EP1203648A2 - Procédé pour la fabrication de panneaux en fibres de bois - Google Patents

Procédé pour la fabrication de panneaux en fibres de bois Download PDF

Info

Publication number
EP1203648A2
EP1203648A2 EP01124400A EP01124400A EP1203648A2 EP 1203648 A2 EP1203648 A2 EP 1203648A2 EP 01124400 A EP01124400 A EP 01124400A EP 01124400 A EP01124400 A EP 01124400A EP 1203648 A2 EP1203648 A2 EP 1203648A2
Authority
EP
European Patent Office
Prior art keywords
component
groups
functional
crosslinker
vinyl
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
EP01124400A
Other languages
German (de)
English (en)
Other versions
EP1203648B1 (fr
EP1203648A3 (fr
Inventor
Konrad Alfons Dr. Wierer
Abdulmajid Dr. Hashemzadeh
Klaus Dr. Marquardt
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.)
Wacker Chemie AG
Original Assignee
Wacker Polymer Systems GmbH and 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 Wacker Polymer Systems GmbH and Co KG filed Critical Wacker Polymer Systems GmbH and Co KG
Publication of EP1203648A2 publication Critical patent/EP1203648A2/fr
Publication of EP1203648A3 publication Critical patent/EP1203648A3/fr
Application granted granted Critical
Publication of EP1203648B1 publication Critical patent/EP1203648B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • 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
    • 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
    • B27N3/002Manufacture of substantially flat articles, e.g. boards, from particles or fibres characterised by the type of binder

