EP2347874A1 - Method and device for mixing a particle mixture with an adhesive - Google Patents

Method and device for mixing a particle mixture with an adhesive Download PDF

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Publication number
EP2347874A1
EP2347874A1 EP10000663A EP10000663A EP2347874A1 EP 2347874 A1 EP2347874 A1 EP 2347874A1 EP 10000663 A EP10000663 A EP 10000663A EP 10000663 A EP10000663 A EP 10000663A EP 2347874 A1 EP2347874 A1 EP 2347874A1
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EP
European Patent Office
Prior art keywords
particles
adhesive
mixing
mixing device
particle
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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.)
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EP10000663A
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German (de)
French (fr)
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EP2347874B1 (en
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Kronotec AG
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Kronotec AG
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Priority to PL10000663T priority Critical patent/PL2347874T3/en
Priority to ES10000663T priority patent/ES2408968T3/en
Priority to EP10000663.4A priority patent/EP2347874B1/en
Publication of EP2347874A1 publication Critical patent/EP2347874A1/en
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Publication of EP2347874B1 publication Critical patent/EP2347874B1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B27WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
    • B27NMANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
    • B27N1/00Pretreatment of moulding material
    • B27N1/02Mixing the material with binding agent
    • B27N1/0227Mixing the material with binding agent using rotating stirrers, e.g. the agent being fed through the shaft of the stirrer
    • B27N1/0236Mixing the material with binding agent using rotating stirrers, e.g. the agent being fed through the shaft of the stirrer with the stirrers rotating about an horizontal axis, e.g. in consecutive casings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B27WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
    • B27NMANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
    • B27N1/00Pretreatment of moulding material
    • B27N1/02Mixing the material with binding agent
    • B27N1/029Feeding; Proportioning; Controlling

Definitions

  • the invention relates to a method for mixing a mixture of particles of different sizes of wood material with an adhesive.
  • the invention also relates to an apparatus for mixing a particle mixture of particles of different sizes with an adhesive having a mixing device, a particle introduction device for introducing the particles of different sizes into the mixing device and an adhesive introduction device.
  • wood is comminuted depending on the desired application and connected by means of an adhesive in a hot pressing process, for example, to an MDF or HDF, chipboard or OSB board.
  • an adhesive for example, to an MDF or HDF, chipboard or OSB board.
  • the chips or fibers must be coated with the adhesive.
  • Particles which are not made of wood, for example plastic particles, may also be added.
  • the amount of adhesive used is one of the critical process and cost factors and therefore requires permanent optimization.
  • the particles to be glued are introduced on one side by a particle introduction device in a mixing device.
  • a particle introduction device in a mixing device.
  • the introduced particles pass through the mixing device as far as a particle discharge device, where they leave the mixing device again.
  • adhesive is introduced into the mixing device at different points within the mixing device via an adhesive introduction device, for example via nozzles.
  • a particle stream is mixed with the adhesive stream, which does not consist of particles of uniform size.
  • the particle flow has within a certain range a characteristic size distribution, which adversely affects the gluing of the individual particles.
  • the amount of adhesive that glues a single particle depends on its surface area.
  • the important mechanical properties of the later wood-based panels such as the transverse tensile strength, bending strength or lift-off, in particular the large chips and fibers are needed.
  • small particles such as fibers or dusts
  • the adhesive used is not only disadvantageous to large and small Particles are dispersed, too much glue is used overall.
  • the adhesive used is thus not handled economically and the properties of the pressed particles from the coated particles never reach the technically conceivable optimum.
  • the invention is therefore based on the object, so to develop a method and apparatus for mixing a mixture of particles of different sizes of wood material with an adhesive that a better distribution of the adhesive is ensured on the particles of different sizes.
  • the two steps (b) and (c) can in particular also be carried out jointly by mixing the particles with one another, for example in the mixing device, while adhesive is introduced into the mixing device.
  • the particles are different Size both mixed with each other and with the adhesive and thereby glued.
  • the particles of different size are glued for different lengths of time in the mixing device.
  • small particles are mixed with the adhesive for less than large particles. Due to the long residence time of the large particles in the mixing device, it is ensured that they are adequately glued in order later to ensure sufficient stability for a plate pressed from the particles.
  • the smaller particles which are less important for these stability characteristics, are less glued in their shorter time that they are in the mixing device. This results in an optimized gluing and approximately in the way, as if all particle sizes would have been provided separately with adhesive. It is possible to achieve a uniform gluing of all particles or a gluing factor dependent on the particle size and, for example, to glaze large particles more strongly than small particles. This in turn is followed by significantly improved plate properties with simultaneously reduced amount of adhesive used, since the mechanically-technologically important particles have a good bond quality and not, as in conventional methods, clearly contain too little adhesive.
  • the particles of different size are conveyed during mixing in the mixing device, in particular from a particle introduction device to a particle discharge device along a conveying path.
  • small particles are introduced in the conveying direction behind large particles in the mixing device.
  • the adhesive is introduced into the mixing device along the entire conveying path. In this way it is ensured that small particles have to travel a shorter distance within the mixing device along the conveying path than larger particles. If the adhesive is introduced along the entire conveying path, for example via nozzles, The small particles pass less of these nozzles through the shorter distance they travel, so they can also absorb less adhesive.
  • the large particles that cover the entire conveying path within the mixing device come in all places where adhesive is introduced into the mixing device over, and can be optimally glued.
  • the amount of adhesive that is applied to a portion of the conveying path is completely freely adjustable, which also size-dependent gluing factors of the particles can be achieved.
  • the density of the particles of different sizes is preferably between 100 kg / m 3 and 800 kg / m 3 .
  • a device according to the invention for mixing a particle mixture of particles of different sizes with an adhesive is a generic device, which is characterized in that a fractionating device is provided, through which the particles of different size dwell in the mixing device for different lengths of time during operation of the device.
  • the differently long residence time of the particles in the mixing device ensures an optimized distribution of the adhesive between large and small particles.
  • a conveying device by means of which the particles of different size introduced into the particle introduction device can be conveyed to a particle discharge device along a conveying path.
  • the adhesive introduction device is designed in particular as distribution nozzles distributed along the conveying path. This ensures that along the entire conveying path a uniform amount of adhesive is introduced into the mixing device. Alternatively, the amount of adhesive introduced can also vary along the conveying path.
  • the fractionating device is preferably in or in the processing direction the particle introduction device arranged. This can ensure that particles of different sizes are introduced at different points of the conveying path in the mixing device. Due to the fact that small particles are introduced into the mixing device later in the conveying direction than large particles, they do not pass through the entire conveying path and, accordingly, do not pass through all the injection nozzles of the adhesive introduction device. You can thus absorb less adhesive than the large particles that go through the entire conveyor.
  • the fractionating device can also be arranged downstream of the particle introduction device in the processing direction.
  • the particles of any size enter the mixing device at the same location.
  • the fractionator is designed to impart different speeds to particles of different sizes along the conveying path. The fact that in this case smaller particles move faster along the conveying path, their residence time is also reduced in the mixing device and thus ensured that they can not absorb too much adhesive.
  • the fractionator is a fan. If this blower is arranged, for example, in the particle introduction device or in the processing direction in front of it, a lateral air flow is directed to the particle flow, which separates the particles based on size and weight, as is the case, for example, in a classic air separation process. Here, the smaller particles and the dust are deflected more than large particles. If the fan is arranged so that the air flow, for example, flows parallel to the conveying direction, smaller particles are fed later in the conveying direction of the mixing device.
  • the blower can also be arranged inside the mixing device, ie in the processing direction after the particle introduction device. Also in this case, a lateral air flow is directed to the particle stream, which preferably accelerates the particles in the conveying direction. Smaller and lighter particles are accelerated faster than large particles. These consequently move faster than large particles in the conveying direction through the mixing device and thus absorb less adhesive.
  • the fractionating device can also be designed as a rotatably mounted brush.
  • the rotatably mounted brush which is set in rotation during operation of the device, may also be arranged in the processing direction in front of or behind or directly in the particle introduction device.
  • the individual particles are preferably accelerated in the conveying direction, with larger particles are less accelerated, so fly less far. Also in this way it can be ensured that smaller particles are introduced into the mixing device so that they no longer pass through the entire conveying path and thus can absorb less adhesive.
  • a throwing device arranged inside the mixing device in particular a rotating brush, drum or the like, it is ensured, as in the case of the blower, that the particles have a speed which depends on their size in the conveying direction.
  • the fractionator preferably has a sieve.
  • this sieve has openings of different sizes.
  • the arrangement of a sieve is particularly advantageous if the fractionating device is arranged inside or in the processing direction in front of the particle introduction device. In this way it can be ensured that large particles, which were too far distracted too far in the conveying direction, are not introduced with the smaller particles in the mixing device, but slide back along the screen preferably inclined and at the intended location for their size in the mixing device be introduced. In this way, it is ensured that in fact all particles of a certain size, the route provided for them along the conveying path within the mixing device return.
  • the device according to the invention and the method according to the invention consequently provide for an optimized distribution of the amount of adhesive on the individual particles of different sizes and are particularly suitable for all types of wood shredding products, such as fibers, chips or strands and thus also for the production of a wide variety of wood-based materials, such as MDF - or HDF, chipboard or OSB boards.
  • wood-based materials such as MDF - or HDF, chipboard or OSB boards.
  • particles can also be provided with an adhesive which is not made of wood, but for example of a plastic. It is also conceivable to mix particles of different materials.
  • FIG. 1 shows a schematic representation of an apparatus according to a first embodiment of the present invention.
  • a mixing device 2 there is a conveying device 4 with a drive unit 6.
  • the conveying device 4 conveys particles introduced from above through a particle introduction device 8 into the mixing device 2 along the conveying direction F. They are mixed by the conveyor 4 and glued from above by a Klebstoffeinbringvorraum in the form of evenly distributed along the conveying path controllable Beleimungsdüsen 10 with adhesive. The particles thus glued leave the mixing device 2 via a particle discharge device 12.
  • the glue injection nozzles 10 can also be distributed irregularly or adjusted to different spray strengths.
  • a fractionating device 14 is provided, which in FIG. 1 only indicated as a schematic box.
  • the fractionator 14 is in FIG. 1 designed as a blower, which blows along the air flow direction L an air flow in the particle introduction device 8.
  • the particles falling from above into the particle introduction device 8 are deflected by this air flow in the direction of air flow L, which is indicated by different arrows.
  • the heavy particles which are hardly or not deflected by the air flow in the direction of air flow L, on the other hand, pass all or most of the envisaged gluing nozzles 10 on their way to the particle discharge device 12 and are therefore provided with more adhesive than the light particles.
  • FIG. 2 shows a second embodiment of the present invention.
  • the particles are introduced via a particle introduction device 8 in a mixing device 2, in which they are conveyed by a conveyor 4 along the conveying direction F in the direction of the particle discharge device 12, being guided past Beleimungsdüsen 10, is introduced by the adhesive into the mixing device 2.
  • FIG. 2 is on the right edge of the mixing device 2, a fractionating device 14 is provided, which is designed as a fan.
  • the fractionator 14 is in FIG. 2 Consequently, disposed within the mixing device 2 and thus in the processing direction after the particle introduction device 8.
  • FIG. 3 shows a device according to a third embodiment of the present invention. Again, the same reference numerals have been used for the same components.
  • a fractionator 14 as in FIG. 1 provided in the processing direction before the mixing device 2.
  • the fractionating device 14 consists of a fan, which is operated via a fan drive unit 16.
  • an air flow is blown into a particle introduction device 8 along an air flow direction L.
  • the particle introduction device 8 introduced particles of this air flow in the air flow direction L deflected. Again, the light particles are deflected more than the heavy ones.
  • a screen 18 is arranged, through which the deflected particles must pass in order to get into the mixing device 2.
  • the sieve 18 has different sized sieve openings (not shown).
  • the sieve 18 has the smaller sieve openings to the left and the larger sieve openings to the right.
  • the air flow in the air flow direction L the light particles are deflected more to the left and meet there on the part of the screen 18, which has the smaller screen openings.
  • the large particles are deflected by the air flow barely or not at all and hit the right part of the screen 18, which has the larger screen openings.
  • the small particles are deflected further to the left in the direction of the air flow direction L and thus also fall further to the left in the mixing device 2. There, they are conveyed further by a conveyor 4 in the conveying direction F and thereby guided past Beleimungsdüsen 10. Due to the fact that the small particles are guided past fewer gluing nozzles 10 than the larger ones, an optimized gluing is ensured here as well.
  • a device according to a fourth embodiment of the present invention differs from that shown in FIG. 1 shown device in that the fractionator 14 not as a fan, but is designed as a rotating brush, drum or the like.
  • the direction of rotation is indicated by the curved arrow.
  • the brush which rotates in the direction of the arrow, of the fractionating device 14 deflects the particles introduced into the particle introduction device 8 to the left. Again, it holds that light particles continue to fly as heavy, so that they are also introduced farther left into the mixing device 2 and are guided by the conveyor 4 to less glueing nozzles 10.

