EP0426793B1 - Procede de fabrication d'un produit moule sous pression en resine synthetique, eventuellement en forme de plaque, et preforme a employer pour ce procede - Google Patents
Procede de fabrication d'un produit moule sous pression en resine synthetique, eventuellement en forme de plaque, et preforme a employer pour ce procede Download PDFInfo
- Publication number
- EP0426793B1 EP0426793B1 EP90906776A EP90906776A EP0426793B1 EP 0426793 B1 EP0426793 B1 EP 0426793B1 EP 90906776 A EP90906776 A EP 90906776A EP 90906776 A EP90906776 A EP 90906776A EP 0426793 B1 EP0426793 B1 EP 0426793B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- binding agent
- weight
- binder
- compressed
- web
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title claims abstract description 33
- 229920003002 synthetic resin Polymers 0.000 title abstract description 8
- 239000000057 synthetic resin Substances 0.000 title abstract description 8
- 239000011230 binding agent Substances 0.000 claims abstract description 53
- 229920002522 Wood fibre Polymers 0.000 claims abstract description 22
- 239000000835 fiber Substances 0.000 claims abstract description 18
- 229920005989 resin Polymers 0.000 claims abstract description 18
- 239000011347 resin Substances 0.000 claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 claims abstract description 14
- 239000000123 paper Substances 0.000 claims abstract description 12
- 238000009833 condensation Methods 0.000 claims abstract description 7
- 230000005494 condensation Effects 0.000 claims abstract description 7
- 229920002678 cellulose Polymers 0.000 claims abstract description 3
- 239000001913 cellulose Substances 0.000 claims abstract description 3
- 239000012876 carrier material Substances 0.000 claims description 16
- 239000011148 porous material Substances 0.000 claims description 10
- 230000006835 compression Effects 0.000 claims description 9
- 238000007906 compression Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 3
- 239000002657 fibrous material Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 239000000654 additive Substances 0.000 claims description 2
- 239000000049 pigment Substances 0.000 claims description 2
- 238000009751 slip forming Methods 0.000 claims description 2
- 238000004040 coloring Methods 0.000 claims 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 claims 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 claims 1
- 150000002989 phenols Chemical class 0.000 claims 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 claims 1
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 abstract description 6
- 229920001568 phenolic resin Polymers 0.000 abstract description 6
- 239000000463 material Substances 0.000 abstract description 5
- 238000003825 pressing Methods 0.000 abstract description 4
- 238000010924 continuous production Methods 0.000 abstract description 3
- 239000005011 phenolic resin Substances 0.000 abstract description 3
- 239000011248 coating agent Substances 0.000 abstract description 2
- 238000000576 coating method Methods 0.000 abstract description 2
- 239000010410 layer Substances 0.000 description 29
- 239000002025 wood fiber Substances 0.000 description 20
- 238000001035 drying Methods 0.000 description 3
- 239000004745 nonwoven fabric Substances 0.000 description 3
- 239000012792 core layer Substances 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000003892 spreading Methods 0.000 description 2
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- 239000004640 Melamine resin Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000011162 core material Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000009969 flowable effect Effects 0.000 description 1
- 238000007731 hot pressing Methods 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Images
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
- B27N3/00—Manufacture of substantially flat articles, e.g. boards, from particles or fibres
- B27N3/06—Making 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
Definitions
- the invention relates to a method for producing a compression molding, in which a fiber cake is continuously formed from cellulose-containing fibers such as wood fibers and is connected under pressure to a carrier web coated with a binder and is then pressed and cured.
- a method of the aforementioned type is known from FR-A 1,099184. This describes a process for the production of plates, a carrier material web loaded with a binder being applied to a moist nonwoven fabric with a moisture content of 67% under pressure at elevated temperature.
- the moist nonwoven fabric is produced by dehydrating a pulp.
- the pulp contains - as is said on page 2, column 1, lines 24 to 28 - lignin, hemicelluloses and other natural binders which ensure the fibers are connected to one another.
- the synthetic resin from the binder layer does not penetrate into the fiber pores filled with water due to the high moisture content of the wet nonwoven fabric, so that mainly the paper of the carrier material web is penetrated.
