EP0952882A1 - Device for separating liquid particles from a gas stream - Google Patents

Device for separating liquid particles from a gas stream

Info

Publication number
EP0952882A1
EP0952882A1 EP97951886A EP97951886A EP0952882A1 EP 0952882 A1 EP0952882 A1 EP 0952882A1 EP 97951886 A EP97951886 A EP 97951886A EP 97951886 A EP97951886 A EP 97951886A EP 0952882 A1 EP0952882 A1 EP 0952882A1
Authority
EP
European Patent Office
Prior art keywords
filter insert
liquid particles
gas stream
gas
module
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.)
Withdrawn
Application number
EP97951886A
Other languages
German (de)
French (fr)
Inventor
Hans-Werner Holch
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mann and Hummel GmbH
Original Assignee
Filterwerk Mann and Hummel GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Filterwerk Mann and Hummel GmbH filed Critical Filterwerk Mann and Hummel GmbH
Publication of EP0952882A1 publication Critical patent/EP0952882A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
    • B01D46/003—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions including coalescing means for the separation of liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
    • B01D46/62—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
    • B01D46/64—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series arranged concentrically or coaxially
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0084—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours provided with safety means
    • B01D46/0087—Bypass or safety valves
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • B01D46/2411—Filter cartridges
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
    • B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01M—LUBRICATING OF MACHINES OR ENGINES IN GENERAL; LUBRICATING INTERNAL COMBUSTION ENGINES; CRANKCASE VENTILATING
    • F01M13/00—Crankcase ventilating or breathing
    • F01M13/0011—Breather valves
    • F01M2013/0016—Breather valves with a membrane
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01M—LUBRICATING OF MACHINES OR ENGINES IN GENERAL; LUBRICATING INTERNAL COMBUSTION ENGINES; CRANKCASE VENTILATING
    • F01M13/00—Crankcase ventilating or breathing
    • F01M13/04—Crankcase ventilating or breathing having means for purifying air before leaving crankcase, e.g. removing oil
    • F01M2013/0422—Separating oil and gas with a centrifuge device
    • F01M2013/0427—Separating oil and gas with a centrifuge device the centrifuge device having no rotating part, e.g. cyclone
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01M—LUBRICATING OF MACHINES OR ENGINES IN GENERAL; LUBRICATING INTERNAL COMBUSTION ENGINES; CRANKCASE VENTILATING
    • F01M13/00—Crankcase ventilating or breathing
    • F01M13/04—Crankcase ventilating or breathing having means for purifying air before leaving crankcase, e.g. removing oil
    • F01M2013/0438—Crankcase ventilating or breathing having means for purifying air before leaving crankcase, e.g. removing oil with a filter

