EP2529829B1 - Dispersal rotor for homogenising flowable media - Google Patents

Dispersal rotor for homogenising flowable media Download PDF

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Publication number
EP2529829B1
EP2529829B1 EP11168428.8A EP11168428A EP2529829B1 EP 2529829 B1 EP2529829 B1 EP 2529829B1 EP 11168428 A EP11168428 A EP 11168428A EP 2529829 B1 EP2529829 B1 EP 2529829B1
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EP
European Patent Office
Prior art keywords
rotor
teeth
dispersing
dispersing rotor
toothing
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EP11168428.8A
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German (de)
French (fr)
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EP2529829A1 (en
Inventor
Erwin Seefried
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Vakumix Ruehr- und Homogenisiertechnik AG
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Vakumix Ruehr- und Homogenisiertechnik AG
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Application filed by Vakumix Ruehr- und Homogenisiertechnik AG filed Critical Vakumix Ruehr- und Homogenisiertechnik AG
Priority to DK11168428.8T priority Critical patent/DK2529829T3/en
Priority to PL11168428T priority patent/PL2529829T3/en
Priority to EP11168428.8A priority patent/EP2529829B1/en
Priority to JP2012117911A priority patent/JP2012250228A/en
Priority to CA2778753A priority patent/CA2778753A1/en
Priority to US13/486,313 priority patent/US9452396B2/en
Publication of EP2529829A1 publication Critical patent/EP2529829A1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/81Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis the stirrers having central axial inflow and substantially radial outflow
    • B01F27/811Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis the stirrers having central axial inflow and substantially radial outflow with the inflow from one side only, e.g. stirrers placed on the bottom of the receptacle, or used as a bottom discharge pump
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/111Centrifugal stirrers, i.e. stirrers with radial outlets; Stirrers of the turbine type, e.g. with means to guide the flow

