WO2007082837A1 - Verfahren zur reduktion der formaldehydemission bei holzwerkstoffen - Google Patents
Verfahren zur reduktion der formaldehydemission bei holzwerkstoffen Download PDFInfo
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- WO2007082837A1 WO2007082837A1 PCT/EP2007/050272 EP2007050272W WO2007082837A1 WO 2007082837 A1 WO2007082837 A1 WO 2007082837A1 EP 2007050272 W EP2007050272 W EP 2007050272W WO 2007082837 A1 WO2007082837 A1 WO 2007082837A1
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- WO
- WIPO (PCT)
- Prior art keywords
- polyamine
- wood
- weight
- formaldehyde
- coating
- Prior art date
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27N—MANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
- B27N1/00—Pretreatment of moulding material
- B27N1/003—Pretreatment of moulding material for reducing formaldehyde gas emission
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27K—PROCESSES, APPARATUS OR SELECTION OF SUBSTANCES FOR IMPREGNATING, STAINING, DYEING, BLEACHING OF WOOD OR SIMILAR MATERIALS, OR TREATING OF WOOD OR SIMILAR MATERIALS WITH PERMEANT LIQUIDS, NOT OTHERWISE PROVIDED FOR; CHEMICAL OR PHYSICAL TREATMENT OF CORK, CANE, REED, STRAW OR SIMILAR MATERIALS
- B27K3/00—Impregnating wood, e.g. impregnation pretreatment, for example puncturing; Wood impregnation aids not directly involved in the impregnation process
- B27K3/02—Processes; Apparatus
- B27K3/15—Impregnating involving polymerisation including use of polymer-containing impregnating agents
- B27K3/153—Without in-situ polymerisation, condensation, or cross-linking reactions
-
- 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
- B27N7/00—After-treatment, e.g. reducing swelling or shrinkage, surfacing; Protecting the edges of boards against access of humidity
- B27N7/005—Coating boards, e.g. with a finishing or decorating layer
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27K—PROCESSES, APPARATUS OR SELECTION OF SUBSTANCES FOR IMPREGNATING, STAINING, DYEING, BLEACHING OF WOOD OR SIMILAR MATERIALS, OR TREATING OF WOOD OR SIMILAR MATERIALS WITH PERMEANT LIQUIDS, NOT OTHERWISE PROVIDED FOR; CHEMICAL OR PHYSICAL TREATMENT OF CORK, CANE, REED, STRAW OR SIMILAR MATERIALS
- B27K2200/00—Wooden materials to be treated
- B27K2200/15—Pretreated particles or fibres
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/14—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers
- B32B37/24—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers with at least one layer not being coherent before laminating, e.g. made up from granular material sprinkled onto a substrate
- B32B2037/243—Coating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2607/00—Walls, panels
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B37/00—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding
- B32B37/14—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers
- B32B37/16—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers with all layers existing as coherent layers before laminating
- B32B37/18—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers with all layers existing as coherent layers before laminating involving the assembly of discrete sheets or panels only
- B32B37/182—Methods or apparatus for laminating, e.g. by curing or by ultrasonic bonding characterised by the properties of the layers with all layers existing as coherent layers before laminating involving the assembly of discrete sheets or panels only one or more of the layers being plastic
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L79/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen or carbon only, not provided for in groups C08L61/00 - C08L77/00
- C08L79/02—Polyamines
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31855—Of addition polymer from unsaturated monomers
- Y10T428/3188—Next to cellulosic
- Y10T428/31895—Paper or wood
Definitions
- the present invention relates to a process for formaldehyde emission reduction in wood-based materials by treatment with polyamines. Furthermore, the present invention relates to a wood material, which can be produced by the present method, as well as laminates produced by the present process and the use of these wood materials and laminates for the production of furniture, packaging materials or interior fittings.
- Wood-based panels are a cost-effective and resource-saving alternative to solid wood and have gained great importance especially in furniture construction and as building materials.
- the starting materials are wood layers of different thicknesses, wood strips, wood shavings or wood fibers from different woods.
- Such wood parts or wood particles are usually pressed with natural and / or synthetic binders and optionally with the addition of further additives to plate or strand-shaped wood materials.