Definitions

  • the invention relates to an arrangement for separating liquid particles from a gas stream, in particular as an oil mist separator, according to the preamble of the main claim.
  • a pressure control valve is switched into an intake path.
  • this pressure control valve is installed in a ventilation line between the crankcase and the intake pipe or the air filter in a motor vehicle by means of two flanges.
  • the invention is based on the object of developing an arrangement for separating liquid particles from a gas stream in accordance with the preamble of the main claim in a simple manner so that a compact module can be constructed in which a high degree of separation is reliably ensured with optimum pressure conditions.
  • the arrangement according to the invention is particularly advantageous in that a compact arrangement of both a cyclone for the first coarse separation of liquid speed particles and a downstream filter insert for further, finer separation stages in connection with a pressure control valve, which sits directly on the filter insert in a common housing, an optimal flow rate of the gas flow is ensured in a structurally simple manner.
  • the flow velocity of the gas corresponds in particular to the passage behavior of the filter inserts, so that the liquid drops that are formed are not carried away again by a gas flowing at too high a speed.
  • the size of the droplets that form as a function of the fiber structure of the filter insert also plays a role here.
  • the arrangement according to the invention is particularly advantageous according to one embodiment of a dependent claim with a multi-stage filter insert. Coarse separation and fine separation can be carried out with different layers of the filter insert, for example with a relatively narrow fiber structure and a relatively coarse fiber structure.
  • the necessary fine tuning of the flow velocity is possible in a simple manner by the pressure control valve immediately following in the flow direction. The flow velocity is optimized in such a way that the droplets with a size determined by the fiber structure are not carried away by the gas flow again, which would reduce the separation effect.
  • FIG. 1 An embodiment of the arrangement according to the invention for separating liquid particles from a gas stream is explained with reference to the drawing.
  • the figure of the drawing shows a section through a module with multi-stage separation of the liquid particles.
  • a separator module 1 is shown in the figure, in which the gas identified by arrows 3 enters the separator module 1 through a raw gas inlet 2.
  • a first cylinder 4 there is a cyclone which is formed by an internal cylinder 5 and which the inflowing raw gas by a guide device or the like. set in rotation. Liquid particles are radially accelerated by the rotation and then flow from the side walls of the cylinder 4 into a collecting container 6.
  • the collecting container 6 shown schematically here in the lower area of the module 1 is connected to a liquid outlet 7.
  • the liquid outlet 7 is designed as a siphon-like drain, not shown here, so that there is no disruptive gas suction in the separating module 1 in this way.
  • the gas cleaned in the first stage described above hits layers 8 and 9 of a filter insert in a second cylinder 10, each of which is held on a gas-permeable support body 11. Liquid droplets also form in these separation stages, which are made from different fiber structures the gas flow (arrows 3) are separated and are also reflected in the collecting container 6.
  • the clean gas now largely freed of liquid particles, is led into the pressure control valve 12 located in the cylinder 10.
  • the pressure control valve 12 which is not explained in greater detail here, is described in the prior art DE-40 22 129 C2 mentioned at the outset and has the task of ensuring a relatively constant pressure and thus a uniform flow rate even when the pressure inside the separating module 1 fluctuates greatly .
  • the clean gas (arrows 3) enters the upper region 13 of the pressure control valve 12 and leaves the separating module 1 via the clean gas outlet 14.

Abstract

A device for separating liquid particles from a gas stream has a filter insert (8, 9, 11) placed in a gas stream (3) generated by an outer pressure difference. Liquid particles remain on the outer surface of the filter insert (8, 9, 11) at the crude gas side, forming droplets which can be fed into a collecting container (6). The device is a compact separating module (1) with several stages, a cyclone (5), a filter insert (8, 9, 11) and a pressure regulating valve (12).