Definitions

  • the invention relates to a dispersing rotor for homogenizing flowable media, which has an axially pointing rotor toothing.
  • Homogenizers are used, inter alia, in the pharmaceutical, cosmetic, chemical and food industries for the production of creams, ointments, pastes, mayonnaises and similar products.
  • a homogenizer is arranged at the bottom of a mixing container, which is usually designed as a rotor-stator dispersing machine.
  • Such a homogenizer is for example in EP 0 988 887 A1 disclosed.
  • Other generic devices are in WO02 / 060569 and DE-A-19537303 described.
  • the invention has for its object to provide a way to homogenize flowable media that is simple, efficient and versatile.
  • a dispersing rotor according to the invention has a rotor toothing, which forms a labyrinth toothing for medium emerging in the radial direction from the direction of the rotor axis to the outside.
  • the dispersing rotor according to the invention is used for dispersing (homogenizing, emulsifying or suspending) flowable media. This includes that too Preparation of single or multi-phase mixtures such as gels, emulsions or suspensions.
  • the dispersing rotor has an axially pointing rotor toothing.
  • gearing refers to openings in a circumferential wall of the rotor through which medium or mixture passes during operation in the radial direction to the outside. Such a toothing may have individual openings in an otherwise closed, circumferentially extending wall.
  • the toothing is formed by a arranged on a peripheral portion of the rotor plurality of axially extending teeth having baffles for the medium to be mixed.
  • the terms axial and radial are related in the context of the present invention to the axis of rotation of the rotor.
  • the rotor toothing forms a labyrinth toothing for medium passing outward in the radial direction from the direction of the rotor axis.
  • labyrinth toothing means that mixed material fed in the region of the axis of the rotor can not escape through the toothing on a straight line pointing in the radial direction, but that due to the arrangement of the teeth it always has to change direction, ie has to flow through a labyrinth path.
  • the invention has recognized that, surprisingly, a good mixing and homogenizing effect can be achieved exclusively by means of such a rotor, without this having to cooperate with a rotor toothing (which is generally fixed) relative to the rotor.
  • the labyrinth toothing according to the invention allows good mixing and homogenization exclusively by using such a dispersing rotor.
  • the homogenization of the medium is much gentler than when using a rotor-stator dispersing machine of the prior art, since a lower energy input and thus also a lower heat development takes place. Accordingly, the mechanical energy to be expended for homogenization is correspondingly lower.
  • the reduced heat input allows a gentler homogenization of sensitive products such as gels or creams.
  • the invention has thus recognized that the large shearing of the medium on alternating rotor and stator teeth considered necessary in the prior art is not required, instead the constant rate changes in the labyrinth path permit elongation and comminution of liquid droplets (for example, emulsions) and thus a homogenization.
  • the medium When passing through a row of teeth, the medium receives a pulse through the rotating rotor which, depending on the speed and flow direction of the medium and the rotational speed of the rotor, leads to a corresponding change in the direction of flow and velocity of the medium.
  • the dispersing rotor according to the invention preferably has so-called rows of teeth. It is a row of teeth to a arranged on a circumferential circle arrangement of teeth, which thus each have the same radial distance from the rotor axis.
  • the dispersing rotor is formed closed at one or both axial ends. This means that in the closed area formed no or at most a slight leakage of medium in the axial direction is possible.
  • the entire circular area of the Rotor formed closed at both axial ends but at least at one axial end is a central opening through which medium can enter from one axial side.
  • at least at one axial end (end face) only that circular ring is formed closed, which is occupied by the rotor toothing. It is thus ensured that the medium passing through penetrates the dispersing rotor radially from the inside to the outside on the intended labyrinth paths.
  • the axial height of the rotor toothing may be 10 to 30 mm, more preferably 12 to 25 mm.
  • the term refers to the free height in the ring plane of the corresponding rotor toothing, through the passage of medium is possible.
  • the diameter of a dispersing rotor according to the invention can be adapted to the installation conditions. For example, when installed in pipelines, small diameters of, for example, 5 to 10 cm may be used. When installed in larger mixing vessels, the diameter can be, for example, between 10 and 30 cm.
  • the stated values can be combined as desired to upper and lower limits according to the invention.
  • the teeth of the rotor toothing in the radial direction between them gaps of 0.3 to 3 mm, preferably 0.5 to 1.5 mm.
  • this is the clear radial distance between each two concentrically arranged rows of teeth.
  • the teeth preferably the teeth of each of the concentric rows of teeth
  • the teeth preferably have gaps of 0.5 to 4 mm, more preferably 1 to 3 mm, more preferably 1.5 to 2.5 mm.
  • the coverage of a row of teeth over the circumference of this row of teeth is preferably between 40 and 80%, more preferably 50 and 70%. These limits can be combined as desired to areas according to the invention.
  • overlap refers to that portion of the circumference of a row of teeth on which the passage of medium in the radial direction is blocked by this row of teeth. For example, a coverage of 60% means that 60% of the circumference of the corresponding row of teeth is blocked by the teeth while the remaining 40% of the circumference allows medium to pass through.
  • two rows of teeth arranged adjacent in the radial direction together have complete coverage. This means that medium can not pass through these two radially successive rows of teeth, without departing from the radial direction.
  • At least a part of the teeth has conveying surfaces pointing in the circumferential direction, which are designed to impart a pulse component radially outwards to the impacting medium.
  • Pointing in the circumferential direction does not mean that these surfaces are aligned exactly in the circumferential direction, that is a perpendicular to these surfaces exactly in the circumferential direction. It deals Rather, as a rule, be inclined surfaces, a perpendicular to these inclined surfaces preferably has a direction component radially outward. If, when the dispersing rotor rotates, this conveying surface encounters passing medium, an impulse is exerted on the medium which has a directional component radially outward. Accordingly, the medium is accelerated radially outward with an acceleration or velocity component.
  • the invention furthermore relates to a homogenizing device for homogenizing flowable media which has a dispersing rotor according to the invention.
  • the omission of a stator toothing offers a number of significant advantages. It is a relatively free positioning of the dispersing within the homogenizer possible because no structural precautions must be taken to vorzuhalten a engaging in the rotor teeth stator toothing.
  • the dispersing rotor can be arranged, for example, in a lower region of a homogenizing container, preferably in its bottom region. It is also possible to arrange a plurality of dispersing rotors within a container, for example to arrange a plurality of such rotors on an axis guided through the lid or bottom of such a container. It is also possible within the scope of the invention to arrange the dispersing rotor in a pipeline through which the medium to be mixed is passed. The dispersing rotor according to the invention can thus be used for so-called in-line mixing in a pipeline.
  • Non-contact drives have the advantage that no penetrations of drive axles through the wall of the homogenizing container are required and thus containers and dispersing rotor can be designed so that the possibilities of cleaning and germ free are optimized.
  • the dispersing rotor according to the invention has a receptacle 1 for a drive shaft (in FIG Fig. 1 not shown). Rotationally connected thereto is a rotor 2, on which pump vanes 4 are arranged, which serve to convey medium entering through the inlet 3 radially outward.
  • the order the pump blade 4 corresponds for example to the arrangement shown in FIG EP 0 988 887 A1 , there pumping 18 in Fig. 2 ,
  • the dispersing rotor according to the invention has four radially staggered rows of teeth 5, is conveyed through the medium entering the inlet 3 radially outward. These rows of teeth form a labyrinth path for radially outward medium, that is, medium can not pass without directional changes through these rows of teeth.
  • the dispersing rotor is closed towards the axial end faces, so that mixed material from the toothing can not escape axially upwards or downwards.
  • Fig. 1 Six radially staggered rows of teeth are arranged.
  • Fig. 2 schematically shows a radial section through these rows of teeth. It can be seen radially staggered rows of teeth, each having teeth 6. It concerns with Fig. 2 an enlarged view.
  • the length of the column in the circumferential direction (reference numeral 7) is about 2 mm, the gap width in the radial direction (reference numeral 8) about 0.5 mm.
  • the teeth 6 form a labyrinth path through which medium must pass outwards.
  • the circumferentially extending surfaces 16 of the teeth form conveying surfaces which when impinged on medium impart a radially outward pulse component thereto.
  • the diameter of the in Fig. 1 shown dispersing rotor may be about 10 cm in this embodiment.
  • Typical rotational speeds during operation may, for example be 6500 to 14,000 min -1.
  • Fig. 3 schematically shows a mounting situation in which a dispersing rotor according to the invention is arranged in a mixing container above the container bottom 9.
  • a drive shaft 10 passes through the container bottom.
  • Fig. 4 shows another variant of a homogenizer according to the invention, in which a longer drive shaft 10 passes through the container bottom 9 passes. At this drive shaft 10 two or more if required, more dispersing rotors according to the invention are arranged.
  • a dispersing rotor according to the invention is installed in the bottom housing of a mixing container.
  • a cover 17 covers the rotor at its outer periphery and forms, together with the bottom housing, an annular gap 11 through which medium emerging on the outer circumference of the rotor can be guided back into the container.
  • this medium through a in Fig. 5 remove circulation line, not shown, from the container and supply, for example, in another (preferably upper) region of the container again.
  • Fig. 6 shows an embodiment in which the rotor is driven via a magnetic coupling.
  • a drive shaft 13 is arranged, which is provided with magnets and within the container arranged magnets 12 entrains, which are rotatably connected to the rotor.
  • Fig. 7 shows an embodiment in which a drive shaft 15 is guided by the lid 14 of a mixing container.
  • Fig. 8 schematically shows further possible embodiments of a labyrinth toothing according to the invention.
  • a toothing is indicated, in which the individual teeth have a rod shape, that are circular in cross section.
  • a toothing is shown, which is formed of checkerboard-like teeth with a square cross-section.
  • an irregular labyrinth toothing is shown.
  • an irregular labyrinth toothing is shown, in which the individual teeth have a different shape from the basic geometric shapes in cross-section. It is understood that sections 16-19 are not present in a single dispersing rotor according to the invention, but schematically show four possible configurations of the labyrinth toothing of a rotor.

Description

Die Erfindung betrifft einen Dispergierrotor zum Homogenisieren fließfähiger Medien, der eine in Axialrichtung weisende Rotorverzahnung aufweist.The invention relates to a dispersing rotor for homogenizing flowable media, which has an axially pointing rotor toothing.

