EP3050687A1 - Procédé de fabrication et de revêtement simultané de décor d'une plaque en bois dotée de décor, en particulier d'un matériau composite bois/matière synthétique - Google Patents

Procédé de fabrication et de revêtement simultané de décor d'une plaque en bois dotée de décor, en particulier d'un matériau composite bois/matière synthétique Download PDF

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Publication number
EP3050687A1
EP3050687A1 EP15153005.2A EP15153005A EP3050687A1 EP 3050687 A1 EP3050687 A1 EP 3050687A1 EP 15153005 A EP15153005 A EP 15153005A EP 3050687 A1 EP3050687 A1 EP 3050687A1
Authority
EP
European Patent Office
Prior art keywords
wood
plastic
weight
double belt
belt press
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP15153005.2A
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German (de)
English (en)
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EP3050687B1 (fr
Inventor
Norbert Dr. Kalwa
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Flooring Technologies Ltd
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Flooring Technologies Ltd
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
Priority to ES15153005.2T priority Critical patent/ES2630181T3/es
Application filed by Flooring Technologies Ltd filed Critical Flooring Technologies Ltd
Priority to PL15153005T priority patent/PL3050687T3/pl
Priority to EP15153005.2A priority patent/EP3050687B1/fr
Priority to ES15726020T priority patent/ES2817085T3/es
Priority to UAA201901546A priority patent/UA123960C2/uk
Priority to PT157260209T priority patent/PT3215327T/pt
Priority to UAA201705502A priority patent/UA119483C2/uk
Priority to CA2966674A priority patent/CA2966674C/fr
Priority to PL15726020T priority patent/PL3215327T3/pl
Priority to CN201580060630.0A priority patent/CN107206620B/zh
Priority to JP2017542277A priority patent/JP6437128B2/ja
Priority to CN201911219585.5A priority patent/CN111037700B/zh
Priority to RU2017119722A priority patent/RU2667757C1/ru
Priority to PCT/EP2015/060622 priority patent/WO2016071007A1/fr
Priority to EP15726020.9A priority patent/EP3215327B1/fr
Priority to US15/524,457 priority patent/US10369721B2/en
Publication of EP3050687A1 publication Critical patent/EP3050687A1/fr
Application granted granted Critical
Publication of EP3050687B1 publication Critical patent/EP3050687B1/fr
Priority to RU2018132176A priority patent/RU2766677C2/ru
Priority to JP2018212342A priority patent/JP6817994B2/ja
Priority to US16/452,031 priority patent/US11072087B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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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
    • B27N3/06Making particle boards or fibreboards, with preformed covering layers, the particles or fibres being compressed with the layers to a board in one single pressing operation
    • 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
    • B27N3/18Auxiliary operations, e.g. preheating, humidifying, cutting-off
    • 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
    • B27N1/006Pretreatment of moulding material for increasing resistance to swelling by humidity
    • 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
    • B27N3/24Moulding or pressing characterised by using continuously acting presses having endless belts or chains moved within the compression zone
    • 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
    • B27N7/00After-treatment, e.g. reducing swelling or shrinkage, surfacing; Protecting the edges of boards against access of humidity
    • B27N7/005Coating boards, e.g. with a finishing or decorating layer

Definitions

  • the present invention relates to a process for the production and simultaneous decorative coating of a wood-based panel, in particular in the form of a wood-plastic composite material according to claim 1.
  • wood-based panels e.g. in the form of wood fiber boards in various configurations for use as a laminate floor or for cladding walls or in the manufacture of furniture has long been known.
  • wood fiber boards in the form of medium density wood fiber boards (MDF boards) or high density wood fiber boards (HDF boards) are used, which are obtained by pressing corresponding wood fibers or chips with a thermosetting plastic resin as a binder.
  • a particular problem with the use of said wood fiber boards is the sensitivity of the wood fibers or wood chips used to high humidity and direct water contact. While this problem can be dealt with relatively easily in the case of furniture or interior products by means of constructional or technological measures, in the case of floor coverings, e.g. Floor laminates based on wood or wood-based materials are often much more problematic.
  • Floor coverings based on wood or wood-based panels such as laminate flooring or parquet quickly react to water contact with swelling and / or dimensional changes. This is caused, inter alia, by the effects of water-based care products, some of which are used very frequently and very intensively. Also, high humidity can trigger comparable processes.