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Wood Science & Technology (AREA)
  • Forests & Forestry (AREA)
  • Mechanical Engineering (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Dry Formation Of Fiberboard And The Like (AREA)

Abstract

The method involves feeding a stream of different sized wooden particles in a mixing device (2), and applying adhesive on the wooden particles, where the amount of adhesive is adjusted according to the size of the wooden particles. The adhesive coated particles are mixed with each other, and a stream of the adhesive coated particles is discharged from the mixing device. The wooden particles are conveyed from a particle introduction device (8) to a particle discharge device (12) along a conveying path, where the amount of adhesive applied in the mixing device varies along the conveying path. The particle has density of about 100 to 800 kg per cubic-millimeter. An independent claim is also included for a device for mixing a different sized wooden particle mixture with an adhesive.

Description

Die Erfindung betrifft ein Verfahren zum Vermischen eines Gemisches aus Partikeln unterschiedlicher Größe aus Holzwerkstoff mit einem Klebstoff.The invention relates to a method for mixing a mixture of particles of different sizes of wood material with an adhesive.

Die Erfindung betrifft zudem eine Vorrichtung zum Vermischen eines Partikelgemisches aus Partikeln unterschiedlicher Größe mit einem Klebstoff mit einer Mischeinrichtung, einer Partikeleinbringvorrichtung zum Einbringen der Partikel unterschiedlicher Größe in die Mischvorrichtung und einer Klebstoffeinbringvorrichtung.The invention also relates to an apparatus for mixing a particle mixture of particles of different sizes with an adhesive having a mixing device, a particle introduction device for introducing the particles of different sizes into the mixing device and an adhesive introduction device.

Bei der Herstellung von Holzwerkstoffen wird Holz je nach gewünschter Anwendung zerkleinert und mittels eines Klebstoffs in einem Heißpressverfahren, beispielsweise zu einer MDF- oder HDF-, Span- oder OSB-Platte, verbunden. Dazu müssen die Späne oder Fasern mit dem Klebstoff beschichtet werden. Es können auch Partikel, die nicht aus Holz bestehen, beispielsweise Kunststoffpartikel, beigemischt werden.In the production of wood-based materials wood is comminuted depending on the desired application and connected by means of an adhesive in a hot pressing process, for example, to an MDF or HDF, chipboard or OSB board. For this, the chips or fibers must be coated with the adhesive. Particles which are not made of wood, for example plastic particles, may also be added.

Dabei ist die Einsatzmenge an Klebstoff eine der kritischen Prozess- und damit Kostengrößen und bedarf daher permanenter Optimierung.The amount of adhesive used is one of the critical process and cost factors and therefore requires permanent optimization.

Herkömmlicherweise werden die zu beleimenden Partikel auf einer Seite durch eine Partikeleinbringvorrichtung in eine Mischeinrichtung eingebracht. Mit Hilfe so genannter Mischwerkzeuge durchlaufen die eingebrachten Partikel die Mischeinrichtung bis zu einer Partikelaustragsvorrichtung, wo sie die Mischeinrichtung wieder verlassen. Entlang dieses Weges wird innerhalb der Mischeinrichtung über eine Klebstoffeinbringvorrichtung an verschiedenen Stellen Klebstoff, beispielsweise über Düsen, in die Mischeinrichtung eingebracht.Conventionally, the particles to be glued are introduced on one side by a particle introduction device in a mixing device. With the help of so-called mixing tools, the introduced particles pass through the mixing device as far as a particle discharge device, where they leave the mixing device again. Along this path, adhesive is introduced into the mixing device at different points within the mixing device via an adhesive introduction device, for example via nozzles.