Homogenisatoren werden unter anderem in der pharmazeutischen, kosmetischen, chemischen und Nahrungsmittelindustrie zur Herstellung von Cremes, Salben, Pasten, Mayonnaisen und ähnlichen Produkten verwendet. Üblicherweise ist am Boden eines Mischbehälters ein Homogenisator angeordnet, der in der Regel als Rotor-Stator-Dispergiermaschine ausgebildet ist. Ein solcher Homogenisator ist beispielsweise in EP 0 988 887 A1 offenbart. Weitere gattungsgemäße Geräte sind in WO02/060569 und DE-A-19537303 beschrieben.Homogenizers are used, inter alia, in the pharmaceutical, cosmetic, chemical and food industries for the production of creams, ointments, pastes, mayonnaises and similar products. Usually, a homogenizer is arranged at the bottom of a mixing container, which is usually designed as a rotor-stator dispersing machine. Such a homogenizer is for example in EP 0 988 887 A1 disclosed. Other generic devices are in WO02 / 060569 and DE-A-19537303 described.

Der Erfindung liegt die Aufgabe zugrunde, eine Möglichkeit zum Homogenisieren fließfähiger Medien zu schaffen, die einfach, effizient und vielseitig anwendbar ist.The invention has for its object to provide a way to homogenize flowable media that is simple, efficient and versatile.

Ein erfindungsgemäßer Dispergierrotor weist eine Rotorverzahnung auf, die ein Labyrinthverzahnung für in Radialrichtung aus Richtung der Rotorachse nach außen tretendes Medium bildet.A dispersing rotor according to the invention has a rotor toothing, which forms a labyrinth toothing for medium emerging in the radial direction from the direction of the rotor axis to the outside.

Zunächst seien einige im Rahmen der Erfindung verwendete Begriffe erläutert. Der erfindungsgemäße Dispergierrotor dient dem Dispergieren (Homogenisieren, Emulgieren oder Suspensieren) fließfähiger Medien. Dazu gehört auch das Herstellen von Ein- oder Mehrphasenmischungen wie Gele, Emulsionen oder Suspensionen. Der Dispergierrotor weist eine in Axialrichtung weisende Rotorverzahnung auf. Der Begriff Verzahnung bezeichnet Öffnungen in einer in Umfangsrichtung verlaufenden Wand des Rotors, durch die Medium bzw. Mischgut im Betrieb in Radialrichtung nach außen durchtritt. Eine solche Verzahnung kann einzelne Öffnungen in einer ansonsten geschlossenen, in Umfangsrichtung verlaufenden Wand aufweisen. In der Regel wird jedoch die Verzahnung gebildet durch eine auf einem Umfangsabschnitt des Rotors angeordnete Vielzahl von sich axial erstreckenden Zähnen, die Prallflächen für das zu mischende Medium aufweisen. Die Begriffe axial bzw. radial sind im Rahmen der vorliegenden Erfindung auf die Drehachse des Rotors bezogen. Die Rotorverzahnung bildet erfindungsgemäß eine Labyrinthverzahnung für in Radialrichtung aus Richtung der Rotorachse nach außen tretendes Medium. Der Begriff Labyrinthverzahnung bedeutet, dass im Bereich der Achse des Rotors zugeführtes Mischgut durch die Verzahnung nicht auf einer in Radialrichtung weisenden Geraden austreten kann, sondern dass es bedingt durch die Anordnung der Zähne in jedem Fall eine Richtungsänderung vollziehen muss, also einen Labyrinthpfad durchströmen muss.First, some terms used in the invention are explained. The dispersing rotor according to the invention is used for dispersing (homogenizing, emulsifying or suspending) flowable media. This includes that too Preparation of single or multi-phase mixtures such as gels, emulsions or suspensions. The dispersing rotor has an axially pointing rotor toothing. The term gearing refers to openings in a circumferential wall of the rotor through which medium or mixture passes during operation in the radial direction to the outside. Such a toothing may have individual openings in an otherwise closed, circumferentially extending wall. In general, however, the toothing is formed by a arranged on a peripheral portion of the rotor plurality of axially extending teeth having baffles for the medium to be mixed. The terms axial and radial are related in the context of the present invention to the axis of rotation of the rotor. According to the invention, the rotor toothing forms a labyrinth toothing for medium passing outward in the radial direction from the direction of the rotor axis. The term labyrinth toothing means that mixed material fed in the region of the axis of the rotor can not escape through the toothing on a straight line pointing in the radial direction, but that due to the arrangement of the teeth it always has to change direction, ie has to flow through a labyrinth path.

Die Erfindung hat erkannt, dass überraschenderweise eine gute Misch- und Homogenisierwirkung ausschließlich durch einen solchen Rotor erzielt werden kann, ohne dass dieser mit einer relativ zum Rotor rotierenden (in der Regel feststehenden) Statorverzahnung zusammenwirken muss. Die erfindungsgemäße Labyrinthverzahnung erlaubt ein gutes Mischen und Homogenisieren ausschließlich durch Einsatz eines solchen Dispergierrotors.The invention has recognized that, surprisingly, a good mixing and homogenizing effect can be achieved exclusively by means of such a rotor, without this having to cooperate with a rotor toothing (which is generally fixed) relative to the rotor. The labyrinth toothing according to the invention allows good mixing and homogenization exclusively by using such a dispersing rotor.

Erfindungsgemäß ist das Homogenisieren des Mediums wesentlich schonender als beim Einsatz einer Rotor-Stator-Dispergiermaschine des Standes der Technik, da ein geringerer Energieeintrag und damit auch eine geringere Wärmeentwicklung erfolgt. Dementsprechend niedriger ist auch die für das Homogenisieren aufzuwendende mechanische Energie. Der verminderte Wärmeeintrag erlaubt eine schonendere Homogenisierung empfindlicher Produkte wie Gels oder Cremes.According to the invention, the homogenization of the medium is much gentler than when using a rotor-stator dispersing machine of the prior art, since a lower energy input and thus also a lower heat development takes place. Accordingly, the mechanical energy to be expended for homogenization is correspondingly lower. The reduced heat input allows a gentler homogenization of sensitive products such as gels or creams.