- Formaldehyde-containing adhesives are frequently used as binders, for example urea-formaldehyde resins or melamine-containing urea-formaldehyde resins.
- the resins are produced by polycondensation of formaldehyde with urea or melamine. In order to obtain good adhesive properties, an excess of formaldehyde is generally used. This can lead to free formaldehyde in the finished wood material. By hydrolysis of the polycondensates additional formaldehyde can be released. The free formaldehyde contained in the wood material and the formaldehyde released by hydrolysis during the lifetime of the wood material can be released to the environment.
- Coated wood-based materials generally have lower emissions of formaldehyde than uncoated substrates ("Wood as Raw Material", Volume 47, 1989, page 227).
- Formaldehyde may cause allergies, skin, respiratory or eye irritation above certain limits in humans.
- the reduction of formaldehyde emission in interior components is therefore an important concern.
- WO 2004/085125 A2 describes a method for reducing the emissions of bonded wood materials, in which mixtures of aldehyde- and isocyanate-reactive substances are applied to the straightened edges lying perpendicular to the direction of adhesive bonding. It should be retained both from the wood as well as from the adhesive escaping pollutants.
- substances which have an amino or amide group or hydroxyl-containing substances can be used. For example, urea, guanamine, ethylamine, ethanolamine, proteins, alcohols and carbohydrates are mentioned.
- JP 2002-273145 A describes a method for reducing the formaldehyde emissions of wood composites, in which a plurality of measures, each individually suitable for reducing the formaldehyde emission, are combined.
- the described aqueous formaldehyde scavenger is composed of 20 to 50 wt .-% urea, and a Residual of a non-volatile amine, a means to increase the permeability of the wood so that the urea and the non-volatile amine can penetrate into the composite, and a film-forming solid which, upon drying, becomes a physical barrier to the formaldehyde on the wood composite. This film can affect the coatability of wood composites.
- non-volatile amines and polyalkylenepolyamines are described.
- Such open areas can be found, for example, as holes in shelf walls or in furniture rear walls, which are required to ensure a flexibly adjustable height of the shelves.
- the edges of shelves that are not directed into the living area usually not surface-coated and thus open. For some shelves, even the entire underside of the shelf is uncoated, which thus presents open surfaces from which formaldehyde escapes.
- the solution of the problem is based on the known methods for reducing the formaldehyde emission in wood materials by applying nitrogen-containing compounds.
- the inventive method is then characterized in that (i) a mixture comprising at least one polyamine and optionally up to 20% by weight, based on the mixture, of urea is applied to the wood-based material;
- polyamine is applied to the open areas; wherein the polyamines have a molecular weight of at least 500 g / mol and at least 6 primary or secondary amino groups
- chip or fiber cake is understood to mean scattered, glued chips or fibers which have been precompressed if necessary, The chip or fiber cake generally has at least twice the thickness of the finished wood material.
- coating substrate is understood as meaning, for example, aminoplast resin films, in particular melamine films, prepregs, films, laminates or veneers, and the like.
- open spots in the present invention, holes, uncoated open edges or surfaces and the like understood, as they arise, for example, by subsequent drilling, milling or sawing after the surface finishing.
- the polyamine can be applied in aqueous form or without the addition of solvents.
- aqueous polyamine solution is used.
- a particular polyamine or mixtures of several polyamines can be used.
- the aqueous polyamine solution advantageously contains from 5 to 90% by weight of polyamine, preferably from 10 to 75% by weight of polyamine, in particular from 15 to 45% by weight of polyamine, particularly preferably from 25 to 40% by weight of polyamine, in each case based on the polymer solution ,
- polyamines which have a molecular weight of at least 500 g / mol, in particular at least 800 g / mol, and at least 6, in particular at least 10, primary or secondary amino groups.
- Preferred polyamines are hyperbranched polyamines, in particular polyethylenimine, or polyvinyl laminates or mixtures thereof.
- hyperbranched polyamines in the present invention means highly functional, highly branched and hyperbranched polymers which contain amino or amido groups.
- hyperbranched polyamines are any highly functional, highly branched and hyperbranched polyamines having a weight-average molecular weight of greater than 500 g / mol, whose main chain is branched, and which have a degree of branching (DB) of greater than or equal to zero , 05.