Definitions

  • the wood particles for example wood fibers or wood chips, with an organic Glue glued under pressure and at elevated temperature.
  • the most important binders for fiber board production are urea-formaldehyde resins (UF) resins.
  • UF urea-formaldehyde resins
  • PF resins phenol-formaldehyde resins
  • MF resins pressed wood panels
  • MDF and HDF fibreboards Another disadvantage of these reactive resins is evident in the production of MDF and HDF fibreboards: in the production of MDF boards (Medium Density Fibreboard) and HDF boards (High Density Fibreboard) the fibers are in a refiner system pretreated hydrothermally in a first step, that means cooked and ground under heat and steam pressure. Subsequently after grinding, the fibers are still under steam pressure and at temperatures from 120 ° C to 150 ° C, by injection from aqueous dispersions of the adhesives to a cooled one Glued valve in the expansion tube. The one at a flow rate Distribute turbulence from 200 to 500 m / s the binder evenly on the fiber surface.
  • the glued fibers are dried evenly stored and pressed into sheets at temperatures of 150 to 250 ° C.
  • the problem is that when gluing in this process the reactive resins due to the thermal load already in Relax tube react and up to 25% of their binding potential get lost during pressing.
  • Formaldehyde-free, thermally curable, aqueous binders for Manufacture of pressed wood panels are for example from WO-A 97/31059 known, in which we use a mixture of carboxyl functional Copolymer and an alkanolamine with at least two hydroxyl groups used.
  • Aqueous adhesive compositions made from polycarboxylic acid and hydroxyalkyl group substituted aminoaliphatics are described in WO-A 97/45461.
  • WO-A 99/02591 relates Compositions of carboxyl functional copolymer and long chain Amines. A disadvantage of these systems, which are crosslink an esterification reaction that crosslinking only in the anhydrous state, takes place during drying.
  • the invention was therefore based on the object of a method for Manufacture of pressed wood panels to provide largely premature reaction of functional groups is prevented and in which the emission of pollutants how formaldehyde is avoided, but still a high quality Gluing is obtained.
  • Suitable two-component binders contain as a component A) a copolymer of one or more comonomer units the group comprising vinyl esters of unbranched or branched Alkyl carboxylic acids with 1 to 18 carbon atoms, acrylic acid esters or Methacrylic acid esters of branched or unbranched alcohols with 1 to 15 carbon atoms, dienes, olefins, vinyl aromatics and vinyl halides, and from 0.1 to 50% by weight, based on the total weight of the copolymer, one or more units which contain carboxyl, Contain hydroxy or NH groups.
  • Suitable NH-functional comonomers are (meth) acrylamide, diacetone acrylamide, maleimide, maleic and fumaric acid monoalkyl ester amide, maleic and fumaric acid diamide, glutaric and succinic acid monovinyl ester amide, glutaric and succinic acid monoallylesteramide.
  • the NH-functional units can also be added to the copolymer A) as amino-functional oligomers with primary or secondary NH groups, preferably with primary NH groups such as Jeffamine.
  • the proportion of functional units in copolymer A) is preferably 1 to 30% by weight, particularly preferably 5 to 20% by weight, in each case based on the total weight of the copolymer.
  • polyester or polyether resins which contain hydroxyl, amine or carboxyl groups.
  • Suitable crosslinkers B) are non-thermoplastic compounds such as bisphenol A type epoxy crosslinkers, that is to say condensation products of bisphenol-A and epichlorohydrin or methylepichlorohydrin.
  • epoxy crosslinkers are commercially available, for example available under the trade names Epicote or Eurepox.
  • Diisocyanates, if appropriate blocked, are also suitable Oligo- or polyisocyanates, for example common commercial products such as m-tetramethylxylene diisocyanate (TMXDI), methylene diphenyl diisocyanate (MDI), toluene diisocyanate, isophorone diisocyanate, Dimethyl-meta-isopropenyl.
  • TXDI m-tetramethylxylene diisocyanate
  • MDI methylene diphenyl diisocyanate
  • toluene diisocyanate isophorone diisocyanate
  • Suitable crosslinkers B) are also connections with two or more groups from the series Aldehyde, keto, reactive CH group such as glutaraldehyde, terephthalaldialdehyde; Bisacetoacetates of ethylene, propylene, butylene, Hexadienglykols; Compounds with multiple aziridine, carbodiimide or oxazoline groups.
  • crosslinker B Also suitable as crosslinker B) are copolymers which contain epoxy, NMethylol, Ethylene carbonate or isocyanate groups or combinations of these groups included.
  • the polymer compositions for crosslinkers B) are suitable as those for copolymer A) described comonomers.
  • (Meth) acrylic acid esters are also particularly preferred here.
