EP0000004B1 - Continuous filtration centrifuge for separation, washing or draining, and application to an automatic coffee machine - Google Patents

Continuous filtration centrifuge for separation, washing or draining, and application to an automatic coffee machine Download PDF

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Publication number
EP0000004B1
EP0000004B1 EP78100037A EP78100037A EP0000004B1 EP 0000004 B1 EP0000004 B1 EP 0000004B1 EP 78100037 A EP78100037 A EP 78100037A EP 78100037 A EP78100037 A EP 78100037A EP 0000004 B1 EP0000004 B1 EP 0000004B1
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EP
European Patent Office
Prior art keywords
fact
end plate
wall
rotary
filtering device
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
Application number
EP78100037A
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German (de)
French (fr)
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EP0000004A1 (en
Inventor
Serge Cailliot
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CAILLIOT Serge
Cor Bertrand
GASTINNE, ARNAUD
Generale Pour Le Financement De L'innovat Ste
Normande de Services Ste
Bpifrance Financement SA
Original Assignee
Cor Bertrand
GENERALE POUR LE FINANCEMENT DE L'INNOVATION SOGINNOVE Ste
Agence National de Valorisation de la Recherche ANVAR
Normande de Services Ste
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Publication of EP0000004A1 publication Critical patent/EP0000004A1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B3/00Centrifuges with rotary bowls in which solid particles or bodies become separated by centrifugal force and simultaneous sifting or filtering
    • B04B3/08Centrifuges with rotary bowls in which solid particles or bodies become separated by centrifugal force and simultaneous sifting or filtering discharging solid particles by bowl walls in the form of endless bands
    • AHUMAN NECESSITIES
    • A47FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47JKITCHEN EQUIPMENT; COFFEE MILLS; SPICE MILLS; APPARATUS FOR MAKING BEVERAGES
    • A47J31/00Apparatus for making beverages
    • A47J31/22Centrifuges for producing filtered coffee