  • the flooring is typically also in direct contact with the building parts such as concrete floors / screed or walls, which may also carry moisture in the flooring. For this reason, in the production of the above-mentioned wood-based products on low-source woods or wood-based materials used, which indeed reduce the problems described, but can not completely prevent.
  • inorganic carrier plates are used for the production of products with wooden surfaces, which can lead to gluing, processing or laying problems.
  • PVC polyvinyl chloride
  • WPC wood-plastic composites
  • WPCs are composites based on wood flour or wood chips and thermoplastics, to which other additives may be added.
  • the mixtures of wood fibers and thermoplastics are melted and processed into agglomerates.
  • the agglomerates are melted in extruders and processed into relatively small-sized plates.
  • the width of the plates is usually in a range of less than one meter due to the manufacturing process in an extruder.
  • the productivity per hour is in a low single-digit square meter range, so that the combination of low productivity and limited board size causes relatively high costs of the WPC boards so produced.
  • the products are only produced in the continuous width in the appropriate widths and separated to the required length.
  • the agglomerates are homogeneously scattered on a belt, pressed in a double-belt press to a plate and cooled.
  • the WPC products have a low swelling, can be worked like wood and are very weather-resistant. In the outdoor area, it is usually sufficient if the elements are monochrome (usually brown). This is based on the wood products that are to substitute the WPC products.
  • the present invention is therefore based on the technical object to overcome the disadvantages described and provide a method available that allows for much of a simpler and cheaper production at least for part of the decorating process. It should, if possible, a procedural step can be saved.
  • This object is achieved with a method for producing wood-based panels according to claim 1, in particular by applying at least one decorative layer to at least the surface already during the production of the WPC boards.
  • a multi-stage process in particular a three-stage process in which first of all a mixture of wood particles, e.g. in the form of wood fibers, and plastics, in particular thermoplastics, a Vorvlies or a Dämpfstoffmatte is produced with a low density.
  • This pre-fleece or Dämpfstoffmatte with a low density is then first compressed on a double belt press under high pressure and high temperature and then cooled in a cooling press.
  • the present method enables the production of wood-based panels in the form of large-format wood-plastic composites (WPCs) which are suitable for making backing sheets for use as floor laminates, coupled with high productivity and thus lower costs.
  • WPCs large-format wood-plastic composites
  • thermoplastic plastic in particular in the form of thermoplastic granules or plastic fibers in the wood particle-plastic mixture is used.
  • the thermoplastic resin is preferably selected from a group comprising polyethylene (PE), polypropylene (PP), polyvinyl chloride (PVC), polyester, polyethylene terephthalate (PET), polyamide (PA), polystyrene (PS), acrylonitrile-butadiene-styrene (ABS ), Polymethylmethacrylate (PMMA), polycarbonate (PC), polyetheretherketone (PEEK), polyisobutylene (PIB), polybutylene (PB), mixtures or copolymers thereof.
  • PE polyethylene
  • PP polypropylene
  • PVC polyvinyl chloride
  • PET polyethylene terephthalate
  • PA polyamide
  • PS polystyrene
  • ABS acrylonitrile-butadiene-styrene
  • PMMA Polymethylmethacrylate
  • PC polycarbonate
  • PEEK polyetheretherketone
  • PIB polyisobutylene
  • PB polybutylene
  • the thermoplastic can be used in the form of plastic fibers.
  • the plastic fibers can be present as monocomponent fibers or as bicomponent fibers.
  • the thermally activatable plastic or binding fibers perform both a binding and a support function in the matrix of wood fibers or wood particles.
  • monocomponent fibers they are preferably made of polyethylene or other low melting point thermoplastics.
  • Bicomponent fibers also referred to as Biko support fibers
  • Biko fibers increase the stiffness of wood fiber boards and also reduce the creep experienced with thermoplastics (such as PVC laminates).
  • the biko fibers are typically made of a Tragfilament or a core fiber made of a plastic with higher temperature resistance, in particular polyester or polypropylene, which are coated or coated by a plastic having a lower melting point, in particular of polyethylene.
  • the shell or the jacket of the biko fibers allows melting of the wood particles together after melting or melting.
  • bicomponent fibers those based on thermoplastics such as PP / PE, polyester / PE or polyester / polyester are used.
