WO2001066324A1 - Procede et dispositif de production d'un non-tisse - Google Patents

Procede et dispositif de production d'un non-tisse Download PDF

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Publication number
WO2001066324A1
WO2001066324A1 PCT/EP2001/002549 EP0102549W WO0166324A1 WO 2001066324 A1 WO2001066324 A1 WO 2001066324A1 EP 0102549 W EP0102549 W EP 0102549W WO 0166324 A1 WO0166324 A1 WO 0166324A1
Authority
WO
WIPO (PCT)
Prior art keywords
sieve
mixture
fraction
particles
homogenization unit
Prior art date
Application number
PCT/EP2001/002549
Other languages
German (de)
English (en)
Inventor
Hans-Joachim Iredi
Friedrich Schröder
Original Assignee
Binos Technologies Gmbh & Co. Kg
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 Binos Technologies Gmbh & Co. Kg filed Critical Binos Technologies Gmbh & Co. Kg
Priority to AU62083/01A priority Critical patent/AU6208301A/en
Publication of WO2001066324A1 publication Critical patent/WO2001066324A1/fr

Links

Classifications

    • 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
    • B27N3/00Manufacture of substantially flat articles, e.g. boards, from particles or fibres
    • B27N3/08Moulding or pressing
    • B27N3/10Moulding of mats
    • B27N3/14Distributing or orienting the particles or fibres
    • B27N3/146Controlling mat weight distribution
    • 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
    • B27N3/00Manufacture of substantially flat articles, e.g. boards, from particles or fibres
    • B27N3/08Moulding or pressing
    • B27N3/10Moulding of mats
    • B27N3/14Distributing or orienting the particles or fibres

