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EP1847185B1 - Manufacture of fibre filters - Google Patents

Manufacture of fibre filters Download PDF

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Publication number
EP1847185B1
EP1847185B1 EP07007588A EP07007588A EP1847185B1 EP 1847185 B1 EP1847185 B1 EP 1847185B1 EP 07007588 A EP07007588 A EP 07007588A EP 07007588 A EP07007588 A EP 07007588A EP 1847185 B1 EP1847185 B1 EP 1847185B1
Authority
EP
European Patent Office
Prior art keywords
suction
shaft
fibres
fibers
conveyor
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.)
Not-in-force
Application number
EP07007588A
Other languages
German (de)
French (fr)
Other versions
EP1847185A1 (en
Inventor
Stephan Wolff
Thorsten Scherbarth
Sönke Horn
Irene Maurer
Alexander Buhl
Jann De Boer
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Koerber Technologies GmbH
Original Assignee
Hauni Maschinenbau GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hauni Maschinenbau GmbH filed Critical Hauni Maschinenbau GmbH
Priority to PL07007588T priority Critical patent/PL1847185T3/en
Publication of EP1847185A1 publication Critical patent/EP1847185A1/en
Application granted granted Critical
Publication of EP1847185B1 publication Critical patent/EP1847185B1/en
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24DCIGARS; CIGARETTES; TOBACCO SMOKE FILTERS; MOUTHPIECES FOR CIGARS OR CIGARETTES; MANUFACTURE OF TOBACCO SMOKE FILTERS OR MOUTHPIECES
    • A24D3/00Tobacco smoke filters, e.g. filter-tips, filtering inserts; Filters specially adapted for simulated smoking devices; Mouthpieces for cigars or cigarettes
    • A24D3/02Manufacture of tobacco smoke filters
    • A24D3/0204Preliminary operations before the filter rod forming process, e.g. crimping, blooming
    • A24D3/0208Cutting filter materials

Definitions

  • the invention relates to a method for producing and an apparatus for producing filter rods of the tobacco-processing industry.
  • the device described there is characterized in that separating devices are provided, which are separated from each other are designed.
  • the devices in the two cited European patent applications process finite fibers, so that nonwovens, filter rods and filters are made of finite fibers and optionally other filter components such as granules.
  • US 4,785,830 A discloses a method and apparatus for producing tobacco rods. A current generated by accumulation of fibrous material is converted to a strand which can be divided into filter rod sections.
  • US 4,185,644 A discloses a distributor for use in a cigarette machine with a relatively long stowage, from which stagnant tobacco is removed by means of a tapping roller. With a bat roller, the extracted tobacco is knocked out and fed to a strand production.
  • the object is achieved by a method for producing filter rods of the tobacco-processing industry comprising fibers of finite length of at least one type of fiber, wherein a step of singulating the fibers is provided in a separating device, wherein the separated fibers emerging from the singulation device counteract a component of movement of gravity towards a conveyor which is a suction belt conveyor.
  • the singulated fibers are spun directly from the singulation device into a suction chute.
  • the Saugstrang originaler connects to the suction shaft, in particular directly, so that after the separating device a very short distance for the fibers is traversed to be in the Saugstranguteer, for example, on one or more Saugb Sn crud.
  • the fibers are mixed with a further filter material, such as granules of activated carbon and / or binder, which has a component of movement in the direction of a Saugstrangbineers, in particular against gravity.
  • a further filter material such as granules of activated carbon and / or binder
  • two juxtaposed suction chutes or a division of a suction chute are provided in two juxtaposed Operaaug.chte, two filter strands can be made simultaneously, so that the throughput or the production amount of filter rods can be increased.
  • the suction shafts are in this case preferably substantially parallel and have an angle between 0 ° and 15 ° to each other.
  • the method for producing filter rods of the tobacco processing industry is further developed in that two different types of fiber are provided, which are brought together and mixed immediately prior to the singulation step.
  • the mixing and merging without any further intermediate step means the separation step or processing step-free, or directly followed by the merging and mixing, a separating step.
  • finite fibers are processed from two or at least two different fiber types.
  • the mixing occurs with the merging or begins with the merging. This also includes, in particular, that the mixing begins with the merging and is continued on a predefinable conveying path.
  • the separating step preferably comprises an acceleration of the fibers, whereby a very homogeneous separation and also a very homogeneous filter rod can be achieved.
  • the acceleration takes place in or by means of a card.
  • a carding or a part of a carding or a carding in particular carding is understood to include one or more rollers, which are formed on the peripheral surface similar to a natural card. These can also be configured with sawtooth or Trapezyakgarnituren. There may also be correspondingly fine spiked rollers.
  • the fibers of two different fiber types are combined unmixed prior to the step of merging and mixing.
  • the term unmixed includes in particular pure type. If the fibers are dammed up unmixed before merging, a particularly good dosage of the fibers is possible. They can then be first pretreated or singulated, then combined and mixed and then separated again to be able to produce homogeneous filter rods. Before the final separation step, a damming up of the fiber mixture can also be provided.
  • a particularly preferred embodiment is when the merged fibers are conveyed by means of a transport air flow to a separating device.
  • the promotion by means of a transport air flow is preferably carried out in the field of mixing of the fibers. This can, however, too already happened shortly before the merging of the different fiber types or immediately before.
  • a particularly efficient embodiment of the separating device is present if it comprises a plurality of rollers arranged one behind the other, whose rotational speeds increase in the fiber conveying direction. This can be very efficient separation take place, which prevents segregation of the fibers.
  • the object is further achieved by a device for producing filter rods of the tobacco-processing industry with at least two Faserzu 2008J, which open into a shaft, wherein adjoining the one slot a separating device, wherein the separating device is formed so that the separated by the separating device Fibers leave the separating device with a movement component against gravity in the direction of a conveyor, wherein the separated fibers of finite length on the conveyor, in particular Saugstrang makeuper, are alsschauerbar.
  • one shaft and the separating device lie directly behind one another in the conveying direction of the fibers or in the vicinity of one another.
  • a device for generating an air flow in the one shaft is provided, which is particularly suitable for conveying the fiber mixture.
  • a device for generating an air flow in the one shaft which may preferably be a fan passing through the one shaft, a very efficient mixing of the material is also possible.
  • the fan may have one or more fan impellers, pass through the fibers, whereby a rotational component is supplied to the fiber mixture, which just allows a very good mixing.
  • one stowage shaft is arranged upstream of the at least two fiber feed shafts or is included in the at least two fiber feed shafts, a very homogeneous fiber mixture and also a very good predosing is possible.
  • the one shaft is designed as a storage shaft.
  • the variant in which a fan passes through a shaft means, in particular, that the fan is integrated into the shaft.
  • the separating device comprises a plurality of rollers arranged one behind the other, whose rotational speeds increase in the fiber conveying direction.
  • at least one roller is designed like a card.
  • the roller on the peripheral surface preferably has a structure such as a natural card, ie in particular engrede pins or spikes.
  • the roller may also be configured as a sawtooth or trapezoidal tooth on the circumferential surface.
  • the sets of successive rolls can be configured ever finer in the fiber conveying direction, so that fibers which are transported by rollers lying one behind the other, a longitudinal alignment, parallelization and separation Experienced.
  • a suction shaft adjoins the separating device directly, which is aligned vertically and is closed with a suction belt conveyor.
  • the SaugstrangIFFer is disposed at the upper end of the suction shaft, resulting in a very uniform fiber web formation in Saugstrang dealter so that very homogeneous filter rods can be produced.
  • two Saugstrang discarder or two suction belts are provided in a Saugstrang considerer to allow a very high throughput and a high production amount of filter rods.
  • Fig. 1 shows a sectional view through a device according to the invention in a first embodiment.
  • fibers 12 of a first type of fiber and fibers 13 of a second type of fiber are fed by a first feed tube 14 and a second feed tube 15 into a first stowage bay 11 and a second stowage bay 11 'by means of, for example, transport air.
  • the first type of fiber 12 may be, for example, a multiple-component fiber, in particular bicomponent fiber
  • the second type of fiber 13 fibers of cellulose acetate, cellulose or carbon fibers Various fiber materials, which have a finite length, can be provided. Regarding the different fiber materials is fully on the DE 102 17 410.5 referred to the applicant.
  • the length of the fibers can preferably be smaller than the length of the filter rod to be produced. Accordingly, this may be between 0.1 mm and 60 mm and in particular preferably between 0.2 mm and 10 mm.
  • the fiber thickness should be 1 to 20 dtex, preferably 2 to 6 dtex.
  • the average fiber diameter may be in the range of preferably 10 to 40 .mu.m, in particular 20 to 38 .mu.m and in particular preferably between 30 and 35 microns.
  • the fibers are preferably crimped, in particular zigzag-shaped and have 10 sheets per 10 mm.
  • the fibers 12 and 13 are taken from the accumulated area of the fibers of the storage spaces 11 and 11' and with a racket roller 17 and 17 'knocked out and into the first Faserzu Foodschacht 19 and the second Faserzu Foodschacht 19' transferred.
  • the different fiber types 12 and 13 are combined to form a fiber mixture 32.
  • the fiber mixture 32 enters a conveyor shaft 21 and can accumulate shortly before the feed roller 22 of a carding device or a part of a carding device.
  • the dosage of the fiber types 12 and 13 is done by, for example, controlling the removal rates of the fibers by means of the feed rollers 16, 16 'and / or racket roller 17, 17'.
  • the feed rollers 16, 16 ' can be made slowly running, such that they promote the fibers against a spring-mounted trough, which is not shown. In this case, the fibers are drawn in and compacted into a thin compact fiber cake, which is not shown.
  • the fibrous cake conveyed down between draw-in rollers 16, 16 'and trough is then milled off or knocked out at the lower end of the trough by a respective fast-running drum 17, 17'.
  • the fibers are loosened, isolated and entered into the shafts 19, 19 '.
  • a supporting air flow can be used, which in Fig. 1 but not shown.
  • the fiber mixture is detected by the feed roller 22 and conveyed against the trough 23 and then a leaf spring battery 24.
  • the trough 23 is spring-loaded. The result is a thin, compact fiber cake, which is not shown, and which is promoted and compressed between the feed roller 22, the trough 23 and the Biattfederbatterie 24.
  • rollers 25, 26 and 27 are designed as a card or equipped with sawtooth or Trapezyakgarnituren. The rolling speeds are increasing from roller 25 to roller 27.
  • the fibers 32 are transferred tangentially to the counter-rotating roller 26. Since the roller 26 rotates faster than the roller 25 and in particular has a finer card structure or a finer sawtooth or Trapez leopardgarnitur, there is a longitudinal alignment, parallelization and separation of the fibers in the transfer.
  • the fibers 32 After the fibers 32 have been held in the clothing of the roller 26 about 180 ° on the circumference, the fibers 32 are tangentially transferred to the turn in opposite directions rotating roller 27. Since the roller 27 rotates faster than the roller 26 and in particular has a finer card-like structure or a finer Sge leopard- or Trapez leopardgarnitur, is again a longitudinal alignment, parallelization and separation of the fibers in the transfer.
  • the fibers 32 are held in the set of the roller 27 by 180 ° were the fibers 32 tangentially upwards in an air flow 44 of the channel or suction shaft 28 passed. Subsequently, the fiber mixture 32 reaches a suction belt 29 of a suction belt conveyor 30.
  • the air flow 44 can additionally via a lateral exhaust 45 (or 45 'in Fig. 4 ) are deposited in front of the suction strand conveyor 30 from the fiber mixture or fiber / granule mixture.
  • the fibers 32 in the suction shaft 28 may first be dropped onto a spreader cloth and then sucked into a suction shaft according to the EP 1 584 248 A1 happen, in which case in the carding preferably a roller more or less use a roller.
  • Fig. 2 shows a further embodiment according to the invention of an apparatus for the production of filter rods, wherein compared to Fig. 1 a fan 31 is provided in direct connection to the Georgialim Society 20.
  • the fan 31 generates a transport air stream 42 in the production well 21. It can take measures be provided to ensure a closed circuit of the transport air flow, for example, 21 transport air openings are provided in the lower part of the conveyor shaft, which ensure that transport air is discharged from the feed chute 21, without carrying fibers, and then fed back to the fan.
  • a drive belt 36 is further provided, which indicates, for example, a drive of the roller 25.
  • the rollers 25 to 27 and the other rollers used can also be driven by a motor with a direct drive.
  • Fig. 2 still another option, namely the supply of a granulate 43 to the fiber mixture. This happens shortly before the filter material shudders on a suction belt of a suction belt conveyor 30 in the suction shaft 28.
  • 33 granules 43 metered with a metering roller 34 is fed from a granule container 33, which ends in a chamber with an accelerator roller 35, which flings the granules tangentially in the direction of the Saugstrangizaers 30 in the suction shaft 28.
  • a fiber fleece 41 or filter material fleece 41 then forms on a suction belt of the suction strand conveyor 30.
  • Fig. 3 is also the bullet portion 37 for granules, which in Fig. 3 not shown, provided.
  • Fig. 4 two complete suction ducts 28, 28 'are provided, which are slightly tilted against each other, in this case at an angle of approximately 3 °.
  • the suction wells 28 and 28 ' may be configured so that these relative to the plane of the Fig. 4 are arranged perpendicular to the plane one behind the other, so that the depth or width of the rollers 27 and 35 are each provided in half to supply the conveyor wells 28 and 28 'with filter material.
  • the bullet area 37 is then for the relative to the plane of the Fig. 4 front conveyor shaft 28 provided with a relatively short granule shaft 40 and with the relative to the plane of the Fig. 4 rear conveyor shaft 28 'provided with a slightly longer granule shaft 40'.
  • the accelerator roller 35 may be formed as a kind of brush roller. Due to the centrifugal force, the granulate is thrown into the respective suction shaft and mixes with the fiber stream. It is preferred if the speeds of the mass flow and of the fed-in granules are different relative to one another. As a result, a good mixing is generated.
  • the stranding machine for the filter rod production decreases considerably, since a suction strand conveyor can be arranged directly on the separating device.
  • the air consumption is reduced because the transport stream and the mixing process in a usual long channel accounts.