Definitions

  • the invention relates to filtration in general, and more particularly to the preparation of coffee.
  • the filtration operation in general consists in passing a liquid through a porous wall which retains solid particles, these solid particles possibly being previously contained in suspension in the liquid, in the case of filtration for separation. , or on the contrary be placed in advance in the filter and then watered by the liquid when it is desired to carry out a washing or exhausting operation using an appropriate solvent of soluble active substances contained in the solid particles .
  • This is particularly the case for the preparation of coffee which consists of passing hot water through ground coffee.
  • the passage of the liquid takes place by simple gravity.
  • the filtration efficiency can be improved by passing the liquid under the effect of centrifugal force by using a porous cylindrical wall driven in rotation at high speed around its axis.
  • the filtration operation is necessarily intermittent, that is to say that filtration phases are followed by cleaning phases for the evacuation of the solid substances accumulated against the porous wall.
  • continuous filters are known in which an endless porous wall is used, either in the form of an endless band, or in the form of a rotary cylinder, and in this case there is a filtration zone or sector followed by another zone. or cleaning sector, this cleaning generally being obtained by scraping using a fixed squeegee then unclogging the porous wall by rinsing in the opposite direction.
  • the passage of the liquid is necessarily by gravity or by suction, but it is excluded to operate by centrifugal means, the displacement or rotation of the porous wall being necessarily slow since it is he who presides the sequence of filtering and washing operations.
  • German patent No. 691,923 to produce a filter which is both continuous and centrifugal, the cylindrical filtering wall of which is rotatable and constituted by a helical winding with contiguous turns of a long strap mounted in a rotary cage constituted by cylindrical rollers arranged according to external generators of this cylindrical wall, the strap being looped on itself in an endless assembly and driven so that the porous cylindrical wall advances slowly in the direction of the axis constantly renewing itself.
  • the drive of the strip is ensured by a central capstan which takes up the strip radially at the base of the cylinder and recycles it at the top, which has the disadvantage of malfunctioning given the difficulty in providing suitable tension.
  • the object of the invention is to produce a continuous centrifugal filter of the above type but which eliminates the aforementioned drawbacks by providing a safe and effective drive while freeing the central part of the cylindrical wall.
  • the invention consists, in an endless centrifugal filter of the preceding type, in ensuring the drive of the strap by the rotational drive on themselves of the rollers of the support cage by an appropriate mechanism, and in carrying out the endless looping by a return channel which extends from one end to the other of the helical winding passing through the outside of the winding and of the roller cage.
  • the strap is advantageously devoid of perforations and constituted by a solid part provided only with suitable notches on the surface.
  • the porous filtration wall is constituted by a long flexible strap 1 of small section arranged in a helical winding with contiguous turns to form a cylindrical sleeve 2, the two ends of the strap being connected to each other by a strap back 3 to form an endless set.
  • This flexible strap 1 can be made of metal or plastic, preferably of square or rectangular section, and it can advantageously include in its upper or lower face notches 4, preferably inclined so as to widen towards the exterior, starting from a very shallow depth on the side intended to constitute the interior, this depth corresponding to the desired filtration fineness, for example 0.1 mm.
  • the cylindrical sleeve 2 thus formed is mounted in a cage constituted by a number of cylindrical rollers 5, four in number in the figures, each arranged along a generatrix of the cylinder.
  • Each of these rollers journals by its base in a lower flange 6 and by a part close to its upper end in an upper flange 7 by means of a notch 8 opening towards the center in a bore 9 of a diameter just sufficient to allow the passage of the sleeve 2.
  • the upper flange 7 is rigidly fixed to the lower flange 6 by spacers 10, and the lower flange 6 is itself rigidly fixed by its hub 11 to an axis 12 journalled in fixed bearings 13 while being driven by a drive motor not shown.
  • the entire cage assembly including the two flanges and the four vertical rollers, therefore rotates as a block around the axis 12 at a suitable speed to obtain centrifugal filtration, for example 1500 revolutions / min.
  • the four rollers 5 are driven at a low speed of rotation on themselves, all in the same direction, thanks to an appropriate mechanism located below the flange 6.
  • This mechanism visible in particular in FIGS. 1 and 4. has a gear 14 integral with each of the lower ends of the rollers 5, below the flange 6, the four gears 14 meshing simultaneously on a single central gear 15 idling around the axis 12, this central gear being itself -Even driven in rotation by a pinion 16 secured to a gear 17 which rotates around an axis 18 carried by the flange 6 and meshes with a central pinion 19 idly mounted on the axis 12 and whose base 20 can be immobilized in rotation by means of a suitable device not shown.
  • the directions of rotation are those represented by the arrows in FIG. 4, remembering that this is a bottom view, and the ratios of the gears are such that the rollers rotate slowly on themselves at a very low speed while the whole of the cage rotates at high speed .
  • the sleeve 2 formed by all of the contiguous turns is applied by centrifugal force against the guide and drive rollers 5 and consequently begins to turn slowly on itself in the direction of the arrow 21 (see fig. 2) in a relative movement of rotation at low speed of the order of 12 revolutions / min in the example chosen.
  • the sleeve 2 actually turns in the same direction as the cage, that is to say in the direction of the needles of a watch in fig. 2, and at a speed barely lower, for example 1500 rpm for the cage and 1448 rpm for the sleeve.
  • the direction of winding of the contiguous turns of the sleeve 2 is chosen in such a way that, in the aforementioned relative movement of the sleeve relative to the cage, the strap takes place at the top, just after passing under one of the axial retaining cheeks 23 of one of the rollers 5, then performs the return turn 3 passing outside the following rollers 5, but preferably inside the spacers 10 to wind continuously 'lower end on the cylindrical outer surface of a bottom wall 24 visible in FIG. 1 and turning madly around the hub 11 in order to be able to take with respect thereto the slow rotational movement of the entire filter.
  • This movement is communicated to the bottom 24 by meshing or by friction on its periphery of a drive zone 25 situated at the base of the rollers 5 below the axial retaining cheeks 26.
  • the filter according to the invention can be operated by successive loads by simply providing for this a braking device controlled from the base 20 of the central pinion 19 relative to the frame 22.
  • the filtering device also has the advantage that it is possible to extend the axis 12 by an upper part 33, separable or not from the previous one and placed in the axis of the cylindrical sleeve 2, to drive at the upper part a screw grinder of the type known for grinding coffee.
  • the grinding screw 34 is cut directly in the upper end of the axis 33 and rotates in an outer part 35 with a conical interior located at the base of a hopper not shown feeding the coffee beans using 'An adjustable flow distributor 36 which can also be driven by the same axis.
  • the fineness of the grinding is adjusted, for example, by moving the base 35 in a helical movement with a vertical axis using a control rod 37 sliding in an inclined lumen 38 integral with the frame 22, the screw 33 being axially fixed.
  • the filter according to the invention When the filter according to the invention is used for washing or depleting a pulverulent solid substance with a liquid substance, it is advantageous to first have the solid substance near the bottom 24 in a uniform cylindrical layer, then to distribute the liquid above the place where the distribution of the solid takes place.
  • a coaxial rotary distributor 39 comprising a central passage for the solid product and an at least partially conical external surface 40 onto which the liquid is poured which is thus projected by centrifugal force, the distributor 39 being for this purpose driven in rotation, for example at the speed of the axis 12 or 33 by being secured to it by means of a through pin 41.
  • this distributor could be secured to the bottom 24 by pins parallel to the axis, the bottom speed being, as we saw above, very little different from that of the axis.
  • the conical outer surface 40 of the distributor 39 can be extended by a cylindrical part which preferably has asperities to distribute the spraying of the liquid over a certain height.
  • these asperities can be constituted by a rib 42 in the form of a helical spiral developing on the cylindrical outer surface 43 of the dispenser.
  • a circular rib 44 forming a deflector can be placed at the base of the dispenser to evacuate the droplets of liquid which could possibly fall outside the exterior surface of the dispenser.
  • the ground coffee can be fed into the axial passage of the rotary distributor 39 by any suitable means.
  • this distributor coaxially and outside this axis by extending it axially by a tubular part 45 of which the upper end journals at the base of the grinding cone 35. If the latter moves axially to allow adjustment as indicated above, an oblong hole 46 is provided in the base of the axis 33 for the passage of the pin 41 and allow this movement to occur.
  • the ground coffee which escapes directly between the screw 33 and the tubular part 45 may be pressed against the latter by centrifugal force and accumulate there.
  • This is avoided according to the invention by having a fixed spiral 47 of helical steel wire freely mounted in the interval between the axis 33 and the bore of the tube 45 and the rotary distributor. 39, being only immobilized axially and in rotation by fixing its upper end 48 in the base of the cone 35. In this way the ground coffee is routed regularly and without the possibility of blocking to the lower end of the distributor 39 where it is thus distributed by centrifugal force in the interval between the bottom 24 and the rib 44 to come to accumulate on an area of the same height on the inner surface of the sleeve 2.
  • the liquid substance which is obviously hot water in this case, can be continuously supplied and heated and distributed on the conical part 40 of the distributor 39. It is however preferable according to the invention to produce a water supply intermittently by supplying a continuous flow to a device well known in physics under the name of intermittent fountain and constituted by a self-priming siphon placed in a container (not shown) which gradually fills and empties under the effect of the siphon.
  • the capacity of this container between the high level and the low level is preferably chosen equal to a cup of coffee.
  • the cold or preferably preheated water is therefore distributed by a continuous distributor, such as a pump, to the intermittent fountain, which distributes it by a pipe 49 at a small capacity 50 in the form of an annular sleeve arranged coaxially with outside the tube 45 and stationary in rotation, this capacity 50 comprising an internal heating resistor 51 supplied by wires 52, while flow spouts 53 are formed all around its bottom and vertically above the surface conical 40 of the dispenser 39.
  • a continuous distributor such as a pump
  • this capacity 50 comprising an internal heating resistor 51 supplied by wires 52, while flow spouts 53 are formed all around its bottom and vertically above the surface conical 40 of the dispenser 39.
  • the periods of intermittent fountain shutdown have two advantages, the first being that there is a cessation of the flow of coffee through the chute 28 thus allowing to remove a full cup and replace it with an empty cup without losing of coffee, and the second being that, on the next arrival of the distribution of water on the hot resistance 51, there occurs a partial vaporization of this water which thus causes the ground coffee beans which have been dispensed to swell. the interval near the bottom 24.
  • the grounds evacuation chute 31 is directed towards a grounds tank forming part of the apparatus and which is emptied periodically.
  • the device also includes a water tank if you want to avoid a connection on the pipeline.
  • the apparatus according to the invention makes it possible to quickly and automatically carry out all the operations of grinding, distribution, vaporization, pouring, passage and spinning as well as cleaning of the filter and evacuation of the grounds, the apparatus being able thus to function in an absolutely uninterrupted manner and to produce as many cups of coffee as desired if simply to supply it and empty its grounds container without it being necessary to stop it.
  • this axis could also be arranged according to any other angle of orientation, for example horizontally, the rotary distributor 39 then being in this case replaced by simple fixed conduits, and the bottom 24 also being optional.

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  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Centrifugal Separators (AREA)
  • Apparatus For Making Beverages (AREA)

Description

L'invention concerne la filtration en général, et plus particulièrement la préparation du café.The invention relates to filtration in general, and more particularly to the preparation of coffee.

On sait que l'opération de filtration en général consiste à faire passer un liquide à travers une paroi poreuse qui retient des particules solides, ces particules solides pouvant être contenues au préalable en suspension dans le liquide, dans le cas d'une filtration pour séparation, ou au contraire être placées à l'avance dans le filtre puis arrosées par le liquide lorsqu'on veut procéder à une opération de lavage ou d'épuisement à l'aide d'un solvant approprié de substances actives solubles contenues dans les particules solides. C'est le cas en particulier de la préparation du café qui consiste à faire passer de l'eau chaude à travers du café moulu.It is known that the filtration operation in general consists in passing a liquid through a porous wall which retains solid particles, these solid particles possibly being previously contained in suspension in the liquid, in the case of filtration for separation. , or on the contrary be placed in advance in the filter and then watered by the liquid when it is desired to carry out a washing or exhausting operation using an appropriate solvent of soluble active substances contained in the solid particles . This is particularly the case for the preparation of coffee which consists of passing hot water through ground coffee.