- DB degree of branching
- the degree of branching is advantageously 0.1 and greater.
- the degree of branching of the hyperbranched polyamines is preferably between 0.2 to 0.99, particularly preferably between 0.3 and 0.95 and in particular between 0.35 and 0.75. To define the degree of branching, see H. Frey et al., Acta Polym. 1997, 48, 30.
- the hyperbranched polyamines have at least four functional end groups, preferably at least eight functional end groups, in particular at least twenty functional end groups.
- the number of functional groups is in principle not limited above, but the hyperbranched polyamines of the present invention advantageously have fewer than 500 functional end groups, preferably less than 300 functional end groups, especially less than 150 functional end groups.
- the method of preparation of the hyperbranched polyamines is described, for example, in WO 1996/19537, WO 1999/16810, WO 2005/075541, WO 2005/044897, WO 2003/0066702 and in the earlier German patent application with the file reference 102005056592.1 and the title "Production and Use of highly functional, hyperbranched or hyperbranched polylysines "described.
- polyureas, polyamides, polythioureas, as well as combination of mixed forms with two or more of these functional groups such as polyamidoureas and polyamidothioureas, polyurea (thiourea) s, polyureaurethanes and polythiourea, polyester ureas and poly esteric thioureas, polyaminoureas and polyaminothioureas, polycarbonate ureas and polycarbonate thioureas, polyether ureas and polyether thioureas, polyamidourethanes, polyamidoesters, polyamidoamines, polyamidocarbonates, polyamidoethers, polyesterurethanes, polyaminourethanes, polycarbonate urethanes, polyetherurethanes, polyaminoesters, polyesteramides, polyamin
- Polyureas, polythioureas, polyureas, polyamides, poly. are particularly preferred as hyperbranched polymers esteramides used, in particular polyureas, polyureas, polyamides and in the polyamides particularly preferably polylysines.
- the weight-average molecular weight of the polyvinylamine is advantageously 5,000 to 500,000 g / mol, preferably 5,000 to 350,000 g / mol, in particular 5,000 to 100,000 g / mol.
- the weight-average molecular weight of the polyethyleneimine is advantageously from 500 to 100,000 g / mol, preferably from 500 to 70,000 g / mol, more preferably from 500 to 50,000 g / mol, very preferably from 800 to 20,000 g / mol and in particular from 2,000 to 20,000 g / mol.
- Polyethyleneimine can be prepared by acid catalyzed polymerization of ethyleneimine and is generally obtained as an aqueous solution at levels of from 20 to 100% by weight, preferably between 40 and 70% by weight, of polyethylenimine.
- Polyvinylamine can be prepared by polymerization of vinylformamide and subsequent hydrolysis and is generally obtained as an aqueous solution of from 2 to 50% by weight, preferably from 5 to 25% by weight. The degree of hydrolysis can be adjusted by the reaction conditions and determines the ratio of amine groups to formamide groups.
- these solutions can be used directly as a basis for the polyamine solutions according to the invention.
- optional component (b) of the aqueous polymer solution in order to improve the wettability, ionic and nonionic surfactants, as described, for example, in H. Stumblee, "Tensid-Taschenbuch", Carl Hanser Verlag, Kunststoff, Vienna, 1981, can be advantageous in concentration 0 to 5 wt .-%, preferably from 0 to 2 wt%, are used.
- the pH can be adjusted by the following additives as optional component (c): mineral or organic acids such as sulfuric acid or formic acid.
- Component (c) may be added to the aqueous polymer solution from 0 to 30% by weight, preferably from 0 to 20% by weight.
- component (d) further additives may be added to the aqueous polymer solution, for example additives from the group of water repellents, e.g. As paraffin emulsions and waxes, fungicides, organic solvents or dyes.
- Component (d) may be added to the aqueous polymer solution from 0 to 30% by weight, preferably from 0 to 10% by weight.
- the aqueous polyamine solution may advantageously contain up to 20% by weight of urea, based on the polymer solution.
- the aqueous polymer solution particularly advantageously contains less than 15% by weight of urea, preferably less than 10% by weight of urea and in particular less than 5% by weight of urea, in each case based on the polymer solution.
- the polymer solution is free of urea.