Die Erfindung hat somit erkannt, dass die im Stand der Technik für erforderlich gehaltene starke Scherung des Mediums an wechselnden Rotor- und Statorzähnen nicht erforderlich ist, stattdessen erlauben die ständigen Geschwindigkeitsänderungen in dem Labyrinthpfad eine Dehnung und Zerkleinerung von Flüssigkeitströpfchen (beispielsweise von Emulsionen) und somit eine Homogenisierung. Beim Durchtritt durch eine Zahnreihe erhält das Medium durch den sich drehenden Rotor einen Impuls, der abhängig von Geschwindigkeit und Strömungsrichtung des Mediums sowie Drehgeschwindigkeit des Rotors zu einer entsprechenden Änderung von Strömungsrichtung und -Geschwindigkeit des Mediums führt.The invention has thus recognized that the large shearing of the medium on alternating rotor and stator teeth considered necessary in the prior art is not required, instead the constant rate changes in the labyrinth path permit elongation and comminution of liquid droplets (for example, emulsions) and thus a homogenization. When passing through a row of teeth, the medium receives a pulse through the rotating rotor which, depending on the speed and flow direction of the medium and the rotational speed of the rotor, leads to a corresponding change in the direction of flow and velocity of the medium.

Vorzugsweise weist der erfindungsgemäße Dispergierrotor sogenannte Zahnreihen auf. Es handelt sich bei einer Zahnreihe um eine auf einem Umfangskreis angeordnete Anordnung von Zähnen, die somit jeweils den gleichen radialen Abstand von der Rotorachse aufweisen.The dispersing rotor according to the invention preferably has so-called rows of teeth. It is a row of teeth to a arranged on a circumferential circle arrangement of teeth, which thus each have the same radial distance from the rotor axis.

Bevorzugt ist der Dispergierrotor an einem oder beiden axialen Enden geschlossen ausgebildet. Dies bedeutet, dass in dem geschlossen ausgebildeten Bereich kein oder allenfalls ein geringfügiger Austritt von Medium in Axialrichtung möglich ist. Bevorzugt ist nicht die gesamte Kreisfläche des Rotors an beiden axialen Enden geschlossen ausgebildet, sondern mindestens an einem axialen Ende ist eine zentrische Öffnung, durch die von einer Axialseite her Medium eintreten kann. Bevorzugt ist zumindest an einem axialen Ende (Stirnseite) nur derjenige Kreisring geschlossen ausgebildet, der von der Rotorverzahnung eingenommen wird. Es wird so sichergestellt, dass durchtretendes Medium auf den vorgesehenen Labyrinthpfaden radial von innen nach außen den Dispergierrotor durchtritt.Preferably, the dispersing rotor is formed closed at one or both axial ends. This means that in the closed area formed no or at most a slight leakage of medium in the axial direction is possible. Preferably, not the entire circular area of the Rotor formed closed at both axial ends, but at least at one axial end is a central opening through which medium can enter from one axial side. Preferably, at least at one axial end (end face), only that circular ring is formed closed, which is occupied by the rotor toothing. It is thus ensured that the medium passing through penetrates the dispersing rotor radially from the inside to the outside on the intended labyrinth paths.

Die axiale Höhe der Rotorverzahnung kann 10 bis 30 mm, weiter vorzugsweise 12 bis 25 mm betragen. Der Begriff bezeichnet die freie Höhe in der Ringebene der entsprechenden Rotorverzahnung, durch die Durchtritt von Medium möglich ist. Der Durchmesser eines erfindungsgemäßen Dispergierrotors kann an die Einbaugegebenheiten angepasst werden. Bei einem Einbau beispielsweise in Rohrleitungen können kleine Durchmesser von beispielsweise 5 bis 10 cm zur Anwendung kommen. Beim Einbau in größeren Mischbehältern kann der Durchmesser beispielsweise zwischen 10 und 30 cm liegen. Die genannten Werte lassen sich beliebig zu erfindungsgemäßen Ober- und Untergrenzen kombinieren.The axial height of the rotor toothing may be 10 to 30 mm, more preferably 12 to 25 mm. The term refers to the free height in the ring plane of the corresponding rotor toothing, through the passage of medium is possible. The diameter of a dispersing rotor according to the invention can be adapted to the installation conditions. For example, when installed in pipelines, small diameters of, for example, 5 to 10 cm may be used. When installed in larger mixing vessels, the diameter can be, for example, between 10 and 30 cm. The stated values can be combined as desired to upper and lower limits according to the invention.

Bevorzugt weisen die Zähne der Rotorverzahnung in Radialrichtung zwischen sich Spalte von 0,3 bis 3 mm, vorzugsweise 0,5 bis 1,5 mm auf. Bevorzugt handelt es sich dabei um den lichten radialen Abstand zwischen jeweils zwei konzentrisch angeordneten Zahnreihen.Preferably, the teeth of the rotor toothing in the radial direction between them gaps of 0.3 to 3 mm, preferably 0.5 to 1.5 mm. Preferably, this is the clear radial distance between each two concentrically arranged rows of teeth.

In Umfangsrichtung weisen die Zähne (bevorzugt die Zähne jeweils einer der konzentrischen Zahnreihen) bevorzugt Spalte von 0,5 bis 4 mm, weiter vorzugsweise 1 bis 3 mm, weiter vorzugsweise 1,5 bis 2,5 mm auf.In the circumferential direction, the teeth (preferably the teeth of each of the concentric rows of teeth) preferably have gaps of 0.5 to 4 mm, more preferably 1 to 3 mm, more preferably 1.5 to 2.5 mm.