Definitions

  • the invention relates to a method according to the preamble of claim 1 and a device according to the preamble of claim 3.
  • the starting mixture from a dosing hopper falls through the upper run and the lower run at one end of an endless, revolving driving belt onto a first, oscillatingly movable sieve element with a small sieve width.
  • the driver belt is provided with driver elements arranged at a distance from one another in its direction of rotation.
  • Driver elements of the lower run scrape over the first screen element and a subsequent second screen element with a larger screen width.
  • Coarse material that does not pass through the second screen element falls from the rear end of the second screen element onto a conveyor belt.
  • Each sieve element allows a fraction mixture to pass through, which inhomogeneously falls directly onto the mold base or the resulting fleece in such a way that initially finer and later increasingly coarser particles of the fraction mixture are scattered. This leads to an undesirable concentration of fine particles in the cover layers, which are later lost when the sheets made from the fleece are sanded.
  • a chain belt loading for a mixer is known per se from Fig. 63.
  • a chip mix is thrown through the upper and lower runs of the chain belt onto the bottom of a loading housing.
  • the chain belt is provided with driver elements for the chip mixture which are arranged at a distance from one another in its circumferential direction.
  • Driver elements of the lower run scrape across the floor to its rear edge, through which the chip mix is thrown directly into the mixer.
  • the invention has for its object to improve the shaping of the fleece.
  • this object is achieved by the features of claim 1.
  • Glue is preferably used as a binder for the particles, in particular chips, in a manner known per se.
  • the fleece is then fed to a press and pressed into a plate-shaped workpiece.
  • the cover layers on this workpiece have a comparatively high density because of the relatively small particles arranged therein. These cover layers are usually sanded smooth afterwards.
  • this grinding process according to the invention, only comparatively small portions of the finest particles are removed. This is achieved by applying the last, on average finest, fraction mixture as a homogenized top layer of the finest and somewhat coarser particles. at only the outermost part of this last layer is removed from the grinding process mentioned.
  • the particular advantage here is that the surface of the plate produced by grinding contains significantly more fines than in the prior art. This desirably results in higher density and less roughness on the outer surface of the plate created by grinding. Similar advantages result according to the invention for the middle layer, because not only the largest particles but also a homogeneous fraction mixture of these largest particles with smaller particles is present there. As a result, the transverse tensile strength of the plate is increased in a favorable manner.
  • Another advantage of the method according to the invention is that the disadvantages of so-called dust spots on the fleece are avoided. Such dust spots have hitherto arisen from the fact that lumps of dust that form somewhere in the device over time suddenly fall down in an uncontrolled manner and reach the fleece.
  • the fleece as a whole is scattered from the lower cover layer to the middle of the middle layer by a first molding machine and from the middle of the middle layer to the upper cover layer by a second molding machine which is mirror-image to the first molding machine.
  • each group can e.g. have three or four rollers.
  • the surface of each roller can be designed in a suitable manner known per se. Rollers of the same diameter, which are driven at the same angular velocity, are preferably used in each group. The angular velocity is preferably infinitely adjustable. The load on the rollers with the respective fraction mixture can thus be controlled.
  • the rotational speed of the driving belt is preferably infinitely adjustable.
  • Each sieve element preferably has a constant sieve width.
  • the arrangement of the sieve elements below the upper run saves construction height, reduces the fall height and prevents dust formation and segregation of the franking mixtures.
  • the driver elements of the active strand preferably come into scraping contact with the screen elements or form a small gap with them.
  • the sieving effect is improved and a contribution to the self-cleaning of the sieves is made.
  • the screen elements can preferably be moved in an oscillating manner in and against the direction of movement of the active strand.
  • the features of claim 9 prevent dust formation, concentrate the respective fraction mixture and facilitate its task on the downstream roller group. With the features of claim 9, an uncontrolled sieving due to the energy inherent in the falling starting mixture can be prevented.
  • the collecting plate can oscillate with the sieve elements.
  • the features of claim 11 lead to a space-saving arrangement of the discharge conveyor, which is e.g. can be a screw conveyor.
  • the arrangement according to claim 12 is particularly space-saving.
  • two fraction mixtures are generated with little structural effort.
  • the driver elements of the active run can come into contact with the screen or can be guided at a short distance from the screen. This relative setting is selected depending on whether or not scraping the driver elements over the sieve is necessary to keep the sieve openings free.
  • the screen can be driven in particular in and against the direction of movement of the active strand.
  • the features of claim 15 lead to a structurally simple and space-saving fractionation device.
  • the transport rollers can come into contact with the screen or be kept at a short distance from the screen. This depends on whether, in addition to the transport effect of the transport rollers, it is also desired that they should have a special cleaning effect on the screen.
  • the features of claim 17 offer a structurally simple and yet very effective fractionation device.
  • the lifting walls can be raised and lowered alternately or all at the same time.