  • styrene polymers for example copolymers with n-butyl acrylate and / or 2-ethylhexyl acrylate; Copolymers of Methyl methacrylate with butyl acrylate and / or 2-ethylhexyl acrylate, and / or 1,3-butadiene; Styrene-1,3-butadiene copolymers and styrene (meth) acrylic acid ester copolymers such as styrene-butyl acrylate, styrene-methyl methacrylate-butyl acrylate or styrene-2-ethylhexyl acrylate, where n-, iso-, t-butyl acrylate are used as butyl acrylate can.
  • the content of epoxy, N-methylol, ethylene carbonate and isocyanate functional Comonomers is 0.1 to 50% by weight, preferably 1 to 30% by weight, particularly preferably 5 to 20% by weight, in each case based on the total weight of the copolymer B).
  • N-methylol-functional comonomers are N-methylol acrylamide (NMA), N-methylol methacrylamide, N-methylolallyl carbamate, Alkyl ethers such as the isobutoxy ether or ester of N-methylol acrylamide, N-methylol methacrylamide and N-methylolallyl carbamate.
  • NMA N-methylol acrylamide
  • N-methylol methacrylamide N-methylolallyl carbamate
  • Alkyl ethers such as the isobutoxy ether or ester of N-methylol acrylamide, N-methylol methacrylamide and N-methylolallyl carbamate.
  • Suitable crosslinkers B) in combination with carboxyl-functional Copolymers A) are di-, oligo- and polyamines such as diaminobutane, Hexamethylene diamine, polyalkylene amines such as triethylene tetramine, polyoxyalkylene amines (Jeffamine). More examples of suitable ones Crosslinker B) in combination with carboxyl-functional copolymers A) are compounds with two or more OH groups, such as ethylene glycol, Butanediol, pentaerythriol, polytetramethylene glycol, Bisphenol A and polyalkylene oxide adducts of ethylene glycol. Suitable as crosslinker B) for carboxyl-functional copolymers A) are also polyvalent metal ions such as aluminum, iron (III) - or Zinc chloride.
  • Suitable crosslinkers B) in combination with hydroxy-functional Copolymers A) are compounds with two or more silanol or Alkoxysilane groups such as methyltriethoxysilane in monomeric or condensed form, as well as polyvalent metal ions such as aluminum, Iron (III) - or zinc chloride.
  • Suitable crosslinkers B) in combination with NH-functional copolymers A) are di-, oligo- and polycarboxylic acids such as adipic acid, Polyacrylic acid.
  • hydroxy and NH-functional copolymers A) can also be used that the crosslinker B) together with a crosslinking catalyst is added.
  • crosslinking catalysts are citric acid, Oxalic acid, butanetetracarboxylic acid, quaternary phosphonium salts such as tetrabutylphosphonium salts, sodium hypophosphite and dibutyltin dilaurate.
  • the copolymer A) together with component B) add first, and add the catalyst in the later step.
  • carboxyl-functional copolymers are used as component A) , these can also be combined with a component B) be the reaction of the carboxyl group with the OH groups catalyzes the cellulose.
  • a component B) be the reaction of the carboxyl group with the OH groups catalyzes the cellulose.
  • Examples include citric acid, Oxalic acid, butanetetracarboxylic acid, quaternary phosphonium salts such as tetrabutylphosphonium salts, sodium hypophosphite and dibutyltin dilaurate.
  • Di-, oligo- and polyamines such as diaminobutane, hexamethylene diamine, Polyalkylene amines such as triethylene tetramine or polyoxyalkylene amines (Jeffamine) can also be used as component A) then as component B) the above-mentioned, if appropriate blocked, diisocyanates, for example m-tetramethylxylene diisocyanate (TMXDI), methylene diphenyl diisocyanate (MDI), toluene diisocyanate, Isophorone diisocyanate, dimethyl-meta-isopropenylbenzyl isocyanate be used.
  • TXDI m-tetramethylxylene diisocyanate
  • MDI methylene diphenyl diisocyanate
  • Isophorone diisocyanate dimethyl-meta-isopropenylbenzyl isocyanate
  • 2-component systems are those which cross-linked polysiloxanes.
  • Such systems contain as Component A) Dialkylpolysiloxanes with the same or different Alkyl radicals with 1 to 4 carbon atoms, which are optionally substituted can be, and which as terminal end groups hydroxyl or Contain vinyl groups.
  • component B) in the case of Hydroxyl end group used silicic acid esters such as tetraethyl silicate.
  • platinum catalysts are used used as component B) (RTV), or peroxides such as aroyl peroxides (Bis-2,4-dichlorobenzoyl peroxide, bis-4-methylbenzoyl peroxide) and alkyl peroxides (dicumyl peroxide, 2,5-di-t-butylperoxy-2,5-dimethylhexane) (HTV).
  • aroyl peroxides Bis-2,4-dichlorobenzoyl peroxide, bis-4-methylbenzoyl peroxide
  • alkyl peroxides dicumyl peroxide, 2,5-di-t-butylperoxy-2,5-dimethylhexane
  • HTV alkyl peroxides
  • Systems with an amino functional are also suitable Polysiloxane as component A) and an epoxy functional Polysiloxane as component B).
  • Other examples are Dimethylpolysiloxanes as component A) and condensation catalysts such as
  • compositions with carboxyl functional Styrene-n-butyl acrylate and / or styrene-methyl methacrylate-n-butyl acrylate copolymer as component A) and with glycidyl methacrylate Styrene-n-butyl acrylate and / or styrene-methyl methacrylate-n-butyl acrylate copolymer as component B).
  • components A) and B) can be in dry, powdered form Form (dry gluing), in the form of an aqueous dispersion or an aqueous solution (wet gluing).