- EP-B1-81147 relates to a process for producing a decorative building board, in which an aqueous alkaline solution or dispersion of a phenol-formaldehyde resin is applied to wood fibers and the wood fibers resinated in this way are dried to a residual moisture content of 2 to 15% .
- a fiber mat is then formed from the resinated and dried wood fibers, the mat is mechanically pre-compressed and then hot-pressed in one or more layers arranged one above the other to form a core layer, the decorative layer being applied to the core layer simultaneously with or after pressing .
- a building board is to be produced which has similar properties to the laminated sheets produced in the usual way, which are produced by hot pressing so-called "prepregs", which are papers impregnated with curable synthetic resins in the dry state.
- prepregs which are papers impregnated with curable synthetic resins in the dry state.
- laminated sheets now have due to the preferred orientation of the cellulose fibers of the paper in the paper production direction under fluctuating climatic conditions, a different shrinking and stretching behavior in the longitudinal or transverse direction of the papers used, which can have a disadvantageous effect when used.
- the paper used is a material that is made from wood as a raw material using a relatively complex and environmentally harmful process.
- the invention is now based on the object of specifying a method of the type mentioned at the outset, in which one does not require a special process step for resin coating the wood fibers and in which, according to an advantageous variant of the invention, using readily flowable condensation resin binders, the disadvantages mentioned of the known method described above can be avoided.
- the object on which the invention is based is first achieved in the process according to the invention, which is characterized in that for the continuous production of a pre-compact or a raw plate on a longitudinally moving web-shaped carrier material made of fibrous materials such as papers which are impregnated with curable binders, a layer a liquid binder is applied, that a fiber cake is applied to this binder layer, that a second web-shaped carrier material, to which a further layer of the liquid binder has previously been applied, is applied with the binder layer down onto the fiber cake, so that the layer structure thus formed is continuous compressed to an average average density in the range between 600 and 1400 kg / m3, but advantageously between 800 and 1400 kg / m3 and heated to a higher temperature at which the viscosity of the binder ls is reduced, so that the binder penetrates at least almost completely into the pore volume of the compressed fiber cake and, if appropriate, is subsequently cured.
- fibrous materials such as paper can advantageously be used as web-
- the method according to the invention is characterized in that with a moisture content of the fiber mass used of at most 10% by weight, preferably at most 8% by weight, a condensation resin or resin mixture in liquid form is used as the binder for producing the binder layers which has a solid resin content of more than 80% by weight and a water content of at most 8% by weight, preferably at most 6% by weight, and the additives like contains color pigments.
- the layer structure is largely heated before it is compressed by means of electromagnetic high-frequency heating.
- the method according to the invention is characterized in that, at or after the end of the heating phase and the compression phase, the layer structure is compressed again briefly and its pore volume is reduced so much that the binder is practically uniformly distributed in the pore volume.
- This brief compression of the layer structure can advantageously take place in a calender.
- the method according to the invention is characterized in that the compressed layer structure passes through a cooling section after the end of the heating phase.
- a device for continuously producing a pre-compact is shown in a schematic representation.
- This device essentially consists - in the production direction (see arrow) of the manufacturing process one after the other - from a rolling device 1 for a first carrier material web 2, a belt conveyor 3 with a first binder application station 4 and a device 5 for producing and feeding a wood fiber cake, a take-off device 6 for a second carrier material web 7 with a second binder application station 8, a heatable belt press 10, as well as a cooled belt press 11 and a cutting device 12.
- the invention 5 for producing and feeding a wood fiber cake consists of a wood fiber spreading device 13 with a belt conveyor 14, a compression belt 15, an isotope thickness measuring device 16 and a downstream transfer belt conveyor 17.
- the carrier material web 2 is continuously drawn off from the unrolling device 1 and runs over a belt conveyor 3.
- the viscous phenolic resin binder 18 is used to form a binder layer 19 with a thickness of 0 , 5 mm applied.
- a wood fiber cake 20 is continuously produced, which is placed at 21 on the binder layer 19 applied to the belt conveyor 3.
- 13 wood fibers in the form of a bed 22 with a bed height of 100 mm and a density of about 30 kg / m3 are scattered with the aid of the scattering device.
- This bed 22 is then compressed to a thickness of approximately 60 mm by means of the circumferential compression belt 15.
