquid accumulating in the fine separator.
- a pressure drop arises between the interior thereof and the container space surrounding the hollow roller-shaped filter. This pressure drop is effective on the discharge line leading from the fan cover to the fine separator and ensures that the auxiliary liquid is conveyed from the fan cover into the fine separator.
- a liquid ring pump 2 is mounted as a vacuum pump.
- an upward inlet connection 4 and an outlet connection 5 are each formed.
- a pipe extension 6 is connected to the outlet nozzle 5, to which a pre-separator 7 is connected.
- the pre-separator 7 has a head part 8 serving to connect various pipelines and a container part 9 receiving the separator elements.
- the head and container parts 8 and 9 are detachably connected to one another by means of a tension lock 10.
- a gas line 11 leads from the head part 8 of the pre-separator 7 to a fan hood 13 which encloses the fan 12 of the electric motor 1 and which forms a gas cooler.
- the fan cover 13 is double-walled, so that the gas supplied via the gas line 11 connected laterally to the fan cover 13 can flow through the cavity 16 existing between the walls 14 and 15 of the fan cover 13.
- the gas is introduced into the head part 18 of a fine separator 19 via a further gas line 17 connected laterally to the circumference of the fan cover 13.
- a container part 20 is connected to the top plate 18 of the fine separator 19, in the same way as for the pre-separator 7, by means of a tension lock 10.
- An outlet opening 21 for the gas is present in the head part 18 of the fine separator 19.
- the head part 18 itself is screwed onto a tubular extension 22 of the inlet connector 4 and is carried by the latter.
- a liquid cooler 23 designed as a tube coil is arranged between the electric motor 1 and the housing of the liquid ring pump 2 concentrically with the housing of the electric motor 1. Depending on the size of the liquid cooler 23, it can extend more or less over the length of the motor housing.
- the liquid cooler 23 is connected at its one end 24 to the head part 8 of the pre-separator 7.
- the other end 25 of the liquid cooler 23 either opens into the inlet connection 4 or into the sector between the inlet and outlet opening of the working space of the liquid ring pump 2.
- a discharge line 26 is connected, which is led into the fine separator 19 from the end face of the head part 18 of the fine separator 19 above the level of the surface of the auxiliary liquid 33 accumulating in the fine separator 19.
- a return line 27 connected to a drain hole 43 of the head part 18 also leads from the head part 18 to the inlet connection 4 of the liquid ring pump 2.
- the pre-separator 7 shown in a slightly schematic representation in FIG. 5 is screwed with an inlet opening 28 provided in its head part 8 onto the pipe extension 6 of the outlet connection 5 of the liquid ring pump 2.
- a gas guide line 29 is connected to the inlet bore 28.
- the gas guide line 29 runs parallel to the boundary wall of the container part 9 and ends shortly before the bottom 30 of the container part 9.
- a shield 31 pointing downward is arranged on the gas guide line 29 and a deflection plate 32 extending perpendicularly from the bottom 30 is arranged on the bottom of the container part 9.
- the gas emerging from the gas guide line 29 and loaded with auxiliary liquid 33 is deflected twice by the screen 31 and the deflection plate 32 by 90 ° each.
- auxiliary liquid 33 The majority of the auxiliary liquid 33 is separated out and collects in the lower region of the container part 9. A further part of the auxiliary liquid 33 is separated from the gas by means of a separating filter 34 arranged transversely in the container part 9. The gas flows behind the separating filter 34 to an outlet bore 35, whereby it is redirected again by a transverse wall 36. During this redirection, a further part of the auxiliary liquid 33 can precipitate on the transverse wall 36 and flow down from here.
- the gas line 11 leading to the fan cover 13 is connected to the outlet bore 35. Below the level of the surface of the auxiliary liquid 33 accumulating in the container part 9, a drain opening 37 is provided, to which the liquid cooler 23 is connected at its one end 24.
- the fine separator 19 shown schematically in FIG. 7 also has a gas supply opening 38 to which a hollow roller-shaped filter 40 is connected by means of a tube 39.
- the gas still loaded with a residual auxiliary liquid 33 enters the cavity of the filter 40 via the gas supply opening 38 and flows through it from the inside to the outside. Since the gas in the fan cover 13 has been cooled to a relatively low temperature after leaving the pre-separator 7, a high degree of separation is achieved in the filter 40. After flowing through the filter 40, the gas leaves the fine separator 19 via a post-filter 42 via the outlet opening 21.