- the polyamine solution is advantageously applied at a pH of 3 to 12.
- the polyamine solution is preferably applied with a pH of 7 to 11, more preferably with a pH of 9 to 1 1, wherein protonation of the polyamines can occur in the less preferred acidic range.
- the polyamine solution is preferably applied at a pH of 5 to 10, especially at a pH of 6 to 8.
- the polyamine solution is preferably applied at a pH of 6 to 11, especially at a pH of 9 to 11.
- a sufficient amount of polyamine solution is applied so that the amount of polyamine per square meter of surface area of the wood material is advantageously between 1 g and 200 g, preferably between 2 g and 50 g, more preferably between 3 g and 30 g (case (i) ).
- a sufficient amount of polyamine solution is applied so that the amount of polyamine per 100 kilograms of chip or fiber cake advantageously between 0.01 kg and 5 kg, preferably between 0.05 kg and 1 kg, in particular between 0, 1 kg and 0.5 kg.
- a sufficient amount of polyamine solution is applied so that the amount of polyamine per square meter of coating substrate is advantageously between 0.1 g and 100 g, preferably between 0.5 g and 30 g, in particular between 1 g and 15 g
- a sufficient amount of polyamine solution is applied so that the amount of active substance polyamine per square meter surface area of the surface of the surface-treated wood material is advantageously between 0.05 g and 200 g, preferably between 0.1 g and 50 g preferably between 0.3 g and 30 g and in particular between 0.5 and 10 g.
- the aqueous polymer solution can be applied to the wood-based material by various measures known to the person skilled in the art (case (i)). These include, for example, spraying, rolling, dipping, knife coating, brushing, curtain coating, preferably the polyamine solution is applied by spraying and rolling.
- the application of the polyamine or the aqueous polyamine solution to the chips or fiber cake can be carried out by various measures known to the person skilled in the art (case (N)). These include, for example, spraying, rolling, knife coating, brushing, curtain coating, preferably the amine solution is applied by spraying.
- the aqueous polyamine solution can be applied to the top and / or bottom of the fiber cake.
- the application of the polyamine or the aqueous polymer solution may be carried out at an elevated temperature or at room temperature.
- the polyamine or aqueous polyamine solution may be applied before or after the cold compression / pre-compression.
- the polyamine or polyamine solution may be in one or more layers and / or present between the individual layers.
- the polyamine is preferably applied to the cover layer (s), preferably to both cover layers, of the chip or fiber cake.
- the application to the lower cover layer for example, indirectly via the application to the conveyor belt, which conveys the fiber cake to the press, take place.
- the required amount of polyamine solution is applied to the conveyor belt, for example by spraying or rolling, and then the glued chips or fibers are scattered onto the conveyor belt.
- the polyamine or polyamine solution may be sprayed together with the vapor used to preheat the material of the press (see WO 2004/87388 and references herein).
- the swarf or fiber cake treated with polyamine is pressed into a wood-based material by processes known to those skilled in the art (see “MDF - Medium-Density Fiberboard", Hans-Joachim Deppe, Kurt Ernst, 1996, DRW-Verlag Weinbrenner GmbH & Co., 70771 Leinfelden-Echterdingen, chapter 4.3, pages 81ff .; see also EP 1 192 223 B1, paragraph [0034] and "Taschenbuch der Spanplattentechnik” Joachim Deppe, Kurt Ernst, 2000, DRW-Verlag Weinbrenner GMbH & Co., 70771 Leinfelden-Echterdingen, chapter 3.5, pages 232ff).
- the application of the aqueous polyamine solution or the polyamine to the coating substrate may be carried out by various means known to those skilled in the art. These include, for example, spraying, rolling, dipping, soaking, knife coating, brushing, curtain coating. Preferably, the amine solution is applied by spraying.
- the polyamine solution is applied to the backside of the coating substrate, i. on the wood material facing side, applied.
- the coating substrate is then pressed with wood-based material by methods known to those skilled in the art.
- the aqueous polyamine solution may be sprayed on the underside of the veneer.
- the glue liquor on the wood-based board, z. B. chipboard the thus treated veneer is placed and pressed under temperature and pressure.