Hierbei ist es grundsätzlich möglich, verschiedene Schichten der herzustellenden Holzwerkstoffplatten in separaten Mischeinrichtungen einzeln mit einem Klebstoff zu versehen. So ist es beispielsweise üblich, die Deckschicht einer Spanplatte aus feineren Spänen herzustellen als die Mittelschicht, um sowohl die Oberflächenoptik als auch die Oberflächenrauheit der dann fertigen Platte zu verbessern.In this case, it is basically possible to provide individual layers of the wood-based panels to be produced in separate mixing devices with an adhesive. For example, it is customary to make the top layer of a chipboard of finer chips than the middle layer in order to improve both the surface appearance and the surface roughness of the then finished plate.

Selbst in diesem Fall wird jedoch ein Partikelstrom mit dem Klebstrom vermischt, der nicht aus Partikeln einer einheitlichen Größe besteht. Der Partikelstrom hat innerhalb einer gewissen Bandbreite eine charakteristische Größenverteilung, die sich nachteilig auf die Beleimung der einzelnen Partikel auswirkt.Even in this case, however, a particle stream is mixed with the adhesive stream, which does not consist of particles of uniform size. The particle flow has within a certain range a characteristic size distribution, which adversely affects the gluing of the individual particles.

Die Menge des Klebstoffes, mit dem ein einzelner Partikel beleimt wird, hängt von dessen Oberfläche ab. Zur Erreichung der wichtigen mechanischen Eigenschaften der späteren Holzwerkstoffplatten, wie beispielsweise die Querzugfestigkeit, Biegefestigkeit oder Abhebefestigkeit, werden insbesondere die großen Späne und Fasern benötigt. Da diese im Verhältnis zu ihrer Oberfläche jedoch ein deutlich größeres Volumen haben als kleine Partikel, wie beispielsweise Fasern oder Stäube, weist die spätere Holzwerkstoffplatte bzw. bereits ein aus den Partikel vor dem Verpressen aufgestreuter Kuchen an den Stellen, an denen sich die für die Stabilität wichtigen großen Partikel befinden, eine deutlich kleinere Klebstoffmenge auf als an den Stellen, an denen die zur Stabilität weniger beitragenden kleinen Partikel vorhanden sind. Aufgrund des Verhältnisses des Volumens der Partikel zu ihrer Oberfläche werden kleine Partikel mit vergleichsweise mehr Klebstoff beleimt als große. Dadurch werden die großen Partikel mit deutlich zu wenig Klebstoff beaufschlagt, insbesondere der Feinanteil und der Staub jedoch mit zu hohen Klebstoffmengen versehen.The amount of adhesive that glues a single particle depends on its surface area. In order to achieve the important mechanical properties of the later wood-based panels, such as the transverse tensile strength, bending strength or lift-off, in particular the large chips and fibers are needed. However, since these have a significantly larger volume in relation to their surface than small particles, such as fibers or dusts, the later wood-based panel or already from the particles scattered before compression cake at the points where the stability important large particles, a much smaller amount of adhesive than at the points where the less contributing to the stability of small particles are present. Due to the ratio of the volume of the particles to their surface, small particles are glued with comparatively more adhesive than large ones. As a result, the large particles are subjected to significantly less adhesive, in particular the fine fraction and the dust, however, provided with excessive amounts of adhesive.

Der verwendete Klebstoff wird jedoch nicht nur ungünstig auf große und kleine Partikel verteilt, es wird auch insgesamt zu viel Klebstoff verwendet. Mit dem verwendeten Klebstoff wird also nicht ökonomisch umgegangen und die Eigenschaften der aus den so beleimten Partikeln verpressten Platten erreichen nie das technisch denkbare Optimum.The adhesive used, however, is not only disadvantageous to large and small Particles are dispersed, too much glue is used overall. The adhesive used is thus not handled economically and the properties of the pressed particles from the coated particles never reach the technically conceivable optimum.

Der Erfindung liegt daher die Aufgabe zugrunde, ein Verfahren und eine Vorrichtung zum Vermischen eines Gemisches aus Partikeln unterschiedlicher Größe aus Holzwerkstoff mit einem Klebstoff so weiter zu entwickeln, dass eine bessere Verteilung des Klebstoffs auf den Partikeln unterschiedlicher Größe sichergestellt ist.The invention is therefore based on the object, so to develop a method and apparatus for mixing a mixture of particles of different sizes of wood material with an adhesive that a better distribution of the adhesive is ensured on the particles of different sizes.

Die Erfindung löst die gestellte Aufgabe durch ein gattungsgemäßes Verfahren, das die folgenden Schritte umfasst:

  1. (a) Zuführen der Partikel unterschiedlicher Größe in einem Strom in eine Mischvorrichtung,
  2. (b) Beleimen der Partikel unterschiedlicher Größe mit dem Klebstoff, wobei die Menge des Klebstoffs auf die Größe des jeweiligen Partikels abgestimmt ist,
  3. (c) Vermischen der beleimten Partikel unterschiedlicher Größe
  4. (d) Abführen der vermischten beleimten Partikel unterschiedlicher Größe in einem Strom aus der Mischvorrichtung.
The invention achieves the stated object by a generic method which comprises the following steps:
  1. (a) feeding the particles of different size in a stream into a mixing device,
  2. (b) gluing the particles of different size with the adhesive, wherein the amount of the adhesive is adapted to the size of the respective particle,
  3. (c) mixing the glued particles of different sizes
  4. (d) discharging the mixed glued particles of different size in a stream from the mixing device.

Dadurch, dass alle Partikel unabhängig von ihrer Größe in der gleichen Mischvorrichtung beleimt werden, wird der apparative Aufwand des Verfahrens deutlich reduziert. Dadurch, dass dennoch die auf die jeweiligen Partikel entfallende Klebstoffmenge von der Größe des Partikels abhängt, wird für eine optimale Verteilung des Klebstoffs gesorgt. Die beiden Schritte (b) und (c) können insbesondere auch gemeinsam erfolgen, indem die Partikel beispielsweise in der Mischvorrichtung untereinander vermischt werden, während Klebstoff in die Mischeinrichtung eingebracht wird. Dabei werden die Partikel unterschiedlicher Größe sowohl untereinander als auch mit dem Klebstoff vermischt und dadurch beleimt.The fact that all particles are glued regardless of their size in the same mixing device, the equipment cost of the process is significantly reduced. Due to the fact that the amount of adhesive attributable to the respective particles depends on the size of the particle, optimum distribution of the adhesive is ensured. The two steps (b) and (c) can in particular also be carried out jointly by mixing the particles with one another, for example in the mixing device, while adhesive is introduced into the mixing device. The particles are different Size both mixed with each other and with the adhesive and thereby glued.