Landscapes

  • Cigarettes, Filters, And Manufacturing Of Filters (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
  • Multicomponent Fibers (AREA)
  • Manufacturing Of Cigar And Cigarette Tobacco (AREA)
  • Filtering Materials (AREA)

Abstract

The method involves unmixing fibers (12, 13) e.g. bi-component fibers and carbon fibers, of two different fiber types and accumulating the unmixed fibers. The fibers of finite length of two different fiber types are combined and mixed. The combined fibers are conveyed to a separating device by a flow of transport air (42). The combined and mixed fibers are separated by accelerating the fibers in a teasel and loosening the fibers, where the combining and mixing occurs directly before the separating process. A fiber web (41) is formed after the separating process. An independent claim is also included for a device for producing filter rods of the tobacco processing industry.

Description

Die Erfindung betrifft ein Verfahren zum Herstellen und eine Vorrichtung zur Herstellung von Filterstäben der Tabak verarbeitenden Industrie.The invention relates to a method for producing and an apparatus for producing filter rods of the tobacco-processing industry.

Aus der EP 1 464 241 A1 der Anmelderin ist ein Verfahren zur Herstellung eines Vlieses für die Herstellung von Filtern bzw. Filterstäben der Tabak verarbeitenden Industrie bekannt. Es ist außerdem eine Filterstrangherstelleinrichtung der Tabak verarbeitenden Industrie offenbart, wobei die Filterstrangherstelleinrichtung wenigstens eine Filtermaterialzuführvorrichtung umfasst, aus der das Filtermaterial dosiert abgebbar ist und eine Strangaufbauvorrichtung, in der das Filtermaterial zu einem Strang aufgeschauert wird. Die aus der EP 1 464 241 A1 bekannte Filterstrangherstelleinrichtung umfasst ferner das Merkmal, dass das Filtermaterial in einem Fließbett von der Filtermaterialzuführvorrichtung zu der Strangaufbauvorrichtung förderbar ist. Das in diesem Dokument offenbarte Verfahren zeichnet sich durch die folgenden Verfahrensschritte auf:

  • Zuführen von vereinzelten Filtermaterialien zu einem Fließbett,
  • Transportieren des Filtermaterials in dem Fließbett im Wesentlichen mittels eines Transportluftstromes in Richtung einer Strangaufbauvorrichtung und
  • Aufschauern des Filtermaterials auf der Strangaufbauvorrichtung.
From the EP 1 464 241 A1 The applicant is a method for producing a nonwoven fabric for the production of filters or filter rods of the tobacco processing industry known. There is also disclosed a Filterstrangherstelleinrichtung the tobacco processing industry, wherein the Filterstrangherstelleinrichtung comprises at least one Filtermaterialzuführvorrichtung from which the dosed material is dispensable and a strand-building device in which the filter material is knit into a strand. The from the EP 1 464 241 A1 The known filter strand production device also has the feature that the filter material can be conveyed in a fluidized bed from the filter material supply device to the strand construction device. The method disclosed in this document characterized by the following process steps:
  • Supplying isolated filter materials to a fluidized bed,
  • Transporting the filter material in the fluidized bed essentially by means of a transport air flow in the direction of a strand-building device and
  • Shuddering of the filter material on the strand building apparatus.