  • a wood particle-plastic mixture which has a mixing ratio of wood particles to plastic between 90% by weight of wood particles: 10% by weight of plastics and 20% by weight of wood particles: 80% by weight of plastics, preferably between 70% by weight of wood particles : 30% by weight of plastics and 40% by weight of wood particles: 60% by weight of plastics.
  • the wood particle-plastic mixture used can be exemplified by 44% by weight of wood fibers or wood particles and 56% by weight of Biko fibers, e.g. Polyethylene terephthalate / polyethylene terephthalate coisophthalate fibers or PP / PE fibers.
  • the plastic component itself is also a mixture of different plastics.
  • other compositions are possible.
  • the present modified wood particles are to be understood as meaning lignocellulose-containing comminution products such as, for example, wood fibers, wood chips or even wood flour.
  • wood fibers in particular dry wood fibers with a length of 1.0 mm to 30 mm, preferably 1.5 mm to 24 mm and a thickness of 0.05 mm to 1 mm are used.
  • the wood fiber moisture content of the fibers used is in a range between 5 and 15%, preferably 6 and 12% based on the total weight of the wood fibers. It is also possible to determine the wood particles used with respect to the mean grain diameter, wherein the average grain diameter d50 between 0.05 mm and 1 mm, preferably 0.1 and 0.8 mm may be.
  • the individual components wood particles and plastic are intimately mixed in a mixer.
  • the mixing of the components can also be done by entering in a blowpipe.
  • intensive mixing by the injected air as a means of transport.
  • the intensive mixing of the components is continued in the reservoir by the blown in transport air.
  • the wood particle-plastic mixture for example, after weighing on a scale, uniformly inflated on a first conveyor belt over its width.
  • the amount of supplied wood particle-plastic mixture depends on the desired layer thickness and the desired bulk density of the produced Vorvlieses.
  • Typical basis weights of the scattered pre-fleece can be in a range between 3,000 and 10,000 g / m 2 , preferably between 5,000 to 7,000 g / m 2 .
  • the width of the scattered fleece is determined by the width of the first conveyor belt, and may be, for example, in a range up to 3,000 mm, preferably 2,800 mm, particularly preferably up to 2,500 mm.
  • the Vorvlies After applying the wood particle-plastic mixture on a first conveyor belt to form a Vorvlieses, the Vorvlies is introduced in at least one first annealing oven for pre-compression.
  • the pre-fleece of wood particles and plastic is heated in the at least one annealing furnace to a temperature which corresponds to the melting temperature of the plastic used or above.
  • the temperatures in the annealing furnace may be between 130 and 200 ° C, preferably 150 and 180 ° C, particularly preferably 160 and 170 ° C.
  • the core temperature of the pre-fleece is preferably in a range between 100 and 150 ° C, particularly preferably at about 130 ° C.
  • the plastic material is melted, whereby an intimate connection between the plastic material, for example the plastic fibers, with the wood fibers is produced and, at the same time, compaction of the pre-fleece takes place.
  • the temperatures in the annealing furnace are obtained, for example, by injected hot air.
  • the precompressed pre-fleece after leaving the tempering furnace, has a bulk density (or density) between 40 and 200 kg / m 3 , preferably 60 and 150 kg / m 3 , particularly preferably between 80 and 120 kg / m 3 up.
  • the thickness of the pre-compressed pre-fleece can be between 20 and 100 mm, preferably 30 and 50 mm, particularly preferably 35 and 45 mm.
  • the feed of the conveyor belt or conveyor belt in the annealing furnace in a range between 5 and 15 m / min, preferably between 6 and 12 m / min.
  • the precompacted fleece After leaving the tempering furnace, the precompacted fleece can be cooled down and made up. Typical packaging measures are e.g. the trimming of the fleece.
  • the resulting waste, in particular the resulting edge strips, can be reduced and returned to the process. Since the desired mixing ratio is given, the material can be fed directly into the reservoir.
  • the precompressed pre-fleece in the at least one double-belt press is compacted to a thickness between 2 and 20 mm, preferably 3 and 15 mm, particularly preferably 4 and 10 mm.
  • a decorative layer is applied simultaneously in this at least one double-belt press at least on the upper side of the pre-compacted pre-fleece during this compacting process. This can be done in a simple manner by feeding the decorative layer to the at least one double belt press by means of an unwinding device.