Vorzugsweise werden die Partikel unterschiedlicher Größe in Abhängigkeit von ihrer Größe unterschiedlich lange in der Mischvorrichtung beleimt. Insbesondere werden kleine Partikel weniger lange mit dem Klebstoff vermischt als große Partikel. Durch die lange Verweildauer der großen Partikel in der Mischeinrichtung ist sichergestellt, dass diese ausreichend beleimt werden, um später bei einer aus den Partikeln verpressten Platte für ausreichende Stabilitätseigenschaft an zu sorgen. Gleichzeitig werden die kleineren Partikel, die für diese Stabilitätseigenschaften unwichtiger sind, in ihrer kürzeren Zeitspanne, die sie sich in der Mischeinrichtung befinden, weniger beleimt. Dadurch ergibt sich eine optimierte Beleimung und zwar ungefähr in der Art und Weise, als ob alle Partikelgrößen separat mit Klebstoff versehen worden wären. Dabei ist es möglich, eine gleichmäßige Beleimung aller Partikel oder einen von der Partikelgröße abhängigen Beleimungsfaktor zu erreichen und beispielsweise große Partikel stärker zu beleimen als kleine Partikel. Hieraus folgen wiederum deutlich verbesserte Platteneigenschaften bei gleichzeitig verringerter verwendeter Klebstoffmenge, da die mechanisch-technologisch wichtigen Partikel eine gute Verklebungsgüte aufweisen und nicht, wie in herkömmlichen Verfahren, deutlich zu wenig Klebstoff enthalten.Preferably, the particles of different size, depending on their size, are glued for different lengths of time in the mixing device. In particular, small particles are mixed with the adhesive for less than large particles. Due to the long residence time of the large particles in the mixing device, it is ensured that they are adequately glued in order later to ensure sufficient stability for a plate pressed from the particles. At the same time, the smaller particles, which are less important for these stability characteristics, are less glued in their shorter time that they are in the mixing device. This results in an optimized gluing and approximately in the way, as if all particle sizes would have been provided separately with adhesive. It is possible to achieve a uniform gluing of all particles or a gluing factor dependent on the particle size and, for example, to glaze large particles more strongly than small particles. This in turn is followed by significantly improved plate properties with simultaneously reduced amount of adhesive used, since the mechanically-technologically important particles have a good bond quality and not, as in conventional methods, clearly contain too little adhesive.

Die Partikel unterschiedlicher Größe werden beim Durchmischen in der Mischeinrichtung insbesondere von einer Partikeleinbringvorrichtung zu einer Partikelaustragsvorrichtung entlang eines Förderwegs gefördert. Vorteilhafterweise werden kleine Partikel in Förderrichtung hinter großen Partikeln in die Mischeinrichtung eingebracht. Insbesondere wird der Klebstoff entlang des gesamten Förderwegs in die Mischeinrichtung eingebracht. Auf diese Weise ist sichergestellt, dass kleine Partikel eine kürzere Strecke innerhalb der Mischeinrichtung entlang des Förderwegs zurücklegen müssen als größere Partikel. Wird der Klebstoff entlang des gesamten Förderwegs, beispielsweise über Düsen, eingebracht, passieren die kleinen Partikel durch die von ihnen zurückgelegte kürzere Strecke weniger dieser Düsen, sodass sie auch weniger Klebstoff aufnehmen können. Die großen Partikel, die den gesamten Förderweg innerhalb der Mischeinrichtung zurücklegen, kommen hingegen an allen Stellen, an denen Klebstoff in die Mischeinrichtung eingebracht wird vorbei, und können so optimal beleimt werden. Die Klebstoffmenge, die auf einem Teilstück des Förderweges aufgebracht wird, ist völlig frei einstellbar, wodurch auch größenabhängige Beleimungsfaktoren der Partikel erreicht werden können. Die Dichte der Partikel unterschiedlicher Größe liegt vorzugsweise zwischen 100 kg/m3 und 800 kg/m3.The particles of different size are conveyed during mixing in the mixing device, in particular from a particle introduction device to a particle discharge device along a conveying path. Advantageously, small particles are introduced in the conveying direction behind large particles in the mixing device. In particular, the adhesive is introduced into the mixing device along the entire conveying path. In this way it is ensured that small particles have to travel a shorter distance within the mixing device along the conveying path than larger particles. If the adhesive is introduced along the entire conveying path, for example via nozzles, The small particles pass less of these nozzles through the shorter distance they travel, so they can also absorb less adhesive. The large particles that cover the entire conveying path within the mixing device, however, come in all places where adhesive is introduced into the mixing device over, and can be optimally glued. The amount of adhesive that is applied to a portion of the conveying path is completely freely adjustable, which also size-dependent gluing factors of the particles can be achieved. The density of the particles of different sizes is preferably between 100 kg / m 3 and 800 kg / m 3 .

Eine erfindungsgemäße Vorrichtung zum Vermischen eines Partikelgemisches aus Partikeln unterschiedlicher Größe mit einem Klebstoff ist eine gattungsgemäße Vorrichtung, die sich dadurch auszeichnet, dass eine Fraktioniereinrichtung vorgesehen ist, durch die im Betrieb der Vorrichtung die Partikel unterschiedlicher Größe unterschiedlich lange in der Mischeinrichtung verweilen.A device according to the invention for mixing a particle mixture of particles of different sizes with an adhesive is a generic device, which is characterized in that a fractionating device is provided, through which the particles of different size dwell in the mixing device for different lengths of time during operation of the device.

Wie oben bereits dargelegt ist, wird durch die unterschiedlich lange Verweildauer der Partikel in der Mischeinrichtung eine optimierte Verteilung des Klebstoffs zwischen großen und kleinen Partikeln gewährleistet.As already explained above, the differently long residence time of the particles in the mixing device ensures an optimized distribution of the adhesive between large and small particles.

Innerhalb der Mischeinrichtung ist eine Fördereinrichtung vorgesehen, durch die die in der Partikeleinbringvorrichtung eingebrachten Partikel unterschiedlicher Größe zu einer Partikelaustragsvorrichtung entlang eines Förderwegs förderbar sind. Die Klebstoffeinbringvorrichtung ist insbesondere als entlang des Förderweges verteilte Einbringdüsen ausgebildet. Dadurch ist gewährleistet, dass entlang des gesamten Förderwegs eine gleichmäßige Menge Klebstoff in die Mischeinrichtung eingebracht wird. Alternativ kann die eingebrachte Klebstoffmenge auch entlang des Förderweges variieren.Within the mixing device, a conveying device is provided, by means of which the particles of different size introduced into the particle introduction device can be conveyed to a particle discharge device along a conveying path. The adhesive introduction device is designed in particular as distribution nozzles distributed along the conveying path. This ensures that along the entire conveying path a uniform amount of adhesive is introduced into the mixing device. Alternatively, the amount of adhesive introduced can also vary along the conveying path.

Die Fraktioniereinrichtung ist vorzugsweise in oder in Verarbeitungsrichtung vor der Partikeleinbringvorrichtung angeordnet. Dadurch kann gewährleistet werden, dass Partikel verschiedener Größe an verschiedenen Stellen des Förderwegs in die Mischeinrichtung eingebracht werden. Dadurch, dass kleine Partikel in Förderrichtung später als große Partikel in die Mischeinrichtung eingebracht werden, durchlaufen sie nicht den gesamten Förderweg und passieren dementsprechend nicht alle Einbringdüsen der Klebstoffeinbringvorrichtung. Sie können somit weniger Klebstoff aufnehmen als die großen Partikel, die den gesamten Förderweg durchlaufen.The fractionating device is preferably in or in the processing direction the particle introduction device arranged. This can ensure that particles of different sizes are introduced at different points of the conveying path in the mixing device. Due to the fact that small particles are introduced into the mixing device later in the conveying direction than large particles, they do not pass through the entire conveying path and, accordingly, do not pass through all the injection nozzles of the adhesive introduction device. You can thus absorb less adhesive than the large particles that go through the entire conveyor.

Die Fraktioniereinrichtung kann auch in Verarbeitungsrichtung nach der Partikeleinbringvorrichtung angeordnet sein. In diesem Fall gelangen die Partikel jeglicher Größe an derselben Stelle in die Mischeinrichtung. In diesem Fall ist die Fraktioniereinrichtung so ausgebildet, dass sie Partikeln verschiedener Größe unterschiedliche Geschwindigkeiten entlang des Förderwegs verleiht. Dadurch, dass in diesem Fall kleinere Partikel sich schneller entlang des Förderwegs bewegen, wird ebenfalls deren Verweilzeit in der Mischeinrichtung reduziert und somit sichergestellt, dass sie nicht zuviel Klebstoff aufnehmen können.The fractionating device can also be arranged downstream of the particle introduction device in the processing direction. In this case, the particles of any size enter the mixing device at the same location. In this case, the fractionator is designed to impart different speeds to particles of different sizes along the conveying path. The fact that in this case smaller particles move faster along the conveying path, their residence time is also reduced in the mixing device and thus ensured that they can not absorb too much adhesive.

