Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
  • B27N—MANUFACTURE 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
  • B27N1/00—Pretreatment of moulding material
  • B27N1/02—Mixing the material with binding agent
  • B27N1/0227—Mixing the material with binding agent using rotating stirrers, e.g. the agent being fed through the shaft of the stirrer
  • B27N1/0254—Mixing the material with binding agent using rotating stirrers, e.g. the agent being fed through the shaft of the stirrer with means for spraying the agent on the material before it is introduced in the mixer

Definitions

• the invention relates to a process for gluing fibers that are used to produce a panel from a wood-based material, and to a device for carrying out the process.
• WO 03/01 3808 and FIG. 3 illustrate a process for producing a plate in the overall context.
• Hardwood or softwood in the form of trunks, branches and / or sawmill and industrial wood are used as the starting material.
• the wood is first shredded into chips with a size of approximately 20 x 5 mm in a shredding device 31.
• These schnitzel can also come directly from the forest or from sawmills. They can be screened to make them too small or too big
• the chips are the right size, they can be washed to remove foreign objects (especially sand and earth). In this way, cutting and other tools are spared and not damaged in the later manufacturing and processing process.
• Sawdust which is placed in a silo 32 is advantageously used.
• the wood components are fed from the shredding device 31 and from the silo 32 to a funnel-shaped pre-steam container by means of conveyor belts.
• the feed is typically in the ratio of about 6: 4 (60% by weight of chips, 40% by weight of sawdust). In this way, sawdust is also used. This further reduces costs. Resource resources are conserved.
• the proportion of chips should predominate, since this creates fibers and later fiber mats that stabilize mechanically.
• the wood components are mixed, pre-steamed and heated to 60 to 70 ° C.
• the wood components are then fed to a cooker 34, for example by means of a stuffing screw.
• the wood components are about 2 to 3 minutes at a pressure of 1 1 cooked to 1 6 bar and a temperature of 1 40 to 1 80 ° C. Pressure and temperature are selected so that they split into liquid and solid wood components.
• the liquid constituents are separated from the solid and fed to a line 36 which is gas-tightly connected to the cooker 34.
• the solid wood components are fed to a fiberizing machine 36 (refiner or defibrator).
• the defibrator 36 typically includes a stator and a rotor that are driven by a motor.
• the solid wood components are broken down into fibers.
• the fibers which are mixed with sawdust in one embodiment, are pneumatically fed to a drying tube 37.
• fibers are spoken of independently.
• the drying tube 37 the fibers are dried at 160 to 220.degree. Drying is relatively quick and inexpensive because the liquid wood components have already been removed.
• the fibers reach cyclones 38 from the drying tube. Here the steam is separated. The fibers are led out below.
• the temperature of the fibers is then typically 50 ° C.
• the fibers are then mechanically glued in gluing devices 39 at comparatively cool temperatures.
• the subsequently glued fibers typically have a temperature of 35 to 40 ° C.
• the glued fibers enter one or more sifting devices 40.
• the sifting devices 40 comprise heating devices in order to heat the fibers to 55 to 60.degree. Increasing the temperature is advantageous if the plates are to be pressed at temperatures of 80 ° C, for example.
• the pressing step can be accelerated in this way since the desired temperature does not have to be reached exclusively by means of the heated press. Shorter press times lead to larger production capacities or lower procurement costs for the presses with rotating belts, as these can then be shorter. The space requirement for such presses is also less. This further saves costs.
• the pre-glued fibers are supplied to one or more separating devices 41.
• the pre-glued fibers get from the separators 41 g to a scattering 42.
• the scattering 42 places the pre-glued fibers on a conveyor belt.
• the conveyor belt leads the fibers to a pre-press 44.
• the fibers are pre-pressed and thus compressed.
• the pre-press comprises circulating belts, between which the fibers are fed and thereby pressed.
• the fibers then pass through a forming line 45 which has various facilities which ensure that the fibers are in the desired shape.
• the molding line leads to an evaporation device 46.
• the fibers are evaporation from above and / or below.
• the fibers can be divided parallel to the conveyor belt and thus vaporized in the "inside".