Dans le cas le plus simple, le passage du liquide s'effectue par simple gravité. On peut cependant améliorer l'efficacité de filtration en faisant passer le liquide sous l'effet de la force centrifuge en utilisant une paroi poreuse cylin- driquie entraînée en rotation en grande vitesse autour de son axe. Dans les deux cas l'opera- tion de filtration est forcément intermittente, c'est-à-dire qu'à des phases de filtration succèdent des phases de nettoyage pour l'évacuation des substances solides accumulées contre la paroi poreuse.In the simplest case, the passage of the liquid takes place by simple gravity. However, the filtration efficiency can be improved by passing the liquid under the effect of centrifugal force by using a porous cylindrical wall driven in rotation at high speed around its axis. In both cases the filtration operation is necessarily intermittent, that is to say that filtration phases are followed by cleaning phases for the evacuation of the solid substances accumulated against the porous wall.

On connaît cependant des filtres continus dans lesquels on utilise une paroi poreuse sans fin, soit sous forme de bande sans fin, soit sous forme de cylindre rotatif, et dans ce cas on a une zone ou un secteur de filtration suivi d'une autre zone ou secteur de nettoyage, ce nettoyage étant obtenu généralement par raclage à l'aide d'une raclette fixe puis décolmatage de la paroi poreuse par un rinçage en sens inverse. Dans le cas de tels filtres continus, le passage du liquide se fait forcément par gravité ou par aspiration mais il est exclu d'opérer par voie centrifuge, le déplacement ou la rotation de la paroi poreuse étant nécessairement lent puisque c'est lui qui préside à la succession des opérations de filtrage et de lavage.However, continuous filters are known in which an endless porous wall is used, either in the form of an endless band, or in the form of a rotary cylinder, and in this case there is a filtration zone or sector followed by another zone. or cleaning sector, this cleaning generally being obtained by scraping using a fixed squeegee then unclogging the porous wall by rinsing in the opposite direction. In the case of such continuous filters, the passage of the liquid is necessarily by gravity or by suction, but it is excluded to operate by centrifugal means, the displacement or rotation of the porous wall being necessarily slow since it is he who presides the sequence of filtering and washing operations.

Pour surmonter les inconvénients précédents il est enfin connu, d'après le brevet allemand n° 691.923, de réaliser un filtre à la fois continu et centrifuge dont la paroi de filtrage cylindrique est rotative et constituée par un enroulement hélicoidal à spires jointives d'une longue lanière montée dans une cage rotative constituée par des rouleaux cylindriques disposés selon des génératrices extérieures de cette paroi cylindrique, la lanière étant bouclée sur elle même en un ensemble sans fin et entrainée de manière que la paroi poreuse cylindrique avance lentement dans le sens de l'axe en se renouvelant constamment. Cependant l'entraînement de la bande est assuré par un cabestan central qui reprend radialement la bande à la base du cylindre et la recycle au sommet, ce qui présente linconvénient de mal fonctionner étant donné la difficulté où l'on est de donner une tension convenable à la bande sans fin qui est simplement supportée à l'intérieur de la cage formées par les rouleaux. D'autre part ce cabestan placé au centre ainsi que les brins radiaux qui y aboutissent et en partent constituent un obstacle ne permettant pas d'utiliser la région centrale du filtre et ne permettant pas non plus de raccorder la paroi cylindrique de filtrage avec une paroi de fond. Enfin la lanière en bande sans fin est elle même perforée ce qui n'élimine pas complètement les difficultés de décolmatage.To overcome the above drawbacks, it is finally known, from German patent No. 691,923, to produce a filter which is both continuous and centrifugal, the cylindrical filtering wall of which is rotatable and constituted by a helical winding with contiguous turns of a long strap mounted in a rotary cage constituted by cylindrical rollers arranged according to external generators of this cylindrical wall, the strap being looped on itself in an endless assembly and driven so that the porous cylindrical wall advances slowly in the direction of the axis constantly renewing itself. However, the drive of the strip is ensured by a central capstan which takes up the strip radially at the base of the cylinder and recycles it at the top, which has the disadvantage of malfunctioning given the difficulty in providing suitable tension. to the endless belt which is simply supported inside the cage formed by the rollers. On the other hand this capstan placed in the center as well as the radial strands which terminate therein and leave it constitute an obstacle which does not allow the central region of the filter to be used and also does not allow the cylindrical filtering wall to be connected with a wall. background. Finally, the endless strip is itself perforated, which does not completely eliminate the problems of unclogging.

Le but de l'invention est de réaliser un filtre centrifuge continu du type précédent mais qui élimine les inconvénients précités en réalisant un entraînement sûr et efficace tout en dégageant la partie centrale de la paroi cylindrique.The object of the invention is to produce a continuous centrifugal filter of the above type but which eliminates the aforementioned drawbacks by providing a safe and effective drive while freeing the central part of the cylindrical wall.

L'invention consiste, dans un filtre centrifuge sans fin du type précédent, à assurer l'entraînement de la lanière par l'entraînement en rotation sur eux même des rouleaux de la cage support par un mécanisme approprié, et à réaliser le bouclage sans fin par une sprie de retour qui s'étend d'une extrémité à l'autre de l'enroulement hélicoidal en passant par l'extérieur de l'enroulement et de la cage à rouleaux. De plus la lanière est avantageusement dépourvue de perforations et constituée par une partie massive munie seulement d'encoches appropriées en surface.The invention consists, in an endless centrifugal filter of the preceding type, in ensuring the drive of the strap by the rotational drive on themselves of the rollers of the support cage by an appropriate mechanism, and in carrying out the endless looping by a return channel which extends from one end to the other of the helical winding passing through the outside of the winding and of the roller cage. In addition, the strap is advantageously devoid of perforations and constituted by a solid part provided only with suitable notches on the surface.

D'autres particularitiés de l'invention apparaîtront dans la description qui va suivre d'un mode de réalisation pris comme exemple et représenté sur le dessin annexé, sur lequel:

  • la fig. 1 est une coupe verticale axiale d'un dispositif de filtrage selon l'invention appliqué à une machine à café;
  • la fig. 2 est une coupe horizontale selon II-II de la fig. 1;
  • la fig. 3 est une vue extérieure en élévation de la partie essentielle du filtre dans sa cage;
  • la fig. 4 est une vue de dessous en coupe selon IV-IV de la fig. 3 montrant la disposition du train d'engrenages;
  • la fig. 5 est une vue en perspective à grande échelle d'un fragment de la lanière flexible constituant la paroi de filtration.
Other p articularities of the invention will appear in the following description of an embodiment taken as an example and represented in the appended drawing, in which:
  • fig. 1 is an axial vertical section of a filtering device according to the invention applied to a coffee machine;
  • fig. 2 is a horizontal section on II-II of FIG. 1;
  • fig. 3 is an external elevation view of the essential part of the filter in its cage;
  • fig. 4 is a bottom view in section on IV-IV of FIG. 3 showing the arrangement of the gear train;
  • fig. 5 is a perspective view on a large scale of a fragment of the flexible strap constituting the filtration wall.