Vorzugsweise ist die Fraktioniereinrichtung ein Gebläse. Wird dieses Gebläse beispielsweise in der Partikeleinbringvorrichtung oder in Verarbeitungsrichtung davor angeordnet, wird ein seitlicher Luftstrom auf den Partikelstrom geleitet, der die Partikel anhand von Größe und Gewicht separiert, wie es beispielsweise bei einem klassischen Windsichtverfahren erfolgt. Hierbei werden die kleineren Partikel und der Staub stärker abgelenkt als große Partikel. Wird das Gebläse so angeordnet, dass der Luftstrom beispielsweise parallel zur Förderrichtung strömt, werden kleinere Partikel in Förderrichtung später der Mischeinrichtung zugeführt.Preferably, the fractionator is a fan. If this blower is arranged, for example, in the particle introduction device or in the processing direction in front of it, a lateral air flow is directed to the particle flow, which separates the particles based on size and weight, as is the case, for example, in a classic air separation process. Here, the smaller particles and the dust are deflected more than large particles. If the fan is arranged so that the air flow, for example, flows parallel to the conveying direction, smaller particles are fed later in the conveying direction of the mixing device.

Das Gebläse kann jedoch auch innerhalb der Mischeinrichtung, in Verarbeitungsrichtung also nach der Partikeleinbringvorrichtung, angeordnet sein. Auch in diesem Fall wird ein seitlicher Luftstrom auf den Partikelstrom geleitet, der die Partikel vorzugsweise in Förderrichtung beschleunigt. Dabei werden kleinere und leichtere Partikel stärker beschleunigt als große Partikel. Diese bewegen sich folglich schneller als große Partikel in Förderrichtung durch die Mischeinrichtung und nehmen somit weniger Klebstoff auf.However, the blower can also be arranged inside the mixing device, ie in the processing direction after the particle introduction device. Also In this case, a lateral air flow is directed to the particle stream, which preferably accelerates the particles in the conveying direction. Smaller and lighter particles are accelerated faster than large particles. These consequently move faster than large particles in the conveying direction through the mixing device and thus absorb less adhesive.

Die Fraktioniereinrichtung kann auch als drehbar gelagerte Bürste ausgebildet sein. Die drehbar gelagerte Bürste, die im Betrieb der Vorrichtung in Rotation versetzt wird, kann ebenfalls in Verarbeitungsrichtung vor oder hinter oder direkt in der Partikeleinbringvorrichtung angeordnet sein. Auch durch die rotierende Bürste werden die einzelnen Partikel vorzugsweise in Förderrichtung beschleunigt, wobei größere Partikel weniger stark beschleunigt werden, also weniger weit fliegen. Auch auf diese Weise kann sichergestellt werden, dass kleinere Partikel so in die Mischeinrichtung eingebracht werden, dass sie nicht mehr den gesamten Förderweg durchlaufen und somit weniger Klebstoff aufnehmen können. Durch eine innerhalb der Mischeinrichtung angeordnete Wurfvorrichtung, insbesondere eine rotierende Bürste, Trommel oder ähnliches wird wie beim Gebläse sichergestellt, dass die Partikel eine von ihrer Größe abhängige Geschwindigkeit in Förderrichtung bekommen.The fractionating device can also be designed as a rotatably mounted brush. The rotatably mounted brush, which is set in rotation during operation of the device, may also be arranged in the processing direction in front of or behind or directly in the particle introduction device. Also by the rotating brush, the individual particles are preferably accelerated in the conveying direction, with larger particles are less accelerated, so fly less far. Also in this way it can be ensured that smaller particles are introduced into the mixing device so that they no longer pass through the entire conveying path and thus can absorb less adhesive. By means of a throwing device arranged inside the mixing device, in particular a rotating brush, drum or the like, it is ensured, as in the case of the blower, that the particles have a speed which depends on their size in the conveying direction.

Die Fraktioniereinrichtung weist vorzugsweise ein Sieb auf. Dieses Sieb hat insbesondere unterschiedlich große Öffnungen. Die Anordnung eines Siebs ist insbesondere dann von Vorteil, wenn die Fraktioniereinrichtung innerhalb oder in Verarbeitungsrichtung vor der Partikeleinbringvorrichtung angeordnet ist. Auf diese Weise kann gewährleistet werden, dass große Partikel, die versehendlich zu weit in Förderrichtung abgelenkt wurden, nicht mit den kleineren Partikeln in die Mischeinrichtung eingebracht werden, sondern entlang des vorzugsweise geneigt angeordneten Siebes zurückrutschen und an der für ihre Größe vorgesehenen Stelle in die Mischeinrichtung eingebracht werden. Auf diese Weise ist sichergestellt, dass tatsächlich alle Partikel einer gewissen Größe die für sie vorgesehene Strecke entlang des Förderwegs innerhalb der Mischeinrichtung zurücklegen.The fractionator preferably has a sieve. In particular, this sieve has openings of different sizes. The arrangement of a sieve is particularly advantageous if the fractionating device is arranged inside or in the processing direction in front of the particle introduction device. In this way it can be ensured that large particles, which were too far distracted too far in the conveying direction, are not introduced with the smaller particles in the mixing device, but slide back along the screen preferably inclined and at the intended location for their size in the mixing device be introduced. In this way, it is ensured that in fact all particles of a certain size, the route provided for them along the conveying path within the mixing device return.

Die erfindungsgemäße Vorrichtung und das erfindungsgemäße Verfahren sorgen folglich für eine optimierte Verteilung der Menge an Klebstoff auf den einzelnen Partikeln verschiedener Größe und sind insbesondere geeignet für alle Arten von Holzzerkleinerungsprodukten, wie beispielsweise Fasern, Spänen oder Strands und damit auch zur Herstellung unterschiedlichster Holzwerkstoffe, wie MDF- oder HDF-, Span- oder OSB-Platten. Natürlich können auch Partikel mit einem Klebstoff versehen werden, die nicht aus Holz sondern beispielsweise aus einem Kunststoff bestehen. Auch Mischungen von Partikeln unterschiedlicher Materialien sind selbstverständlich denkbar.The device according to the invention and the method according to the invention consequently provide for an optimized distribution of the amount of adhesive on the individual particles of different sizes and are particularly suitable for all types of wood shredding products, such as fibers, chips or strands and thus also for the production of a wide variety of wood-based materials, such as MDF - or HDF, chipboard or OSB boards. Of course, particles can also be provided with an adhesive which is not made of wood, but for example of a plastic. It is also conceivable to mix particles of different materials.

Mit Hilfe einer Zeichnung werden nachfolgend verschiedene Ausführungsbeispiele einer erfindungsgemäßen Vorrichtung näher erläutert. Gleiche Bauteile sind dabei in allen Figuren mit gleichen Bezugszeichen versehen.With the aid of a drawing, various embodiments of a device according to the invention are explained in more detail below. The same components are provided in all figures with the same reference numerals.

Es zeigen:

Figur 1
eine schematische Darstellung eines ersten Ausführungsbeispiels einer erfindungsgemäßen Vorrichtung;
Figur 2
eine schematische Darstellung eines zweiten Ausführungsbeispiels einer erfindungsgemäßen Vorrichtung;
Figur 3
eine schematische Darstellung eines dritten Ausführungsbeispiels einer erfindungsgemäßen Vorrichtung und
Figur 4
eine schematische Darstellung eines vierten Ausführungsbeispiels einer erfindungsgemäßen Vorrichtung.
Show it:
FIG. 1
a schematic representation of a first embodiment of a device according to the invention;
FIG. 2
a schematic representation of a second embodiment of a device according to the invention;
FIG. 3
a schematic representation of a third embodiment of a device according to the invention and
FIG. 4
a schematic representation of a fourth embodiment of a device according to the invention.

Figur 1 zeigt eine schematische Darstellung einer Vorrichtung gemäß einem ersten Ausführungsbeispiel der vorliegenden Erfindung. FIG. 1 shows a schematic representation of an apparatus according to a first embodiment of the present invention.