• the fibers finally reach the main press 47, which consists of two rotating steel belts pressed against each other.
• the pressing takes place, for example, at 80 ° C.
• the plates are then pressed using a Saw device 48 is sawn and fed to a holding device 49.
• the plates are held in the holding device in such a way that they do not touch each other.
• the plates are cooled in this way.
• the separated liquid constituents which were fed to line 35 are cooled within the gas-tight system Once these liquid constituents have been adequately cooled, they are either disposed of or fed to the gluing device 39.
• the plates are then further processed, for example into panels, and the plates are then coated with papers, for example, and the layer system is fed to a press.
• the layer system is pressed in the press at temperatures above 1,50 ° C, for example at temperatures between 180 ° C and 230 ° C.
• the resins used then harden.
• the panel is sawn further and provided with coupling elements by milling.
• the panels can serve as a covering for walls or floors. If these are used as floor covering, they are
• WO 03/01 3808 discloses gluing of already dried fibers by forming fibers into a mat. Glue is then sprayed onto this mat. The glue gets onto the fibers in the form of droplets.
• a gluing device for the application of glue to fibers and the subsequent production of fiberboard is known from the document EP 0 744 259 A2.
• a process for the production of boards from a wood-based material can be found in US Pat. No. 5,554,330.
• GB 791, 554 discloses a method for mixing solid and liquid components.
• a device for the continuous gluing of wood chips can be found in the document DE 41 1 5 047 CI.
• the object of the invention is the creation of a method with which inexpensive high-quality plates of the type mentioned can be produced.
• the object of the invention is also to provide a device for performing the method.
• a device for performing the method comprises the features of the subclaim. Advantageous refinements result from the subordinate claims.
• the glue is applied to the fibers at relatively low temperatures of preferably 20 to 40 ° C.
• glue is not only sprayed on, but before it is applied to the Fibers atomized or nebulized. Instead of relatively large drops, the glue is sprayed onto the fibers.
• atomization is achieved in particular by conveying glue under very high pressure until it emerges through nozzles. The glue then emerges under very high pressure
• High pressure nozzles The outlet pressure is then preferably 1 5 bar to 250 bar, particularly preferably 40 to 90 bar.
• the flow rate per nozzle is then preferably about 1.3 to 1.4 l / min in order to achieve high flow rates on the one hand and to ensure nebulization in the sense of the invention.
• compressed air is fed in in addition to the glue, so as to ensure at relatively large delivery rates of 1.3 to 1.4 l / min per nozzle that edge areas at the outlet cone from the nozzles are atomized in the sense of the invention .
• the compressed air is fed to the nozzles at a pressure of, for example, about 2 bar.
• the water content in the glue can be reduced by the present invention, in particular when using a glue which consists entirely or predominantly of urea resin.
• the glue content in the glue-water mixture can now be 45 to 65% by weight.
• the glue content is preferably 50 to 60% by weight. If the glue-coated fibers are pressed, the glue hardens faster. It can do that
• the high glue pressure is advantageously generated by means of a high-pressure pump, the speed of which can be regulated. By regulating the speed, the degree of atomization of the glue can advantageously be set very precisely. In contrast to the state of the art, there is a very sensitive dosing and optimization option available during the application of glue. The ratio of fibers to applied glue can thus be further optimized. Production costs can be further reduced by minimizing the amount of glue, since the amount of glue in particular contributes significantly to the manufacturing costs.
• the solid wood components are therefore fed to a belt weigher before gluing the solid wood components are transported on one side by means of a circulating conveyor belt, on the other hand they are weighed. This provides information on the amount of glue to be added to the solid wood components of the wood in the subsequent step.
• the solid wood components are transferred to the subsequent facility using the belt scale.
• Weight fluctuations of the supplied solid wood components are recorded during transport, registered and, in one embodiment, stored. This data is processed and can serve as a control variable for the amount of glue that is subsequently applied to the solid wood components.
• the transport speed in the belt weigher is controlled so that a uniform amount of solid wood components is fed to the subsequent gluing device (device in which the solid wood components are provided with glue).