  • the Components A) and B) can both be powder or both can be used as an aqueous solution or aqueous dispersion. Powders, aqueous solutions or aqueous dispersions can also be used are used, which each contain a component, can be used in any combination.
  • the binder components A) and B) are generally separated as a 2-component system used. When using powdered binder if necessary, the fibers with water or a Olefin wax emulsion to be moistened. 2 to 10% by weight Water (olefin wax emulsion), based on binder, on the Sprayed on fibers or chips.
  • the binder composition is shown in an amount of 2 to 30% by weight, preferably in an amount of 7 up to 15% by weight, based on wood (solid / solid).
  • Wood chips are used to manufacture MDF or HDF fibreboards usually via a hopper and a Snail transported into the refiner system cooker. There will be the wood chips for a few minutes, generally 5 to 15 minutes, at a water vapor pressure of 1 to 8 bar and a temperature from 120 to 200 ° C. Then they are softened Schnitzel, for example by means of another snail, conveyed to the mill of the refining plant, usually one Disc refiner, where the wood chips between grinding discs be frayed. For gluing, the fibers are still under steam pressure and at temperatures from 120 ° C to Conveyed 150 ° C into the expansion pipe (blow-line) of the refiner system.
  • Spruce wood chips were refined at 5 bar and 147 ° C for 5 min cooked and with grinding wheel spacing 0.1 mm with a power consumption of approximately 20 kW.
  • the fibers were glued without Dried to 2% residual moisture and temporarily stored without compression.
  • the glued fibers were evenly spread by hand in a 50 x 50 cm 2 , 40 cm high frame and compacted at room temperature. This mat was removed from the frame and placed in a flat press and pressed to a nominal density of 3 mm at 200 ° C. for up to 50 bar. The hot plate was placed in an insulation box to complete the crosslinking reaction and kept warm for 12 hours, then cut to size and subjected to the property tests.
  • Spruce wood chips were refined at 5 bar and 147 ° C for 5 min cooked and with grinding wheel spacing 0.1 mm with a power consumption of approximately 20 kW.
  • the glued Fibers were then dried to 2% residual moisture and temporarily stored without compression.
  • the glued fibers were evenly spread by hand in a 50 x 50 cm 2 , 40 cm high frame and compacted at room temperature. This mat was removed from the frame and placed in a flat press and pressed for 180 seconds at 200 ° C. with a pressure of up to 50 bar to a target density of 3 mm. The plate was then cut to size and subjected to property tests.
  • Spruce wood chips were cooked in the refiner at 5 bar and 147 ° C for 5 min and ground with a grinding wheel spacing of 0.1 mm with a power consumption of approx. 20 kW.
  • an aqueous dispersion of a styrene-butyl acrylate-acrylic acid copolymer with a Tg> 50 ° C. was added in an amount of 9% by weight (solid / solid).
  • the glued fibers were then dried to 2% residual moisture, and the dried fibers were mixed with 6% by weight of powdered styrene-butyl acrylate-glycidyl methacrylate copolymer with a Tg> 50 ° C.
  • Comparative example 1 shows high transverse tensile and bending strength, as well as low water swelling. Since the phenolic resin was not added in the refiner, but at room temperature on dry fibers, full crosslinking was available during pressing. The subsequent long thermal treatment is disadvantageous in order to allow the crosslinking reaction to proceed to completion. Another disadvantage is the high risk of splintering of the press plates, due to the high degree of crosslinking and the low flexibility of the resin. This is particularly undesirable in automotive applications because of the risk of injury in the event of an accident. The plate was colored yellow-brown and had a distinct unpleasant smell.
  • Comparative example 2 leads to similar strengths and swelling values like comparative example 1. Particularly striking is the bending tests the deflection of more than 29 mm without a plate break to get. Because the binder after the fiber drying full networking capacity has been added.
  • Comparative example 3 was bonded via wet sizing with the same resin as comparative example 2 via dry sizing.
  • wet gluing the resin is generally distributed more evenly on the fiber surface due to the stronger turbulence and the long mixing section. A stronger bond of the fibers in the press plate is expected.
  • a comparison of the values shows, however, that wet gluing is slightly weaker than dry gluing. The cause of the loss of binding is that some of the networking already takes place in the refiner. When pressing, the resin then flows poorly and can no longer set as well.
  • Example 4 shows the best strengths.
  • only one component with thermally stable functional groups was introduced in the wet gluing and an optimal binder distribution was achieved.
  • the second component with crosslinkable, thermally unstable groups was added by means of dry gluing at short-term and low thermal loads. This means that the full networking capacity is available for pressing.