Die Überdeckung einer Zahnreihe über den Umfang dieser Zahnreihe liegt bevorzugt zwischen 40 und 80 %, weiter vorzugsweise 50 und 70 %. Diese Grenzen sind beliebig zu erfindungsgemäßen Bereichen kombinierbar. Der Begriff Überdeckung bezeichnet dabei denjenigen Anteil des Kreisumfangs einer Zahnreihe, auf dem der Durchtritt von Medium in Radialrichtung durch diese Zahnreihe blockiert ist. Eine Überdeckung von 60 % bedeutet beispielsweise, dass 60 % des Umfangs der entsprechenden Zahnreihe durch die Zähne blockiert sind während auf den verbleibenden 40 % des Umfangs ein Durchtritt von Medium möglich ist.The coverage of a row of teeth over the circumference of this row of teeth is preferably between 40 and 80%, more preferably 50 and 70%. These limits can be combined as desired to areas according to the invention. The term overlap refers to that portion of the circumference of a row of teeth on which the passage of medium in the radial direction is blocked by this row of teeth. For example, a coverage of 60% means that 60% of the circumference of the corresponding row of teeth is blocked by the teeth while the remaining 40% of the circumference allows medium to pass through.

Bei einer besonders bevorzugten Ausführungsform der Erfindung weisen zwei in Radialrichtung benachbart angeordnete Zahnreihen gemeinsam eine vollständige Überdeckung auf. Dies bedeutet, dass Medium diese beiden radial aufeinander folgenden Zahnreihen nicht durchtreten kann, ohne von der Radialrichtung abzuweichen. Eine Gerade in Radialrichtung, die in einer der beiden Zahnreihen durch eine Lücke zwischen zwei Zähnen durchtritt, trifft somit in der anderen dieser beiden Zahnreihen auf einen Zahn. Diese vollständige Überdeckung zweier in Radialrichtung benachbart angeordneter Zahnreihen bewirkt durch die damit verstärkte Richtungsänderung des Mediums eine verbesserte Homogenisierung.In a particularly preferred embodiment of the invention, two rows of teeth arranged adjacent in the radial direction together have complete coverage. This means that medium can not pass through these two radially successive rows of teeth, without departing from the radial direction. A straight line in the radial direction, which passes in one of the two rows of teeth through a gap between two teeth, thus meets in the other of these two rows of teeth on a tooth. This complete overlap of two adjacently arranged in the radial direction rows of teeth caused by the increased directional change of the medium improved homogenization.

Erfindungsgemäß weist bevorzugt wenigstens ein Teil der Zähne in Umfangsrichtung weisenden Förderflächen auf, die dazu ausgebildet sind, auftreffendem Medium eine Impulskomponente radial nach außen zu verleihen. "In Umfangsrichtung weisend" bedeutet dabei nicht, dass diese Flächen exakt in Umfangsrichtung ausgerichtet sind, eine Senkrechte auf diesen Flächen also genau in Umfangsrichtung weist. Es handelt sich in der Regel vielmehr um Schrägflächen, eine Senkrechte auf diesen Schrägflächen weist bevorzugt eine Richtungskomponente radial nach außen auf. Trifft bei drehendem Dispergierrotor diese Förderfläche auf durchtretendes Medium, wird ein Impuls auf das Medium ausgeübt, der eine Richtungskomponente radial nach außen aufweist. Dementsprechend wird das Medium beschleunigt mit einer Beschleunigungs- bzw. Geschwindigkeitskomponente radial nach außen.According to the invention, preferably at least a part of the teeth has conveying surfaces pointing in the circumferential direction, which are designed to impart a pulse component radially outwards to the impacting medium. "Pointing in the circumferential direction" does not mean that these surfaces are aligned exactly in the circumferential direction, that is a perpendicular to these surfaces exactly in the circumferential direction. It deals Rather, as a rule, be inclined surfaces, a perpendicular to these inclined surfaces preferably has a direction component radially outward. If, when the dispersing rotor rotates, this conveying surface encounters passing medium, an impulse is exerted on the medium which has a directional component radially outward. Accordingly, the medium is accelerated radially outward with an acceleration or velocity component.

Gegenstand der Erfindung ist ferner eine Homogenisiervorrichtung zum Homogenisieren fließfähiger Medien, die einen erfindungsgemäßen Dispergierrotor aufweist. Der Verzicht auf eine Statorverzahnung bietet eine Reihe wesentlicher Vorteile. Es ist eine relativ freie Positionierung des Dispergierrotors innerhalb der Homogenisiervorrichtung möglich, da keinerlei bauliche Vorsorge dafür getroffen werden muss, eine in die Rotorverzahnung eingreifende Statorverzahnung vorzuhalten. Erfindungsgemäß kann der Dispergierrotor beispielsweise in einem unteren Bereich eines Homogenisierbehälters, vorzugsweise in dessen Bodenbereich, angeordnet sein. Es ist ebenfalls möglich, mehrere Dispergierrotoren innerhalb eines Behälters anzuordnen, beispielsweise mehrere solcher Rotoren auf einer durch den Deckel oder Boden eines solchen Behälters geführten Achse anzuordnen. Es ist im Rahmen der Erfindung ebenfalls möglich, den Dispergierrotor in einer Rohrleitung anzuordnen, durch die zu mischendes Medium geführt wird. Der erfindungsgemäße Dispergierrotor kann somit eingesetzt werden für das sogenannte In-Line-Mischen in einer Rohrleitung.The invention furthermore relates to a homogenizing device for homogenizing flowable media which has a dispersing rotor according to the invention. The omission of a stator toothing offers a number of significant advantages. It is a relatively free positioning of the dispersing within the homogenizer possible because no structural precautions must be taken to vorzuhalten a engaging in the rotor teeth stator toothing. According to the invention, the dispersing rotor can be arranged, for example, in a lower region of a homogenizing container, preferably in its bottom region. It is also possible to arrange a plurality of dispersing rotors within a container, for example to arrange a plurality of such rotors on an axis guided through the lid or bottom of such a container. It is also possible within the scope of the invention to arrange the dispersing rotor in a pipeline through which the medium to be mixed is passed. The dispersing rotor according to the invention can thus be used for so-called in-line mixing in a pipeline.