Conformément à l'invention, la paroi poreuse de filtration est constituée par une longue lanière flexible 1 de faible section disposée selon un enroulement hélicoïdal à spires jointives pour constituer un manchon cylindrique 2, les deux extrémités de la lanière étant raccordées entre elles par une sprie de retour 3 pour constituer un ensemble sans fin. Cette lanière flexible 1 peut être en métal ou en matière plastique, de préférence de section carrée ou rectangulaire, et elle peut avantageusement comporter dans sa face supérieure ou inférieure des encoches 4, de préférence inclinées pour aller en s'évasant vers l'extérieur en partant d'une très faible profondeur du côté destiné à constituer l'intérieur, cette profondeur correspondant à la finesse de filtration désirée, par exemple 0,1 mm.According to the invention, the porous filtration wall is constituted by a long flexible strap 1 of small section arranged in a helical winding with contiguous turns to form a cylindrical sleeve 2, the two ends of the strap being connected to each other by a strap back 3 to form an endless set. This flexible strap 1 can be made of metal or plastic, preferably of square or rectangular section, and it can advantageously include in its upper or lower face notches 4, preferably inclined so as to widen towards the exterior, starting from a very shallow depth on the side intended to constitute the interior, this depth corresponding to the desired filtration fineness, for example 0.1 mm.

La manchon cylindrique 2 ainsi constitué est monté dans une cage constituée par un certain nombre de rouleaux cylindriques 5, au nombre de quatre sur les figures, chacun disposés selon une génératrice du cylindre. Chacun de ces rouleaux tourillonne par sa base dans un flasque inférieur 6 et par une partie voisine de son extrémité supérieure dans un flasque supérieur 7 au moyen d'une encoche 8 débouchant vers le centre dans un alésage 9 d'un diamètre juste suffisant pour permettre le passage du manchon 2. Le flasque supérieur 7 est rigidement fixé au flasque inférieur 6 par des entretoises 10, et le flasque inférieur 6 est lui-même rigidement fixé par son moyeu il à un axe 12 tourillonnant dans des paliers fixes 13 en étant entraînés par un moteur d'entrainement non représenté.The cylindrical sleeve 2 thus formed is mounted in a cage constituted by a number of cylindrical rollers 5, four in number in the figures, each arranged along a generatrix of the cylinder. Each of these rollers journals by its base in a lower flange 6 and by a part close to its upper end in an upper flange 7 by means of a notch 8 opening towards the center in a bore 9 of a diameter just sufficient to allow the passage of the sleeve 2. The upper flange 7 is rigidly fixed to the lower flange 6 by spacers 10, and the lower flange 6 is itself rigidly fixed by its hub 11 to an axis 12 journalled in fixed bearings 13 while being driven by a drive motor not shown.

Tout l'ensemble de la cage, comprenant les deux flasques et les quatre rouleaux verticaux, tourne donc en bloc autour de l'axe 12 à une vitesse appropriée pour obtenir la filtration centrifuge, par exemple 1500 tours/mn. En outre, les quatre rouleaux 5 sont entrainés à une faible vitesse de rotation sur eux-mêmes, tous dans le même sens, grâce à un mécanisme approprié situé en dessous du flasque 6.The entire cage assembly, including the two flanges and the four vertical rollers, therefore rotates as a block around the axis 12 at a suitable speed to obtain centrifugal filtration, for example 1500 revolutions / min. In addition, the four rollers 5 are driven at a low speed of rotation on themselves, all in the same direction, thanks to an appropriate mechanism located below the flange 6.

Ce mécanisme, visible en particulier sur les fig. 1 et 4. comporte un engrenage 14 solidaire de chacune des extrémités inférieures des rouleaux 5, en dessous du flasque 6, les quatre engrenages 14 engrenant simultanément sur un seul engrenage central 15 tournant fou autour de l'axe 12, cet engrenage central étant lui-même entraîné en rotation par un pignon 16 solidaire d'un engrenage 17 qui tourillonne autour d'un axe 18 porté par le flasque 6 et engrène avec un pignon central 19 monté fou sur l'axe 12 et dont la base 20 peut être immobilisée en rotation au moyen d'un dispositif approprié non représenté. Les sens de rotation sont ceux représentés par les flèches sur la fig. 4, en rappelant qu'il s'agit d'une vue de dessous, et les rapports des engrenages sont tels que les rouleaux tournent lentement sur eux-mêmes à une très faible vitesse tandis que l'ensemble de la cage tourne à grande vitesse.This mechanism, visible in particular in FIGS. 1 and 4. has a gear 14 integral with each of the lower ends of the rollers 5, below the flange 6, the four gears 14 meshing simultaneously on a single central gear 15 idling around the axis 12, this central gear being itself -Even driven in rotation by a pinion 16 secured to a gear 17 which rotates around an axis 18 carried by the flange 6 and meshes with a central pinion 19 idly mounted on the axis 12 and whose base 20 can be immobilized in rotation by means of a suitable device not shown. The directions of rotation are those represented by the arrows in FIG. 4, remembering that this is a bottom view, and the ratios of the gears are such that the rollers rotate slowly on themselves at a very low speed while the whole of the cage rotates at high speed .

Dans ces conditions, le manchon 2 constitué par l'ensemble des spires jointives se trouve appliqué par la force centrifuge contre les rouleaux de guidage et d'entraînement 5 et par suite se met à tourner lentement sur lui-même dans le sens de la flèche 21 (voir fig. 2) dans un mouvement relatif de rotation à faible vitesse de l'ordre de 12 tours/mn dans l'exemple choisi. Bien entendu, si l'on se repère au bâti 22 de l'appareil et non plus à la cage tournante, le manchon 2 tourne en réalité dans le même sens que la cage, c'est-à-dire dans le sens des aiguilles d'une montre sur la fig. 2, et à une vitesse à peine inférieure, par exemple 1500 tours/mn pour la cage et 1448 tours/mn pour le manchon. En variante, il serait naturellement possible de faire tourner le manchon dans un sens tel que sa vitesse lente différentielle s'ajoute à celle de la cage au lieu de se retrancher.Under these conditions, the sleeve 2 formed by all of the contiguous turns is applied by centrifugal force against the guide and drive rollers 5 and consequently begins to turn slowly on itself in the direction of the arrow 21 (see fig. 2) in a relative movement of rotation at low speed of the order of 12 revolutions / min in the example chosen. Of course, if we refer to the frame 22 of the device and no longer to the rotating cage, the sleeve 2 actually turns in the same direction as the cage, that is to say in the direction of the needles of a watch in fig. 2, and at a speed barely lower, for example 1500 rpm for the cage and 1448 rpm for the sleeve. As a variant, it would naturally be possible to rotate the sleeve in a direction such that its slow differential speed is added to that of the cage instead of being entrenched.