Description

Anordnuncr zum Abscheiden von Flüssicrkeitspartikeln aus einem Gasstrom Arrangement for separating liquid particles from a gas stream
Stand der TechnikState of the art
Die Erfindung betrifft eine Anordnung zum Abscheiden von Flüssigkeitspartikeln aus einem Gasstrom, insbesondere als Ölnebelabscheider, nach dem Oberbegriff des Hauptanspruchs .The invention relates to an arrangement for separating liquid particles from a gas stream, in particular as an oil mist separator, according to the preamble of the main claim.
Es ist beispielsweise aus der GB 988 692 bekannt, dass solche Filtereinsätze in den Strömungsweg eines Gasstroms geschaltet werden und dabei die Flüssigkeitspartikel an den festen Strukturen der Filtereinsätze, beispielsweise an den Elementarfäden eines Vlieses, hängen bleiben und Flüssigkeitstropfen bilden die nach unten in einen Sammelbehälter tropfen und von dort entsorgt oder wieder in einen Flüssigkeitskreislauf zurück gelangen können. Für viele Anwendungsfälle, beispielsweise eine Anordnung im Ansaugtrakt eines Verbrennungsmotors für ein Kraftfahrzeug, ist wichtig, dass ein hoher Abscheidegrad bei geringem Druckverlust im Strömungsweg erreicht wird ohne eine Vielzahl zusätzlicher Aggregate räumlich aufwendig zusammenschalten zu müssen.It is known, for example from GB 988 692, that such filter inserts are switched into the flow path of a gas stream and the liquid particles get caught on the solid structures of the filter inserts, for example on the filaments of a nonwoven, and form liquid drops that drip down into a collecting container and can be disposed of or returned to a liquid cycle. For Many applications, for example an arrangement in the intake tract of an internal combustion engine for a motor vehicle, it is important that a high degree of separation is achieved with a low pressure loss in the flow path without having to interconnect a large number of additional units in a spatially complex manner.
Für sich gesehen ist es beispielsweise aus der DE-40 22 129 C2 bekannt, dass in einen Ansaugweg ein Druckregel- ventil geschaltet wird. Beispielsweise wird dieses Druckregelventil in eine Entlüftungsleitung zwischen dem Kurbelgehäuse und dem Ansaugrohr bzw. dem Luftfilter in einem Kraftfahrzeug mittels zweier Flansche eingebaut .Seen in isolation, it is known, for example from DE-40 22 129 C2, that a pressure control valve is switched into an intake path. For example, this pressure control valve is installed in a ventilation line between the crankcase and the intake pipe or the air filter in a motor vehicle by means of two flanges.
AufgabenstellungTask
Der Erfindung liegt die Aufgabe zugrunde, eine Anordnung zum Abscheiden von Flüssigkeitspartikeln aus einem Gas- strom, nach dem Oberbegriff des Hauptanspruchs auf einfache Weise so fortzubilden, daß ein kompaktes Modul aufbaubar ist, in dem zuverlässig ein hoher Abscheidegrad bei optimalen Druckverhältnissen gewährleistet ist.The invention is based on the object of developing an arrangement for separating liquid particles from a gas stream in accordance with the preamble of the main claim in a simple manner so that a compact module can be constructed in which a high degree of separation is reliably ensured with optimum pressure conditions.
Vorteile der ErfindungAdvantages of the invention
Die erfindungsgemäße Anordnung zum Abscheiden von Flüssigkeitspartikeln aus einem Gasstrom, insbesondere als Ölnebelabscheider, löst die gestellte Aufgabe mit den im Kennzeichen des Hauptanspruchs angegebenen Merkmalen.The arrangement according to the invention for separating liquid particles from a gas stream, in particular as an oil mist separator, achieves the stated object with the features specified in the characterizing part of the main claim.