Aus der EP 1 464 240 A1 der Anmelderin ist ein Verfahren und eine Vorrichtung zur Herstellung eines Vlieses für die Herstellung von Filterstäben bekannt, wobei das Verfahren sich durch die folgenden Verfahrensschritte auszeichnet:

  • Vereinzeln von Fasern wenigstens einer Sorte Filtermaterials in einer Vereinzelungsvorrichtung,
  • Zuführen der vereinzelten Fasern zu einem Förderer, der sich in einer Förderrichtung bewegt,
  • Aufschauern der vereinzelten Fasern auf dem Förderer, wodurch sich ein Vlies bildet, wobei die Vereinzelungsvorrichtung wenigstens ein Vereinzelungselement umfasst, das um eine Rotationsachse rotiert, wobei die Rotationsachse im Wesentlichen parallel der Förderrichtung des Förderers ausgerichtet ist.
From the EP 1 464 240 A1 the applicant is a method and an apparatus for producing a nonwoven fabric for the production of filter rods is known, wherein the method is characterized by the following method steps:
  • Separating fibers of at least one sort of filter material in a separating device,
  • Feeding the singulated fibers to a conveyor moving in a conveying direction,
  • Churning of the separated fibers on the conveyor, whereby a fleece forms, wherein the separating device comprises at least one separating element which rotates about an axis of rotation, wherein the axis of rotation is aligned substantially parallel to the conveying direction of the conveyor.

Die dort beschriebene Vorrichtung zeichnet sich dadurch aus, dass Vereinzelungsvorrichtungen vorgesehen sind, die getrennt voneinander ausgestaltet sind.The device described there is characterized in that separating devices are provided, which are separated from each other are designed.

Die Vorrichtungen in den beiden genannten europäischen Patentanmeldungen verarbeiten endliche Fasern, so dass Vliese, Filterstäbe und Filter aus endlichen Fasern und ggf. weiteren Filterbestandteilen wie Granulaten hergestellt werden.The devices in the two cited European patent applications process finite fibers, so that nonwovens, filter rods and filters are made of finite fibers and optionally other filter components such as granules.

US 4 785 830 A offenbart ein Verfahren und eine Vorrichtung zum Herstellen von Tabaksträngen. Ein durch Akkumulation von faserigem Material erzeugter Strom wird in einen Strang konvertiert, der in Filterstababschnitte unterteilt werden kann. US 4,785,830 A discloses a method and apparatus for producing tobacco rods. A current generated by accumulation of fibrous material is converted to a strand which can be divided into filter rod sections.

US 4 185 644 A offenbart einen Verteiler zur Benutzung in einer Zigarettenmaschine mit einem relativ langen Stauschacht, aus dem aufgestauter Tabak mittels einer Entnahmewalze entnommen wird. Mit einer Schlägerwalze wird der entnommene Tabak ausgeschlagen und einer Strangherstellung zugeführt. US 4,185,644 A discloses a distributor for use in a cigarette machine with a relatively long stowage, from which stagnant tobacco is removed by means of a tapping roller. With a bat roller, the extracted tobacco is knocked out and fed to a strand production.

Es ist Aufgabe der vorliegenden Erfindung, eine effiziente Variante eines Filterstabherstellverfahrens und einer Vorrichtung zur Herstellung von Filterstäben anzugeben.It is an object of the present invention to provide an efficient variant of a filter rod manufacturing method and a device for producing filter rods.

Die Aufgabe wird durch ein Verfahren zum Herstellen von Filterstäben der Tabak verarbeitenden Industrie umfassend Fasern endlicher Länge wenigstens einer Fasersorte gelöst, wobei ein Schritt des Vereinzelns der Fasern in einer Vereinzelungsvorrichtung vorgesehen ist, wobei die vereinzelten Fasern, die aus der Vereinzelungsvorrichtung austreten, eine Bewegungskomponente entgegen der Schwerkraft in Richtung eines Förderers, der ein Saugstrangförderer ist, aufweisen. Hierdurch ist es möglich, dass die Menge des Luftstromes, die im Stand der Technik beispielsweise gemäß der EP 1 464 241 A1 benötigt wird, deutlich verringert ist und dass auch weniger Luft aus dem Verfahrensprozess entnommen werden muss, was eine Vereinfachung der Verfahrensführung ermöglicht.The object is achieved by a method for producing filter rods of the tobacco-processing industry comprising fibers of finite length of at least one type of fiber, wherein a step of singulating the fibers is provided in a separating device, wherein the separated fibers emerging from the singulation device counteract a component of movement of gravity towards a conveyor which is a suction belt conveyor. This makes it possible that the amount the air flow, which in the prior art, for example, according to the EP 1 464 241 A1 is needed, is significantly reduced and that less air must be removed from the process process, which allows a simplification of the process.

Vorzugsweise werden die vereinzelten Fasern unmittelbar aus der Vereinzelungsvorrichtung in einen Saugschacht geschleudert. Vorzugsweise schließt sich an den Saugschacht der Saugstrangförderer an, und zwar insbesondere unmittelbar, so dass nach der Vereinzelungsvorrichtung eine sehr kurze Wegstrecke für die Fasern zurückzulegen ist, um in dem Saugstrangförderer, beispielsweise auf einem oder mehreren Saugbändern, aufgeschauert zu werden.Preferably, the singulated fibers are spun directly from the singulation device into a suction chute. Preferably, the Saugstrangförderer connects to the suction shaft, in particular directly, so that after the separating device a very short distance for the fibers is traversed to be in the Saugstrangförderer, for example, on one or more Saugbändern crud.

In einer bevorzugten Ausführungsform werden in Förderrichtung stromabwärts der Vereinzelungsvorrichtung die Fasern mit einem weiteren Filtermaterial gemischt, wie beispielsweise einem Granulat aus Aktivkohle und/oder Bindemittel, das eine Bewegungskomponente in Richtung eines Saugstrangförderers, insbesondere entgegen der Schwerkraft aufweist. Hierdurch ergeben sich insbesondere eine gute Durchmischung der Fasern mit dem weiteren Filtermaterial und auch die Möglichkeit eines Transports mit möglichst wenig Saugluft bzw. Transportluft.In a preferred embodiment, in the conveying direction downstream of the separating device, the fibers are mixed with a further filter material, such as granules of activated carbon and / or binder, which has a component of movement in the direction of a Saugstrangförderers, in particular against gravity. This results in particular in a good mixing of the fibers with the other filter material and also the possibility of transport with as little suction air or transport air.

Wenn zwei nebeneinander angeordnete Saugschächte oder eine Aufteilung eines Saugschachtes in zwei nebeneinander angeordnete Teilsaugschächte vorgesehen sind, können zwei Filterstränge gleichzeitig hergestellt werden, so dass der Durchsatz bzw. die Produktionsmenge von Filterstäben erhöht werden kann. Die Saugschächte sind hierbei vorzugsweise im Wesentlichen parallel und weisen einen Winkel zwischen 0° und 15 ° zueinander auf. Vorzugsweise ist das Verfahren zum Herstellen von Filterstäben der Tabak verarbeitenden Industrie dadurch weitergebildet, dass zwei unterschiedliche Fasersorten vorgesehen sind, die unmittelbar vor dem Vereinzelungsschritt zusammengeführt und gemischt werden.If two juxtaposed suction chutes or a division of a suction chute are provided in two juxtaposed Teilaugschächte, two filter strands can be made simultaneously, so that the throughput or the production amount of filter rods can be increased. The suction shafts are in this case preferably substantially parallel and have an angle between 0 ° and 15 ° to each other. Preferably, the method for producing filter rods of the tobacco processing industry is further developed in that two different types of fiber are provided, which are brought together and mixed immediately prior to the singulation step.