- the aqueous polyamine solution (A) may be applied to the paper, e.g. Decorative paper or overlay paper,
- (B1) can be added to the impregnating resin liquor for pre-impregnation
- (B2) can be added to the impregnating resin liquor for post-impregnation / coating
- the aqueous polyamine solution is applied after drying the impregnated paper.
- the preparation of the coating substrates resin film or laminate is generally carried out by the impregnation of papers, for example a) kraft papers with a basis weight between 50 to 150 g / m 2 , b) printed decorative papers with a basis weight between 50 to 150 g / m 2 or c ) Overlay papers with a basis weight of 20 to 50 g / m 2 , by means of aqueous resin solutions, wherein the papers soaked with the resin solution and / or the resin solution is alsgerakelt or painted on the paper. Subsequently, the substrate is up to a residual moisture / water content dried from 2 to 8%. It is usually a basis weight in the case of a) from 100 to 250 g / m 2 and in the case of b) and c) of 50 to 150 g / m 2 .
- a laminate usually consists of several layers of impregnated core paper, preferably 2 to 15 core papers, one or more impregnated decorative and / or overlay papers as the surface layer and optionally one or more impregnated webs of, for example, kraft paper.
- all the films used, only individual films, only the core papers or only the interface (s) coated film (s) may be polyamine treated, in particular sprayed.
- the outer paper (s) is treated.
- the pressing pressure is typically below 100 bar, the pressing time is usually up to 90 minutes and the pressing temperature is usually at a maximum of 150 ° C.
- the correspondingly produced laminates are then glued to the wood material by methods known to the person skilled in the art.
- application of the aqueous polymer solution to the open sites can be accomplished by various means known to those skilled in the art. These include, for example, spraying, rolling, knife coating, brushing or dripping.
- the polyamine solution is applied by spraying.
- the surface-treated wood material may have an elevated temperature during application or be at room temperature; Further, the polyamine solution can have an elevated temperature or room temperature during application.
- the application of the polyamine solution takes place under room temperature conditions.
- the device for applying, in particular spraying, the polyamine solution may be coupled to the device for drilling or arranged laterally offset therefrom.
- the device for applying, in particular spraying, the polyamine solution may be coupled to the device for drilling or arranged laterally offset therefrom.
- the device for rolling or spraying may be integrated into a device for rolling or spraying the polyamine solution.
- Wood-based materials are all materials which are made of wood strips, such as veneer boards or plywood boards, wood-based materials produced from wood chips, for example chipboard or OSB boards, and wood fiber boards. Materials such as LDF, MDF and HDF boards. These wood-based materials are produced from the corresponding wood particles with the addition of natural and / or synthetic binders by hot pressing.
- wood-based materials containing formaldehyde are produced by the process according to the invention. Preference is given to OSB, wood fiber and chipboard.
- the wood-based materials can be surface-treated after pressing by grinding.
- the application of the polyamines according to the invention can be carried out before or after the grinding, preferably after grinding.
- the wood-based material may have an elevated temperature during application or may be at room temperature.
- the wood-based material can also be heat-treated after application, for example by infrared radiation, heated rollers or in a heat channel.
- the polyamines can be applied on one side or on both sides, preferably on both sides.
- the invention further provides the wood materials obtainable by the process according to the invention, in particular formaldehyde-containing binders, optionally surface-refined wood-based materials. Preference is given to treated optionally surface-treated chipboard and wood fiber boards according to the invention.
- the wood-based materials obtained by the process in the case of (i) and (ii) can then optionally be surface-treated.
- the surface finishing can be done by coating with different materials.
- a coating, veneering, lamination or lamination can be carried out or a coating with melamine films, prepregs or films can be carried out.
- Such surface-treated wood materials are also the subject of the invention.
- the invention also relates to laminates which contain at least one polyamine-treated film selected from the group of the counteracting films, core films, decorative films or overlay films.
- the wood material produced according to the invention advantageously has a formaldehyde emission of 0 to 0.1 ppm, preferably from 0 to 0.04 ppm, in particular from 0 to 0.02 ppm (EN 717-1 "Formaldehyde emission by the test chamber method"), or a formaldehyde emission of advantageously 0 to 3.5 mg / m 2 h, preferably from 0 to 2 mg / m 2 h, in particular from 0 to 1 mg / m 2 h (EN 717-2 "Formaldehyde release by the gas analysis method").