  • the control of the lifting walls can also be done in such a way that they remain in their lowest position for a relatively long time. In this lowest position, the lifting walls can be in contact with the screen or can be kept at a small distance from the screen.
  • the desired two fraction mixtures can be obtained with little structural effort.
  • the features of claim 18 are used to collect and forward the fraction mixtures.
  • the feed of the starting mixture into the fractionation device is improved.
  • the features of claim 20 offer a very powerful fractionation device for two fraction mixtures.
  • the circumference of the circumferential pockets can be in contact with the screen or can be kept at a short distance from the screen.
  • the peripheral pockets can be formed in a particularly simple and stable manner.
  • FIG. 2 shows a diagram relating to the layer structure of the nonwoven according to FIG. 1,
  • Fig. 6 is a schematic section through yet another embodiment of the device.
  • FIG. 1 shows a device 1 for the continuous production of a nonwoven 2 from glued, fibrous particles 3, in particular chips, of different sizes.
  • An initial mixture 4 of the particles is fed into a dosing bunker 5 and distributed by a group of rotating rake scrapers 6 to form a layer 7 on the upper run 8 of a dosing belt 9.
  • the upper run 8 moves continuously in the direction of an arrow 10 and guides the layer 7 through a weighing unit 11, which measures the weight of the layer 7 over its entire width.
  • the weighing signals can be used in a manner known per se to control and regulate the manufacturing process for the fleece 2.
  • the starting mixture 4 is continuously discharged between the metering belt 9 and a discharge roller 12.
  • the starting mixture 4 falls through an upper run 13 of an endless carrier belt 14 onto an imperforate collecting plate 15 which is fastened to a sieve frame 16.
  • the driver belt 14 runs in the direction of the arrow and has driver elements 17 which are arranged at a distance from one another in its direction of rotation.
  • Driver elements 17 of the upper run 13 scrape over the upper surfaces of the collecting plate 15 and, in alignment with the collecting plate 15, adjoining sieve elements 18, 19 and 20, which are also releasably attached to the sieve frame 16.
  • Each of the sieve elements 18 to 20 has a constant sieve width increasing in a direction of movement 21 of the upper strand 13.
  • the coarse material 25 which also does not pass through the sieve element 20, falls onto a discharge conveyor 27, in this case a screw conveyor, which extends between the upper strand 13 and a lower strand 26 of the driving belt 14.
  • the discharge conveyor 27 discharges the coarse material 25 from the device 1 for further use.
  • the screen frame 16 can be driven in an oscillating manner in the directions of the double arrow 28 by a crank mechanism 29.
  • a crank 30 drives the sieve frame 16 via a connecting rod 31.
  • Each fraction mixture 22 to 24 falls out of its guide housing 32 to 34 through the lower run 26 onto an associated homogenization unit 35, 36 and 37.
  • a mold base 38 is arranged below the homogenization units 35 to 37.
  • the mold base 38 is an endless forming belt 39, the upper strand 40 of which moves in a continuous relative movement 41 relative to the rest of the device 1.
  • Each homogenization unit 35 to 37 has a group 42, 43 and 44 of rollers.
  • the rollers of each group 42 to 44 are arranged with longitudinal axes which are parallel to one another and oriented transversely to the relative movement 41 and can be driven to rotate in the direction of the arrows shown.
  • the gap between the rollers in group 42 is minimal and the gap between the rollers in group 4 is maximum.
  • the gaps between the rollers of group 43 based on the size of the column of groups 42 and 44, can have an average size.
  • the gaps between the rollers of group 43 can also be either the columns of group 42 or the columns of group 44.
  • each partial stream 45 to 47 ultimately consists of a homogeneous mixture of the particle sizes from which the associated fraction mixture 22 to 24 is composed.
  • the device 1 is preceded by a device of the same type, but arranged in mirror image (not shown).
  • This upstream device has already sprinkled a lower cover layer 48 of relatively small particles 3 and approximately half of a middle layer 49 of relatively large particles 3 on the upper strand 40 of the forming belt 39.
  • the forming belt 39 is moved continuously in the direction of the relative movement 41.
  • the homogenized partial streams 47 with the largest particles 3 are first sprinkled on this "half" fleece 2.
  • the rollers of group 44 can be designed as disc rollers known per se. These disc rollers then orient the long chips essentially parallel to the relative movement 41.
  • the properties, in particular the strength properties, of the middle layer 49 in the finished plate to be pressed later can be improved.
  • the partial flows 46 are then sprinkled one after the other onto the layer of the fleece 2 containing the partial flows 47.
  • the partial streams 46 form the transition from the on average largest particles 3 of the middle layer 49 to the on average relatively small particles of an upper cover layer 50 of the fleece 2.
  • This upper cover layer 50 is scattered by the partial streams 45.
  • the thickness 51 of the resulting fleece 2 is shown in FIG. 1.
  • the structure and the layer structure of the fleece 2 are illustrated in FIG. 2.
  • the thickness 51 of the fleece 2 is plotted on the abscissa and the particle size 52 is plotted on the ordinate. 2 shows only one half of the thickness 51 of the fleece 2, namely the lower cover layer 48 and half of the middle layer 49.
  • the remaining half of the middle layer 49 and the upper cover layer 50 according to FIG. 1 can be thought of as a mirror image in FIG. 2 on the right.
  • each fraction mixture 22 to 24 creates a plateau 59, 60 and 61.
  • the average particle size of the associated, homogenized fraction mixture 22 to 24 is over a relatively large part of the thickness 51 of the fleece constant. If a plate has been pressed from a fleece 2 according to the invention and the same outer layer 56 as in the aforementioned prior art according to curve 53 is subsequently ground away, significantly fewer particles of the smallest size are lost.