- a drain bore 43 Below the surface of the auxiliary liquid 33 that collects in the lower area of the fine separator 19 is a drain bore 43, and the return line 27 is connected.
- a hole 44 leading into the lateral pipe socket 22 can also be provided, via which the auxiliary liquid 33 flows into the pipe socket 22 and from here into the inlet connection 4 of the liquid ring pump.
- the return line 27 must be provided if, prior to the return of the auxiliary liquid 33 into the liquid ring pump 2, a condensate present in the auxiliary liquid 33 is separated by means of a condensate separator or if the auxiliary liquid 33 is located at a certain point between the inlet and outlet openings of the working space of the vacuum pump to be reintroduced into the pump.
- FIGS. 6 and 8 show that these head parts have the same shape and size.
- Appropriate finish bores then prepare the head sections either for use on the pre-separator or fine separator.
- the inlet bore 28 and the drain opening 37 must be made on the head part 8 for the pre-separator 7 and the outlet opening 21 and the drain bore 43 and the bore 44 on the head part 18 for the fine separator 19.
- the device works as follows: Air is drawn in from a space in which a vacuum is to be created, via the inlet connection 4. The air is compressed in the liquid ring pump and, together with part of the auxiliary liquid 33 present in the liquid ring pump 2, is expelled into the pre-separator 7 via the outlet connection 5 and the pipe extension 6 connected to it. Most of the auxiliary liquid 33 is already separated out of the air-liquid mixture in the pre-separator 7. The auxiliary liquid 33 accumulating in the pre-separator 7 is conveyed into the liquid cooler 23 by the pressure prevailing in the pre-separator 7 and is cooled there by a certain temperature difference.
- the auxiliary liquid 33 flows from the liquid cooler 23 back into the inlet connection 4 or into the sector between the inlet and outlet opening of the working space of the pump and is thus available again for the further operation of the liquid ring pump 2.
- the liquid cooler 23 is dimensioned such that the auxiliary liquid 33 is cooled only by a relatively small temperature difference and leaves the liquid cooler 23 at a temperature which is favorable for the operation of the liquid ring pump 2.
- the air When flowing through the fan cover 13, the air is cooled down to a temperature which is substantially, ie. that is, by more than 10 ° C., below the outlet temperature of the auxiliary liquid 33 when it emerges from the liquid cooler 25.
- condensation of the auxiliary liquid vapors still present in it sets in, by means of which the separation of the auxiliary liquid 33 in the filter 40 is promoted.
- the air After flowing through the filter 40, the air leaves the fine separator 19 through the outlet opening 21.
- the auxiliary liquid 33 that accumulates in the fine separator 19 is returned to the circuit of the device via the drain hole 43 and the return line 27 or the hole 44 connected to it.
- the auxiliary liquid 33 By cooling the gas in the fan cover 13, part of the auxiliary liquid 33 can already condense here and collects at the lowest point of the fan cover 13. From here, the auxiliary liquid 33 is conveyed into the fine separator 19 via the discharge line 26. Since the discharge line 26 opens into the fine separator behind the filter 40, there is a pressure difference between their connection to the fan cover 13 and the opening in the fine separator 19, which pressure difference is sufficient to convey the auxiliary liquid 33 from the fan cover 13 into the fine separator. As a result of this arrangement of the discharge line 26, there is no need for a separate conveying device for the removal of the auxiliary liquid 33 from the fan cover 13.
- a liquid ring pump 2 as a vacuum pump is particularly advantageous for the operation of the liquid cooler 23 at a temperature level which is substantially higher than the temperature level of the Gaa cooler 13.
- a relatively large amount of auxiliary liquid 33 is expelled together with the compressed gas. This means that a large mass of liquid is available for the removal of the heat lost in the pump. It is therefore sufficient to have a relatively small temperature difference in the cooling of the auxiliary liquid in the liquid cooler in order to dissipate the heat loss to the outside.
- a relatively small gas cooler 13 is required to cool this gas.
- This gas cooler 13 is dimensioned such that the gas is cooled in the liquid cooler 23 by a substantially greater temperature difference than the auxiliary liquid 33.