Vorteilhaft ist die erfindungsgemäße Anordnung insbesondere dadurch, daß durch eine kompakte Anordnung sowohl eines Zyklons zur ersten Grobabscheidung von Flüssig- keitspartikeln und einem nachgeschaltetem Filtereinsatz für weitere, feinere Abscheidungsstufen in Verbindung mit einem Druckregelventil, das direkt auf dem Filtereinsatz in einem gemeinsamen Gehäuse sitzt, in konstruktiv einfacher Weise eine optimale Strömungsgeschwindigkeit das Gasstroms sichergestellt ist.The arrangement according to the invention is particularly advantageous in that a compact arrangement of both a cyclone for the first coarse separation of liquid speed particles and a downstream filter insert for further, finer separation stages in connection with a pressure control valve, which sits directly on the filter insert in a common housing, an optimal flow rate of the gas flow is ensured in a structurally simple manner.
Für die möglichst vollständige Abscheidung der Flüssigkeitspartikel ist es wichtig, dass die Strömungsgeschwindigkeit des Gases insbesondere mit dem Durchlassverhalten der Filtereinsätze korrespondiert, damit die sich bildenden Flüssigkeitstropfen nicht von einem mit zu hoher Geschwindigkeit strömenden Gases wieder mitgerissen werden. Auch die Größe der sich bildenden Tropfen in Abhängigkeit von der Faserstruktur des Filtereinsatzes spielt hierbei eine Rolle.For the most complete possible separation of the liquid particles, it is important that the flow velocity of the gas corresponds in particular to the passage behavior of the filter inserts, so that the liquid drops that are formed are not carried away again by a gas flowing at too high a speed. The size of the droplets that form as a function of the fiber structure of the filter insert also plays a role here.
Besonders vorteilhaft ist die erfindungsgemäße Anordnung gemäß einer Ausführungsform eines Unteranspruchs mit einem mehrstufigen Filtereinsatz. Hierbei können mit unterschiedlichen Schichten des Filtereinsatzes, beispielsweise mit relativ enger Faserstruktur und relativ grober Faserstruktur, eine Grobabscheidung und eine Feinabscheidung vorgenommen werden. Die hierzu notwendige Feinabstimmung der Strömungsgeschwindigkeit ist durch das unmittelbar in Strömungsrichtung folgende Druckregelventil auf einfache Weise möglich. Die Strömungsgeschwindigkeit ist dahingehend optimiert, dass die Tropfen mit einer durch die Faserstruktur bestimmten Größe nicht durch den Gasstrom wieder mitgerissen werden, wodurch der Abscheideeffekt geschmälert werden würde.The arrangement according to the invention is particularly advantageous according to one embodiment of a dependent claim with a multi-stage filter insert. Coarse separation and fine separation can be carried out with different layers of the filter insert, for example with a relatively narrow fiber structure and a relatively coarse fiber structure. The necessary fine tuning of the flow velocity is possible in a simple manner by the pressure control valve immediately following in the flow direction. The flow velocity is optimized in such a way that the droplets with a size determined by the fiber structure are not carried away by the gas flow again, which would reduce the separation effect.
Andere vorteilhafte Ausführungsformen sind in den weiteren Unteransprüchen angegeben. ZeichnungOther advantageous embodiments are specified in the further subclaims. drawing
Ein Ausführungsbeispiel der erfindungsgemäßen Anordnung zum Abscheiden von Flüssigkeitspartikeln aus einem Gasstrom wird anhand der Zeichnung erläutert . Die Figur der Zeichnung zeigt einen Schnitt durch ein Modul mit mehrstufiger Abscheidung der Flüssigkeitspartikel.An embodiment of the arrangement according to the invention for separating liquid particles from a gas stream is explained with reference to the drawing. The figure of the drawing shows a section through a module with multi-stage separation of the liquid particles.