Hierdurch wird erreicht, dass eine Entmischung von Fasermaterialien vor dem Vereinzelungsschritt vermieden wird. Im Rahmen der Erfindung bedeutet unmittelbar vor einem Vereinzelungsschritt, dass das Mischen und Zusammenführen ohne weiteren Zwischenschritt zu dem Vereinzelungsschritt geschieht bzw. verarbeitungsschrittfrei ist, bzw. unmittelbar an das Zusammenführen und Mischen schließt sich ein Vereinzelungsschritt an. Im Rahmen der Erfindung werden insbesondere endliche Fasern aus zwei bzw. wenigstens zwei unterschiedlichen Fasersorten verarbeitet. Vorzugsweise geschieht das Mischen mit dem Zusammenführen bzw. beginnt mit dem Zusammenführen. Hiervon ist insbesondere auch umfasst, dass das Mischen mit dem Zusammenführen beginnt und auf einem vorgebbaren Förderweg fortgeführt wird.This ensures that a separation of fiber materials is avoided before the separating step. In the context of the invention, immediately prior to a separating step, the mixing and merging without any further intermediate step means the separation step or processing step-free, or directly followed by the merging and mixing, a separating step. In the context of the invention, in particular finite fibers are processed from two or at least two different fiber types. Preferably, the mixing occurs with the merging or begins with the merging. This also includes, in particular, that the mixing begins with the merging and is continued on a predefinable conveying path.

Wenn nach dem Schritt des Vereinzeins ein Schritt des Aufschauerns zu einem Faservlies geschieht, kann ein sehr homogener Filterstab hergestellt werden. Der Vereinzelungsschritt umfasst vorzugsweise ein Beschleunigen der Fasern, wodurch eine sehr homogene Vereinzelung und auch ein sehr homogener Filterstab erzielbar sind. In einer besonders einfachen Verfahrensführung geschieht das Beschleunigen in oder mittels einer Karde. Unter Karde wird im Rahmen der Erfindung auch eine Kardiervorrichtung bzw. ein Teil einer Kardiervorrichtung oder eine Krempel verstanden, insbesondere wird unter Karde auch eine oder mehrere Walzen verstanden, die auf der Umfangsfläche ähnlich einer natürlichen Karde ausgebildet sind. Diese können auch mit Sägezahn- oder Trapezzahngarnituren ausgestaltet sein. Es können auch entsprechend feine Stachelwalzen vorliegen.When a step of shuddering to a nonwoven fabric occurs after the step of blending, a very homogeneous filter rod can be made. The separating step preferably comprises an acceleration of the fibers, whereby a very homogeneous separation and also a very homogeneous filter rod can be achieved. In a particularly simple procedure, the acceleration takes place in or by means of a card. Under carding is understood in the context of the invention, a carding or a part of a carding or a carding, in particular carding is understood to include one or more rollers, which are formed on the peripheral surface similar to a natural card. These can also be configured with sawtooth or Trapezzahngarnituren. There may also be correspondingly fine spiked rollers.

Vorzugsweise werden die Fasern aus zwei unterschiedlichen Fasersorten vor dem Schritt des Zusammenführens und Mischens ungemischt zusammengeführt. Im Rahmen der Erfindung beinhaltet der Begriff ungemischt insbesondere sortenrein. Wenn die Fasern vor dem Zusammenführen ungemischt aufgestaut werden, ist eine besonders gute Dosierung der Fasern möglich. Sie können dann anschließend zunächst vorvereinzelt oder vereinzelt werden, werden dann zusammengeführt und gemischt und anschließend wieder vereinzelt, um homogene Filterstäbe herstellern zu können. Vor dem abschließenden Vereinzelungsschritt kann auch ein Aufstauen des Fasergemisches vorgesehen sein.Preferably, the fibers of two different fiber types are combined unmixed prior to the step of merging and mixing. In the context of the invention, the term unmixed includes in particular pure type. If the fibers are dammed up unmixed before merging, a particularly good dosage of the fibers is possible. They can then be first pretreated or singulated, then combined and mixed and then separated again to be able to produce homogeneous filter rods. Before the final separation step, a damming up of the fiber mixture can also be provided.

Eine besonders bevorzugte Ausführungsform liegt dann vor, wenn die zusammengeführten Fasern mittels eines Transportluftstroms zu einer Vereinzelungsvorrichtung gefördert werden. Die Förderung mittels eines Transportluftstromes geschieht vorzugsweise im Bereich der Durchmischung der Fasern. Dieses kann allerdings auch schon kurz vor dem Zusammenführen der verschiedenen Fasersorten bzw. unmittelbar davor geschehen.A particularly preferred embodiment is when the merged fibers are conveyed by means of a transport air flow to a separating device. The promotion by means of a transport air flow is preferably carried out in the field of mixing of the fibers. This can, however, too already happened shortly before the merging of the different fiber types or immediately before.

Eine besonders effiziente Ausgestaltung der Vereinzelungsvorrichtung liegt dann vor, wenn diese mehrere hintereinander angeordnete Walzen umfasst, deren Drehgeschwindigkeiten in Faserförderrichtung zunehmen. Hierdurch kann sehr effizient eine Vereinzelung stattfinden, die ein Entmischen der Fasern verhindert.A particularly efficient embodiment of the separating device is present if it comprises a plurality of rollers arranged one behind the other, whose rotational speeds increase in the fiber conveying direction. This can be very efficient separation take place, which prevents segregation of the fibers.

Die Aufgabe wird ferner durch eine Vorrichtung zur Herstellung von Filterstäben der Tabak verarbeitenden Industrie mit wenigstens zwei Faserzuführschächten gelöst, die in einen Schacht münden, wobei sich an den einen Schacht eine Vereinzelungsvorrichtung anschließt, wobei die Vereinzelungsvorrichtung so ausgebildet ist, dass die durch die Vereinzelungsvorrichtung vereinzelten Fasern die Vereinzelungsvorrichtung mit einer Bewegungskomponente entgegen der Schwerkraft in Richtung eines Förderers verlassen, wobei die vereinzelten Fasern endlicher Länge auf den Förderer, insbesondere Saugstrangförderer, aufschauerbar sind. Hierbei liegen insbesondere der eine Schacht und die Vereinzelungsvorrichtung unmittelbar hintereinander in Förderrichtung der Fasern bzw. in Nachbarschaft zueinander. Durch die erfindungsgemäße Vorrichtung ist eine besonders einfache Durchmischung verschiedener Fasersorten möglich, wobei eine Entmischung im weiteren Verfahren bzw. bei der weiteren Verarbeitung der Fasermischung vermieden wird. Ferner ist eine sehr kleinbauende Vorrichtung ermöglicht.The object is further achieved by a device for producing filter rods of the tobacco-processing industry with at least two Faserzuführschächten, which open into a shaft, wherein adjoining the one slot a separating device, wherein the separating device is formed so that the separated by the separating device Fibers leave the separating device with a movement component against gravity in the direction of a conveyor, wherein the separated fibers of finite length on the conveyor, in particular Saugstrangförderer, are aufschauerbar. In this case, in particular, one shaft and the separating device lie directly behind one another in the conveying direction of the fibers or in the vicinity of one another. By the device according to the invention a particularly simple mixing of different fiber types is possible, with a segregation in the further process or in the further processing of the fiber mixture is avoided. Furthermore, a very small-sized device is made possible.

Vorzugsweise ist eine Vorrichtung zur Erzeugung eines Luftstroms in dem einen Schacht vorgesehen, die insbesondere zum Fördern der Fasermischung geeignet ist. Durch Vorsehen einer Vorrichtung zur Erzeugung eines Luftstroms in dem einen Schacht, die vorzugsweise ein Ventilator sein kann, der den einen Schacht durchsetzt, ist ferner eine sehr effiziente Mischung des Materials möglich. Hierzu kann beispielsweise der Ventilator ein oder mehrere Ventilatorflügelräder aufweisen, durch die Fasern hindurch treten, wodurch eine Rotationskomponente dem Fasergemisch zugeführt wird, was eben eine sehr gute Durchmischung ermöglicht.Preferably, a device for generating an air flow in the one shaft is provided, which is particularly suitable for conveying the fiber mixture. By providing a device for generating an air flow in the one shaft, which may preferably be a fan passing through the one shaft, a very efficient mixing of the material is also possible. For this purpose, for example, the fan may have one or more fan impellers, pass through the fibers, whereby a rotational component is supplied to the fiber mixture, which just allows a very good mixing.

Wenn jeweils ein Stauschacht den wenigstens zwei Faserzuführschächten vorgeschaltet ist oder in den wenigstens zwei Faserzuführschächten umfasst ist, ist eine sehr homogene Fasermischung und auch eine sehr gute Vordosierung möglich.If in each case one stowage shaft is arranged upstream of the at least two fiber feed shafts or is included in the at least two fiber feed shafts, a very homogeneous fiber mixture and also a very good predosing is possible.