Durch den Verzicht auf eine Statorverzahnung ist es möglich, den erfindungsgemäßen Dispergierrotor mit vergleichsweise größeren Toleranzen in ein Homogenisiergefäß einzubauen, als im Stand der Technik, wo ein passgenaues Zusammenwirken mit einer Statorverzahnung erforderlich ist. Dies erlaubt insbesondere die Verwendung von Antrieben, bei denen der Rotor üblicherweise mit größeren Toleranzen gelagert ist, beispielsweise berührungslosen Antrieben wie Magnetantrieben. Berührungslose Antriebe haben den Vorteil, dass keine Durchführungen von Antriebsachsen durch die Wand des Homogenisierbehälters erforderlich sind und somit Behälter und Dispergierrotor so ausgestaltet werden können, dass die Möglichkeiten der Reinigung und Keimfreihaltung optimiert werden.By dispensing with a stator toothing, it is possible to install the dispersing rotor according to the invention with comparatively larger tolerances in a homogenizing vessel, as in the prior art, where a precise interaction with a stator toothing is required. This allows in particular the use of drives in which the rotor is usually mounted with larger tolerances, such as non-contact drives such as magnetic drives. Non-contact drives have the advantage that no penetrations of drive axles through the wall of the homogenizing container are required and thus containers and dispersing rotor can be designed so that the possibilities of cleaning and germ free are optimized.

Ausführungsbeispiele der Erfindung werden nachfolgend anhand der Zeichnungen beschrieben. Es zeigen:

Fig. 1:
schematisch einen teilweisen Axialschnitt durch einen erfindungsgemäßen Dispergierrotor;
Fig. 2:
schematisch einen Schnitt in der Radialebene durch eine erfindungsgemäße Rotorverzahnung;
Fig. 3-7:
schematisch unterschiedliche Einbausituationen eines erfindungsgemäßen Dispergierrotors in einer Homogenisiervorrichtung;
Fig. 8:
schematisch weitere mögliche Ausgestaltungen bei Labyrinthverzahnung.
Embodiments of the invention will be described below with reference to the drawings. Show it:
Fig. 1:
schematically a partial axial section through a dispersing rotor according to the invention;
Fig. 2:
schematically a section in the radial plane through a rotor toothing according to the invention;
Fig. 3-7:
schematically different installation situations of a dispersing rotor according to the invention in a homogenizer;
Fig. 8:
schematically further possible embodiments of labyrinth teeth.

Der erfindungsgemäße Dispergierrotor weist eine Aufnahme 1 für eine Antriebswelle (in Fig. 1 nicht dargestellt) auf. Damit drehfest verbunden ist ein Rotor 2, an dem Pumpflügel 4 angeordnet sind, die zur Förderung von durch den Einlass 3 eintretenden Mediums radial nach außen dienen. Die Anordnung der Pumpflügel 4 entspricht beispielsweise der Anordnung, die dargestellt ist in EP 0 988 887 A1 , dort Pumpflügel 18 in Fig. 2.The dispersing rotor according to the invention has a receptacle 1 for a drive shaft (in FIG Fig. 1 not shown). Rotationally connected thereto is a rotor 2, on which pump vanes 4 are arranged, which serve to convey medium entering through the inlet 3 radially outward. The order the pump blade 4 corresponds for example to the arrangement shown in FIG EP 0 988 887 A1 , there pumping 18 in Fig. 2 ,

In einem radial außen angeordneten Kreisring weist der erfindungsgemäße Dispergierrotor vier radial gestaffelte Zahnreihen 5 auf, durch die in den Einlass 3 eintretendes Medium radial nach außen abgefördert wird. Diese Zahnreihen bilden für radial nach außen tretendes Medium einen Labyrinthpfad, das heißt, Medium kann durch diese Zahnreihen nicht ohne Richtungsänderungen hindurch treten. Im Bereich der Verzahnung 5 ist der Dispergierrotor zu den axialen Stirnseiten hin abgeschlossen, sodass Mischgut aus der Verzahnung nicht nach axial oben oder unten entweichen kann.In a radially outer ring arranged the dispersing rotor according to the invention has four radially staggered rows of teeth 5, is conveyed through the medium entering the inlet 3 radially outward. These rows of teeth form a labyrinth path for radially outward medium, that is, medium can not pass without directional changes through these rows of teeth. In the area of the toothing 5, the dispersing rotor is closed towards the axial end faces, so that mixed material from the toothing can not escape axially upwards or downwards.

Im Ausführungsbeispiel der Fig. 1 sind sechs radial gestaffelte Zahnreihen angeordnet. Fig. 2 zeigt schematisch einen Radialschnitt durch diese Zahnreihen. Man erkennt radial gestaffelte Zahnreihen, die jeweils Zähne 6 aufweisen. Es handelt sich bei Fig. 2 um eine vergrößerte Darstellung. Die Länge der Spalte in Umfangsrichtung (Bezugsziffer 7) beträgt etwa 2 mm, die Spaltbreite in Radialrichtung (Bezugsziffer 8) etwa 0,5 mm. Man erkennt, dass die Zähne 6 einen Labyrinthpfad bilden, durch den Medium nach außen durchtreten muss. Wenn der Rotor in der Umfangsrichtung 15 gedreht wird, bilden die in Umfangsrichtung verlaufenden Flächen 16 der Zähne Förderflächen, die beim Auftreffen auf Medium dieser eine radial nach außen weisende Impulskomponente verleihen.In the embodiment of Fig. 1 Six radially staggered rows of teeth are arranged. Fig. 2 schematically shows a radial section through these rows of teeth. It can be seen radially staggered rows of teeth, each having teeth 6. It concerns with Fig. 2 an enlarged view. The length of the column in the circumferential direction (reference numeral 7) is about 2 mm, the gap width in the radial direction (reference numeral 8) about 0.5 mm. It can be seen that the teeth 6 form a labyrinth path through which medium must pass outwards. When the rotor is rotated in the circumferential direction 15, the circumferentially extending surfaces 16 of the teeth form conveying surfaces which when impinged on medium impart a radially outward pulse component thereto.