D'autre part, le sens d'enroulement des spires jointives du manchon 2 est choisi de telle manière que, dans le mouvement relatif précité du manchon par rapport à la cage, la lanière se déroule à la partie supérieure, juste après le passage sous une des joues de retenue axiale 23 d'un des rouleaux 5, puis effectue la spire de retour 3 en passant à l'extérieur des rouleaux 5 suivants, mais de préférence à l'intérieur des entretoises 10 pour s'enrouler en continu à l'extrémité inférieure sur la surface extérieure cylindrique d'une paroi de fond 24 visible sur la fig. 1 et tournant folle autour du moyeu 11 pour pouvoir prendre par rapport à celui-ci le lent mouvement de rotation de l'ensemble du filtre. Ce mouvement est communiqué au fond 24 par engrènement ou par friction sur sa périphérie d'une zone d'entrâinement 25 située à la base des rouleaux 5 au-dessous des joues de retenue axiales 26.On the other hand, the direction of winding of the contiguous turns of the sleeve 2 is chosen in such a way that, in the aforementioned relative movement of the sleeve relative to the cage, the strap takes place at the top, just after passing under one of the axial retaining cheeks 23 of one of the rollers 5, then performs the return turn 3 passing outside the following rollers 5, but preferably inside the spacers 10 to wind continuously 'lower end on the cylindrical outer surface of a bottom wall 24 visible in FIG. 1 and turning madly around the hub 11 in order to be able to take with respect thereto the slow rotational movement of the entire filter. This movement is communicated to the bottom 24 by meshing or by friction on its periphery of a drive zone 25 situated at the base of the rollers 5 below the axial retaining cheeks 26.

De cette manière l'enroulement à force d'une nouvelle spire en continu sous les précédentes oblige l'ensemble du manchon à progresser lentement vers le haut, c'est-à-dire vers son extrémité ouverte, le nombre de spires étant constant ce qui permet aux joues 23 et 26 de maintenir les spires effectivement jointives avec un léger serrage ou un jeu calculé. Dans l'exemple de réalisation, une spire se trouvant en position inférieure met environ 2 minutes 36 secondes pour arriver en haut et effectuer un cycle complet.In this way the winding by force of a new continuous winding under the previous ones obliges the whole of the sleeve to progress slowly upwards, that is to say towards its open end, the number of turns being constant this which allows the cheeks 23 and 26 to maintain the actually contiguous turns with a slight tightening or a calculated clearance. In the embodiment, a coil in the lower position takes approximately 2 minutes 36 seconds to reach the top and complete a complete cycle.

On comprend dès lors qu'avec un tel filtre, il suffit d'introduire le ou les produits à filtrer axialement, et de les déposer par exemple sur le fond 24, pour que ces produits se trouvent projetés sur la face intérieure du manchon 2 où a lieu la filtration, le filtrat étant projeté tangentiellement contre la paroi 22 qui entoure la cage pour s'écouler ensuite par une rigole périphérique 27 vers un goulotte d'évacuation 28, tandis que les résidus solides progressent lentement vers le haut en étant systématiquement essorés jusqu'à épuisement et finissent par être éjectés par la force centrifuge au-delà de la dernière spire c'est-à-dire au-dessus du flasque supérieur 7. Pour éviter le retour des résidus solides vers le compartiment inférieur, l'amorce supérieure de la spire en retour 3 traverse ce flasque 7 à travers une lumière ajustée entourée par un cache 29 également ajusté.It is therefore understood that with such a filter, it suffices to introduce the product or products to be filtered axially, and to deposit them for example on the bottom 24, so that these products are projected onto the inner face of the sleeve 2 where filtration takes place, the filtrate being projected tangentially against the wall 22 which surrounds the cage to then flow through a peripheral channel 27 towards a discharge chute 28, while the solid residues progress slowly upwards while being systematically wrung until exhausted and end up being ejected by centrifugal force beyond the last turn, that is to say above the upper flange 7. To prevent the return of solid residues to the lower compartment, the primer upper of the back turn 3 passes through this flange 7 through an adjusted light surrounded by a cover 29 also adjusted.

Etant donné que la lanière 1 une fois déroulée ne comporte plus aucune perforation, mais simplement de légères encoches, aucun décolmatage, ni aucun rinçage n'est nécessaire. Tout au plus on peut prévoir un raclage des trois faces lisses de la lanière et éventuellement un brossage de la face comportant les encoches 4, à l'aide d'une brosse fixe ou rotative solidaire par exemple d'un des rouleaux 5, ceci dans le cas où la force centrifuge ne suffirait pas à éjecter les résidus solides. Pour faciliter l'évacuation des résidus solides on peut également avoir deux pelles 30 situées en position fixe et inclinées d'une manière plongeante vers l'intérieur des dernières spires supérieures du manchon pour évacuer les résidus solides avant le début de déroulement de la lanière. Ces résidus solides sont donc tous les cas projetés par la force centrifuge contre la paroi 22 mais dans le compartiment supérieure où il sont évacués par une goulotte tangentielle 31. Deux pales flexibles 32, fixées verticalement sur le dessus du flasque 7 pour lécher la surface intérieure de la paroi 22, facilitent le ramassage et l'évacuation des résidus solides.Since the strap 1 once unrolled no longer has any perforation, but simply slight notches, no unclogging, no rinsing is necessary. At most, provision can be made for scraping the three smooth faces of the strap and possibly brushing the face comprising the notches 4, using a fixed or rotary brush integral for example from one of the rollers 5, this in the case where the centrifugal force is not sufficient to eject the solid residues. To facilitate the evacuation of solid residues, it is also possible to have two shovels 30 located in a fixed position and inclined downwardly towards the inside of the last upper turns of the sleeve in order to evacuate solid residues before the beginning of the unwinding of the strap. These solid residues are therefore all cases projected by centrifugal force against the wall 22 but in the upper compartment where they are discharged by a tangential chute 31. Two flexible blades 32, fixed vertically on the top of the flange 7 to lick the interior surface of the wall 22, facilitate the collection and evacuation of solid residues.

Avec un tel filtre, on peut donc alimenter en permanence dans l'axe le mélange hétérogène à séparer, ou séparément le produit pulvérulent et le liquide en cas de lavage ou d'épuisement, et évacuer en continu les résidus solides à la partie supérieure et le filtrat à la partie inférieure, et ceci dans un fonctionnement continu sans nécessiter aucun arrêt de nettoyage. Cette continuité du fonctionnement mécanique et cette automaticité du nettoyage ne sont cependant pas liées nécessairement à la continuité dans le temps des opérations. En effet, si on le désire on peut faire fonctionner le filtre selon l'invention par charges successives en prévoyant pour cela simplement un dispositif de freinage commandé de la base 20 du pignon central 19 par rapport au bâti 22. Il suffit alors dans un premier temps d'alimenter les produits tout en freinant ce dispositif, ce qui permet par l'ascension de la spirale de répartir les produits, puis dans un deuxième temps de supprimer le freinage ce qui supprime par là même le mouvement différentiel de la spirale qui cesse par conséquent son mouvement ascensionnel tout en continuant à tourner à grande vitesse, ce qui permet de poursuivre l'opération de filtrage et d'essorage aussi longtemps qu'on le désire. Enfin dans un troisième temps, il suffit de remettre en action le frein de la partie 20 pour produire à nouveau l'ascension de la spirale et l'évacuation des produits, cette phase pouvant être combinée avec la première d'un cycle suivant.With such a filter, it is therefore possible to permanently supply the heterogeneous mixture to be separated in the axis, or the pulverulent product and the liquid separately in the event of washing or exhaustion, and continuously discharge the solid residues at the top and the filtrate at the bottom, and this in continuous operation without requiring any cleaning stop. This continuity of mechanical operation and this automaticity of cleaning is however not necessarily linked to continuity over time of operations. Indeed, if desired, the filter according to the invention can be operated by successive loads by simply providing for this a braking device controlled from the base 20 of the central pinion 19 relative to the frame 22. It is then sufficient in a first time to feed the products while braking this device, which allows by the ascent of the spiral to distribute the products, then in a second time to remove the braking which thereby eliminates the differential movement of the spiral which ceases consequently its upward movement while continuing to rotate at high speed, which makes it possible to continue the filtering and spinning operation for as long as desired. Finally in a third step, it suffices to put the brake of part 20 back into action to produce again the ascent of the spiral and the evacuation of the products, this phase being able to be combined with the first of a following cycle.