  • the application of the decorative layer on the pre-compressed Vorvlies can, as in a conventional laminate, by applying a decorative layer based on cellulose, such as by the application of decorative paper, the variety of differently patterned decorative papers are no limits.
  • a decorative layer based on cellulose such as by the application of decorative paper
  • Decor papers with an impregnation such as a thermosetting resin impregnation or a radiation-curable varnish, used for producing the decorative layer on the wood-plastic composite panels.
  • the decorative layer can be applied to the pre-compressed pre-fleece by applying at least one plastic, finish and / or primer film. It is also possible to apply a plurality of films, for example 2, 3, 4 or 5 films, selected from the plastic, finish and / or primer films. It is particularly preferred if a decorative finish film is used to apply the decorative layer.
  • the pattern generator can also perform the protective function in addition to the structuring.
  • the structured decorative film according to option a) can be, for example, a plastic film, which in turn is already structured.
  • the method according to the invention may comprise the simultaneous application of an overlay layer above the decorative layer during the transfer of the precompacted pre-fleece into the double belt press.
  • this overlay layer can be structured accordingly.
  • the overlay layer may be filled or unfilled, ie. H. be equipped with particles of high hardness to increase the abrasion resistance.
  • an overlay paper is used, which is also impregnated with a thermosetting resin or a radiation-curable lacquer. It is particularly preferred if the impregnated overlay papers are additionally provided with abrasion-resistant particles.
  • the abrasion-resistant particles are preferably selected from the group consisting of aluminum oxides, boron carbides, silicon dioxides, silicon carbides and glass particles.
  • a plastic film for example a PP film, can also be used as the overlay layer.
  • a counter-pull can be applied to the underside of the wood-plastic composite material plate.
  • the counter-pull is carried out as a cellulose layer which is impregnated.
  • the counter-pull may be embodied as paper impregnated with a thermosetting resin.
  • the layer structure of the counter-contact corresponds exactly to the layer structure and the respective layer thickness of the layer sequence of decorative and overlay layers applied on the upper side.
  • the decor, overlay and the Gegenzuglage are all designed as a cellulose layer. It is particularly preferred if the cellulose layers are impregnated with a thermosetting synthetic resin or or radiation-curable lacquer for the production of the decorative, overlay and the counter-tension layer.
  • thermosetting resin for the impregnation of the cellulose layers is therefore preferably selected from urea resin, phenolic resin, melamine resin or mixtures thereof.
  • the radiation-curable lacquer is typically a non-water-compatible lacquer, e.g. selected from the group of acrylates, modified acrylates and / or epoxides.
  • release papers or release films can be used at least on the upper side in order to avoid adhesions or thermal overloading of the decorative layer with or through the metal bands of the double belt press.
  • the temperature applied during the compaction of the nonwoven fabric in the at least one double-belt press is between 150 and 250 ° C., for example at 160 ° C., preferably between 180 and 230 ° C. or 200 and 220 ° C.
  • the pressure applied in the at least one double belt press may be between 2 MPa and 10 MPa, preferably 3 MPa and 8 MPa, particularly preferably 5 and 7 MPa.
  • the feed of the double belt press is between 5 and 15 m / min, preferably between 6 and 12 m / min.
  • the compacted wood material board leaving the double belt press is introduced into at least one cooling press, in which cooling the compacted wood-based panel to temperatures between 10 and 100 ° C, preferably 15 and 70 ° C, particularly preferably 20 and 40 ° C.
  • a pressure is used in the at least one cooling press, which is identical or at least almost identical to the pressure in the double belt press, ie in the cooling press prevails a pressure between 2 MPa and 10 MPa, preferably 3 MPa and 8 MPa, more preferably 5 and 7 MPa.
  • the compacted wood-based panels After leaving the cooling press, the compacted wood-based panels have a thickness between 2 and 15 mm, preferably 3 and 12 mm, particularly preferably 4 and 10 mm.
  • the bulk density of the compacted wood-based panels after leaving the cooling press is in a range between 500 and 1500 kg / m 3 , preferably between 650 and 1300 kg / m 3 , particularly preferably between 800 and 1100 kg / m 3 .