Beschreibung des AusführungsbeispielsDescription of the embodiment
In der Figur ist ein Abscheidemodul 1 gezeigt, bei dem durch einen Rohgaseintritt 2 das mit Pfeilen 3 gekennzeichnete Gas in das Abscheidemodul 1 eintritt. In einem ersten Zylinder 4 befindet sich eine Zyklone, die durch einen innenliegenden Zylinder 5 gebildet ist und die das einströmende Rohgas durch eine Leitvorrichtung oder dgl . in Rotation versetzt. Durch die Rotation werden Flüssigkeitspartikel radial beschleunigt und fließen dann von den Seitenwänden des Zylinders 4 in einen Sammelbehälter 6 ab.A separator module 1 is shown in the figure, in which the gas identified by arrows 3 enters the separator module 1 through a raw gas inlet 2. In a first cylinder 4 there is a cyclone which is formed by an internal cylinder 5 and which the inflowing raw gas by a guide device or the like. set in rotation. Liquid particles are radially accelerated by the rotation and then flow from the side walls of the cylinder 4 into a collecting container 6.
Der hier schematisch dargestellte Sammelbehälter 6 im unteren Bereich des Moduls 1 ist mit einem Flüssigkeitsaustritt 7 verbunden. Der Flüssigkeitsaustritt 7 ist als ein hier nicht näher dargestellter syphonartiger Abfluss ausgeführt, damit auf diesem Wege keine störende Gasansau- gung im Abscheidemodul 1 erfolgt .The collecting container 6 shown schematically here in the lower area of the module 1 is connected to a liquid outlet 7. The liquid outlet 7 is designed as a siphon-like drain, not shown here, so that there is no disruptive gas suction in the separating module 1 in this way.
Das in der oben beschriebenen ersten Stufe gereinigte Gas trifft in einem zweiten Zylinder 10 auf Schichten 8 und 9 eines Filtereinsatzes, die jeweils an einem gasdurchlässigen Stützkörper 11 gehalten sind. In diesen aus unterschiedlichen Faserstrukturen hergestellten Abscheidestufen bilden sich ebenfalls Flüssigkeitstropfen, die aus dem Gasstrom (Pfeile 3) abgeschieden werden und sich auch im Sammelbehälter 6 niederschlagen.The gas cleaned in the first stage described above hits layers 8 and 9 of a filter insert in a second cylinder 10, each of which is held on a gas-permeable support body 11. Liquid droplets also form in these separation stages, which are made from different fiber structures the gas flow (arrows 3) are separated and are also reflected in the collecting container 6.
Das nunmehr weitgehend von Flüssigkeitspartikeln befreite Reingas wird im Zylinder 10 in das oben liegende Druckregelventil 12 geführt . Das hier nicht näher erläuterte Druckregelventil 12 ist im eingangs erwähnten Stand der Technik DE-40 22 129 C2 beschrieben und hat die Aufgabe auch bei großen Schwankungen des von außen beaufschlagten Drucks im Inneren des Abscheidemoduls 1 einen relativ konstanten Druck und damit eine gleichmäßige Strömungsgeschwindigkeit zu gewährleisten. Das Reingas (Pfeile 3) tritt hierbei in den oberen Bereich 13 des Druckregelventils 12 ein und verläßt das Abscheidemodul 1 über den Reingasaustritt 14. The clean gas, now largely freed of liquid particles, is led into the pressure control valve 12 located in the cylinder 10. The pressure control valve 12, which is not explained in greater detail here, is described in the prior art DE-40 22 129 C2 mentioned at the outset and has the task of ensuring a relatively constant pressure and thus a uniform flow rate even when the pressure inside the separating module 1 fluctuates greatly . The clean gas (arrows 3) enters the upper region 13 of the pressure control valve 12 and leaves the separating module 1 via the clean gas outlet 14.