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)
  • Chemical And Physical Treatments For Wood And The Like (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Adhesives Or Adhesive Processes (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Diaphragms For Electromechanical Transducers (AREA)
  • Die Bonding (AREA)
  • Optical Couplings Of Light Guides (AREA)
EP01124400A 2000-11-02 2001-10-25 Procédé pour la fabrication de panneaux en fibres de bois Expired - Lifetime EP1203648B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10054163 2000-11-02
DE10054163A DE10054163A1 (de) 2000-11-02 2000-11-02 Verfahren zur Herstellung von Holzpressplatten

Publications (3)

Publication Number Publication Date
EP1203648A2 true EP1203648A2 (fr) 2002-05-08
EP1203648A3 EP1203648A3 (fr) 2002-06-12
EP1203648B1 EP1203648B1 (fr) 2005-09-21

Family

ID=7661795

Family Applications (1)

Application Number Title Priority Date Filing Date
EP01124400A Expired - Lifetime EP1203648B1 (fr) 2000-11-02 2001-10-25 Procédé pour la fabrication de panneaux en fibres de bois

Country Status (5)

Country Link
US (1) US6998078B2 (fr)
EP (1) EP1203648B1 (fr)
AT (1) ATE304926T1 (fr)
DE (2) DE10054163A1 (fr)
PL (1) PL194920B1 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008152018A1 (fr) * 2007-06-13 2008-12-18 Basf Se Procédé de réalisation de corps moulés
WO2009037143A1 (fr) * 2007-09-17 2009-03-26 Basf Se Billes de cellulose consolidées par un liant
CN113279289A (zh) * 2021-07-23 2021-08-20 南通跃香拉链有限公司 一种纤维板的半干式气流成型制备工艺

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1541568A1 (fr) * 2003-12-09 2005-06-15 Deutsches Wollforschungsinstitut an der Rheinisch-Westfälischen Technischen Hochschule Aachen e.V. Carbonates et urées cycliques et réactifs pour la modification de biomolecules, polymères et surfaces
EP1754012A1 (fr) * 2004-05-24 2007-02-21 Basf Aktiengesellschaft Corps moules realises dans des materiaux contenant de la lignocellulose
DE102005019627B3 (de) * 2005-04-26 2006-10-26 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Verfahren zur Herstellung von mitteldichten Faserplatten und Faserformteilen mit verringerter Emission und niedriger Dickenquellung
CA2686564C (fr) 2007-05-15 2018-04-17 American Power Conversion Corporation Procedes et systemes pour gerer la puissance et le refroidissement d'une installation
EP2300205A4 (fr) 2008-06-08 2013-06-19 Robert N Clausi Processus de production d un hdf, d un mdf et d un panneau de particules de bois élastiques
US8219362B2 (en) 2009-05-08 2012-07-10 American Power Conversion Corporation System and method for arranging equipment in a data center
RU2474545C1 (ru) * 2011-11-01 2013-02-10 Юлия Алексеевна Щепочкина Сырьевая смесь для изготовления теплоизоляционных изделий
WO2013095516A1 (fr) 2011-12-22 2013-06-27 Schneider Electric It Corporation Analyse d'effet d'événements transitoires sur la température dans un centre de données
RU2484037C1 (ru) * 2012-02-22 2013-06-10 Юлия Алексеевна Щепочкина Сырьевая смесь для изготовления теплоизоляционных изделий