  • a compacting pressure in the double belt press (and also cooling press) of 5.5 to 6 MPa (55-60 bar) at a press temperature in the double belt press of the flow of 235 ° C and a pressing temperature on the surface of the plate of 220 ° C applied advantageously a compacting pressure in the double belt press (and also cooling press) of 5.5 to 6 MPa (55-60 bar) at a press temperature in the double belt press of the flow of 235 ° C and a pressing temperature on the surface of the plate of 220 ° C applied.
  • the wood-based panels or wood-plastic composites (WPC) produced by the present method are characterized by a swelling of less than 5%, preferably less than 3%, particularly preferably less than 1%.
  • the wood-based material panel in the form of a WPC has a profiling at least in an edge region of the panel, the profile enabling, for example, the introduction of a tongue and / or groove profile into an edge or side surface of the wood-based panel, wherein the panels or wood-based panels obtained in this way can be connected to one another and allow a floating installation and covering of a floor.
  • Flame retardants, luminescent or antibacterial substances may be added to the wood particle / plastic mixture as suitable additives.
  • Suitable flame retardants may be selected from the group comprising phosphates, borates, in particular ammonium polyphosphate, tris (tri-bromneopentyl) phosphate, zinc borate or boric acid complexes of polyhydric alcohols.
  • UV-stabilizing compounds such as the so-called HALS compounds.
  • antifungicides and antibacterial agents i.a. Polyimines are used.
  • an inorganic filler e.g. Materials such as talc, chalk, titanium dioxide, or others that give the plate a specific color.
  • FIG. 1 Process diagram shown comprises a mixing device 1, in which wood fibers H and plastic K, eg Biko fibers are introduced.
  • the mixing device 1 may be in the form of a blowpipe, for example, in which an intensive mixing of the wood fibers and biko fibers is effected by the injected air.
  • the fiber mixture passes into a spreader 2, from which the fiber mixture is mechanically discharged and is scattered onto a conveyor belt 3 to form a preliminary web.
  • the spreader 2 may e.g. be formed in the form of a roller litter.
  • a scale may e.g. be arranged in the form of a belt scale, which continuously determines the weight of Vorvlieses.
  • the conveyor belt 3 leads the pre-fleece into a tempering oven 4, e.g. in the form of a flow-through furnace with a feed rate of up to 15 m / min.
  • a tempering oven e.g. in the form of a flow-through furnace with a feed rate of up to 15 m / min.
  • a pre-compaction of Vorvlieses wherein the Biko fibers are melted and a connection of the Biko fibers is effected with the wood fibers.
  • the thickness of the pre-batt leaving the tempering furnace can be between 20 and 100 mm.
  • the precompacted fleece is introduced directly into a double belt press 8 with a feed rate of up to 12 m / min.
  • a decorative finish foil is applied to the upper side of the pre-fleece and, by means of the unwinding device 7, a back-pull paper is applied to the underside of the pre-fleece.
  • a release paper or release film can be applied to the unwinding device 6.
  • the double belt press 8 further densification of the web or pre-fleece takes place at a pressure of e.g. 3 MPa and a temperature of e.g. 160 ° to a thickness between 2 and 15 mm, for example to 4.5 mm.
  • the compression state of the double belt press 8 leaving plate must be kept constant until the Biko fibers have cooled down so far that the softening temperature of the same is certainly below, to a "rising" of the compacted plate due to to prevent the restoring forces of the biko fibers.
  • the compacted plate leaving the double belt press 8 is introduced directly into a cooling press 10 in which cooling of the compacted plate takes place at temperatures between 15 and 40 ° C.
  • the cooling of the cooling press can be done eg by means of water cooling.
  • the compacted (WPC) plate After leaving the cooling press 10, the compacted (WPC) plate has a thickness of between 2 and 12 mm and a bulk density of, for example, 800 to 1100 kg / m 3 .
  • the WPC plate can then be further processed and assembled as desired.
  • the method according to the invention differs from the conventional production methods for decorated floor, ceiling or wall panels, such as e.g. Laminates, characterized in that the order of the decorative layer, optionally the Overlaylage and the Gegenzuglage already much earlier in the production process, namely simultaneously in the process step of densification of Vorvlieses to a support plate, in this case the compression of the Vorvlieses to a WPC plate is performed ,
  • the method according to the present invention has numerous advantages.