In einer Mischeinrichtung 2 befindet sich eine Fördereinrichtung 4 mit einer Antriebseinheit 6. Durch die Fördereinrichtung 4 werden von oben durch eine Partikeleinbringvorrichtung 8 in die Mischeinrichtung 2 eingebrachte Partikel entlang der Förderrichtung F gefördert. Dabei werden sie von der Fördereinrichtung 4 durchmischt und von oben durch eine Klebstoffeinbringvorrichtung in Form von gleichmäßig entlang des Förderweges verteilten steuerbaren Beleimungsdüsen 10 mit Klebstoff beleimt. Die so beleimten Partikel verlassen die Mischeinrichtung 2 über eine Partikelaustragsvorrichtung 12. Die Beleimungsdüsen 10 können auch unregelmäßig verteilt oder auf unterschiedliche Sprühstärken eingestellt sein.In a mixing device 2 there is a conveying device 4 with a drive unit 6. The conveying device 4 conveys particles introduced from above through a particle introduction device 8 into the mixing device 2 along the conveying direction F. They are mixed by the conveyor 4 and glued from above by a Klebstoffeinbringvorrichtung in the form of evenly distributed along the conveying path controllable Beleimungsdüsen 10 with adhesive. The particles thus glued leave the mixing device 2 via a particle discharge device 12. The glue injection nozzles 10 can also be distributed irregularly or adjusted to different spray strengths.

In der Partikeleinbringvorrichtung 8 ist eine Fraktioniereinrichtung 14 vorgesehen, die in Figur 1 nur als schematischer Kasten angedeutet ist. Die Fraktioniereinrichtung 14 ist in Figur 1 als Gebläse ausgebildet, das entlang der Luftstromrichtung L einen Luftstrom in die Partikeleinbringvorrichtung 8 einbläst. Die von oben in die Partikeleinbringvorrichtung 8 fallenden Partikel, werden von diesem Luftstrom in Luftstromrichtung L abgelenkt, was durch verschiedene Pfeile angedeutet wird.In the particle introduction device 8, a fractionating device 14 is provided, which in FIG. 1 only indicated as a schematic box. The fractionator 14 is in FIG. 1 designed as a blower, which blows along the air flow direction L an air flow in the particle introduction device 8. The particles falling from above into the particle introduction device 8 are deflected by this air flow in the direction of air flow L, which is indicated by different arrows.

Dabei werden leichte Partikel in Figur 1 weiter nach links abgelenkt als schwere Partikel und fallen somit auch weiter links in die Mischeinrichtung 2. Die leichten Partikel fallen durch die sich trichterförmig erweiterte Partikeleinbringvorrichtung 8 hinter die in Förderrichtung F gesehen ersten Beleimungsdüsen 10. Durch die Fördereinrichtung 4 werden alle in die Mischeinrichtung 2 einfallenden Partikel entlang der Förderrichtung F in Richtung auf die Partikelaustragsvorrichtung 12 gefördert, wobei die leichten Partikel an weniger Beleimungsdüsen 10 vorbeigeführt werden. Daher können die leichten Partikel nur eine geringere Menge des Klebstoffs, das durch die Beleimungsdüsen 10 in die Mischeinrichtung 2 eingebracht wird, aufnehmen. Die schweren Partikel, die vom Luftstrom in die Luftstromrichtung L kaum oder gar nicht abgelenkt werden, passieren hingegen auf ihrem Weg zur Partikelaustragsvorrichtung 12 alle oder doch die meisten der vorgesehenen Beleimungsdüsen 10 und werden somit mit mehr Klebstoff versehen als die leichten Partikel.This will be light particles in FIG. 1 The light particles fall through the funnel-shaped widened particle introduction device 8 behind the first Beleimungsdüsen 10 seen in the conveying direction F. By the conveyor 4 are all incident in the mixing device 2 Particles along the conveying direction F in the direction of the Partikelaustragsvorrichtung 12 promoted, wherein the light particles are guided past fewer Beleimungsdüsen 10. Therefore, the light particles can only absorb a smaller amount of the adhesive introduced into the mixer 2 by the gluing nozzles 10. The heavy particles, which are hardly or not deflected by the air flow in the direction of air flow L, on the other hand, pass all or most of the envisaged gluing nozzles 10 on their way to the particle discharge device 12 and are therefore provided with more adhesive than the light particles.

Figur 2 zeigt ein zweites Ausführungsbeispiel der vorliegenden Erfindung. FIG. 2 shows a second embodiment of the present invention.

Für gleiche Bauteile wurden die gleichen Bezugszeichen wie in Figur 1 verwendet. Auch hier werden die Partikel über eine Partikeleinbringvorrichtung 8 in eine Mischeinrichtung 2 eingebracht, in der sie durch eine Fördereinrichtung 4 entlang der Förderrichtung F in Richtung zur Partikelaustragsvorrichtung 12 gefördert werden, wobei sie an Beleimungsdüsen 10 vorbeigeführt werden, durch die Klebstoff in die Mischeinrichtung 2 eingebracht wird.For the same components, the same reference numerals as in FIG. 1 used. Again, the particles are introduced via a particle introduction device 8 in a mixing device 2, in which they are conveyed by a conveyor 4 along the conveying direction F in the direction of the particle discharge device 12, being guided past Beleimungsdüsen 10, is introduced by the adhesive into the mixing device 2.

In Figur 2 ist am rechten Rand der Mischeinrichtung 2 eine Fraktioniereinrichtung 14 vorgesehen, die als Ventilator ausgebildet ist. Die Fraktioniereinrichtung 14 ist in Figur 2 folglich innerhalb der Mischeinrichtung 2 und somit in Verarbeitungsrichtung nach der Partikeleinbringvorrichtung 8 angeordnet.In FIG. 2 is on the right edge of the mixing device 2, a fractionating device 14 is provided, which is designed as a fan. The fractionator 14 is in FIG. 2 Consequently, disposed within the mixing device 2 and thus in the processing direction after the particle introduction device 8.

Anders als in Figur 1 gelangen hier alle Partikel durch die Partikeleinbringvorrichtung 8 an der gleichen Stelle in die Mischeinrichtung 2. Sie werden von der durch die Fraktioniereinrichtung 14 entlang einer Luftstromrichtung L eingebrachten Luftströmung in Förderrichtung F abgelenkt. Auch hier werden die leichten Partikel stärker in Förderrichtung F beschleunigt, als die schweren Partikel. Dadurch ist gewährleistet, dass die leichten Partikel zumindest an den ersten Beleimungsdüsen 10 deutlich schneller vorbeifliegen als wenn sie nur von der Fördereinrichtung 4 in Förderrichtung F bewegt würden. Dadurch ist die Aufnahme von Klebstoff von diesen ersten Beleimungsdüsen 10 äußerst gering. Auch damit ist somit sichergestellt, dass die großen Partikel optimal mit Klebstoff benetzt werden, da sie an allen Beleimungsdüsen 10 mit der von der Fördereinrichtung 4 vorgegebenen Geschwindigkeit vorbeigeführt werden. Da sie, wie in Figur 1 auch, dabei von der Fördereinrichtung 4 durchmischt werden, ist eine allseitige homogene Beleimung aller Partikel mit Klebstoff gewährleistet.Unlike in FIG. 1 Here, all the particles pass through the particle introduction device 8 at the same location in the mixing device 2. They are deflected by the introduced through the fractionator 14 along an air flow direction L air flow in the conveying direction F. Again, the light particles are accelerated more in the conveying direction F, as the heavy particles. This ensures that the light particles, at least at the first gluing nozzles 10, pass much faster than if they were moved only by the conveyor 4 in the conveying direction F. As a result, the absorption of adhesive from these first gluing nozzles 10 is extremely small. This also ensures that the large particles are optimally wetted with adhesive since they are guided past all Beleimungsdüsen 10 with the predetermined speed of the conveyor 4. Since she, as in FIG. 1 Also, while being mixed by the conveyor 4, an all-round homogeneous gluing of all particles is ensured with adhesive.