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1983004387A1 (fr) * 1982-06-07 1983-12-22 Sunds Defibrator Ab Procede de fabrication de plaques de fibres par la technique par voie seche
WO1997028935A1 (fr) * 1996-02-08 1997-08-14 Kramer Juergen Procede de production de panneaux de particules ou de panneaux de fibres

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6227107A (ja) * 1985-07-29 1987-02-05 Mitsui Toatsu Chem Inc パ−チクルボ−ド
DE4316498C2 (de) * 1993-05-17 2001-03-01 Lignotock Gmbh Verfahren zur Herstellung von bindemittelhaltigen Holzfaserformteilen
DE19511130A1 (de) * 1995-03-27 1996-10-02 Basf Ag Verwendung kationisch stabilisierter wäßriger Polymerisatdispersionen als Bindemittel für Formkörper auf der Basis von eine negative Oberflächenladung aufweisenden feinteiligen Materialien
DE19606393A1 (de) * 1996-02-21 1997-08-28 Basf Ag Formaldehydfreie Bindemittel für Formkörper
DE19618271C2 (de) * 1996-05-07 1999-10-28 Edmund Zimmermann Verfahren zur Herstellung von Formkörpern aus fasrigen Pflanzenteilen und/oder Naturfasern und entsprechende Formkörper
DE19621573A1 (de) 1996-05-29 1997-12-04 Basf Ag Thermisch härtbare, wäßrige Zusammensetzungen
DE19729161A1 (de) * 1997-07-08 1999-01-14 Basf Ag Thermisch härtbare, wässrige Zusammensetzungen
DE19735959A1 (de) * 1997-08-19 1999-02-25 Basf Ag Verwendung thermisch härtbarer, wässriger Zusammensetzungen als Bindemittel für Formkörper
DE10054162A1 (de) * 2000-11-02 2002-05-16 Wacker Polymer Systems Gmbh Verfahren zur Herstellung von Holzpressplatten

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1983004387A1 (fr) * 1982-06-07 1983-12-22 Sunds Defibrator Ab Procede de fabrication de plaques de fibres par la technique par voie seche
WO1997028935A1 (fr) * 1996-02-08 1997-08-14 Kramer Juergen Procede de production de panneaux de particules ou de panneaux de fibres

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008152018A1 (fr) * 2007-06-13 2008-12-18 Basf Se Procédé de réalisation de corps moulés
US8512618B2 (en) 2007-06-13 2013-08-20 Basf Se Process for the production of moldings
WO2009037143A1 (fr) * 2007-09-17 2009-03-26 Basf Se Billes de cellulose consolidées par un liant
CN113279289A (zh) * 2021-07-23 2021-08-20 南通跃香拉链有限公司 一种纤维板的半干式气流成型制备工艺
CN113279289B (zh) * 2021-07-23 2021-09-28 南通跃香拉链有限公司 一种纤维板的半干式气流成型制备工艺

Also Published As

Publication number Publication date
DE10054163A1 (de) 2002-06-06
PL350381A1 (en) 2002-05-06
EP1203648B1 (fr) 2005-09-21
US20020074096A1 (en) 2002-06-20
PL194920B1 (pl) 2007-07-31
DE50107476D1 (de) 2006-02-02
US6998078B2 (en) 2006-02-14
ATE304926T1 (de) 2005-10-15
EP1203648A3 (fr) 2002-06-12