Vorzugsweise ist der eine Schacht als Stauschacht ausgebildet. Die Variante, in der ein Ventilator den einen Schacht durchsetzt, bedeutet insbesondere, dass der Ventilator in den Schacht integriert ist.Preferably, the one shaft is designed as a storage shaft. The variant in which a fan passes through a shaft means, in particular, that the fan is integrated into the shaft.

Vorzugsweise umfasst die Vereinzelungsvorrichtung mehrere hintereinander angeordnete Walzen, deren Drehgeschwindigkeiten in Faserförderrichtung zunehmen. Vorzugsweise ist wenigstens eine Walze kardenartig ausgestaltet. Hierzu hat die Walze an der Umfangsfläche vorzugsweise eine Struktur wie eine natürliche Karde, d.h. insbesondere engliegende Stifte oder Stacheln. Die Walze kann an der Umfangsfläche auch sägezahnförmig oder trapezzahnförmig ausgestaltet sein. Die Garnituren der hintereinander liegenden Walzen können in Faserförderrichtung immer feiner ausgestaltet sein, so dass Fasern, die durch hintereinander liegende Walzen transportiert werden, eine Längsausrichtung, Parallelisierung und Vereinzelung erfahren.Preferably, the separating device comprises a plurality of rollers arranged one behind the other, whose rotational speeds increase in the fiber conveying direction. Preferably, at least one roller is designed like a card. For this purpose, the roller on the peripheral surface preferably has a structure such as a natural card, ie in particular engliegende pins or spikes. The roller may also be configured as a sawtooth or trapezoidal tooth on the circumferential surface. The sets of successive rolls can be configured ever finer in the fiber conveying direction, so that fibers which are transported by rollers lying one behind the other, a longitudinal alignment, parallelization and separation Experienced.

Vorzugsweise schließt sich unmittelbar an die Vereinzelungsvorrichtung ein Saugschacht an, der vertikal ausgerichtet ist und mit einem Saugstrangförderer abgeschlossen ist. Hierdurch ist eine sehr kompaktbauende Vorrichtung möglich. Vorzugsweise ist der Saugstrangförderer am oberen Ende des Saugschachtes angeordnet, wodurch sich eine sehr gleichmäßige Faservliesausbildung im Saugstrangförderer ergibt, so dass sehr homogene Filterstäbe produziert werden können. Vorzugsweise sind zwei Saugstrangförderer oder zwei Saugbänder in einem Saugstrangförderer vorgesehen, um einen sehr hohen Durchsatz und eine hohe Produktionsmenge an Filterstäben zu ermöglichen.Preferably, a suction shaft adjoins the separating device directly, which is aligned vertically and is closed with a suction belt conveyor. As a result, a very compact device is possible. Preferably, the Saugstrangförderer is disposed at the upper end of the suction shaft, resulting in a very uniform fiber web formation in Saugstrangförderer so that very homogeneous filter rods can be produced. Preferably, two Saugstrangförderer or two suction belts are provided in a Saugstrangförderer to allow a very high throughput and a high production amount of filter rods.

Wenn zwei Saugschächte vorgesehen sind oder ein Saugschacht in Faserförderrichtung kurz vor den Saugstrangförderern oder dem Saugstrangförderer mit zwei Saugbändern in zwei Schächte aufgeteilt ist, ist eine gleichmäßige Verteilung der Fasern möglich.If two suction shafts are provided or a suction chute in the fiber conveying direction is divided into two shafts shortly before the Saugstrangförderern or Saugstrangförderer with two suction belts, a uniform distribution of the fibers is possible.

Eine gleichmäßige Verteilung der Mengen der Fasern, die von den Saugbändern oder den Saugstrangförderern aufgenommen werden, kann beispielsweise durch Einstellung des Luftstromes bzw. des Saugluftstromes durch die jeweiligen Saugbänder bzw. Saugstrangförderer erfolgen.A uniform distribution of the amounts of fibers that are absorbed by the suction belts or Saugstrangförderern, for example, by adjusting the air flow or the Saugluftstromes done by the respective suction belts or Saugstrangförderer.

Die Erfindung wird nachstehend ohne Beschränkung des allgemeinen Erfindungsgedankens anhand von Ausführungsbeispielen unter Bezugnahme auf die Zeichnungen beschrieben. Bezüglich aller im Text nicht näher erläuterten erfindungsgemäßen Einzelheiten wird ausdrücklich auf die Zeichnungen verwiesen. Es zeigen:

Fig. 1
eine schematische Schnittdarstellung einer erfindungsgemäßen Vorrichtung,
Fig. 2
eine schematische Schnittdarstellung einer erfindungsgemäßen Vorrichtung in einer weiteren Ausführungsform,
Fig. 3
einen Ausschnitt aus einer erfindungsgemäßen Vorrichtung in einer weiteren Ausführungsform in schematischer Darstellung,
Fig. 4
einen Ausschnitt aus einer erfindungsgemäßen Vorrichtung in noch einer weiteren Ausführungsform in schematischer Darstellung.
The invention will be described below without limiting the general inventive idea by means of embodiments with reference to the drawings. With respect to all details of the invention not explained in detail, reference is expressly made to the drawings. Show it:
Fig. 1
a schematic sectional view of an inventive Contraption,
Fig. 2
a schematic sectional view of a device according to the invention in a further embodiment,
Fig. 3
a section of a device according to the invention in a further embodiment in a schematic representation,
Fig. 4
a section of a device according to the invention in yet another embodiment in a schematic representation.

In den folgenden Figuren sind jeweils gleiche oder gleichartige Elemente bzw. entsprechende Teile mit denselben Bezugsziffern versehen, so dass von einer entsprechenden erneuten Vorstellung abgesehen wird.In the following figures, identical or similar elements or corresponding parts are provided with the same reference numerals, so that a corresponding renewed idea is dispensed with.

Fig. 1 zeigt eine Schnittdarstellung durch eine erfindungsgemäße Vorrichtung in einer ersten Ausführungsform. In einer Faseraufbereitungsvorrichtung 10 werden Fasern 12 einer ersten Fasersorte und Fasern 13 einer zweiten Fasersorte durch ein erstes Zuführrohr 14 und ein zweites Zuführrohr 15 in einen ersten Stauschacht 11 und einen zweiten Stauschacht 11' mittels beispielsweise Transportluft zugeführt. Die erste Fasersorte 12 kann beispielsweise eine Mehrfachkomponentenfaser, insbesondere Bikomponentenfaser sein, und die zweite Fasersorte 13 Fasern aus Celluloseacetat, Cellulose oder Kohlefasern. Es können diverse Fasermateralien, die eine endliche Länge aufweisen, vorgesehen sein. Bezüglich der verschiedenen Fasermaterialien wird vollumfänglich auf die DE 102 17 410.5 der Anmelderin verwiesen. Die Länge der Fasern kann vorzugsweise kleiner sein als die Länge des herzustellenden Filterstabs. Diese kann demnach zwischen 0,1 mm und 60 mm und insbesondere vorzugsweise zwischen 0,2 mm und 10 mm liegen. Bei künstlich hergestellten Fasern sollte die Faserstärke 1 bis 20 dtex, bevorzugt 2 bis 6 dtex, betragen. Der mittlere Faserdurchmesser kann im Bereich von vorzugsweise 10 bis 40 µm, insbesondere 20 bis 38 µm liegen und insbesondere vorzugsweise zwischen 30 und 35 µm liegen. Die Fasern sind vorzugsweise gekräuselt, insbesondere zick-zack-förmig und weisen 10 Bögen pro 10 mm auf. Fig. 1 shows a sectional view through a device according to the invention in a first embodiment. In a fiber processing apparatus 10, fibers 12 of a first type of fiber and fibers 13 of a second type of fiber are fed by a first feed tube 14 and a second feed tube 15 into a first stowage bay 11 and a second stowage bay 11 'by means of, for example, transport air. The first type of fiber 12 may be, for example, a multiple-component fiber, in particular bicomponent fiber, and the second type of fiber 13 fibers of cellulose acetate, cellulose or carbon fibers. Various fiber materials, which have a finite length, can be provided. Regarding the different fiber materials is fully on the DE 102 17 410.5 referred to the applicant. The length of the fibers can preferably be smaller than the length of the filter rod to be produced. Accordingly, this may be between 0.1 mm and 60 mm and in particular preferably between 0.2 mm and 10 mm. For man-made fibers, the fiber thickness should be 1 to 20 dtex, preferably 2 to 6 dtex. The average fiber diameter may be in the range of preferably 10 to 40 .mu.m, in particular 20 to 38 .mu.m and in particular preferably between 30 and 35 microns. The fibers are preferably crimped, in particular zigzag-shaped and have 10 sheets per 10 mm.