  • the new outer surface 57 of the lower cover layer 48 after this grinding is then characterized by a point 62 which, owing to the homogenization of the fraction mixture 22, contains a higher proportion of the smallest particles than a corresponding point 63 on the curve 53.
  • the homogenized fraction mixture 24 is present, which not only — like the prior art in point 65 — has particles of the largest size, but also the homogenized fraction mixture 24 of particles the largest size and smaller particles.
  • the device 1 Via the parameters of the device 1 (FIG. 1) it is in your hand to adjust the layer structure of the fleece 2 to the respective application in any way.
  • the franking device has a flat screen 66 which is parallel to the active lower run 26 of the driving belt 14.
  • the sieve 66 is thus arranged below the lower strand 26 and allows the first fraction mixture 22 to pass through to the first homogenization unit 35.
  • the rest of the starting mixture 4 which has not passed through the sieve 66 is thrown behind, in FIG. 3 to the right of the sieve 66 through the driver elements 17 onto the second homogenization unit 36. Part of this remainder is, where appropriate, coarse material 25 which cannot pass through the second homogenization unit 36 and in FIG. 3 at the right end of the second homogenization unit 36 in the e.g. trained as a screw conveyor conveyor 27 is delivered.
  • the fractionation device has a transport drum 69 which receives the starting mixture 4 in peripheral pockets 67 and can be driven to rotate in the direction of an arrow 68.
  • the transport drum 69 is rotatably mounted in a housing 71 about a horizontal longitudinal axis 70.
  • the peripheral pockets 67 are defined by radial driver elements 72, which scrape in a lower section of the transport drum 69 via a cylindrical screen 73.
  • the driver elements 72 can also have a small radial distance from the screen 73.
  • the screen 73 can be driven back and forth pivoting about the longitudinal axis 70 of the transport drum 69 in the directions of the double arrow 74 by a drive, not shown in detail.
  • the screen 73 is shown in broken lines in FIG. 4 in its one end position and in dash-dot lines in its other end position.
  • a rear drop end 75 of the screen 73 is always in FIG. 4 to the right of a separating edge 76 between the guide housings 32 and 33.
  • the sieve 73 allows the first fraction mixture 22 to pass through to the first homogenization unit 35.
  • the rest of the starting mixture 4 which has not passed through the screen 73 is thrown off by the driver elements 72 via the rear end 75 onto the second homogenization unit 36.
  • This remainder comprises the second fraction mixture 23 on the one hand and coarse material 25 on the other hand.
  • the coarse material 25 is passed on top via the group 43 of the homogenizing rollers until it is picked up on the right in FIG ,
  • the device 1 according to FIG. 5 is constructed essentially similarly to that according to FIG. 3. In FIG. 5 only the different areas of the fractionation device are shown.
  • the starting mixture 4 or the layer 7 thus reaches the collecting plate 15 in the direction of the arrow and is removed from there by a first transport roller 77.
  • the first transport roller 77 and subsequent transport rollers 78 to 81 as well as a last transport roller 82 are adjacent to one another and can be driven in the direction of arrows 83 to rotate in the same direction.
  • Longitudinal axes 84 of the transport rollers 77 to 82 are arranged parallel to one another and transversely to the relative movement 41.
  • each transport roller 77 to 82 has two diametrically opposite, radial transport vanes 85 and 86. 5, the transport rollers 77 to 82 are, so to speak, nested one inside the other because the movement paths of the transport wings of adjacent transport rollers 77 to 82 interlock such that the transport wings 85, 86 of adjacent transport rollers 77 to 82 are offset from one another.
  • the transport wings 85, 86 can each scrape over the surface of the screen 66 in their lowest position, but on the other hand can also have a small distance from the surface of the screen 66.
  • the function of the device 1 according to FIG. 5 is otherwise the same as that according to FIG. 3. In the exemplary embodiment according to FIG.
  • the fractionation device has middle lifting walls 88 to 93 which are arranged at a distance 87 from one another in the direction of the relative movement 41 and extend transversely to the relative movement 41.
  • Each lifting wall 88 to 93 can be raised and lowered in accordance with the double arrows 94.
  • a sieve 66 which can be oscillated in the directions of the double arrow 28, is arranged below the lifting walls 89, 91 and 93 in their lowest position.
  • the screen 66 is drawn in Fig. 6 in its left end position with solid lines.
  • the right end position of the screen 66 is indicated by dash-dotted lines in FIG. 6. In the lowest position, the lifting walls 88 to 93 can scrape over the surface of the sieve 66, but on the other hand can also maintain a small distance from the surface of the sieve.
  • the screen 66 is in its right-hand end position, dash-dotted in FIG. 6.
  • the lifting walls 90 to 92 are drawn.
  • the lifting walls 90 and 92 are lowered and the lifting walls 91 and 93 are raised.
  • a quantity of particles 95 is schematically arranged behind the lifting wall 92.
  • the lifting walls 91 and 93 are now also lowered.
  • the screen 66 is then moved to the left.
  • the amount of particles 95 is taken to the left by friction on the sieve 66 until it builds up on the front of the lifting wall 91 according to FIG. 8.
  • the first fraction mixture 22 falls through the sieve 66, as can be seen more clearly in FIG. 6.
  • the lifting walls 90 and 92 are lowered according to FIG. 10 and the screen 66 is moved to the left.
  • the amount of particles 95 is taken to the left and accumulated on the front of the lifting wall 92.
  • the quantity of particles 95 is thus transported from the left to the right across the surface of the sieve 66 in FIGS. 6 to 11.
  • the direction of movement for the quantity of particles 95 is repeatedly changed in the manner described. This leads to a deliberately intensive mixing of the particle quantity 95, so that it can discharge the first fraction mixture 22 very completely through the sieve 66.
  • the second fraction mixture 23 and any coarse material 25 are treated further according to FIG. 6 and FIG. 3.