  • the process steps "pre-treatment of the carrier plate by grinding” and the very energy-consuming pressing of the layer structure to a laminate in a short-cycle press can be omitted.
  • the production process of decorated carrier plates can be greatly simplified. This leads to high energy and cost savings. Further savings are that no use of adhesives for fixing the decorative and overlay layers and the counter-pull is more necessary.
  • the method according to the present invention has numerous advantages.
  • the process steps "pre-treatment of the carrier plate by grinding” and the very energy-consuming pressing of the layer structure to a laminate in a short-cycle press can be omitted.
  • the production process of decorated carrier plates can be greatly simplified. This leads to high energy and cost savings.
  • Fiber cake blanks consisting of 54% by weight of plastic fibers (27% by weight of PE fibers and 27% by weight of PET bico fibers), 44% by weight of wood and 2% by weight of paraffin having a weight per unit area of 3150 g / m 2 Thickness of 35 mm and a format of 1300 x 1400 mm were placed on a conveyor belt before a double belt press.
  • the double belt press had a heating zone with a length of three meters and a cooling zone with a length of six meters.
  • a decorative finish film was applied to the fiber cake via an unwinding device, which was coated on top with a corundum-containing, radiation-curing lacquer.
  • the weight of the coated paper was about 200 g / m 2 .
  • a release paper was applied to the decorative film.
  • a Gegenzugpapier (grammage: 80 g / m 2 ) was fed via an unwinding device.
  • the fiber cake then entered the double belt press and was compressed to a thickness of 4.5 mm at a feed rate of 2 m / min., A pressure of 30 bar and a temperature at the upper and lower steel strip of 160 ° C. With a running thermocouple, the temperature was determined in the fiber cake center. It was 140 ° C at the end of the heating zone.
EP15153005.2A 2014-11-06 2015-01-29 Procédé de fabrication et de revêtement simultané de décor d'une plaque en bois dotée de décor, en particulier d'un matériau composite bois/matière synthétique Active EP3050687B1 (fr)

Priority Applications (19)

Application Number Priority Date Filing Date Title
PL15153005T PL3050687T3 (pl) 2015-01-29 2015-01-29 Sposób wytwarzania i równoczesnego powlekania wzorem płyty z tworzywa drzewnego, zwłaszcza kompozytu drewna i tworzywa sztucznego
EP15153005.2A EP3050687B1 (fr) 2015-01-29 2015-01-29 Procédé de fabrication et de revêtement simultané de décor d'une plaque en bois dotée de décor, en particulier d'un matériau composite bois/matière synthétique
ES15153005.2T ES2630181T3 (es) 2015-01-29 2015-01-29 Procedimiento para la fabricación y el revestimiento decorativo simultáneo de un tablero de material derivado de la madera, especialmente un material compuesto de madera y plástico
EP15726020.9A EP3215327B1 (fr) 2014-11-06 2015-05-13 Procédé de fabrication d'une plaque en matériau dérivé du bois, notamment un composite constitué de bois/plastique
PT157260209T PT3215327T (pt) 2014-11-06 2015-05-13 Painel de derivados de madeira, em particular na forma de um material compósito de madeira e material sintético e um processo para a sua produção
UAA201705502A UA119483C2 (uk) 2014-11-06 2015-05-13 Плита з деревного матеріалу, зокрема у вигляді деревно-пластикового композитного матеріалу, і спосіб її виготовлення
CA2966674A CA2966674C (fr) 2014-11-06 2015-05-13 Procede de production d'un panneau composite bois-plastique
PL15726020T PL3215327T3 (pl) 2014-11-06 2015-05-13 Płyta drewnopochodna, zwłaszcza w postaci kompozytu z drewna i tworzywa sztucznego i sposób jej produkcji
CN201580060630.0A CN107206620B (zh) 2014-11-06 2015-05-13 尤其呈木塑复合材料形式的木质材料板和用于其制造的方法
JP2017542277A JP6437128B2 (ja) 2014-11-06 2015-05-13 木質材パネル、特に木−プラスチック複合材の形をとる木質材パネル、および該木質材パネルを製造する方法