Mittels der Einzugswalzen 16 und 16' werden die Fasern 12 bzw. 13 aus dem aufgestauten Bereich der Fasern der Stauschächte 11 und 11' entnommen und mit einer Schlägerwalze 17 bzw. 17' ausgeschlagen und in den ersten Faserzuführschacht 19 bzw. den zweiten Faserzuführschacht 19' überführt. In einem Zusammenführbereich 20 werden die verschiedenen Fasersorten 12 bzw. 13 zu einem Fasergemisch 32 zusammengeführt. Das Fasergemisch 32 gelangt in einen Förderschacht 21 und kann sich kurz vor der Einzugswalze 22 einer Kardiervorrichtung bzw. eines Teils einer Kardiervorrichtung aufstauen. Die Dosierung der Fasersorten 12 und 13 geschieht durch beispielsweise Steuerung der Entnahmegeschwindigkeiten der Fasern mittels der Einzugswalzen 16, 16' und/oder Schlägerwalze 17, 17'. Die Einzugswalzen 16, 16' können langsam laufend ausgestaltet sein, dergestalt, dass diese die Fasern gegen eine federnd gelagerte Mulde, die nicht dargestellt ist, fördern. Hierbei werden die Fasern eingezogen und zu einem dünnen kompakten Faserkuchen, der nicht dargestellt ist, verdichtet.By means of the feed rollers 16 and 16 ', the fibers 12 and 13 are taken from the accumulated area of the fibers of the storage spaces 11 and 11' and with a racket roller 17 and 17 'knocked out and into the first Faserzuführschacht 19 and the second Faserzuführschacht 19' transferred. In a merging region 20, the different fiber types 12 and 13 are combined to form a fiber mixture 32. The fiber mixture 32 enters a conveyor shaft 21 and can accumulate shortly before the feed roller 22 of a carding device or a part of a carding device. The dosage of the fiber types 12 and 13 is done by, for example, controlling the removal rates of the fibers by means of the feed rollers 16, 16 'and / or racket roller 17, 17'. The feed rollers 16, 16 'can be made slowly running, such that they promote the fibers against a spring-mounted trough, which is not shown. In this case, the fibers are drawn in and compacted into a thin compact fiber cake, which is not shown.

Der zwischen Einzugswalzen 16, 16' und Mulde nach unten geförderte Faserkuchen wird anschließend am unteren Ende der Mulde von jeweils einer schnell laufenden Schlägerwalze 17, 17' abgefräst bzw. ausgeschlagen. Dabei werden die Fasern aufgelockert, vereinzelt und in die Schächte 19, 19' eingetragen. Hierbei kann ein unterstützender Luftstrom Verwendung finden, der in Fig. 1 allerdings nicht dargestellt ist. Am Ende des Förderschachts 21 wird das Fasergemisch von der Einzugswalze 22 erfasst und gegen die Mulde 23 und anschließend eine Blattfederbatterie 24 gefördert. Die Mulde 23 ist federgelagert. Es entsteht ein dünner, kompakter Faserkuchen, der nicht dargestellt ist, und der zwischen der Einzugswalze 22, der Mulde 23 und der Biattfederbatterie 24 gefördert und verdichtet wird.The fibrous cake conveyed down between draw-in rollers 16, 16 'and trough is then milled off or knocked out at the lower end of the trough by a respective fast-running drum 17, 17'. The fibers are loosened, isolated and entered into the shafts 19, 19 '. In this case, a supporting air flow can be used, which in Fig. 1 but not shown. At the end of the conveyor shaft 21, the fiber mixture is detected by the feed roller 22 and conveyed against the trough 23 and then a leaf spring battery 24. The trough 23 is spring-loaded. The result is a thin, compact fiber cake, which is not shown, and which is promoted and compressed between the feed roller 22, the trough 23 and the Biattfederbatterie 24.

Verlässt der Faserkuchen den Wirkbereich der Blattfederbatterie 24, wird er von der schnelllaufenden Walze 25 erfasst und übernommen. Die Walzen 25, 26 und 27 sind wie bei einer Karde ausgestaltet bzw. mit Sägezahn- oder Trapezzahngarnituren ausgestattet. Die Walzendrehzahlen sind von Walze 25 zu Walze 27 hin steigend.Leaves the fiber cake the effective range of the leaf spring battery 24, it is detected by the high-speed roller 25 and taken over. The rollers 25, 26 and 27 are designed as a card or equipped with sawtooth or Trapezzahngarnituren. The rolling speeds are increasing from roller 25 to roller 27.

Nachdem die Fasern des Fasergemischs 32 für eine Umdrehung von ca. 180° in der Garnitur der Walze 25 gehalten wurden, werden die Fasern 32 tangential an die gegensinnig drehende Walze 26 übergeben. Da die Walze 26 schneller dreht als die Walze 25 und insbesondere eine feinere Kardenstruktur bzw. eine feinere Sägezahn- oder Trapezzahngarnitur aufweist, erfolgt eine Längsausrichtung, Parallelisierung und Vereinzelung der Fasern bei der Übergabe.After the fibers of the fiber mixture 32 have been held for a rotation of approximately 180 ° in the clothing of the roller 25, the fibers 32 are transferred tangentially to the counter-rotating roller 26. Since the roller 26 rotates faster than the roller 25 and in particular has a finer card structure or a finer sawtooth or Trapezzahngarnitur, there is a longitudinal alignment, parallelization and separation of the fibers in the transfer.

Nachdem die Fasern 32 in der Garnitur der Walze 26 ca. 180° auf dem Umfang gehalten wurden, werden die Fasern 32 tangential an die wiederum gegensinnig drehende Walze 27 übergeben. Da die Walze 27 schneller dreht als die Walze 26 und insbesondere eine feinere kardenartige Struktur bzw. eine feinere Sägezahn- oder Trapezzahngarnitur aufweist, erfolgt wieder eine Längsausrichtung, Parallelisierung und Vereinzelung der Fasern bei der Übergabe. Nachdem die Fasern 32 in der Garnitur der Walze 27 um 180° gehalten wurden, werden die Fasern 32 tangential nach oben in einen Luftstrom 44 des Kanals bzw. Saugschachtes 28 übergeben. Anschließend gelangt das Fasergemisch 32 auf ein Saugband 29 eines Saugstrangförderers 30. Der Luftstrom 44 kann zusätzlich über eine seitliche Absaugung 45 (bzw. 45' in Fig. 4) vor dem Saugstrangförderer 30 vom Fasergemisch, bzw. Faser-/Granulatgemisch, abgeschieden werden.After the fibers 32 have been held in the clothing of the roller 26 about 180 ° on the circumference, the fibers 32 are tangentially transferred to the turn in opposite directions rotating roller 27. Since the roller 27 rotates faster than the roller 26 and in particular has a finer card-like structure or a finer Sägezahn- or Trapezzahngarnitur, is again a longitudinal alignment, parallelization and separation of the fibers in the transfer. After the fibers 32 are held in the set of the roller 27 by 180 ° were the fibers 32 tangentially upwards in an air flow 44 of the channel or suction shaft 28 passed. Subsequently, the fiber mixture 32 reaches a suction belt 29 of a suction belt conveyor 30. The air flow 44 can additionally via a lateral exhaust 45 (or 45 'in Fig. 4 ) are deposited in front of the suction strand conveyor 30 from the fiber mixture or fiber / granule mixture.

An den Saugstrangförderer schließt sich, was in der Fig. nicht dargestellt ist, eine übliche Strangbildevorrichtung an, wie beispielsweise gemäß Fig. 10 der EP 1 464 241 A1 . Diesbezüglich wird vollumfänglich auf die Offenbarung dieser europäischen Patentanmeldung verwiesen. Nach Erzeugen eines Faserkuchens auf dem Saugband 29 des Saugstrangförderers 30 wird der Faserkuchen üblicherweise getrimmt, einer Formatvorrichtung zugeführt, um aus den sich bildenden Fasern, aus dem gebildeten Faserkuchen bzw. Faservlies einen Faserstrang mit gewünschter Querschnittsgeometrie zu erzeugen und ggf. mit einem Umhüllungsmaterial zu umhüllen, um anschließend in Filterstäbe abgelängt zu werden.What is not shown in the FIGURE is followed by a conventional strand forming device, for example as shown in FIG. 10, of the suction strand conveyor EP 1 464 241 A1 , In this respect, reference is made in full to the disclosure of this European patent application. After producing a fiber cake on the suction belt 29 of the Saugstrangförderers 30 of the fiber cake is usually trimmed, fed to a formatting device to produce from the fibers forming, from the formed fiber cake or nonwoven fabric a fiber strand with desired cross-sectional geometry and possibly to envelop a wrapping material to be subsequently cut into filter rods.