• a constant amount of material is supplied to the following devices.
• the weight of the solid wood components which can be in the form of fibers or chips, can be carried out in the smallest steps and enables the solid wood components to be fed evenly with an accuracy of, for example, ⁇ 1%.
• Wood components are in the form of fibers. Fibers tend to bulge together like wadding. It is then difficult to evenly distribute the glue on the fibers.
• the gluing is therefore carried out in a mixer in which glue and solid wood components are mixed with one another. After drying the solid wood components, they are distributed over a large area in one embodiment of the invention and a kind of curtain or mat is formed. This is particularly the case when the solid wood components are in the form of fibers, since a mat or a curtain can be easily formed from them. Glue is then nebulized and fed to the curtain in nebulized form.
• the formation of a curtain ensures that the glue is evenly distributed over the solid wooden components. This is particularly the case when the solid wood components are in the form of fibers.
• a curtain or mat formed from solid wooden components is introduced into the mixer.
• the curtain or mat is then fed with the glue mist via high-pressure nozzles.
• the curtain or mat is then preferably passed through the mixer without contact.
• the contactless implementation advantageously prevents the solid wooden components from sticking to the walls.
• the glue is blown into the dried solid wood components of the wood, in particular at a temperature of 35 to 70 ° C., preferably at a temperature of up to 60 ° C. This ensures that the glue reaches a dry outer skin. So it is activated minimally. In this way it is improved that the subsequent mixture of solid wood components and glue does not stick to transport devices and equipment, for example inside the mixer.
• the glue mist is atomized together with heated compressed air and this mist is the dried one solid wood components, e.g. fibers or chips added.
• the warm air which is introduced into the mixer together with the glue and the dried solid wood components, for example, activates glue a little on its surface. This suitably counteracts the adherence of solid wood components to subsequent equipment, for example mixer walls.
• Reactive resins that is to say resins with constituents which can chemically build up a network
• reactive resins are: solid or liquid phenol resins, amino resins such as urea resins, melamine resins, acrylate resins, epoxy resins and / or polyester resins.
• a calender press is preferably used for the pressing of the fibers provided with glue, in particular for the production of plates with a thickness of less than 10 mm.
• the gluing according to the invention is particularly well suited, in particular, in the production of boards with the specified thickness.
• a calender press with a rotating press belt as disclosed for example in DE 20303207 U l, enables particularly high processing speeds.
• the high processing speed is of particular advantage in order to now process the unusually well-distributed glue very quickly and thus to avoid undesired premature activation of the glue.
• FIG. 1 shows a section through a belt scale 1 and a subsequent mixer 2. As indicated by the arrow 3, dried fibers which were produced from wood chips are fed to the belt scale 1 via an opening 4 in a housing 4. A slope 5 directs the incoming fibers onto the belt of the belt scale.
• the belt scale detects and controls the amount of material that is transported in the direction of the three rollers 6.
• the three rollers 6 are arranged one above the other and offset such that they enclose an acute angle alpha with the belt scale 1.
• the fibers on the belt scale come into this acute angle. They pass through the rotating rollers 6.
• a curtain is formed from the fibers, which, due to gravity, is transported vertically downwards along the arrow 7. The curtain thus enters the mixer 2, namely between a plurality of nozzles 8 and tools 9.
• the mixer consists of a tubular housing.
• the housing is formed by a double wall 1 0 and 1 1. Central inside the
• An axis 1 2 is arranged on the housing, on which the tools 9 are fastened.
• a tool 9 forms a right i angle with the axis 1 2.
• Four rudder blade-like tools 9 are combined in a star shape. Several of these combined tools are attached to the axis 12 at uniform intervals. The front one
• the area where the curtain made of fibers is inserted is free of tools. This ensures that there is a sufficiently large distance between the tools 9 and the nozzles 8.
• This distance is provided so that it emerges from the nozzles 8
• the diameter of the mixer housing corresponds to the width of the opening through which the fiber curtain is introduced into the mixer.
• the width of the curtain is adapted to the width of the opening.