ES15726020T ES2817085T3 (es) 2014-11-06 2015-05-13 Tablero de material derivado de la madera, en particular en forma de un material compuesto de madera-plástico, y un procedimiento para su fabricación
RU2017119722A RU2667757C1 (ru) 2014-11-06 2015-05-13 Плита из древесного материала, в частности, в виде древесно-пластикового композитного материала, и способ ее изготовления
PCT/EP2015/060622 WO2016071007A1 (fr) 2014-11-06 2015-05-13 Panneau dérivé du bois, en particulier sous la forme d'un matériau composite bois-plastique, et procédé pour sa fabrication
UAA201901546A UA123960C2 (uk) 2014-11-06 2015-05-13 Плита з деревного матеріалу, зокрема у вигляді деревно-пластикового композитного матеріалу, та її застосування
US15/524,457 US10369721B2 (en) 2014-11-06 2015-05-13 Wooden material panel, in particular in the form of a wood-plastic composite material, and a method for producing the same
CN201911219585.5A CN111037700B (zh) 2014-11-06 2015-05-13 地板嵌板、地板嵌板的应用和制造本质材料板的方法
RU2018132176A RU2766677C2 (ru) 2014-11-06 2018-09-10 Плита из материала на основе древесины, содержащая древесно-пластиковый композит, и способ ее изготовления
JP2018212342A JP6817994B2 (ja) 2014-11-06 2018-11-12 木質材パネル、特に木−プラスチック複合材の形をとる木質材パネル、および該木質材パネルを製造する方法
US16/452,031 US11072087B2 (en) 2014-11-06 2019-06-25 Wooden material panel, in particular in the form of a wood-plastic composite material, and a method for producing the same

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EP15153005.2A EP3050687B1 (fr) 2015-01-29 2015-01-29 Procédé de fabrication et de revêtement simultané de décor d'une plaque en bois dotée de décor, en particulier d'un matériau composite bois/matière synthétique

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4030774A1 (de) * 1990-09-28 1992-04-02 Dieffenbacher Gmbh Maschf Verfahren zum herstellen einer mehrschichtholzplatte und nach diesem verfahren hergestellte mehrschichtholzplatte
US20040028958A1 (en) * 2002-06-18 2004-02-12 Total Innovative Manufacturing Llc Recyclable fire-resistant moldable batt and panels formed therefrom
WO2009135883A1 (fr) * 2008-05-06 2009-11-12 Fritz Egger Gmbh & Co. Panneau en bois reconstitué comportant un revêtement laminé brillant et procédé de fabrication d'un tel panneau
WO2014111192A1 (fr) 2013-01-18 2014-07-24 Akzenta Paneele + Profile Gmbh Panneau décoratif avec une plaque support modifiée par une poudre d'élastomère
EP2762328A1 (fr) * 2013-01-30 2014-08-06 Flooring Technologies Ltd. Procédé de fabrication d'un panneau en bois décoré revêtu de chaque côté
EP2808463A1 (fr) * 2013-05-30 2014-12-03 Flooring Technologies Ltd. Plaque en bois dotée de particules de cuir ou d'une couche imprimée en particules de cuir et procédé de fabrication de celle-ci

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4030774A1 (de) * 1990-09-28 1992-04-02 Dieffenbacher Gmbh Maschf Verfahren zum herstellen einer mehrschichtholzplatte und nach diesem verfahren hergestellte mehrschichtholzplatte
US20040028958A1 (en) * 2002-06-18 2004-02-12 Total Innovative Manufacturing Llc Recyclable fire-resistant moldable batt and panels formed therefrom
WO2009135883A1 (fr) * 2008-05-06 2009-11-12 Fritz Egger Gmbh & Co. Panneau en bois reconstitué comportant un revêtement laminé brillant et procédé de fabrication d'un tel panneau
WO2014111192A1 (fr) 2013-01-18 2014-07-24 Akzenta Paneele + Profile Gmbh Panneau décoratif avec une plaque support modifiée par une poudre d'élastomère
EP2762328A1 (fr) * 2013-01-30 2014-08-06 Flooring Technologies Ltd. Procédé de fabrication d'un panneau en bois décoré revêtu de chaque côté
EP2808463A1 (fr) * 2013-05-30 2014-12-03 Flooring Technologies Ltd. Plaque en bois dotée de particules de cuir ou d'une couche imprimée en particules de cuir et procédé de fabrication de celle-ci

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PL3050687T3 (pl) 2017-09-29
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