- the wood-based materials according to the invention can be used for the production of furniture, packaging materials, in building construction, in dry construction or in interior work, for example as a laminate, insulating material, wall or ceiling element.
- Example 2 pure urea solution (not according to the invention)
- a 30% urea solution was applied to the chipboard in an amount that leads to a urea amount of 40 g / m 2 , heated to 60 ° C for 150 seconds and then stored for 1 day at 20 ° C / 65% humidity.
- Example 3 Polyethyleneimine solution (according to the invention)
- a 30% aqueous solution of a polyethyleneimine having an average molecular weight of 5,000 g / mol was sprayed on the chipboard so that 40 g / m 2 of polyethylenimine was applied to the chipboard. Thereafter, the surface was heated to 60 ° C. within 150 seconds and then stored for 1 day at 20 ° C./65% air humidity.
- Example 4 Polyethyleneimine solution (according to the invention)
- a 25% aqueous solution of a polyethyleneimine having an average molecular weight of 5,000 g / mol was sprayed onto the chipboard so that 5 g / m 2 of polyethylenimine was applied to the chipboard. Subsequently, 1 day at 20 ° C / 65% humidity was stored.
- Example 5 Adjustment of the formaldehyde scavenger of Examples 4 to 6 of JP 2002 273145 (Comparative Example)
- Formaldehyde emission with or without aftertreatment was determined in accordance with the DIN standard DIN EN717-2 (Determination of formaldehyde release Part 2: Formaldehyde release by the gas analysis method) from 1994, and the DIN standard DIN-EN717-1 (determination of formaldehyde release Part 1: formaldehyde release according to the test chamber method) from the year 2004 and the DIN standard DIN-EN 120 (determination of the formaldehyde content: extraction method, called perforator method) from the year 1992 determined.
- DIN standard DIN EN717-2 Determination of formaldehyde release Part 2: Formaldehyde release by the gas analysis method
- DIN standard DIN-EN717-1 determination of formaldehyde release Part 1: formaldehyde release according to the test chamber method
- DIN standard DIN-EN 120 determination of the formaldehyde content: extraction method, called perforator method
- the air flow is set to 60 l / h.
- the escaping air is collected in a gas wash bottle containing an aqueous solution of acetylacetone and ammonium acetate.
- Formaldehyde reacts in aqueous solution with ammonium ions and acetylacetone to diacetyldihydrolutidine (DDL). This reaction is highly specific for formaldehyde.
- the DDL has an absorption maximum at 412 nm and can be quantitatively detected by spectroscopy. To determine the formaldehyde concentration, the values for the last 3 hours are averaged.
- test specimens with the dimensions 0.5 x 0.5 x thickness x in the 3 with 0.75 m open edge are placed in a test chamber with the volume 1 in the 3 .
- the measurement is carried out for at least 10 to a maximum of 28 days at 23 ° C and a relative humidity of 45 +/- 3%.
- the air intake and exhaust is chosen so that the entire air is replaced once within 1 hour.
- 120 l of air are passed at a rate of 2 l / min into a gas scrubber bottle filled with aqueous ammonium acetate and acetylacetone solution.
- the formaldehyde concentration is also determined spectroscopically.
- the formaldehyde emission results from this method from a compensation curve, while 4 consecutive values may vary by no more than 5%. Is after 28 days If this condition is not fulfilled, the last 4 values are used for averaging.
- the EN 120 uses test specimens measuring 25 mm x 25 mm x thickness. About 110 g of test specimen are added together with 600 ml of toluene to the flask with perforator attachment. The toluene is boiled. The formaldehyde is released in the perforator to the water and determined photometrically.
- the chipboards 1-3 were coated after 24 h under standard conditions (20 ° C / 65% humidity) as follows:
- a white decorative paper (80 g / m 2 ) was impregnated with 100 g / m 2 of a resin liquor of Kauramin impregnating resin 792 and hardener 529 (100: 0.3) and dried in the oven at 160 ° C. The resulting film is placed on the surface of the chipboard and pressed (190 ° C, 25 bar, 35 s). To stabilize the test piece, a counter pull film is simultaneously pressed on the back side.