• the high pressure nozzles 8 are arranged in a semicircle around the axis 1 2 in an upper area and are both with Glue in the range of 40 to 90 bar and fed with compressed air.
• the high-pressure nozzles used are designed as single-substance nozzles or also as two-substance nozzles if both glue and compressed air are to be fed to a nozzle.
• the glue pressure of 40 to 90 bar is swirled as it emerges from the nozzle. Leaving the intended very narrow opening gap, the glue escaping "explodes" into a mist.
• the nozzles are designed in such a way that glue is atomized even at a pressure of 250 bar.
• the glue pressure is provided by a pump, the output of which is controlled can and in particular by regulating the speed.
• the curtain is uniformly provided with nebulous glue and, on the other hand, the nebulized glue emerging from the nozzles 8 does not directly hit parts of the mixer.
• a distance is arranged between the nozzles 8 and the housing 1 0, 1 1, so that a type of annular gap is formed. Air is sucked in through this annular gap, which additionally ensures that a glue mist is created.
• the curtain provided with glue (in other words a mat made entirely or predominantly of fibers) is transported by the air flow parallel to the axis 1 2 through the mixer 2. The axis rotates during transport and thus the tools 9.
• the glue is further mixed with the fibers.
• a cooled liquid is introduced between the two walls 1 0 and 1 1 of the double wall in order to allow a layer of condensation to form on the inside of the mixer on its inside walls.
• FIG. 2 shows a top view of the mixer parallel to axis 1 2. For the sake of clarity, only two tools 9 are shown. A single-row, semicircular arrangement of the nozzles in the upper region is particularly illustrated with the aid of FIG. In particularly advantageous embodiments, the invention comprises one or more steps which are disclosed by FIG. 3 in conjunction with the associated description.
• Glue is fed to a pump 51 via a line 50.
• the performance of the pump can be regulated.
• Glue is transported further by the pump 51, then passes a first shut-off valve 52 and finally arrives at the shut-off valves 53 and 54. If the glue passes through the shut-off valve 53, it then flows through a flow meter 55. This serves for control and / or controlling the amount of glue that is transported.
• the glue can be passed via a parallel line 56 in order to allow large flow rates.
• the glue reaches a distributor 57, from which the glue is directed in the direction of the high-pressure nozzles 58 and 59.
• the glue emerges in atomized form from the high-pressure nozzles 58 and 59.
• compressed air is brought to the side of the nozzles.
• the compressed air is fed into a line 60, passes shut-off valves 61, 62, 63, 64, which serve for the individual control of the supplied compressed air, and finally emerges adjacent to the high-pressure nozzles 58 and 59.
• the compressed air is blown in the direction of the emerging glue mist.
• the glue mist is swirled further.
• Another supply line 65 is used to supply warm water with which the lines, valves and nozzles can be cleaned.
• the high-pressure nozzles can be closed with compressed air in order to be able to close the nozzles when the system is at a standstill and to prevent glue from escaping.

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• 2003
  • 2003-09-12 SI SI200330942T patent/SI1663593T1/sl unknown
  • 2003-09-12 CA CA002537981A patent/CA2537981A1/fr not_active Abandoned
  • 2003-09-12 WO PCT/EP2003/010142 patent/WO2005035213A1/fr active IP Right Grant
  • 2003-09-12 AT AT03818847T patent/ATE371528T1/de not_active IP Right Cessation
  • 2003-09-12 CN CNA038270609A patent/CN1845815A/zh active Pending
  • 2003-09-12 EP EP03818847A patent/EP1663593B1/fr not_active Expired - Lifetime
  • 2003-09-12 DE DE50308089T patent/DE50308089D1/de not_active Expired - Fee Related
  • 2003-09-12 AU AU2003266383A patent/AU2003266383A1/en not_active Abandoned
  • 2003-09-12 ES ES03818847T patent/ES2295709T3/es not_active Expired - Lifetime
  • 2003-09-12 US US10/571,661 patent/US20080271850A1/en not_active Abandoned
  • 2003-09-12 PT PT03818847T patent/PT1663593E/pt unknown

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