Der Durchmesser des in Fig. 1 dargestellten Dispergierrotors kann bei diesem Ausführungsbeispiel etwa 10 cm betragen. Typische Drehzahlen im Betrieb können beispielsweise 6.500 bis 14.000 min-1 betragen.The diameter of the in Fig. 1 shown dispersing rotor may be about 10 cm in this embodiment. Typical rotational speeds during operation may, for example be 6500 to 14,000 min -1.

Fig. 3 zeigt schematisch eine Einbausituation, bei der ein erfindungsgemäßer Dispergierrotor in einem Mischbehälter über dem Behälterboden 9 angeordnet ist. Eine Antriebswelle 10 tritt durch den Behälterboden hindurch. Fig. 3 schematically shows a mounting situation in which a dispersing rotor according to the invention is arranged in a mixing container above the container bottom 9. A drive shaft 10 passes through the container bottom.

Fig. 4 zeigt eine andere Variante einer erfindungsgemäßen Homogenisiervorrichtung, bei der eine längere Antriebswelle 10 durch den Behälterboden 9 hindurch tritt. An dieser Antriebswelle 10 sind zwei oder bei Bedarf auch mehr erfindungsgemäße Dispergierrotoren angeordnet. Fig. 4 shows another variant of a homogenizer according to the invention, in which a longer drive shaft 10 passes through the container bottom 9 passes. At this drive shaft 10 two or more if required, more dispersing rotors according to the invention are arranged.

Bei der Ausführungsform der Fig. 5 ist ein erfindungsgemäßer Dispergierrotor im Bodengehäuse eines Mischbehälters eingebaut. Eine Abdeckung 17 deckt den Rotor an seinem Außenumfang ab und bildet zusammen mit dem Bodengehäuse einen Ringspalt 11, durch den am Außenumfang des Rotors austretendes Medium zurück in den Behälter geführt werden kann. Alternativ ist es möglich, dieses Medium durch eine in Fig. 5 nicht dargestellte Zirkulationsleitung aus dem Behälter abzuführen und beispielsweise in einem anderen (vorzugsweise oberen) Bereich des Behälters wieder zuzuführen.In the embodiment of the Fig. 5 If a dispersing rotor according to the invention is installed in the bottom housing of a mixing container. A cover 17 covers the rotor at its outer periphery and forms, together with the bottom housing, an annular gap 11 through which medium emerging on the outer circumference of the rotor can be guided back into the container. Alternatively, it is possible to use this medium through a in Fig. 5 remove circulation line, not shown, from the container and supply, for example, in another (preferably upper) region of the container again.

Fig. 6 zeigt eine Ausführungsform, bei der der Rotor über eine Magnetkupplung angetrieben wird. Außerhalb der Behälterwand 9 ist eine Antriebswelle 13 angeordnet, die mit Magneten versehen ist und innerhalb des Behälters angeordnete Magnete 12 mitnimmt, die drehfest mit dem Rotor verbunden sind. Fig. 6 shows an embodiment in which the rotor is driven via a magnetic coupling. Outside the container wall 9, a drive shaft 13 is arranged, which is provided with magnets and within the container arranged magnets 12 entrains, which are rotatably connected to the rotor.

Fig. 7 zeigt eine Ausführungsform, bei der eine Antriebswelle 15 durch den Deckel 14 eines Mischbehälters geführt ist. Fig. 7 shows an embodiment in which a drive shaft 15 is guided by the lid 14 of a mixing container.

Fig. 8 zeigt schematisch weitere mögliche Ausgestaltungen einer erfindungsgemäßen Labyrinthverzahnung. Bei 16 ist eine Verzahnung angedeutet, bei der die einzelnen Zähne eine Stabform aufweisen, also im Querschnitt kreisförmig sind. Bei 17 ist eine Verzahnung gezeigt, die aus schachbrettartig angeordneten Zähnen mit quadratischem Querschnitt gebildet ist. Im Abschnitt 18 ist eine unregelmäßige Labyrinthverzahnung dargestellt. Hier ist vorzugsweise darauf zu achten, dass sich über den gesamten Umfang des Rotors eine gleichmäßige Masseverteilung ergibt und es nicht zu einer Unwucht kommt. Bei 19 ist schematisch eine unregelmäßige Labyrinthverzahnung dargestellt, bei der die einzelnen Zähne im Querschnitt eine von den geometrischen Grundformen abweichende Gestalt aufweisen. Es versteht sich, dass die Abschnitte 16-19 nicht bei einem einzigen erfindungsgemäßen Dispergierrotor vorhanden sind sondern schematisch vier mögliche Gestaltungen der Labyrinthverzahnung eines Rotors zeigen. Fig. 8 schematically shows further possible embodiments of a labyrinth toothing according to the invention. At 16, a toothing is indicated, in which the individual teeth have a rod shape, that are circular in cross section. At 17, a toothing is shown, which is formed of checkerboard-like teeth with a square cross-section. In section 18 an irregular labyrinth toothing is shown. Here it is preferable to ensure that over the entire circumference of the rotor results in a uniform mass distribution and it does not come to an imbalance. At 19 schematically an irregular labyrinth toothing is shown, in which the individual teeth have a different shape from the basic geometric shapes in cross-section. It is understood that sections 16-19 are not present in a single dispersing rotor according to the invention, but schematically show four possible configurations of the labyrinth toothing of a rotor.