Similar Documents

Publication Publication Date Title
EP1203647B1 (fr) Procédé pour la fabrication de panneaux en fibres de bois
EP1448733B1 (fr) Liants thermodurcissables
EP2242797B1 (fr) Liants exempts de formaldéhyde utilisés pour produire des matériaux ligneux
EP1240205B1 (fr) Dispersion polymere thermodurcissable
DE69915700T2 (de) Gemischte pmdi/resolharz-bindemittel zur herstellung von holzverbundprodukten
EP1203648B1 (fr) Procédé pour la fabrication de panneaux en fibres de bois
EP1858677A1 (fr) Production de corps moules en materiaux finements divises a base de lignocellulose
EP2346682A1 (fr) Corps moulés multicouches contenant de la lignocellulose, à faible émission de formaldéhyde
EP1260530A1 (fr) Liant thermodurcissable
EP2614117B1 (fr) Corps moulés multicouches contenant de la lignocellulose, à faible émission de formaldéhyde
DE60120376T2 (de) Klebstoffsystem enthaltend veretherte aminoplastharze
EP1232211B1 (fr) Liant utilise pour la production de corps moules et corps moules produits par utilisation dudit liant
DE69828342T2 (de) Holzverbundwerkstoffe
WO2007071387A2 (fr) Fibre vegetale, element moule a base de fibres et procede de production de fibres vegetales dotees de novolak
EP1525264A1 (fr) Procede de fabrication de pieces usinees en fibres de bois ignifugees
DE4229396C2 (de) Verfahren zur Herstellung von Span- oder Faserplatten
DE19949591A1 (de) Thermisch härtbare, wässrige Zusammensetzung
DE69810574T2 (de) Phenol-Melamin-Harnstoff-Formaldehyd-Copolymerharzmischungen, Verfahren zu ihrer Herstellung und Härtungskatalysatoren
EP0067426B1 (fr) Fabrication de planches de construction par utilisation de liant isocyanate-aldéhyde
EP3694641B1 (fr) Système de support poreux destiné à réduire l'émission de formaldéhyde dans un matériau dérivé du bois
EP1430101B1 (fr) Procede de production de corps faconnes contenant de la lignocellulose
WO2024088944A1 (fr) Procédé de production d'un composite lignocellulosique et composition de liant correspondante, composite lignocellulosique, kit et utilisation
DE1198055B (de) Verfahren zur Herstellung von Holzspanplatten und Holzspanformteilen aus vorgeformten Holzspanwerkstoffen
DE2336979A1 (de) Verfahren zur herstellung schwerentflammbarer holzwerkstoffe

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

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

17P Request for examination filed

Effective date: 20011025

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

AX Request for extension of the european patent

Free format text: AL;LT;LV;MK;RO;SI

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

AX Request for extension of the european patent

Free format text: AL;LT;LV;MK;RO;SI

AKX Designation fees paid

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

17Q First examination report despatched

Effective date: 20030616

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

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 CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20050921

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20050921

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20050921

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20051025

REF Corresponds to:

Ref document number: 50107476

Country of ref document: DE

Date of ref document: 20051027

Kind code of ref document: P

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20051031

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20051031

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20051031

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20051031

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20051121

GBT Gb: translation of ep patent filed (gb section 77(6)(a)/1977)

Effective date: 20051114

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20051221

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20051221

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20060101

REG Reference to a national code

Ref country code: SE

Ref legal event code: TRGR

REF Corresponds to:

Ref document number: 50107476

Country of ref document: DE

Date of ref document: 20060202

Kind code of ref document: P

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20060221

REG Reference to a national code

Ref country code: IE

Ref legal event code: FD4D

ET Fr: translation filed
REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

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

Effective date: 20060622

BERE Be: lapsed

Owner name: WACKER POLYMER SYSTEMS G.M.B.H. & CO. KG

Effective date: 20051031

NLS Nl: assignments of ep-patents

Owner name: WACKER CHEMIE AG

Effective date: 20080916

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

REG Reference to a national code

Ref country code: FR

Ref legal event code: TP

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 20101014

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20101022

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20101021

Year of fee payment: 10

Ref country code: IT

Payment date: 20101025

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20111025

Year of fee payment: 11

Ref country code: SE

Payment date: 20111021

Year of fee payment: 11

Ref country code: FR

Payment date: 20111103

Year of fee payment: 11

REG Reference to a national code

Ref country code: NL

Ref legal event code: V1

Effective date: 20130501

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 304926

Country of ref document: AT

Kind code of ref document: T

Effective date: 20121025

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20121025

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20130628

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20121025

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20121025

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130501

Ref country code: SE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20121026

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 50107476

Country of ref document: DE

Effective date: 20130501

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

Effective date: 20121025

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20121031

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20130501