- the basis weight of the wood fiber cake 20 thus produced is then determined using the isotope thickness measuring device and e.g. kept constant by controlling the spreading device.
- the second carrier material web 7 is continuously withdrawn from the take-off device 6, which has a supply roll 23, a support plate 24 and a plurality of deflection rollers 25, and when it slides over the support plate 24 from the second binder application station 8 - in an analogous manner to the first carrier material web 2 - provided with a 0.5 mm thick binder layer 26.
- the carrier material web 7 coated in this way is then continuously pressed onto the wood fiber cake 20 with the binder layer 26 facing downward, so that a layer structure 27 now results, which consists of the wood fiber cake 20 which is provided on both sides by carrier material webs 2 provided with binder layers 19, 26 , 7 is covered.
- This layer structure 27 now passes through the high-frequency heating device 9, in which it is heated to a temperature of 80-140 ° C. At these temperatures, the viscosity of the binder drops to viscosity values of 100 to 300 mPa.s.
- the layer structure 27 heated in this way is fed to the entrance of the heated belt press 10 and compressed to a density of approximately 300 kg / m 3 in its feed area.
- the binder penetrates into the pore volume of the compressed wood fiber cake due to its reduced viscosity due to the heating, with a long residence time in the belt press 10 of 3 min Uniformity of the binder distribution over the pore volume is achieved.
- the compressed layer structure 27 ' passes through an infrared heating device after leaving the belt press 10 and then through a calender in which the layer structure 27' which has already been compressed is briefly further strongly compacted.
- the pore volume in the layer structure is reduced to such an extent that it is practically completely filled by the amount of binder and the binder is thereby uniformly wetted the surface of the wood fibers. This can cause any irregularities in the distribution of the binder within the wood fiber mass, which still exist in the layer structure 27 'when leaving the belt press 10, are advantageously further compensated for.
- the plate-shaped high-pressure molded article removed from the press after cooling and cooled has a bending strength of 140 N / mm2, a tensile strength of 70 N / mm2 and a water absorption of approx. 0.8%.
- the method described in the figure for the production of a preform, which is used in the production of a plate-shaped high-pressure molded article, can also be used directly with corresponding modifications for the production of high-pressure molded articles.
- This is then realized, for example, by increasing the pressing pressure in the belt press 10, for example to 70 bar and the pressing temperature to 150 ° C., and extending the dwell time of the layer structure, for example to 6 minutes, so that the synthetic resin binder contained in the layer structure initially flows well and then hardens.
- a raw plate is then removed from the belt press 10 and is cooled to 30 ° C. in the downstream cooled belt press 11. The raw plate is then cut to length and decorative lacquered or coated for further use in a known manner.
- the printing moldings produced by the process according to the invention can largely be used in the same field of application as the conventional decorative synthetic resin high-pressure laminates of greater thickness (e.g. between 3 and 15 mm thick), e.g. So for the production of self-supporting components or as weatherproof panels for outdoor use.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Wood Science & Technology (AREA)
- Forests & Forestry (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
- Laminated Bodies (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Diaphragms For Electromechanical Transducers (AREA)
- Paper (AREA)
- Printing Methods (AREA)
- Moulding By Coating Moulds (AREA)
Claims (6)
- Procédé de fabrication d'un corps moulé par compression dans lequel un matelas de fibres composé de fibres contenant de la cellulose, telles que des fibres de bois, est formé en continu et est relié sous pression à une bande de support revêtue d'un liant liquide en étant ensuite comprimé et durci, caractérisé en ce que pour la fabrication en continu d'une préforme ou d'une plaque brute, une couche du liant liquide est appliquée sur un matériau de support (2) en forme de bande qui se déplace dans la direction longitudinale et qui est composée de matériaux fibreux tels que des papiers qui sont imprégnés avec des liants susceptibles de durcir, en ce que le matelas de fibres (20) présentant une teneur en humidité maximale de 10% en poids, est appliqué sur cette couche de liant (19), en ce qu'un deuxième matériau de support (7) en forme de bande sur lequel a été appliqué auparavant une autre couche (26) du liant liquide, est appliqué vers le bas sur le matelas de fibres avec la couche de liant (26), en ce que la structure stratifiée (27) ainsi obtenue est comprimée en continu jusqu'à un poids volumique moyen courant compris entre 600 et 1400 Kg/m³, mais de préférence entre 800 et 1400 Kg/m³, et est chauffé à une température plus élevée pour laquelle la viscosité du liant est réduit de sorte que le liant pénètre au moins presque complètement dans le volume des pores du matelas de fibres comprimé et est ensuite durci, et en ce que, lors de la compression le matelas de fibres se trouve relié de façon durable avec le matériau de support en forme de bande, et dans lequel le liant liquide est une résine de condensation ou un mélange de résine de condensation à base de phénoliques et/ou amino et d'aldéhydes, tel que le formaldéhyde qui présente une teneur en résine solide supérieure à 80% en poids et une teneur en eau d'au plus 8%, et de préférence d'au plus 6% en poids.