Claims (13)

  1. Dispersing rotor for homogenising free-flowing media, said dispersing rotor having an axially oriented rotor toothing formation, characterised in that the rotor toothing formation forms a labyrinth toothing formation for medium passing radially outward from the direction of the rotor axis.
  2. Dispersing rotor according to claim 1, characterised in that it has at least 2, preferably 2 to 16, more preferably 2 to 8, more preferably 4 to 8 radially spaced-apart rows (5) of teeth.
  3. Dispersing rotor according to either claim 1 or claim 2, characterised in that it is closed at one or both axial ends.
  4. Dispersing rotor according to any of claims 1 to 3, characterised in that the axial height of the rotor toothing formation is 10 to 30 mm, preferably 12 to 25 mm.
  5. Dispersing rotor according to any of claims 1 to 4, characterised in that the teeth (6) of the rotor toothing formation have radially directed gaps of 0.3 to 3 mm, preferably 0.5 to 1.5 mm.
  6. Dispersing rotor according to any of claims 1 to 5, characterised in that the teeth (6) or rows of teeth of the rotor toothing formation have circumferentially directed gaps of 0.5 to 4 mm, preferably 1 to 3 mm, more preferably 1.5 to 2.5 mm.
  7. Dispersing rotor according to any of claims 1 to 6, characterised in that the coverage of a row of teeth over the circumference of this row of teeth is 40 to 80%, preferably 50 to 70%.
  8. Dispersing rotor according to any of claims 1 to 7, characterised in that two radially adjacent rows of teeth together provide full coverage.
  9. Dispersing rotor according to any of claims 1 to 8, characterised in that at least some of the teeth have circumferentially oriented delivery surfaces (16) that are designed to subject medium that comes into contact therewith to an impulse component in the radially outward direction.
  10. Homogenisation apparatus for homogenising free-flowing media, characterised in that it has a dispersing rotor according to any of claims 1 to 9, the homogenisation apparatus not having a stator toothing formation engaging in the rotor toothing formation.
  11. Homogenisation apparatus according to claim 10, characterised in that the dispersing rotor is arranged in a lower region, preferably a base region, of a homogenisation tank.
  12. Homogenisation apparatus according to claim 10, characterised in that the dispersing rotor is arranged in a medium-channelling conduit.
  13. Homogenisation apparatus according to any of claims 10 to 12, characterised in that the dispersing rotor has a contactless drive, preferably a magnetic drive.
EP11168428.8A 2011-06-01 2011-06-01 Dispersal rotor for homogenising flowable media Active EP2529829B1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
DK11168428.8T DK2529829T3 (en) 2011-06-01 2011-06-01 Dispersion rotor for homogenizing liquid media
PL11168428T PL2529829T3 (en) 2011-06-01 2011-06-01 Dispersal rotor for homogenising flowable media
EP11168428.8A EP2529829B1 (en) 2011-06-01 2011-06-01 Dispersal rotor for homogenising flowable media
JP2012117911A JP2012250228A (en) 2011-06-01 2012-05-23 Dispersing rotor for homogenizing flowable media
CA2778753A CA2778753A1 (en) 2011-06-01 2012-05-30 Dispersing rotor for homogenizing free-flowing media
US13/486,313 US9452396B2 (en) 2011-06-01 2012-06-01 Rotor for homogenizing flowable media

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP11168428.8A EP2529829B1 (en) 2011-06-01 2011-06-01 Dispersal rotor for homogenising flowable media

Publications (2)

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EP2529829A1 EP2529829A1 (en) 2012-12-05
EP2529829B1 true EP2529829B1 (en) 2013-10-16

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US (1) US9452396B2 (en)
EP (1) EP2529829B1 (en)
JP (1) JP2012250228A (en)
CA (1) CA2778753A1 (en)
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PL (1) PL2529829T3 (en)

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US2619330A (en) * 1949-09-09 1952-11-25 Willems Peter Mixing and dispersing device
DE3243671A1 (en) * 1982-11-25 1984-05-30 Karg Ytron Gmbh DEVICE FOR CONTINUOUSLY MIXING POWDERED SUBSTANCES WITH LIQUIDS
JPS60176237U (en) * 1984-09-28 1985-11-21 不二製油株式会社 Continuous whipper
SU1380975A2 (en) * 1986-04-10 1988-03-15 Всесоюзный Научно-Исследовательский Институт Пленочных Материалов И Искусственной Кожи Mixer for polymeric materials
DE3729708A1 (en) * 1986-09-05 1988-03-17 Fuji Photo Film Co Ltd MAGNETIC PUMP
DE19537303B4 (en) * 1995-08-29 2005-04-21 Vakumix Rühr- und Homogenisiertechnik AG Device for homogenizing flowable substances
JP3623044B2 (en) * 1996-04-17 2005-02-23 株式会社イマイ Stirrer
JP3255072B2 (en) * 1997-02-17 2002-02-12 日本ピー・エム・シー株式会社 Method for producing aqueous emulsion of rosin-based material, aqueous emulsion composition and sizing agent
DE59807124D1 (en) 1998-08-25 2003-03-13 Vakumix Ruehr Und Homogenisier Homogenizer with protective device on the rotor
WO2002060569A2 (en) * 2000-10-30 2002-08-08 Silverson Machines Ltd. Mixing head with axial flow
KR100527665B1 (en) * 2003-09-27 2005-11-09 맹재석 Impeller for gas and liquid mixing pump and gas and liquid mixing pump containing the same
JP4508968B2 (en) * 2005-07-27 2010-07-21 有限会社Os技研 Stirring device and monitoring system using the same
CN2882772Y (en) * 2005-12-19 2007-03-28 庄翠娣 High sheared stirring foam maker
JP5263877B2 (en) * 2008-10-22 2013-08-14 アイセル株式会社 Mixing apparatus and mixing system
JP5500575B2 (en) * 2008-06-16 2014-05-21 アイセル株式会社 Mixing element, mixing device, mixing method, stirring blade, stirring device, and stirring method
EP2286905B1 (en) * 2008-06-16 2017-09-27 Isel Co.,ltd. Mixing element, mixing device, agitation blade, mixing machine, mixing system and reaction device
KR20100137109A (en) * 2009-06-22 2010-12-30 나노인텍 주식회사 Rotor and apparatus for milling and dispersing with the same
CN102596379B (en) * 2009-11-02 2015-04-01 曼康公司 Reactor for producing pharmaceutical particles in a precipitation process

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DK2529829T3 (en) 2014-01-20
CA2778753A1 (en) 2012-12-01
US20120307585A1 (en) 2012-12-06
PL2529829T3 (en) 2014-03-31
JP2012250228A (en) 2012-12-20
EP2529829A1 (en) 2012-12-05
US9452396B2 (en) 2016-09-27

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