Figur 3 zeigt eine Vorrichtung gemäß einem dritten Ausführungsbeispiel der vorliegenden Erfindung. Wieder wurden für gleiche Bauteile die gleichen Bezugszeichen verwendet. In Figur 3 ist eine Fraktioniereinrichtung 14 wie in Figur 1 in Verarbeitungsrichtung vor der Mischeinrichtung 2 vorgesehen. Wie in Figur 2 besteht die Fraktioniereinrichtung 14 aus einem Ventilator, der über eine Ventilatorantriebseinheit 16 betrieben wird. Durch die Fraktioniereinrichtung 14 in Figur 3 wird entlang einer Luftstromrichtung L ein Luftstrom in eine Partikeleinbringvorrichtung 8 eingeblasen. Wie in Figur 1 werden die in die Partikeleinbringvorrichtung 8 eingeführten Partikel von diesem Luftstrom in Luftstromrichtung L abgelenkt. Dabei werden wieder die leichten Partikel stärker abgelenkt als die schweren. Innerhalb der Partikeleinbringvorrichtung 8 ist ein Sieb 18 angeordnet, durch das die abgelenkten Partikel hindurch müssen, um in die Mischeinrichtung 2 zu gelangen. Dabei hat das Sieb 18 unterschiedlich große Sieböffnungen (nicht gezeigt). In Figur 3 weist das Sieb 18 nach links hin die kleineren Sieböffnungen und nach rechts die größeren Sieböffnungen auf. Durch den Luftstrom in Luftstromrichtung L werden die leichten Partikel stärker nach links abgelenkt und treffen dort auf den Teil des Siebs 18, der die kleineren Sieböffnungen hat. Die großen Partikel werden vom Luftstrom kaum oder gar nicht abgelenkt und treffen auf den rechten Teil des Siebs 18, der über die größeren Sieböffnungen verfügt. FIG. 3 shows a device according to a third embodiment of the present invention. Again, the same reference numerals have been used for the same components. In FIG. 3 is a fractionator 14 as in FIG. 1 provided in the processing direction before the mixing device 2. As in FIG. 2 the fractionating device 14 consists of a fan, which is operated via a fan drive unit 16. By the fractionator 14 in FIG. 3 an air flow is blown into a particle introduction device 8 along an air flow direction L. As in FIG. 1 become the particle introduction device 8 introduced particles of this air flow in the air flow direction L deflected. Again, the light particles are deflected more than the heavy ones. Within the particle introduction device 8, a screen 18 is arranged, through which the deflected particles must pass in order to get into the mixing device 2. In this case, the sieve 18 has different sized sieve openings (not shown). In FIG. 3 the sieve 18 has the smaller sieve openings to the left and the larger sieve openings to the right. By the air flow in the air flow direction L, the light particles are deflected more to the left and meet there on the part of the screen 18, which has the smaller screen openings. The large particles are deflected by the air flow barely or not at all and hit the right part of the screen 18, which has the larger screen openings.

Sollte nun durch unsauberes Einstreuen oder aufgrund von Stößen zwischen den einzelnen Partikeln ein relativ großes Partikel soweit nach links abgelenkt werden, dass es für die dort im Sieb 18 vorhandenen Sieböffnungen zu groß ist, rutscht er entlang des Siebes 18 nach unten und gelangt so auf den rechten Teil des Siebes 18, wo die Sieböffnungen groß genug sind. Dazu ist das Sieb 18 in Figur 3 geneigt angeordnet.If a relatively large particle is deflected so far to the left due to improper littering or due to collisions between the individual particles, that it is too large for the sieve openings present in the sieve 18, it slides downwards along the sieve 18 and thus reaches the right part of the screen 18, where the screen openings are large enough. For this, the sieve is 18 in FIG. 3 arranged inclined.

Wie in der Ausführungsform gemäß Figur 1 werden auch in der Ausführungsform Figur 3 folglich die kleinen Partikel weiter nach links in Richtung der Luftstromrichtung L abgelenkt und fallen somit auch weiter links in die Mischeinrichtung 2. Dort werden sie durch eine Fördereinrichtung 4 in Förderrichtung F weitergefördert und dabei an Beleimungsdüsen 10 vorbeigeführt. Dadurch, dass die kleinen Partikel an weniger Beleimungsdüsen 10 vorbeigeführt werden als die großen, ist auch hier eine optimierte Beleimung gewährleistet.As in the embodiment according to FIG. 1 are also in the embodiment FIG. 3 Consequently, the small particles are deflected further to the left in the direction of the air flow direction L and thus also fall further to the left in the mixing device 2. There, they are conveyed further by a conveyor 4 in the conveying direction F and thereby guided past Beleimungsdüsen 10. Due to the fact that the small particles are guided past fewer gluing nozzles 10 than the larger ones, an optimized gluing is ensured here as well.

Die in Figur 4 gezeigte Vorrichtung gemäß einem vierten Ausführungsbeispiel der vorliegenden Erfindung unterscheidet sich von der in Figur 1 gezeigten Vorrichtung dadurch, dass die Fraktioniereinrichtung 14 nicht als Gebläse, sondern als rotierende Bürste, Trommel oder ähnliches ausgebildet ist. Die Drehrichtung ist durch den gebogenen Pfeil angedeutet.In the FIG. 4 A device according to a fourth embodiment of the present invention differs from that shown in FIG FIG. 1 shown device in that the fractionator 14 not as a fan, but is designed as a rotating brush, drum or the like. The direction of rotation is indicated by the curved arrow.

Durch die in Pfeilrichtung rotierende Bürste der Fraktioniereinrichtung 14 werden die in die Partikeleinbringvorrichtung 8 eingebrachten Partikel nach links abgelenkt. Auch hier gilt, dass leichte Partikel weiter fliegen als schwere, sodass sie auch weiter links in die Mischeinrichtung 2 eingebracht werden und durch die Fördereinrichtung 4 an weniger Beleimungsdüsen 10 vorbeigeführt werden.The brush, which rotates in the direction of the arrow, of the fractionating device 14 deflects the particles introduced into the particle introduction device 8 to the left. Again, it holds that light particles continue to fly as heavy, so that they are also introduced farther left into the mixing device 2 and are guided by the conveyor 4 to less glueing nozzles 10.

In allen in den Figuren 1 bis 4 gezeigten Ausführungsbeispiel ist somit sichergestellt, dass kleine Partikel weniger lange mit über die Beleimungsdüsen 10 eingebrachtem Klebstoff vermischt werden als die großen Partikel.In all in the FIGS. 1 to 4 In the embodiment shown, it is thus ensured that small particles are mixed with adhesive introduced via the gluing nozzles 10 for less than the large particles.

Durch erfindungsgemäße Vorrichtungen wird somit gewährleistet, dass der Beleimungsfaktor von Partikeln unterschiedlicher Größen von ihrer Größe abhängig gesteuert werden kann. Dazu ist nur noch eine Beleimungsvorrichtung nötig, wodurch Zeit, Platz und Kosten gespart werden.By means of devices according to the invention, it is thus ensured that the gluing factor of particles of different sizes can be controlled depending on their size. All that is needed is a gluing device, which saves time, space and costs.

BezugszeichenlisteLIST OF REFERENCE NUMBERS

FF
Förderrichtungconveying direction
LL
LuftstromrichtungAirflow direction
22
Mischeinrichtungmixing device
44
FördereinrichtungConveyor
66
Antriebseinheitdrive unit
88th
PartikeleinbringvorrichtungPartikeleinbringvorrichtung
1010
BeleimungsdüsenBeleimungsdüsen
1212
PartikelaustragsvorrichtungPartikelaustragsvorrichtung
1414
Fraktioniereinrichtungfractionator
1616
VentilatorantriebseinheitFan drive unit
1818
Siebscreen

Claims (15)