Statt eines unmittelbaren Einschießens der Fasern 32 in den Saugschacht 28 kann zunächst ein Abwerfen auf ein Streutuch und ein anschließendes Absaugen in einen Saugschacht gemäß der EP 1 584 248 A1 geschehen, wobei dann in der Kardiervorrichtung vorzugsweise eine Walze mehr oder eine Walze weniger Verwendung findet.Instead of an immediate Einschießens the fibers 32 in the suction shaft 28 may first be dropped onto a spreader cloth and then sucked into a suction shaft according to the EP 1 584 248 A1 happen, in which case in the carding preferably a roller more or less use a roller.

Fig. 2 zeigt eine weitere erfindungsgemäße Ausführungsform einer Vorrichtung zur Herstellung von Filterstäben, wobei im Vergleich zu Fig. 1 ein Ventilator 31 in unmittelbarem Anschluss an den Zusammenführbereich 20 vorgesehen ist. Der Ventilator 31 erzeugt einen Transportluftstrom 42 in dem Förderschacht 21. Es können Maßnahmen vorgesehen sein, um einen geschlossenen Kreislauf des Transportluftstromes zu gewährleisten, wobei beispielsweise im unteren Bereich des Förderschachts 21 Transportluftöffnungen vorgesehen sind, die dafür sorgen, dass Transportluft aus dem Förderschacht 21 abgeführt wird, ohne Fasern mitzuführen, um dann wieder dem Ventilator zugeführt zu werden. Fig. 2 shows a further embodiment according to the invention of an apparatus for the production of filter rods, wherein compared to Fig. 1 a fan 31 is provided in direct connection to the Zusammenführbereich 20. The fan 31 generates a transport air stream 42 in the production well 21. It can take measures be provided to ensure a closed circuit of the transport air flow, for example, 21 transport air openings are provided in the lower part of the conveyor shaft, which ensure that transport air is discharged from the feed chute 21, without carrying fibers, and then fed back to the fan.

In Fig. 2 ist ferner noch ein Antriebsriemen 36 vorgesehen, der beispielsweise einen Antrieb der Walze 25 andeutet. Die Walzen 25 bis 27 und auch die weiteren verwendeten Walzen können allerdings auch mit einem Direktantrieb durch jeweils einen Motor angetrieben werden.In Fig. 2 Furthermore, a drive belt 36 is further provided, which indicates, for example, a drive of the roller 25. However, the rollers 25 to 27 and the other rollers used can also be driven by a motor with a direct drive.

Im Vergleich zum Ausführungsbeispiel gemäß Fig. 1 ist in Fig. 2 noch eine weitere Option erfüllt, nämlich die der Zuführung eines Granulats 43 zu dem Fasergemisch. Dieses geschieht kurz vor dem Aufschauern des Filtermaterials auf einem Saugband eines Saugstrangförderers 30 in dem Saugschacht 28.Compared to the embodiment according to Fig. 1 is in Fig. 2 still another option, namely the supply of a granulate 43 to the fiber mixture. This happens shortly before the filter material shudders on a suction belt of a suction belt conveyor 30 in the suction shaft 28.

Hierzu wird aus einem Granulatbehälter 33 Granulat 43 mit einer Dosierwalze 34 dosiert einem Fallschacht zugeführt, der in einer Kammer mit einer Beschleunigerwalze 35 endet, die das Granulat tangential in Richtung des Saugstrangförderers 30 in den Saugschacht 28 schleudert. Hierdurch ergibt sich eine gute Durchmischung des Granulats mit den Fasern. Es bildet sich dann ein Faservlies 41 bzw. Filtermaterialvlies 41 auf einem Saugband des Saugstrangförderers 30.For this purpose, 33 granules 43 metered with a metering roller 34 is fed from a granule container 33, which ends in a chamber with an accelerator roller 35, which flings the granules tangentially in the direction of the Saugstrangförderers 30 in the suction shaft 28. This results in a good mixing of the granules with the fibers. A fiber fleece 41 or filter material fleece 41 then forms on a suction belt of the suction strand conveyor 30.

Um eine höhere Produktionsgeschwindigkeit bzw. einen höheren Durchsatz von Material zu ermöglichen und die Anzahl der Filterstäbe pro Zeiteinheit zu vergrößern, ist es möglich, zwei Saugbänder 29, 29', wie in Fig. 3 und Fig. 4 angedeutet ist, vorzusehen.In order to enable a higher production speed or a higher throughput of material and to increase the number of filter rods per unit of time, it is possible to use two suction belts 29, 29 ', as in FIG FIG. 3 and FIG. 4 is suggested to provide.

Hierzu kann wie in Fig. 3 angedeutet ist, ein Saugschacht 28 in zwei Teilschächte 39 und 39' aufgeteilt sein, die dann in zwei im Wesentlichen parallele Teilschächte 39, 39' kurz vor den Saugbändern 29, 29' des Saugstrangförderers 30 übergehen. In Fig. 3 ist ferner der Einschussbereich 37 für Granulat, das in Fig. 3 nicht dargestellt ist, vorgesehen.This can be done as in Fig. 3 is indicated, a suction shaft 28 in two sub-shafts 39 and 39 'be divided, which then pass into two substantially parallel sub-shafts 39, 39' just before the suction belts 29, 29 'of the Saugstrangförderers 30. In Fig. 3 is also the bullet portion 37 for granules, which in Fig. 3 not shown, provided.

Gemäß Fig. 4 sind zwei vollständige Saugschächte 28, 28' vorgesehen, die gegeneinander etwas verkippt sind, in diesem Fall mit einem Winkel von ungefähr 3°. Die Saugschächte 28 und 28' können so ausgestaltet sein, dass diese relativ zur Zeichenebene der Fig. 4 senkrecht zur Zeichenebene hintereinander angeordnet sind, so dass die Tiefe bzw. Breite der Walzen 27 bzw. 35 jeweils zur Hälfte zur Versorgung der Förderschächte 28 bzw. 28' mit Filtermaterial vorgesehen sind. Der Einschussbereich 37 ist dann für den relativ zur Zeichenebene der Fig. 4 vorderen Förderschacht 28 mit einem relativ kurzen Granulatschacht 40 versehen und mit dem relativ zur Zeichenebene der Fig. 4 hinteren Förderschacht 28' mit einem etwas längeren Granulatschacht 40' versehen. Die Beschleunigerwalze 35 kann als eine Art Bürstenwalze ausgebildet sein. Durch die Fliehkraft wird das Granulat in den jeweiligen Saugschacht geschleudert und vermischt sich mit dem Faserstrom. Es ist bevorzugt, wenn die Geschwindigkeiten des Massenstromes und des eingespeisten Granulates relativ zueinander unterschiedlich sind. Hierdurch wird eine gute Vermischung erzeugt.According to Fig. 4 two complete suction ducts 28, 28 'are provided, which are slightly tilted against each other, in this case at an angle of approximately 3 °. The suction wells 28 and 28 'may be configured so that these relative to the plane of the Fig. 4 are arranged perpendicular to the plane one behind the other, so that the depth or width of the rollers 27 and 35 are each provided in half to supply the conveyor wells 28 and 28 'with filter material. The bullet area 37 is then for the relative to the plane of the Fig. 4 front conveyor shaft 28 provided with a relatively short granule shaft 40 and with the relative to the plane of the Fig. 4 rear conveyor shaft 28 'provided with a slightly longer granule shaft 40'. The accelerator roller 35 may be formed as a kind of brush roller. Due to the centrifugal force, the granulate is thrown into the respective suction shaft and mixes with the fiber stream. It is preferred if the speeds of the mass flow and of the fed-in granules are different relative to one another. As a result, a good mixing is generated.

Durch den erfindungsgemäßen Aufbau verkleinert sich die Strangmaschine für die Filterstabproduktion erheblich, da direkt an die Vereinzelungsvorrichtung ein Saugstrangförderer angeordnet werden kann. Außerdem verringert sich der Luftverbrauch, da der Transportstrom und der Mischprozess in einem sonst üblichen langen Kanal entfallen.As a result of the structure according to the invention, the stranding machine for the filter rod production decreases considerably, since a suction strand conveyor can be arranged directly on the separating device. In addition, the air consumption is reduced because the transport stream and the mixing process in a usual long channel accounts.