- a lattice test is carried out. To do this, use a razor blade to make two parallel four parallel cuts (0.5 cm apart) the surface is made so that a diamond-shaped pattern is created. In the corners of the diamonds, there is a partial flaking of the coating. The percentage of destroyed surface is determined. The smaller the value, the better the coatability of the chipboard.
- a 0.6 mm beech veneer was coated on the underside with a) 10 g / m 2 (3 g / m 2 active substance) and b) 20 g / m 2 (6 g / m 2 active substance) of a 30% aqueous polyethylenimine. Solution (weight-average molecular weight of the polyethyleneimine: 5000 g / mol) sprayed and then dried.
- a glue liquor consisting of 100 parts of Kaurit® glue 329 and 20 parts of Bonit® hardener 12926 were applied to a commercially available chipboard (thickness of 16 mm and density of 650 kg / m 3 ).
- the veneer was laid on and pressed at 105 ° C press temperature and a pressure of 0.6 N / mm 2 .
- the pressing time was 100 seconds.
- the decorative film was coated on the underside with a) 10 g / m 2 (3 g / m 2 active substance) and b) 20 g / m 2 (6 g / m 2 active substance) of a 30% polyethyleneimine aqueous solution (weight average molecular weight of Polyethyleneimine: 5000 g / mol) sprayed and then dried.
- the polyamine-treated decorative film was pressed on a commercially available chipboard (thickness of 16 mm and density of 650 kg / m 3 ) by means of a laboratory press at 180 ° C, the pressing pressure was 25 bar and the pressing time was 30 seconds.
- Example 8 Uranium-aftertreated wood material according to the prior art A 30% urea solution was applied to a commercial chipboard (thickness of 16 mm and density of 650 kg / m 3) in an amount which resulted in a urea amount of 40 g / m 2 ), heated to 60 ° C in 150 seconds and then stored for 1 day at 20 ° C / 65% humidity.
- a white decorative paper (80 g / m 2 ) was impregnated with 100 g / m 2 of a resin liquor of Kauramin® impregnating resin 792 and hardener 529, in a ratio of 100: 0.3, and dried in the oven at 160 ° C.
- the film thus obtained was placed on the surface of the chipboard and pressed (190 ° C, 25 bar, 35 s). To stabilize the test piece, a counter pull film was simultaneously pressed on the back side.
- Table 3 Overview of the formaldehyde emissions of the particleboard of Examples 6 to 8
- PEI polyethyleneimine
- U urea
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Forests & Forestry (AREA)
- Manufacturing & Machinery (AREA)
- Chemical And Physical Treatments For Wood And The Like (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
- Finished Plywoods (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
Abstract
Description
Claims
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP07703814A EP1979139A1 (de) | 2006-01-17 | 2007-01-12 | Verfahren zur reduktion der formaldehydemission bei holzwerkstoffen |
CN200780002439.6A CN101370626B (zh) | 2006-01-17 | 2007-01-12 | 降低木材中甲醛排放的方法 |
NZ569380A NZ569380A (en) | 2006-01-17 | 2007-01-12 | Method for the reduction of formaldehyde emissions in wood materials |
BRPI0706437-3A BRPI0706437A2 (pt) | 2006-01-17 | 2007-01-12 | processo para a redução da emissão de formaldeìdo de material à base de madeiras, material à base de madeira, laminado, e, uso do material à base de madeira |
CA 2631869 CA2631869C (en) | 2006-01-17 | 2007-01-12 | Method for the reduction of formaldehyde emissions in wood materials |
AU2007206994A AU2007206994B2 (en) | 2006-01-17 | 2007-01-12 | Method for the reduction of formaldehyde emissions in wood materials |