- the respective coolers Due to the separate cooling of the auxiliary liquid 33 and the gas, the respective coolers can be designed specifically for the cooling capacity required in each case. Overall, this leads to less cooling effort.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Applications Or Details Of Rotary Compressors (AREA)
- Motor Or Generator Cooling System (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Compressor (AREA)
- Separation By Low-Temperature Treatments (AREA)
Claims (17)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT85114893T ATE40583T1 (de) | 1984-12-07 | 1985-11-25 | Vorrichtung zur erzeugung eines vakuums. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3444731 | 1984-12-07 | ||
DE3444731 | 1984-12-07 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0186776A1 EP0186776A1 (fr) | 1986-07-09 |
EP0186776B1 true EP0186776B1 (fr) | 1989-02-01 |
Family
ID=6252194
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP85114893A Expired EP0186776B1 (fr) | 1984-12-07 | 1985-11-25 | Dispositif de production d'un vide |
Country Status (8)
Country | Link |
---|---|
US (1) | US4657487A (fr) |
EP (1) | EP0186776B1 (fr) |
JP (1) | JPS61138897A (fr) |
CN (1) | CN1005642B (fr) |
AT (1) | ATE40583T1 (fr) |
DE (1) | DE3568071D1 (fr) |
ES (1) | ES8701917A1 (fr) |
IN (1) | IN162159B (fr) |
Families Citing this family (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4761166A (en) * | 1986-01-21 | 1988-08-02 | Cash Engineering Research Pty. Ltd. | Compressor system |
US5087178A (en) * | 1990-01-04 | 1992-02-11 | Rogers Machinery Company, Inc. | Oil flooded screw compressor system with moisture separation and heated air dryer regeneration, and method |
US5320501A (en) * | 1991-04-18 | 1994-06-14 | Vickers, Incorporated | Electric motor driven hydraulic apparatus with an integrated pump |
US5181837A (en) * | 1991-04-18 | 1993-01-26 | Vickers, Incorporated | Electric motor driven inline hydraulic apparatus |
BR9305877A (pt) * | 1992-02-14 | 1997-08-19 | Cash Eng Res | Vaso separador |
US5355901A (en) * | 1992-10-27 | 1994-10-18 | Autoclave Engineers, Ltd. | Apparatus for supercritical cleaning |
US5345771A (en) * | 1993-03-25 | 1994-09-13 | John Zink Company, A Division Of Koch Engineering Company, Inc. | Process for recovering condensable compounds from inert gas-condensable compound vapor mixtures |
DE4417607C1 (de) * | 1994-05-19 | 1995-10-19 | Siemens Ag | Pumpenaggregat |
ES2106611T3 (es) * | 1994-12-06 | 1997-11-01 | Siemens Ag | Grupo compresor. |
US7980753B2 (en) | 1998-04-16 | 2011-07-19 | Air Liquide Electronics U.S. Lp | Systems and methods for managing fluids in a processing environment using a liquid ring pump and reclamation system |
US20070119816A1 (en) * | 1998-04-16 | 2007-05-31 | Urquhart Karl J | Systems and methods for reclaiming process fluids in a processing environment |
US7871249B2 (en) * | 1998-04-16 | 2011-01-18 | Air Liquide Electronics U.S. Lp | Systems and methods for managing fluids using a liquid ring pump |
US20070109912A1 (en) * | 2005-04-15 | 2007-05-17 | Urquhart Karl J | Liquid ring pumping and reclamation systems in a processing environment |
US8056182B2 (en) * | 2005-08-30 | 2011-11-15 | Tacony Corporation | Heating system for a portable carpet extractor |
WO2009069090A2 (fr) | 2007-11-27 | 2009-06-04 | L'air Liquide-Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Fonction de récupération améliorée pour systèmes de traitement de semi-conducteurs |
DE102010061494A1 (de) * | 2010-12-22 | 2012-06-28 | Herborner Pumpenfabrik J. H. Hoffmann Gmbh & Co. Kg | Pumpvorrichtung |
WO2015188266A1 (fr) | 2014-06-10 | 2015-12-17 | Vmac Global Technology Inc. | Procédés et appareil pour simultanément refroidir et séparer un mélange de gaz chaud et de liquide |