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Wood Science & Technology (AREA)
  • Forests & Forestry (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Nonwoven Fabrics (AREA)

Abstract

La présente invention concerne un procédé et un dispositif de production d'un non-tissé. Selon ce procédé, un mélange initial (4), constitué de particules (3) de tailles différentes, est projeté, de manière dosée, à travers un brin supérieur (13) d'une bande d'entraînement (14), sur une plaque de réception (15). Cette plaque de réception (15) oscille (28) conjointement avec des éléments filtre (18, 19, 20). Chaque élément filtre laisse passer un mélange de fractions (22, 23, 24) qui traverse le brin inférieur (26) de la bande d'entraînement (14) et tombe sur une unité d'homogénéisation associée (35, 36, 37). Le mélange de fractions y est alors agité et homogénéisé. Le mélange de fractions homogénéisé est divisé en flux partiels (45, 46, 47) au moyen de groupes de cylindres (42, 43, 44) des unités d'homogénéisation, ces flux partiels étant dispersés les uns après les autres sur le non-tissé en formation (2).
PCT/EP2001/002549 2000-03-10 2001-03-07 Procede et dispositif de production d'un non-tisse WO2001066324A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU62083/01A AU6208301A (en) 2000-03-10 2001-03-07 Method and device for producing a nonwoven

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10011808.9 2000-03-10
DE2000111808 DE10011808C1 (de) 2000-03-10 2000-03-10 Verfahren und Vorrichtung zur Herstellung eines Vlieses

Publications (1)

Publication Number Publication Date
WO2001066324A1 true WO2001066324A1 (fr) 2001-09-13

Family

ID=7634292

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2001/002549 WO2001066324A1 (fr) 2000-03-10 2001-03-07 Procede et dispositif de production d'un non-tisse

Country Status (3)