Claims

SchutzansprücheProtection claims
1) Anordnung zum Abscheiden von Flüssigkeitspartikeln aus einem Gasstrom, mit einem Filtereinsatz (8,9,11), der in einen aufgrund einer äußeren Druckdifferenz hervorgerufenen Gasstrom (3) geschaltet ist und an dessen Oberfläche an der Rohgasseite Flüssigkeitspartikel tropfenbildend hängenbleiben und einem Sammelbehälter (6) zuführbar sind, dadurch gekennzeichnet, dass1) Arrangement for separating liquid particles from a gas stream, with a filter insert (8, 9, 11) which is connected to a gas stream (3) caused by an external pressure difference and on the surface of which liquid particles stick to the raw gas side and form a collecting container ( 6) can be fed, characterized in that
- die Anordnung ein kompaktes mehrstufiges Abscheidemodul (1) ist, das einen obenliegenden Rohgaseintritt (2) , den untenliegenden Sammelbehälter (6) für die abgeschiedene Flüssigkeit und einen Reingasaustritt (14) aufweist und in seinem Inneren folgenden Bauelemente hat,- The arrangement is a compact, multi-stage separation module (1) which has an overhead raw gas inlet (2), the bottom collection container (6) for the separated liquid and a clean gas outlet (14) and has the following components in its interior,
- für eine erste Abscheidestufe ist eine Zyklone (5) zur Abscheidung von Flüssigkeitspartikeln durch Rotationsbeschleunigung vorhanden,a cyclone (5) for separating liquid particles by rotational acceleration is present for a first separation stage,
- für eine zweite Abscheidestufe ist der Filtereinsatz (8,9,11) direkt benachbart der Zyklone (5) im Gasstrom angeordnet und- For a second separation stage, the filter insert (8,9,11) is arranged directly adjacent to the cyclones (5) in the gas stream and
- oberhalb des Filtereinsatzes ist ein Druckregelventil (12) zwischen dem Reingasaustritt (14) des Filtereinsatzes (8,9,11) und dem Reingasaustritt (14) des Abscheidemoduls (1) angeordnet. 2) Anordnung nach Anspruch 1, dadurch gekennzeichnet, dass- Above the filter insert, a pressure control valve (12) is arranged between the clean gas outlet (14) of the filter insert (8, 9, 11) and the clean gas outlet (14) of the separating module (1). 2) Arrangement according to claim 1, characterized in that
- das Abscheidemodul (1) in Inneren zwei, im unteren Bereich miteinander verbundene Hohlzylinder aufweist, von denen- The separator module (1) has two hollow cylinders, one of which is connected to one another in the lower region
- einer die Zyklone (5) beinhaltet, in der das Rohgas beim Einströmen in Rotation versetzbar ist und Flüssigkeitspartikel aufgrund der Rotation an einer Wand niedergeschlagen werden und nach unten zum Sammelbehälter (6) fließen sowie- One contains the cyclones (5) in which the raw gas can be set into rotation when flowing in and liquid particles are deposited on a wall due to the rotation and flow down to the collecting container (6) and
- der zweite Zylinder (10) den ebenfalls über dem Sammelbehälter (6) liegenden hohlzylindrischen Filtereinsatz (8,9,11) mit dem darüber angeordneten Druckregelventil (12) beinhaltet.- The second cylinder (10) contains the hollow cylindrical filter insert (8, 9, 11) also lying above the collecting container (6) with the pressure control valve (12) arranged above it.
3) Anordnung nach Anspruch 1 oder 2, dadurch gekennzeichnet, dass3) Arrangement according to claim 1 or 2, characterized in that
der Filtereinsatz aus mindestens zwei radial ineinan- derliegenden, an gasdurchlässigen, hohlzylindrigen Stützen (11) gehaltenen, Fasergewebeschichten (8,9) besteht.the filter insert consists of at least two radially nested fiber fabric layers (8, 9) held on gas-permeable, hollow-cylindrical supports (11).
4) Anordnung nach Anspruch 3, dadurch gekennzeichnet, dass4) Arrangement according to claim 3, characterized in that
- das Abscheidemodul (1) zum Abscheiden eines Ölnebels im Ansaugtrakt eines Verbrennungsmotors einsetzbar ist. - The separation module (1) can be used to separate an oil mist in the intake tract of an internal combustion engine.
EP97951886A 1997-01-15 1997-11-11 Device for separating liquid particles from a gas stream Withdrawn EP0952882A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE29700579U 1997-01-15
DE29700579U DE29700579U1 (en) 1997-01-15 1997-01-15 Arrangement for separating liquid particles from a gas stream
PCT/EP1997/006293 WO1998031452A1 (en) 1997-01-15 1997-11-11 Device for separating liquid particles from a gas stream

Publications (1)

Publication Number Publication Date
EP0952882A1 true EP0952882A1 (en) 1999-11-03

Family

ID=8034562

Family Applications (1)

Application Number Title Priority Date Filing Date
EP97951886A Withdrawn EP0952882A1 (en) 1997-01-15 1997-11-11 Device for separating liquid particles from a gas stream

Country Status (7)

Country Link
US (1) US6309436B1 (en)
EP (1) EP0952882A1 (en)
JP (1) JP2001508148A (en)
BR (1) BR9714206A (en)
CA (1) CA2277993A1 (en)
DE (1) DE29700579U1 (en)
WO (1) WO1998031452A1 (en)

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Also Published As

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BR9714206A (en) 2000-03-28
CA2277993A1 (en) 1998-07-23
JP2001508148A (en) 2001-06-19
US6309436B1 (en) 2001-10-30
WO1998031452A1 (en) 1998-07-23
DE29700579U1 (en) 1997-03-13

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