CN105257546B (zh) * | 2015-09-08 | 2017-06-30 | 无锡压缩机股份有限公司 | 用于喷油螺杆真空泵的油气分离系统 |
US20160296902A1 (en) | 2016-06-17 | 2016-10-13 | Air Liquide Electronics U.S. Lp | Deterministic feedback blender |
CN110821832A (zh) * | 2019-10-28 | 2020-02-21 | 佛山百策机电设备有限公司 | 一种中央吸引真空机组 |
DE102020208731A1 (de) * | 2020-07-13 | 2022-01-13 | BSH Hausgeräte GmbH | Wäschepflegegerät mit einer Flüssigkeitsring-Pumpe |
GB2603971A (en) * | 2021-02-19 | 2022-08-24 | Leybold Tianjin Int Trade Co Ltd | Filtering module for use with a vacuum pump |
CN116838610B (zh) * | 2023-08-29 | 2023-11-17 | 泉州市中力机电有限公司 | 一种螺杆式空压机散热和热能回收装置 |
Family Cites Families (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1991548A (en) * | 1930-09-30 | 1935-02-19 | Prest O Lite Co Inc | Gas pumping system |
DE677399C (de) * | 1936-11-27 | 1939-06-24 | Otto Becker | Aus mehreren Einzelgeblaesen bestehendes, von einer gemeinsamen Grundplatte getragenes Drehkolbengeblaese zum Erzeugen von Saug- und Blasluft |
FR1329699A (fr) * | 1962-05-04 | 1963-06-14 | Perfectionnements aux compresseurs à piston rotatif | |
FR81597E (fr) * | 1962-05-11 | 1963-10-11 | Perfectionnements aux compresseurs à piston rotatif | |
US3156409A (en) * | 1962-08-07 | 1964-11-10 | Jaeger Machine Co | Enclosed rotary industrial air compressor |
US3291385A (en) * | 1965-06-01 | 1966-12-13 | Gardner Denver Co | Receiver-separator unit for liquidinjected compressor |
DE1628327A1 (de) * | 1966-09-29 | 1970-12-17 | Wittig Gmbh Maschf Karl | Vorrichtung zur Aussetz- bzw. Leerlaufregelung von Drehkolbenverdichtern |
DE2240018C3 (de) * | 1971-12-01 | 1979-01-25 | Airfina Ets., Vaduz | Ein- oder mehrstufiger Flügelzellen- oder Schraubenkolbenverdichter |
DE2217022C3 (de) * | 1972-04-08 | 1975-03-27 | Sihi Gmbh & Co Kg, 2210 Itzehoe | Flüssigkeitsring-Vakuumpumpe mit Umlaufbehälter |
NL7606975A (nl) * | 1975-09-22 | 1977-03-24 | Siemens Ag | Vloeistofpompopstelling. |
US4087208A (en) * | 1976-06-08 | 1978-05-02 | Mitsubishi Jukogyo Kabushiki Kaisha | Method for compressing mixed gas consisting of combustible gas and air |
DE2636493A1 (de) * | 1976-08-13 | 1978-02-16 | Guenter Kirsten | Vorrichtung zur erzeugung von druckluft mittels eines schraubenverdichters |
DE2841906C2 (de) * | 1978-09-26 | 1980-02-21 | Siemens Ag, 1000 Berlin Und 8000 Muenchen | Flüssigkeitsringverdichter oder -vakuumpumpe |
DE2912938C2 (de) * | 1979-03-31 | 1985-03-14 | Lederle Gmbh Pumpen Und Maschinenfabrik, 7800 Freiburg | Flüssigkeitsring-Gaspumpe |
DE3022147A1 (de) * | 1980-06-13 | 1982-01-07 | Klöckner-Humboldt-Deutz AG, 5000 Köln | Verdichter |
-
1985
- 1985-09-10 CN CN85106797.2A patent/CN1005642B/zh not_active Expired
- 1985-09-30 IN IN685/CAL/85A patent/IN162159B/en unknown
- 1985-11-15 US US06/798,565 patent/US4657487A/en not_active Expired - Fee Related
- 1985-11-25 AT AT85114893T patent/ATE40583T1/de not_active IP Right Cessation
- 1985-11-25 EP EP85114893A patent/EP0186776B1/fr not_active Expired
- 1985-11-25 DE DE8585114893T patent/DE3568071D1/de not_active Expired
- 1985-12-03 JP JP60273150A patent/JPS61138897A/ja active Pending
- 1985-12-06 ES ES549668A patent/ES8701917A1/es not_active Expired
Non-Patent Citations (1)
Title |
---|
"Fluid" Okt 1982; Helmut Jansen "Oleingespritzte Kompressoren" S.58 * |
Also Published As
Publication number | Publication date |
---|---|
CN85106797A (zh) | 1986-06-10 |
IN162159B (fr) | 1988-04-09 |
DE3568071D1 (en) | 1989-03-09 |
US4657487A (en) | 1987-04-14 |
CN1005642B (zh) | 1989-11-01 |
ES8701917A1 (es) | 1986-12-01 |
EP0186776A1 (fr) | 1986-07-09 |
ATE40583T1 (de) | 1989-02-15 |
JPS61138897A (ja) | 1986-06-26 |
ES549668A0 (es) | 1986-12-01 |
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