Country Link
AU (1) AU6208301A (fr)
DE (1) DE10011808C1 (fr)
WO (1) WO2001066324A1 (fr)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1256426A1 (fr) * 2001-05-11 2002-11-13 Siempelkamp Maschinen- und Anlagenbau GmbH & Co. KG Dispositif pour répandre des particules, particulièrement copeaux de bois, fibres de bois ou semblable sur une bande transporteuse
DE20203427U1 (de) * 2002-03-02 2003-04-17 BINOS TECHNOLOGIES GmbH & Co. KG, 31832 Springe Vorrichtung zur Herstellung eines Vlieses
DE10163054A1 (de) * 2001-12-21 2003-07-17 Siempelkamp Gmbh & Co Streugutanlage zum Streuen von Streugut, insbesondere beleimten Holzspänen, Holzfasern, oder dergleichen auf einen Streubandförderer
DE10224497A1 (de) * 2002-05-31 2003-12-11 Dieffenbacher Gmbh Maschf Vorrichtung zur Längsorientierung von länglichen Holzspänen
US7004300B2 (en) 2002-07-08 2006-02-28 Maschinenfabrik J. Dieffenbacher Gmbh & Co. Adjustable disc roll for longitudinally orienting elongated wood chips
WO2011095356A1 (fr) * 2010-02-05 2011-08-11 Dieffenbacher Gmbh + Co. Kg Procédé et installation de fabrication d'un mat de matériau granulaire constitué d'au moins une couche distribuée et mat de matériau granulaire destiné à être comprimé dans une presse au cours de la fabrication de panneaux en matériau dérivé du bois (l)
WO2011095357A1 (fr) * 2010-02-05 2011-08-11 Dieffenbacher Gmbh + Co. Kg Procédé et installation de réalisation d'une nappe de matière particulaire à partir d'au moins une couche de matière particulaire, et nappe de matière particulaire à comprimer dans une presse au cours de la réalisation de plaques en matériau dérivés du bois
CN107345321A (zh) * 2017-07-28 2017-11-14 贵州金州兔产业有限公司 一种新型兔毛分梳机
CN108483055A (zh) * 2018-04-16 2018-09-04 广西路桥工程集团有限公司 一种沥青搅拌站冷骨料在线筛分装置
CN108914255A (zh) * 2018-07-04 2018-11-30 安徽万利达羽绒制品有限公司 一种羽绒加工用筛分装置

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US3071822A (en) * 1959-03-03 1963-01-08 Bowater Board Company Method and apparatus for forming a mat
DE2847109A1 (de) * 1978-10-30 1980-05-14 Baehre & Greten Vorrichtung zum streuen eines vlieses
US5404990A (en) * 1994-08-12 1995-04-11 Macmillan Bloedel Limited Vane type orienter
EP0860254A1 (fr) * 1997-02-07 1998-08-26 Sunds Defibrator Loviisa Oy Procédé et appareil pour la fabrication d'une ébauche pour un produit structurel, et produit ainsi préparé
WO1998040173A1 (fr) * 1997-03-12 1998-09-17 Pal S.R.L. Dispositif a rouleaux servant a separer des granulats et des particules presentant differentes granulometries, et machine de formation correspondante mettant en oeuvre ce dispositif
WO1998047677A1 (fr) * 1997-04-17 1998-10-29 Kvaerner Panel Systems Gmbh Maschinen- Und Anlagenbau Dispositif pour fractionner et disseminer en particulier des particules fibreuses

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3071822A (en) * 1959-03-03 1963-01-08 Bowater Board Company Method and apparatus for forming a mat
DE2847109A1 (de) * 1978-10-30 1980-05-14 Baehre & Greten Vorrichtung zum streuen eines vlieses
US5404990A (en) * 1994-08-12 1995-04-11 Macmillan Bloedel Limited Vane type orienter
EP0860254A1 (fr) * 1997-02-07 1998-08-26 Sunds Defibrator Loviisa Oy Procédé et appareil pour la fabrication d'une ébauche pour un produit structurel, et produit ainsi préparé
WO1998040173A1 (fr) * 1997-03-12 1998-09-17 Pal S.R.L. Dispositif a rouleaux servant a separer des granulats et des particules presentant differentes granulometries, et machine de formation correspondante mettant en oeuvre ce dispositif
WO1998047677A1 (fr) * 1997-04-17 1998-10-29 Kvaerner Panel Systems Gmbh Maschinen- Und Anlagenbau Dispositif pour fractionner et disseminer en particulier des particules fibreuses