Verfahren zum Vermischen eines Gemisches aus Partikeln unterschiedlicher Größe aus Holzwerkstoff mit einem Klebstoff, das die folgenden Schritte umfasst: (a) Zuführen der Partikel unterschiedlicher Größe in einem Strom in eine Mischvorrichtung (2), (b) Beleimen der Partikel unterschiedlicher Größe mit einem Klebstoff, wobei die Menge des Klebstoffs auf die Größe des jeweiligen Partikels abgestimmt ist, (c) Vermischen der beleimten Partikel unterschiedlicher Größe, (d) Abführen der vermischten beleimten Partikel unterschiedlicher Größe in einem Strom aus der Mischvorrichtung (2). Method for mixing a mixture of particles of different size of wood material with an adhesive, comprising the following steps: (a) feeding the particles of different size in a stream into a mixing device (2), (b) gluing the particles of different size with an adhesive, wherein the amount of the adhesive is adapted to the size of the respective particle, (c) mixing the glued particles of different sizes, (D) discharging the mixed glued particles of different sizes in a stream from the mixing device (2). Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass die Partikel unterschiedlicher Größe in Abhängigkeit von ihrer Größe unterschiedlich lange in der Mischvorrichtung (2) beleimt werden.A method according to claim 1 , characterized in that the particles of different size depending on their size for different lengths of time in the mixing device (2) are glued. Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, dass die Partikel unterschiedlicher Größe in der Mischeinrichtung (2) von einer Partikeleinbringvorrichtung (8) zu einer Partikelaustragsvorrichtung (12) entlang eines Förderwegs gefördert werden.A method according to claim 1 or 2, characterized in that the particles of different size are conveyed in the mixing device (2) from a particle introduction device (8) to a particle discharge device (12) along a conveying path. Verfahren nach einem der Ansprüche 1, 2 oder 3, dadurch gekennzeichnet, dass kleine Partikel in Förderrichtung (F) hinter großen Partikeln in die Mischeinrichtung (2) eingebracht werden.Method according to one of claims 1, 2 or 3, characterized in that small particles are introduced in the conveying direction (F) behind large particles in the mixing device (2). Verfahren nach einem oder mehreren der vorstehenden Ansprüche, dadurch gekennzeichnet, dass der Klebstoff entlang des Förderwegs in die Mischeinrichtung (2) eingebracht wird.Method according to one or more of the preceding claims, characterized in that the adhesive along the conveying path in the mixing device (2) is introduced. Verfahren nach Anspruch 5, dadurch gekennzeichnet, dass der in die Mischeinrichtung (2) eingebrachte Klebstoff entlang des Förderweges variiert.A method according to claim 5, characterized in that in the mixing device (2) introduced adhesive varies along the conveying path. Verfahren nach einem oder mehreren der vorstehenden Ansprüche, dadurch gekennzeichnet, dass die Dichte der Partikel zwischen 100 kg/m3 und 800 kg/m3 beträgt.Method according to one or more of the preceding claims, characterized in that the density of the particles between 100 kg / m 3 and 800 kg / m 3 . Vorrichtung zum Vermischen eines Partikelgemisches aus Partikeln unterschiedlicher Größe mit einem Klebstoff, mit a) einer Mischeinrichtung (2), b) einer Partikeleinbringvorrichtung (8) zum Einbringen der Partikel unterschiedlicher Größe in die Mischvorrichtung (2), c) einer Klebstoffeinbringvorrichtung (10),
dadurch gekennzeichnet, dass eine Fraktioniereinrichtung (14) vorgesehen ist, durch die im Betrieb der Vorrichtung die Partikel unterschiedlicher Größe unterschiedlich lange in der Mischeinrichtung verweilen.
Device for mixing a particle mixture of particles of different sizes with an adhesive, with a) a mixing device (2), b) a particle introduction device (8) for introducing the particles of different sizes into the mixing device (2), c) an adhesive introduction device (10),
characterized in that a fractionating device (14) is provided, through which the particles of different size dwell in the mixing device for different lengths of time during operation of the device.
Vorrichtung nach Anspruch 8, dadurch gekennzeichnet, dass eine Fördereinrichtung (4) innerhalb der Mischeinrichtung (2) vorgesehen ist, durch die die eingebrachten Partikel unterschiedlicher Größe zu einer Partikelaustragsvorrichtung (12) entlang eines Förderwegs förderbar sind.Apparatus according to claim 8, characterized in that a conveying device (4) within the mixing device (2) is provided, through which the introduced particles of different size to a particle discharge device (12) along a conveying path can be conveyed. Vorrichtung nach Anspruch 9, dadurch gekennzeichnet, dass die Klebstoffeinbringvorrichtung als über den Förderweg verteilte Einbringdüsen 10 ausgebildet ist.Apparatus according to claim 9, characterized in that the Klebstoffeinbringvorrichtung is formed as distributed over the conveying Einbringdüsen 10. Vorrichtung nach Anspruch 9 oder 10, dadurch gekennzeichnet, dass die Fraktioniereinrichtung (14) in oder in Verarbeitungsrichtung vor der Partikeleinbringvorrichtung (8) angeordnet ist.Apparatus according to claim 9 or 10, characterized in that the fractionating device (14) is arranged in or in the processing direction in front of the particle introduction device (8). Vorrichtung nach Anspruch 9 oder 10, dadurch gekennzeichnet, dass die Fraktioniereinrichtung (14) in Verarbeitungsrichtung nach der Partikeleinbringvorrichtung (8) angeordnet ist.Apparatus according to claim 9 or 10, characterized in that the fractionating device (14) is arranged downstream of the particle introduction device (8) in the processing direction. Vorrichtung nach einem der Ansprüche 8 bis 12, dadurch gekennzeichnet, dass die Fraktioniereinrichtung (14) ein Gebläse ist.Device according to one of claims 8 to 12, characterized in that the fractionating device (14) is a fan. Vorrichtung nach einem der Ansprüche 8 bis 12, dadurch gekennzeichnet, dass die Fraktioniereinrichtung (14) eine Wurfvorrichtung, insbesondere eine drehbar gelagerte Bürste, Trommel oder ähnliches ist.Device according to one of claims 8 to 12, characterized in that the fractionating device (14) is a throwing device, in particular a rotatably mounted brush, drum or the like. Vorrichtung nach einem der Ansprüche 8 bis 14 dadurch gekennzeichnet, dass die Fraktioniereinrichtung (14) ein Sieb (18) aufweist, das unterschiedlich große Öffnungen hat.Device according to one of claims 8 to 14, characterized in that the fractionating device (14) comprises a sieve (18) having different sized openings.
EP10000663.4A 2010-01-22 2010-01-22 Method and device for mixing a particle mixture with an adhesive Active EP2347874B1 (en)

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PL10000663T PL2347874T3 (en) 2010-01-22 2010-01-22 Method and device for mixing a particle mixture with an adhesive
ES10000663T ES2408968T3 (en) 2010-01-22 2010-01-22 Procedure and equipment for mixing a mixture of particles with an adhesive
EP10000663.4A EP2347874B1 (en) 2010-01-22 2010-01-22 Method and device for mixing a particle mixture with an adhesive

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EP10000663.4A EP2347874B1 (en) 2010-01-22 2010-01-22 Method and device for mixing a particle mixture with an adhesive

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EP2347874B1 EP2347874B1 (en) 2013-04-24

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Publication number Priority date Publication date Assignee Title
CN108621280A (en) * 2018-06-01 2018-10-09 千年舟新材科技集团有限公司 Negative ion flame-retardant sheet machining apparatus
WO2019042760A1 (en) 2017-08-29 2019-03-07 Huntsman International Llc Process for binding lignocellulosic materials using polyisocyanate compositions

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EP0805008A1 (en) * 1996-05-02 1997-11-05 C.M.P. Costruzioni Meccaniche Pomponesco S.p.A. Gluing unit for wood-based panel production plants, and a plant using the gluing unit

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DE1201541B (en) * 1961-07-29 1965-09-23 Draiswerke Ges Mit Beschraenkt Trough mixer with a nozzle for mixing wood chips and other chip-shaped materials
DE1180121B (en) * 1962-08-25 1964-10-22 Baehre Metallwerk K G Process and device for gluing chips
DE1528238A1 (en) * 1965-03-27 1970-05-06 Draiswerke Gmbh Trough mixer for the continuous mixing of wood chips and other chip-shaped materials with binders, dyes or the like.
US3343814A (en) * 1965-06-01 1967-09-26 Bahre Metallwerk K G Fa Device for coating chips with glue
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WO2019042760A1 (en) 2017-08-29 2019-03-07 Huntsman International Llc Process for binding lignocellulosic materials using polyisocyanate compositions
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CN108621280A (en) * 2018-06-01 2018-10-09 千年舟新材科技集团有限公司 Negative ion flame-retardant sheet machining apparatus

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ES2408968T3 (en) 2013-06-24
PL2347874T3 (en) 2013-08-30

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