Pour l'application à la fabrication du café, le dispositif de filtrage selon l'invention présente en outre l'avantage qu'il est possible de prolonger l'axe 12 par une partie supérieure 33, séparable ou non du précédent et se plaçant dans l'axe du manchon cylindrique 2, pour entraîner à la partie supérieure un broyeur à vis de type connu pour moudre le café. Pour cela la vis de broyage 34 est taillée directement dans l'extrémité supérieure de l'axe 33 et tourne dans une partie extérieure 35 à intérieur conique située à la base d'une trémie non représentée alimentant le café en grains à l'aide d'un distributeur à débit réglable 36 qui peut être entraîné également par le même axe. Le réglage de la finesse de la mouture se fait par exemple en déplaçant la base 35 dans un mouvement hélicoïdal d'axe vertical à l'aide d'une tige de commande 37 coulissant dans une lumière inclinée 38 solidaire du bâti 22, la vis 33 étant axialement fixe.For the application to the manufacture of coffee, the filtering device according to the invention also has the advantage that it is possible to extend the axis 12 by an upper part 33, separable or not from the previous one and placed in the axis of the cylindrical sleeve 2, to drive at the upper part a screw grinder of the type known for grinding coffee. For this, the grinding screw 34 is cut directly in the upper end of the axis 33 and rotates in an outer part 35 with a conical interior located at the base of a hopper not shown feeding the coffee beans using 'An adjustable flow distributor 36 which can also be driven by the same axis. The fineness of the grinding is adjusted, for example, by moving the base 35 in a helical movement with a vertical axis using a control rod 37 sliding in an inclined lumen 38 integral with the frame 22, the screw 33 being axially fixed.

Lorsqu'on utilise le filtre selon l'invention pour le lavage ou l'épuisement d'une substance solide pulvérulente par une substance liquide, on a intérêt à disposer d'abord la substance solide au voisinage du fond 24 en une couche cylindrique uniforme, puis à distribuer le liquide au-dessus de l'endroit où a lieu la distribution du solide. Ceci peut ètre réalisé très facilement selon l'invention en disposant un distributeur rotatif coaxial 39 comportant un passage central pour le produit solide et une surface extérieure au moins partiellement conique 40 sur laquelle est déversé le liquide qui se trouve ainsi projeté par la force centrifuge, le distributeur 39 étant à cet effet entraîné en rotation, par exemple à la vitesse de l'axe 12 ou 33 en étant solidarisé avec celui-ci à l'aide d'une broche traversante 41. En variante ce distributeur pourrait être solidarisé du fond 24 par des broches parallèles à l'axe, la vitesse du fond étant comme on l'a vu plus haut très peu différente de celle de l'axe.When the filter according to the invention is used for washing or depleting a pulverulent solid substance with a liquid substance, it is advantageous to first have the solid substance near the bottom 24 in a uniform cylindrical layer, then to distribute the liquid above the place where the distribution of the solid takes place. This can be done very easily according to the invention by arranging a coaxial rotary distributor 39 comprising a central passage for the solid product and an at least partially conical external surface 40 onto which the liquid is poured which is thus projected by centrifugal force, the distributor 39 being for this purpose driven in rotation, for example at the speed of the axis 12 or 33 by being secured to it by means of a through pin 41. As a variant, this distributor could be secured to the bottom 24 by pins parallel to the axis, the bottom speed being, as we saw above, very little different from that of the axis.

La surface extérieure conique 40 du distributeur 39 peut se prolonger par une partie cylindrique qui comporte de préférence des aspérités pour répartir sur une certaine hauteur la pulvérisation du liquide. A titre d'exemple ces aspérités peuvent être constituées par une nervure 42 en forme de spirale hélicoidale se développant sur la surface extérieure cylindrique 43 du distributeur. En outre, une nervure circulaire 44 formant déflecteur peut être placée à la base du distributeur pour évacuer les gouttelettes de liquide qui pourraient éventuellement tomber en dehors de la surface extérieure du distributeur.The conical outer surface 40 of the distributor 39 can be extended by a cylindrical part which preferably has asperities to distribute the spraying of the liquid over a certain height. By way of example, these asperities can be constituted by a rib 42 in the form of a helical spiral developing on the cylindrical outer surface 43 of the dispenser. In addition, a circular rib 44 forming a deflector can be placed at the base of the dispenser to evacuate the droplets of liquid which could possibly fall outside the exterior surface of the dispenser.

Pour l'application à une machine à café, le café moulu peut être alimenté à l'intérieur du passage axial du distributeur rotatif 39 par tout moyen approprié. En particulier, si l'on dispose d'un axe 33 et d'un broyeur 34 coaxial comme exposé plus haut, on peut parfaitement placer ce distributeur coaxialement et à l'extérieur de cet axe en le prolongeant axialement par une partie tubulaire 45 dont l'extrémité supérieure vient tourillonner à la base du cône de broyage 35. Si celui-ci se déplace axialement pour permettre le réglage comme indiqué plus haut, on prévoit une lumière oblongue 46 dans la base de l'axe 33 pour le passage de la broche 41 et permettre à ce mouvement de se produire.For application to a coffee machine, the ground coffee can be fed into the axial passage of the rotary distributor 39 by any suitable means. In particular, if there is an axis 33 and a coaxial grinder 34 as explained above, it is perfectly possible to place this distributor coaxially and outside this axis by extending it axially by a tubular part 45 of which the upper end journals at the base of the grinding cone 35. If the latter moves axially to allow adjustment as indicated above, an oblong hole 46 is provided in the base of the axis 33 for the passage of the pin 41 and allow this movement to occur.

Dans ce cas le café moulu qui s'échappe directement entre la vis 33 et la partie tubulaire 45 risque de se trouver plaqué par la force centrifuge contre ce dernier et de s'y accumuler. Ceci est évité selon l'invention en disposant une spirale fixe 47 en fil d'acier hélicoïdal montée librement dans l'intervalle entre l'axe 33 et l'alésage du tube 45 et du distributeur rotatif 39, en étant seulement immobilisée axialement et en rotation par fixation de son extrémité supérieure 48 dans la base du cône 35. De cette manière le café moulu se trouve acheminé régulièrement et sans possibilité de blocage jusqu'à l'extrémité inférieure du distributeur 39 où il se trouve ainsi distribué par la force centrifuge dans l'intervalle entre le fond 24 et la nervure 44 pour venir s'accumuler sur une zone de même hauteur sur la surface intérieure du manchon 2.In this case the ground coffee which escapes directly between the screw 33 and the tubular part 45 may be pressed against the latter by centrifugal force and accumulate there. This is avoided according to the invention by having a fixed spiral 47 of helical steel wire freely mounted in the interval between the axis 33 and the bore of the tube 45 and the rotary distributor. 39, being only immobilized axially and in rotation by fixing its upper end 48 in the base of the cone 35. In this way the ground coffee is routed regularly and without the possibility of blocking to the lower end of the distributor 39 where it is thus distributed by centrifugal force in the interval between the bottom 24 and the rib 44 to come to accumulate on an area of the same height on the inner surface of the sleeve 2.