- Procédé selon la revendication 1, caractérisé en ce que pour une teneur en humidité maximale du matelas de fibres utilisé de 10% en poids, de préférence d'au plus 8% en poids, on utilise comme liant pour la fabrication des couches de liants, une résine de condensation ou un mélange de résine de condensation sous forme liquide qui présente une teneur en résine solide supérieure à 80% en poids et une teneur en eau d'au plus 8% en poids , de préférence d'au plus 6% en poids, et qui contient des adjuvants tels que des pigments colorants.
- Procédé selon la revendication 1 ou 2, caractérisé en ce que l'échauffement de la structure stratifiée (27) est réalisé pour la plus grande partie avant sa compression en utilisant un chauffage électromagnétique à haute fréquence.
- Procédé selon l'un des revendications 1 à 3, caractérisé en ce qu'au moins après la fin de la phase de chauffage, la structure stratifiée (27') est comprimée de nouveau pendant une courte période, le volume de ses pores étant ainsi réduit de façon si importante que le liant soit distribué de façon pratiquement uniforme dans le volume des pores.
- Procédé selon la revendication 4, caractérisé en ce que la compression de courte durée de la structure stratifiée (27') est réalisée dans une calandre.
- Procédé selon l'une des revendications 1 à 5, caractérisé en ce que la structure stratifiée comprimée (27') parcourt, après la fin de la phase de compression, un trajet de refroidissement.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT1061/89 | 1989-05-03 | ||
AT1061/89A AT392758B (de) | 1989-05-03 | 1989-05-03 | Verfahren zum herstellen eines gegebenenfalls plattenfoermigen kunstharz-druckformkoerpers sowie vorprodukt zum einsatz bei einem solchen verfahren |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0426793A1 EP0426793A1 (fr) | 1991-05-15 |
EP0426793B1 true EP0426793B1 (fr) | 1993-08-04 |
Family
ID=3505743
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP90906776A Expired - Lifetime EP0426793B1 (fr) | 1989-05-03 | 1990-04-27 | Procede de fabrication d'un produit moule sous pression en resine synthetique, eventuellement en forme de plaque, et preforme a employer pour ce procede |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0426793B1 (fr) |
JP (1) | JPH03506001A (fr) |
AT (2) | AT392758B (fr) |
AU (1) | AU632811B2 (fr) |
BR (1) | BR9006755A (fr) |
CA (1) | CA2032170A1 (fr) |
WO (1) | WO1990013403A1 (fr) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT397805B (de) * | 1992-03-04 | 1994-07-25 | Isovolta | Verfahren zur herstellung eines kunstharz-druckformkörpers |
DE69513982T2 (de) * | 1994-08-01 | 2000-05-31 | Tarkett Sommer S.A., Nanterre | Verfahren zur herstellung eines bodenbelages mit einem holz- oder holzähnlichem zierschicht und die so hergestellten produkte |
DE69805317T2 (de) * | 1997-10-20 | 2002-11-28 | Syntech Holdings B.V., Venlo | Formteil, insbesondere plattenförmiges formteil, welches ein komprimiertes gemisch aus bindemittel und füllstoff enthält, verfahren und vorrichtung zur herstellung solch eines formteils, bodenbelagplatten, sporthalle versehen mit solchen platten, deckenplatten, werbegeschenke, kunstgegenstände und möbelstücke |
NL1008899C2 (nl) * | 1998-04-16 | 1999-10-19 | Syntech Holdings Bv | Vormdeel, in het bijzonder in de vorm van een plaat, dat een samengeperst mengsel van bindmiddel en vulmiddel omvat, werkwijze en inrichting voor het vervaardigen van een dergelijk vormdeel, alsmede vloerplaten, een sporthal voorzien van dergelijke vloerplaten, plafondplaten, relatiegeschenken, kunstvoorwerpen en meubels. |