BezugszeichenlisteLIST OF REFERENCE NUMBERS

1010
FaseraufbereitungsvorrichtungFiber processing device
11, 11'11, 11 '
Stauschachtaccumulating shaft
1212
erste Fasersortefirst type of fiber
1313
zweite Fasersortesecond type of fiber
1414
erstes Zuführrohrfirst feed tube
1515
zweites Zuführrohrsecond feed tube
16, 16'16, 16 '
Einzugswalzefeed roller
17, 17'17, 17 '
SchlägerwalzeBeater roller
1919
erster Faserzuführschachtfirst fiber feed shaft
19'19 '
zweiter Faserzuführschachtsecond fiber feed shaft
2020
ZusammenführbereichMerging area
2121
Förderschachtproduction well
2222
Einzugswalzefeed roller
2323
Muldetrough
2424
BlattfederbatterieLeaf spring battery
2525
Walzeroller
2626
Walzeroller
2727
Walzeroller
28, 28'28, 28 '
Saugschachtsuction well
29, 29'29, 29 '
Saugbandsuction belt
3030
Saugstrangförderersuction rod
3131
Ventilatorfan
3232
Fasergemischfiber mixture
3333
Granulatbehältergranule units
3434
Dosierwalzemetering
3535
Beschleunigerwalzeaccelerator roller
3636
Antriebsriemendrive belts
3737
Einschussbereichbullet area
3838
Gabelungcrotch
39, 39'39, 39 '
Teilschachtsupply bay
40, 40'40, 40 '
Granulatschachtgranules shaft
4141
Faservliesnon-woven fabric
4242
Transportlufttransport air
4343
Granulatgranules
4444
Förderrichtungconveying direction
45, 45'45, 45 '
Absaugungsuction

Claims (24)

  1. Method of producing filter rods for the tobacco processing industry, comprising fibres (12, 13, 32) of finite length of at least one fibre type, incorporating a step of separating the fibres (12, 13, 32) in a separating device (22, 25-27), whereby the separated fibres (12, 13, 32) leaving the separating device (22, 25-27) have a motion component opposite the force of gravity in the direction of a conveyor (30), and the conveyer (30) is a suction rod conveyor, and the separating step includes an acceleration of the fibres (32), and the acceleration takes place in or by means of a teasel (22, 25-27).
  2. Method as claimed in claim 1, characterised in that the separated fibres (12, 13, 32) are flung directly out of the separating device (22, 25-27) into a suction shaft (28, 28').
  3. Method as claimed in claim 2, characterised in that the suction rod conveyor (30) adjoins the suction shaft (28, 28').
  4. Method as claimed in one of claims 1 to 3, characterised in that the fibres (12, 13, 32) are mixed with another filter material (43) which has amotion component in the direction of a suction rod conveyor (30), in particular opposite the force of gravity, downstream of the separating device (22, 25-27) in the conveying direction.
  5. Method as claimed in one of claims 2 to 4, characterised in that two suction shafts (28, 28') disposed adjacent to one another are provided or a suction shaft (28) is split into two adjacent partial suction shafts (39, 39').
  6. Method as claimed in one of claims 1 to 5, characterised in that two different sorts of fibre are provided, which are combined and mixed directly prior to the separation step.
  7. Method as claimed in claim 6, characterised in that mixing takes place at the same time as combining.
  8. Method as claimed in one of claims 1 to 7, characterised in that a step of showering to form a fibre web (41) takes place after the separation step.
  9. Method as claimed in one of claims 6 to 8, characterised in that the fibres (12, 13, 32) from two different sorts of fibre are unmixed prior to the step of combining and mixing.
  10. Method as claimed in claim 9, characterised in that the fibres (12, 13, 32) are accumulated unmixed prior to combining.
  11. Method as claimed in one of claims 6 to 10, characterised in that the combined fibres (12, 13, 32) are conveyed to a separating device (22, 25-27) by means of a conveying air flow (42).
  12. Method as claimed in claim 11, characterised in that the separating device (22, 25-27) comprises several rollers (25-27) disposed one after the other, the rotation speeds of which increase in the direction in which the fibres are conveyed.
  13. Device for producing filter rods for the tobacco processing industry, with at least two fibre inlet shafts (19, 19') opening into one shaft (21), and a separating device (22, 25-27) adjoins the one shaft (21), and the separating device (22, 25-27) is designed so that the fibres separated by the separating device (22, 25-27) leave the separating device (22, 25-27) with a motion component opposite the force of gravity in the direction of a conveyor (30), and the separated fibres (12, 13, 32) of finite length can be showered onto the conveyor (30), and the separating device (22, 25-27) comprises several rollers (25-27) disposed one after the other, the rotation speeds of which increase in the direction in which the fibres are conveyed.
  14. Device as claimed in claim 13, characterised in that a device (31) for generating an air flow (42) in the one shaft (21) is provided.
  15. Device as claimed in claim 13 or 14, characterised in that an accumulation shaft (11, 11') is disposed respectively upstream of the at least two fibre inlet shafts (19, 19') or is incorporated in the at least two fibre inlet shafts (19, 19').
  16. Device as claimed in one of claims 13 to 15, characterised in that the one shaft (21) is designed as an accumulation shaft.
  17. Device as claimed in one of claims 14 to 16, characterised in that a ventilator (31) extends through the one shaft (21).
  18. Device as claimed in one of claims 13 to 17, characterised in that at least one roller (25-27) is of a teasel-type design.
  19. Device as claimed in one of claims 13 to 18, characterised in that the conveyor (30) is a suction rod conveyor.
  20. Device as claimed in claim 19, characterised in that a vertically oriented suction shaft (28, 28') terminating in the suction rod conveyor (30) directly adjoins the separating device (22, 25-27) .
  21. Device as claimed in claim 20, characterised in that the suction rod conveyor (30) is disposed at the top end of the suction shaft (28, 28').
  22. Device as claimed in one of claims 19 to 21, characterised in that two suction rod conveyors (30) are provided or two suction belts (29, 29') are provided in one suction rod conveyor (30).
  23. Device as claimed in claim 22, characterised in that two suction shafts (28, 28') are provided.
  24. Device as claimed in claim 22, characterised in that a suction shaft (28) is split into two suction shafts (39, 39') shortly before the suction rod conveyors (30) or the suction rod conveyor (30) with two suction belts (29, 29') in the direction in which the fibres are conveyed.
EP07007588A 2006-04-18 2007-04-13 Manufacture of fibre filters Not-in-force EP1847185B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL07007588T PL1847185T3 (en) 2006-04-18 2007-04-13 Manufacture of fibre filters

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102006018102A DE102006018102A1 (en) 2006-04-18 2006-04-18 Fiber filter production

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EP1847185A1 EP1847185A1 (en) 2007-10-24
EP1847185B1 true EP1847185B1 (en) 2011-08-10

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US (1) US7588524B2 (en)
EP (1) EP1847185B1 (en)
JP (2) JP4614985B2 (en)
CN (1) CN101057709A (en)
AT (1) ATE519387T1 (en)
DE (1) DE102006018102A1 (en)
PL (1) PL1847185T3 (en)

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KR101178251B1 (en) * 2009-11-19 2012-08-29 동양물산기업 주식회사 Apparatus for supplying and adhering particulate matter to cigarette filter
DE102010000680A1 (en) 2010-01-05 2011-07-07 Hauni Maschinenbau AG, 21033 Production of filter strands and filter rod machine
DE102010000677A1 (en) 2010-01-05 2011-07-07 Hauni Maschinenbau AG, 21033 Apparatus for the simultaneous production of at least two fibrous webs for the production of filter rods of the tobacco processing industry
DE102010063564A1 (en) 2010-12-20 2012-06-21 Hauni Maschinenbau Ag Method for producing fibrous web for production of filter bars of tobacco processing industry, involves removing filter material bar with single threads or individual fibers from filter material strips stock
EP3171717B1 (en) * 2014-07-22 2020-10-21 JT International SA Method and apparatus for forming a filter rod

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JP2007282634A (en) 2007-11-01
US7588524B2 (en) 2009-09-15
DE102006018102A1 (en) 2007-10-25
JP4614985B2 (en) 2011-01-19
PL1847185T3 (en) 2012-01-31
JP2010279380A (en) 2010-12-16
EP1847185A1 (en) 2007-10-24
JP5050082B2 (en) 2012-10-17
ATE519387T1 (en) 2011-08-15
US20070243985A1 (en) 2007-10-18
CN101057709A (en) 2007-10-24

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