Toujours dans le cas de la machine à café, la substance liquide, qui est évidemment de l'eau chaude dans ce cas, peut être alimentée et chauffée en continu et distribuée sur la partie conique 40 du distributeur 39. Il est cependant préférable selon l'invention de produire une distribution d'eau par intermittence en alimentant par un débit continu un dispositif bien connu en physique sous le nom de fontaine intermittente et constitué par un siphon auto- amorçable placé dans un récipient non représenté qui se remplit progressivement et se vide sous l'effet du siphon. Dans ce cas, la capacité de ce récipient entre le niveau haut et le niveau bas est choisi de préférence égale à une tasse de café.Still in the case of the coffee machine, the liquid substance, which is obviously hot water in this case, can be continuously supplied and heated and distributed on the conical part 40 of the distributor 39. It is however preferable according to the invention to produce a water supply intermittently by supplying a continuous flow to a device well known in physics under the name of intermittent fountain and constituted by a self-priming siphon placed in a container (not shown) which gradually fills and empties under the effect of the siphon. In this case, the capacity of this container between the high level and the low level is preferably chosen equal to a cup of coffee.

L'eau froide ou de préférence pré-chauffée se trouve donc distribuée par un distributeur continu, tel qu'une pompe, à la fontaine intermittente, laquelle la distribue par un tuyau 49 à une petite capacité 50 en forme de manchon annulaire disposée coaxialement à l'extérieur du tube 45 et immobile en rotation, cette capacité 50 comportant une résistance intérieure de chauffage 51 alimentée par des fils 52, tandis que des becs d'écoulement 53 sont pratiqués tout autour de son fond et à l'aplomb de la surface conique 40 du distributeur 39. De la sorte l'eau se trouve chauffée ou réchauffée par cette résistance avant de s'écouler sur le distributeur et, de là, être projetée sur la couche cylindrique de café avant de passer à travers celui-ci et d'être essoré contre la paroi 22.The cold or preferably preheated water is therefore distributed by a continuous distributor, such as a pump, to the intermittent fountain, which distributes it by a pipe 49 at a small capacity 50 in the form of an annular sleeve arranged coaxially with outside the tube 45 and stationary in rotation, this capacity 50 comprising an internal heating resistor 51 supplied by wires 52, while flow spouts 53 are formed all around its bottom and vertically above the surface conical 40 of the dispenser 39. In this way the water is heated or reheated by this resistance before flowing over the dispenser and, from there, is projected onto the cylindrical layer of coffee before passing through it and to be wrung against the wall 22.

Les périodes d'arrêt de la fontaine intermittente présentent deux avantages, le premier étant qu'il se produit un arrêt de l'écoulement du café par la goulotte 28 permettant ainsi de retirer une tasse pleine et de la remplacer par une tasse vide sans perdre de café, et le deuxième étant que, lors de l'arrivée suivante de la distribution d'eau sur la résistance chaude 51, il se produit une vaporisation partielle de cette eau qui fait ainsi gonfler les grains de café moulus qui ont été distribués dans l'intervalle au voisinage du fond 24.The periods of intermittent fountain shutdown have two advantages, the first being that there is a cessation of the flow of coffee through the chute 28 thus allowing to remove a full cup and replace it with an empty cup without losing of coffee, and the second being that, on the next arrival of the distribution of water on the hot resistance 51, there occurs a partial vaporization of this water which thus causes the ground coffee beans which have been dispensed to swell. the interval near the bottom 24.

On peut ainsi distinguer sur la surface intérieure du manchon 2 et de bas en haut trois zones distinctes successives de largeur progressivement croissante, la première c'est-à-dire la plus basse correspondant à la distribution du café puis à son gonflage à la vapeur, le deuxième située à la hauteur de la nervure 42 correspondant à l'arrosage du café qui produit le maximum de café liquide par passage centrifuge, et la troisième qui surmonte la précédente correspondant à l'essorage poussé de la couronne de marc pour récupérer les dernières gouttes de café et évacuer du marc pratiquement sec à la partie supérieure grâce au moyen général indiqué plus haut. Bien entendu, la goulotte d'évacuation de marc 31 est dirigée vers une cuve à marc faisant partie de l'appareil et qui est vidée périodiquement. L'appareil comporte également une cuve à eau si l'on veut éviter un raccordement sur canalisation.We can thus distinguish on the inner surface of the sleeve 2 and from bottom to top three successive distinct zones of progressively increasing width, the first that is to say the lowest corresponding to the distribution of the coffee and then to its inflation with steam. , the second located at the height of the rib 42 corresponding to the watering of the coffee which produces the maximum amount of liquid coffee by centrifugal passage, and the third which overcomes the previous one corresponding to the advanced wringing of the marc crown to recover the last drops of coffee and evacuate almost dry grounds at the top using the general means indicated above. Of course, the grounds evacuation chute 31 is directed towards a grounds tank forming part of the apparatus and which is emptied periodically. The device also includes a water tank if you want to avoid a connection on the pipeline.

On voit ainsi que l'appareil selon l'invention, avec des moyens relativement simples et tous montés coaxialement sur le même axe, excepté les diverses cuves, permet de réaliser rapidement et automatiquement toutes les opérations de mouture, de distribution, de vaporisation, de verse, de passage et d'essorage ainsi que de nettoyage du filtre et d'évacuation du marc, l'appareil pouvant ainsi fonctionner d'une manière absolument ininterrompue et produire un aussi grand nombre de tasses de café qu'on le désire à condition simplement de l'approvisionner et de vider sa cuve à marc sans qu'il soit nécessaire pour cela de l'arrêter. Inversement, il est parfaitement possible d'arrêter sa production lorsqu'on le désire en arrêtant la distribution d'eau, puis le moteur après un temps déterminé, la production pouvant reprendre immédiatement dès qu'on le désire à condition que l'eau ait été maintenue à la température.It can thus be seen that the apparatus according to the invention, with relatively simple means and all mounted coaxially on the same axis, except for the various tanks, makes it possible to quickly and automatically carry out all the operations of grinding, distribution, vaporization, pouring, passage and spinning as well as cleaning of the filter and evacuation of the grounds, the apparatus being able thus to function in an absolutely uninterrupted manner and to produce as many cups of coffee as desired if simply to supply it and empty its grounds container without it being necessary to stop it. Conversely, it is perfectly possible to stop its production when desired by stopping the distribution of water, then the engine after a determined time, production can resume immediately as soon as desired, provided that the water has been kept at temperature.

Bien que l'exemple de réalisation qui précède soit à axe de rotation vertical, cet axe pourrait également être disposé selon tout autre angle d'orientation, par exemple horizontalement, le distributeur rotatif 39 étant alors dans ce cas remplacé par de simples conduits fixes, et le fond 24 étant également facultatif.Although the above embodiment is with a vertical axis of rotation, this axis could also be arranged according to any other angle of orientation, for example horizontally, the rotary distributor 39 then being in this case replaced by simple fixed conduits, and the bottom 24 also being optional.