NL1007314C2 (nl) * | 1997-10-20 | 1999-04-21 | Syntech Holdings Bv | Vormdeel, in het bijzonder in de vorm van een plaat, dat een samengeperst mengsel van polyurethan, bindmiddel en vulmiddel omvat, werkwijze en inrichting voor het vervaardigen van een dergelijk vormdeel, alsmede vloerplaten, een sporthal voorzien van dergelijke vloerplaten, relatiegeschenken en meubels. |
CN101758540B (zh) * | 2010-01-25 | 2013-03-20 | 西北农林科技大学 | 一种重组材板坯铺装机 |
PL3181315T3 (pl) * | 2015-12-16 | 2020-11-16 | SWISS KRONO Tec AG | Sposób produkowania płyty osb z gładką powierzchnią |
CN106003275B (zh) * | 2016-07-01 | 2018-01-05 | 鄂尔多斯市华林沙柳科技有限公司 | 一种以灌木为原料制造木基型材的自动生产设备及方法 |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2831794A (en) * | 1958-04-22 | Process for manufacturing veneer panels | ||
BE500838A (fr) * | 1950-01-27 | |||
FR1099184A (fr) * | 1953-02-19 | 1955-08-31 | Abitibi Power & Paper Co | Planches artificielles |
FR1283609A (fr) * | 1961-03-13 | 1962-02-02 | Svenska Cellulosa Ab | Procédé de préparation d'articles moulés durs ou demi-durs en fibre de bois, et notamment de panneaux en fibre de bois possédant une surface de recouvrement résistante |
DE1453390A1 (de) * | 1962-05-26 | 1969-03-06 | Holztechnik Anstalt | Verfahren zur Oberflaechenveredelung von Pressplatten |
DE1653237B1 (de) * | 1967-12-23 | 1971-05-13 | Hombak Maschinenfab Kg | Verfahren und Vorrichtung zum Kalibrieren und zur gleichzeitigen Quellungsverguetung von Holzwerkstoffplatten |
DE1703076A1 (de) * | 1968-03-28 | 1972-01-05 | Teutoburger Sperrholzwerk Geor | Spanplatte sowie Verfahren zu ihrer Herstellung |
-
1989
- 1989-05-03 AT AT1061/89A patent/AT392758B/de not_active IP Right Cessation
-
1990
- 1990-04-27 CA CA002032170A patent/CA2032170A1/fr not_active Abandoned
- 1990-04-27 WO PCT/AT1990/000042 patent/WO1990013403A1/fr active IP Right Grant
- 1990-04-27 EP EP90906776A patent/EP0426793B1/fr not_active Expired - Lifetime
- 1990-04-27 BR BR909006755A patent/BR9006755A/pt unknown
- 1990-04-27 AU AU55505/90A patent/AU632811B2/en not_active Ceased
- 1990-04-27 JP JP2506510A patent/JPH03506001A/ja active Pending
- 1990-04-27 AT AT90906776T patent/ATE92393T1/de active
Also Published As
Publication number | Publication date |
---|---|
JPH03506001A (ja) | 1991-12-26 |
ATE92393T1 (de) | 1993-08-15 |
EP0426793A1 (fr) | 1991-05-15 |
CA2032170A1 (fr) | 1990-11-04 |
AU632811B2 (en) | 1993-01-14 |
AU5550590A (en) | 1990-11-29 |
AT392758B (de) | 1991-06-10 |
WO1990013403A1 (fr) | 1990-11-15 |
ATA106189A (de) | 1990-11-15 |
BR9006755A (pt) | 1991-08-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0344231B1 (fr) | Procede de fabrication d'un corps en resine synthetique, eventuellement en forme de panneau, moule par compression et produit preliminaire utilise dans ce procede | |
DE69302484T2 (de) | Verbundfilm | |
DE3147989A1 (de) | Dekoratives, insbesondere plattenfoermiges formteil, verfahren zu seiner herstellung und seine verwendung | |
DE2654981A1 (de) | Hartplattenerzeugnis und verfahren und vorrichtung zu seiner herstellung | |
DE102007015969A1 (de) | Verfahren zur Herstellung einer Bauplatte | |
EP0426793B1 (fr) | Procede de fabrication d'un produit moule sous pression en resine synthetique, eventuellement en forme de plaque, et preforme a employer pour ce procede | |
EP0424909A2 (fr) | Procédé pour la fabrication d'objets faÀ§onnés | |
EP1110687B2 (fr) | Procédé de production d'un panneau de fibres léger à surface fermée | |
EP1691991B1 (fr) | Stratifie decoratif et procede de fabrication associe | |
CH641408A5 (de) | Verfahren zur herstellung eines melaminharzbeschichteten papiers. | |
DE19647240B4 (de) | Holzfaserplatte und Verfahren zu ihrer Herstellung | |
DE2542511C2 (de) | Verfahren zum Herstellen einer mehrschichtigen Bahn aus Zellulosematerial | |
AT397805B (de) | Verfahren zur herstellung eines kunstharz-druckformkörpers | |