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1256426A1 (fr) * 2001-05-11 2002-11-13 Siempelkamp Maschinen- und Anlagenbau GmbH & Co. KG Dispositif pour répandre des particules, particulièrement copeaux de bois, fibres de bois ou semblable sur une bande transporteuse
US6780002B2 (en) * 2001-05-11 2004-08-24 Siempelkamp Maschinen- Und Anlagenbau Gmbh & Co. Kg Spreader for wood chips, wood particle and sawdust
DE10163054A1 (de) * 2001-12-21 2003-07-17 Siempelkamp Gmbh & Co Streugutanlage zum Streuen von Streugut, insbesondere beleimten Holzspänen, Holzfasern, oder dergleichen auf einen Streubandförderer
DE10163054B4 (de) * 2001-12-21 2004-01-08 G. Siempelkamp Gmbh & Co. Streugutanlage zum Streuen von Streugut, insbesondere beleimten Holzspänen, Holzfasern oder dergleichen, auf einen Streubandförderer
DE20203427U1 (de) * 2002-03-02 2003-04-17 BINOS TECHNOLOGIES GmbH & Co. KG, 31832 Springe Vorrichtung zur Herstellung eines Vlieses
DE10224497A1 (de) * 2002-05-31 2003-12-11 Dieffenbacher Gmbh Maschf Vorrichtung zur Längsorientierung von länglichen Holzspänen
US7004300B2 (en) 2002-07-08 2006-02-28 Maschinenfabrik J. Dieffenbacher Gmbh & Co. Adjustable disc roll for longitudinally orienting elongated wood chips
WO2011095357A1 (fr) * 2010-02-05 2011-08-11 Dieffenbacher Gmbh + Co. Kg Procédé et installation de réalisation d'une nappe de matière particulaire à partir d'au moins une couche de matière particulaire, et nappe de matière particulaire à comprimer dans une presse au cours de la réalisation de plaques en matériau dérivés du bois
WO2011095356A1 (fr) * 2010-02-05 2011-08-11 Dieffenbacher Gmbh + Co. Kg Procédé et installation de fabrication d'un mat de matériau granulaire constitué d'au moins une couche distribuée et mat de matériau granulaire destiné à être comprimé dans une presse au cours de la fabrication de panneaux en matériau dérivé du bois (l)
CN102802895A (zh) * 2010-02-05 2012-11-28 迪芬巴赫机械工程有限公司 在生产木材板的过程中用于生产由至少一个散布的层构成的散布材料垫的方法和设备以及用于在压力机内压制的散布材料垫
CN102821920A (zh) * 2010-02-05 2012-12-12 迪芬巴赫机械工程有限公司 在生产木材板的过程中用于生产由至少一个散布层构成的散布材料垫的方法和设备以及用于在压力机内压制的散布材料垫
CN102802895B (zh) * 2010-02-05 2016-08-03 迪芬巴赫机械工程有限公司 用于生产散布材料垫的方法和设备以及散布材料垫
CN107345321A (zh) * 2017-07-28 2017-11-14 贵州金州兔产业有限公司 一种新型兔毛分梳机
CN108483055A (zh) * 2018-04-16 2018-09-04 广西路桥工程集团有限公司 一种沥青搅拌站冷骨料在线筛分装置
CN108483055B (zh) * 2018-04-16 2024-03-29 广西路桥工程集团有限公司 一种沥青搅拌站冷骨料在线筛分装置
CN108914255A (zh) * 2018-07-04 2018-11-30 安徽万利达羽绒制品有限公司 一种羽绒加工用筛分装置
CN108914255B (zh) * 2018-07-04 2021-08-13 安徽万利达羽绒制品有限公司 一种羽绒加工用筛分装置

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