Claims (11)

1. A continuous centrifugal filtering device for separation, washing or draining by passing a liquid substance through a porous cylinder wall rotating at high speed which holds back the solid particles contained in the liquid or deposited beforehand on the filter, the cylinder wall being formed by a helical winding with touching turns of a long band mounted inside a rotary cage formed by cylindrical rollers around the outer generatrices of the cylindrical wall, with the band forming a continuous loop on itself in an endless system and so driven that the porous cylinder wall advances slowly along the centre line and constantly gets renewed, which device is characterized by the fact that the band drive is formed by the rotary drive of the said rollers on their axis through a suitable mechanism and that the endless loop is achieved by means of a return turn which stretches from one end of the said helical winding to the other passing outside the winding.
2. The device according to claim 1, characterized by the fact that the band has a square or rectangular cross-section with three smooth faces and one surface containing notches or slots flared towards the outer side.
3. The filtering device according to either claim 1 or claim 2, characterized by the fact that the cage is formed by two end plates connected by spacers, one end plate being solid and rigidly connected to a drive shaft and one end plate being annular with a centre hole bored through it through which passes the helical winding forming the cylindrical filter wall, with the guide rollers being extended through the annular end plate through notches acting as half (sleeve) bearings which open onto the said centre hole on the inside, whilst a suitably shaped window permits the said return turn also to pass through the annular end plate, the directions of rotation of the shaft, of the rollers and of the band winding in the touching turns section being such that the whole of the porous wall moves slowly round its axis in the same direction as the annular end plate.
4. The filtering device according to claim 3, characterized by the fact that on the solid end plate side the band coming from the return turn is wound continuously onto the cylindrical outer surface of an end wall fitted loose on the shaft and driven with respect to the solid end plate with a low speed rotary motion corresponding to the rotary motion of the filter wall.
5. The filtering device according to any of the previous claims, characterized by the fact that the various cylindrical rollers of the cage are driven in rotation round their axis simultaneously with the rotation of the cage by means of a gear train from a centre pinion mounted on the shaft and capable of being fixed in rotation.
6. The filtering device according to claim 5, characterized by the fact that the said centre pinion is fixed by a controlled brake device which enables the axial motion to be interrupted without interrupting the rotary motion of the filter.
7. The filtering device according to any of the previous claims, characterized by the fact that the cage is surrounded by a casing of which the section located on the same side of the annular end plate collects the filtrate and the part located on the other side of this end plate collects the solid residues, detached from the inside of the cylindrical wall, or from the outside of the band by suitable scraper devices, and sent to an outlet port by devices for scraping the inside wall of the casing.
8. The filtering device according to any of the previous claims, characterized by the fact that its axis is vertical and that it contains inside a rotary distributor with an axial duct for the powder product and an outer surface which is tapered, at least in part, for distribution of the liquid product.
9. The filtering device according to claim 8, more especially designed for producing coffee, characterized by the fact that its centre shaft is extended through the rotary distributor to a screw mill of known type mounted coaxially with the filter, the rotary distributor being extended by a tubular part as far as the base of the screw mill.
10. The device according to claim 9, characterized by the fact that, in the space located between the extension of the rotary shaft and axial duct of the rotary distributor and its tubular extension, a helical wire with a large coil pitch is placed and fixed axially and in rotation at the top.
11. The device according to claim 10, characterized by the fact that the distribution of the liquid which consists of water, preheated or not, occurs at a constant flow rate but through an intermittent fountain or feed system holding the contents of one cup of coffee and feeding a heating or superheating and steam generation device arranged coaxially outside the tubular extension to the rotary distributor and discharging onto the tapered part of this rotary distributor.
EP78100037A 1977-06-02 1978-06-01 Continuous filtration centrifuge for separation, washing or draining, and application to an automatic coffee machine Expired EP0000004B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR7716927A FR2372658A1 (en) 1977-06-02 1977-06-02 CONTINUOUS CENTRIFUGAL FILTRATION DEVICE FOR SEPARATION, WASHING OR EXHAUST, AND APPLICATION TO AN AUTOMATIC COFFEE MACHINE
FR7716927 1977-06-02

Publications (2)

Publication Number Publication Date
EP0000004A1 EP0000004A1 (en) 1978-12-20
EP0000004B1 true EP0000004B1 (en) 1980-09-03

Family

ID=9191604

Family Applications (1)

Application Number Title Priority Date Filing Date
EP78100037A Expired EP0000004B1 (en) 1977-06-02 1978-06-01 Continuous filtration centrifuge for separation, washing or draining, and application to an automatic coffee machine

Country Status (5)

Country Link
US (1) US4204964A (en)
EP (1) EP0000004B1 (en)
DE (1) DE2860125D1 (en)
FR (1) FR2372658A1 (en)
IT (1) IT1206574B (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2936659A1 (en) * 1979-09-11 1981-03-19 Braunschweigische Maschinenbauanstalt AG, 3300 Braunschweig CONTINUOUSLY WORKING SUGAR CENTRIFUGE
US5265517A (en) * 1991-10-09 1993-11-30 Industria Columbiana De Electronicos Y Electrodomesticos, Incelt S.A. Of Carrera Method and apparatus for brewing coffee
AU2012293675B2 (en) * 2011-08-09 2017-05-18 Société des Produits Nestlé S.A. Centrifugal brewing machine with flow collecting assembly
BR112015013132A2 (en) * 2012-12-06 2017-07-11 Nestec Sa device for preparing a beverage by centrifugation
KR20160082508A (en) * 2013-10-31 2016-07-08 네퓨레 코포레이션 Operation method for strainer
CA2958603A1 (en) * 2014-10-08 2016-04-14 Nestec S.A. Extraction unit of beverage preparation machine
WO2020167623A1 (en) * 2019-02-11 2020-08-20 North Carolina State University Self-cleaning screen
US20210346824A1 (en) * 2020-04-13 2021-11-11 Evoqua Water Techhnologies LLC Regenerative Media Filtration Apparatus Improvements
US12179238B2 (en) * 2022-08-22 2024-12-31 Watershed Systems, LLC Debris clearing system and method
NL2034898B1 (en) * 2023-05-23 2024-12-04 Spinn Holding B V Improved centrifugal coffee brewer

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Publication number Priority date Publication date Assignee Title
US1767905A (en) * 1926-02-27 1930-06-24 William C Walker Continuous centrifugal separator
US1846168A (en) * 1929-08-10 1932-02-23 Mine And Smelter Supply Compan Filter
US1950869A (en) * 1931-06-08 1934-03-13 Hercules Powder Co Ltd Centrifugal
DE691923C (en) 1938-12-16 1940-06-08 Hans Decker Spin machine with endless belt
US2321207A (en) * 1941-08-25 1943-06-08 B H & M Company Screen for centrifugal machines
GB1108407A (en) * 1965-09-30 1968-04-03 Ceskoslovenska Akademie Ved Continuous filtration centrifuge

Also Published As

Publication number Publication date
DE2860125D1 (en) 1980-12-11
EP0000004A1 (en) 1978-12-20
IT7868230A0 (en) 1978-05-30
IT1206574B (en) 1989-04-27
US4204964A (en) 1980-05-27
FR2372658A1 (en) 1978-06-30
FR2372658B1 (en) 1981-07-17

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