EP1185587B1 (fr) | Produit semi-fini en fibres de bois et son procede de production | |
DE10314974A1 (de) | Verfahren zur Herstellung von Formkörpern mit einer zusammenhängende lignocellulosehaltige Fasern aufweisenden formgebenden Struktur und Formkörper | |
DE2434558C3 (de) | Verfahren und Einrichtung zum Befeuchten eines Faservlieses | |
DE2513764B2 (de) | Verfahren zum Herstellen einer mindestens einseitig beschichteten Holzwerkstoff-Platte, wie Spanplatte o.dgl | |
DE2945977A1 (de) | Fasermatte zur trockenen herstellung von gepressten formkoerpern aus zellulose- oder lignozellulosefasern | |
DE2550768C2 (de) | Verfahren zur Herstellung einer dekorativen Schichtstoffplatte | |
DE967962C (de) | Verfahren zur Herstellung von Pressschichtkoerpern | |
DE102008057262A1 (de) | Beschichten von Holzwerkstoffplatten mit einer Verschleißschicht | |
DE884274C (de) | Verfahren zur Herstellung von Holzfaserplatten | |
DE2511262C3 (de) | Herstellungsverfahren für mit härtbarem Faser-Kunstharzvorkondensat gefüllten Faserstoffbahnen | |
DE102020132063A1 (de) | Verfahren und Vorrichtung zur Herstellung von Formteilen | |
EP1059152B1 (fr) | Procédé de production d'un article à base de fibres de cellulose, en particulier en forme de panneau de fibres |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19901227 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FR GB IT LI NL SE |
|
17Q | First examination report despatched |
Effective date: 19920522 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH DE DK ES FR GB IT LI NL SE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: THE PATENT HAS BEEN ANNULLED BY A DECISION OF A NATIONAL AUTHORITY Effective date: 19930804 Ref country code: DK Effective date: 19930804 |
|
REF | Corresponds to: |
Ref document number: 92393 Country of ref document: AT Date of ref document: 19930815 Kind code of ref document: T |
|
REF | Corresponds to: |
Ref document number: 59002191 Country of ref document: DE Date of ref document: 19930909 |
|
ITF | It: translation for a ep patent filed | ||
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) |
Effective date: 19931029 |
|
ET | Fr: translation filed | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
EAL | Se: european patent in force in sweden |
Ref document number: 90906776.1 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19960313 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19960314 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19960318 Year of fee payment: 7 Ref country code: BE Payment date: 19960318 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CH Payment date: 19960320 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 19960321 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 19960322 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19960328 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Effective date: 19970427 Ref country code: AT Effective date: 19970427 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Effective date: 19970428 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19970430 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19970430 Ref country code: BE Effective date: 19970430 |
|
BERE | Be: lapsed |
Owner name: ISOVOLTA OSTERREICHISCHE ISOLIERSTOFFWERKE A.G. Effective date: 19970430 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Effective date: 19971101 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 19970427 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19971231 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19980101 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 19971101 |
|
EUG | Se: european patent has lapsed |
Ref document number: 90906776.1 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED. Effective date: 20050427 |