US12/161,276 US8460761B2 (en) | 2006-01-17 | 2007-01-12 | Method for reduction of formaldehyde emissions in wood materials |
JP2008550726A JP5328370B2 (ja) | 2006-01-17 | 2007-01-12 | 木質材料においてホルムアルデヒド放散を減少させるための方法 |
NO20082648A NO20082648L (no) | 2006-01-17 | 2008-06-05 | Fremgangsmate for reduksjon av formaldehydutslipp i trematerialer |
Applications Claiming Priority (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP06100479.2 | 2006-01-17 | ||
EP06100479A EP1808278A1 (de) | 2006-01-17 | 2006-01-17 | Verfahren zur Reduktion der Formaldehydemission bei Holzwerkstoffen |
EP06118010.5 | 2006-07-27 | ||
EP06118001 | 2006-07-27 | ||
EP06118004 | 2006-07-27 | ||
EP06118004.8 | 2006-07-27 | ||
EP06118001.4 | 2006-07-27 | ||
EP06118010 | 2006-07-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2007082837A1 true WO2007082837A1 (de) | 2007-07-26 |
Family
ID=37969917
Family Applications (1)
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---|---|---|---|
PCT/EP2007/050272 WO2007082837A1 (de) | 2006-01-17 | 2007-01-12 | Verfahren zur reduktion der formaldehydemission bei holzwerkstoffen |
Country Status (10)
Country | Link |
---|---|
US (1) | US8460761B2 (de) |
EP (1) | EP1979139A1 (de) |
JP (1) | JP5328370B2 (de) |
AU (1) | AU2007206994B2 (de) |
BR (1) | BRPI0706437A2 (de) |
CA (1) | CA2631869C (de) |
MY (1) | MY146656A (de) |
NO (1) | NO20082648L (de) |
NZ (1) | NZ569380A (de) |
WO (1) | WO2007082837A1 (de) |
Cited By (9)
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WO2008005729A2 (en) * | 2006-06-30 | 2008-01-10 | Georgia-Pacific Chemicals Llc | Reducing formaldehyde emissions from fiberglass insulation |
WO2008005635A2 (en) * | 2006-06-30 | 2008-01-10 | Georgia-Pacific Chemicals Llc | Reducing formaldehyde emissions from fiberglass insulation |
DE102008049963A1 (de) | 2008-10-02 | 2010-04-08 | Treffert Coatings Gmbh | Wässriger Lack zur Reduktion der Formaldehydemission aus Holzwerkstoffen |
WO2011026977A1 (de) | 2009-09-07 | 2011-03-10 | Basf Se | Verbundformteil insbesondere für den möbelbau |
US8043383B2 (en) | 2006-06-30 | 2011-10-25 | Georgia-Pacific Chemicals Llc | Reducing formaldehyde emissions |
US8173219B2 (en) | 2006-06-09 | 2012-05-08 | Georgia-Pacific Chemicals Llc | Porous fiberglass materials having reduced formaldehyde emissions |
EP2565223A1 (de) | 2011-08-31 | 2013-03-06 | Basf Se | Expandierbares Granulat |
CN108070776A (zh) * | 2017-12-19 | 2018-05-25 | 南京蒙福液压机械有限公司 | 一种用于叶片泵的合金钢材料 |
EP2301344B2 (de) † | 2009-09-03 | 2020-01-15 | SWISS KRONO Tec AG | Fungizid wirksames Holzschutzmittel zur Verwendung in Holzfaserplatten |
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CN104645800B (zh) * | 2013-11-25 | 2016-08-17 | 北京市理化分析测试中心 | 甲醛捕捉剂及其制备方法 |
US20190016008A1 (en) * | 2015-08-07 | 2019-01-17 | Basf Se | Method for coating wood-based materials without abrading the surface |
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EP3290172A1 (de) * | 2016-09-02 | 2018-03-07 | SWISS KRONO Tec AG | Verwendung von schmelzklebstoffen zur reduzierung der emission von flüchtigen organischen verbindungen aus holzwerkstoffen |
JP2023549560A (ja) | 2020-11-17 | 2023-11-27 | オウェンス コーニング インテレクチュアル キャピタル リミテッド ライアビリティ カンパニー | ホルムアルデヒド捕捉配合物 |
CN114481694B (zh) * | 2022-02-28 | 2023-03-31 | 广东劳卡家具有限公司 | 浸胶纸板的制作方法 |
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
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US8173219B2 (en) | 2006-06-09 | 2012-05-08 | Georgia-Pacific Chemicals Llc | Porous fiberglass materials having reduced formaldehyde emissions |
WO2008005729A2 (en) * | 2006-06-30 | 2008-01-10 | Georgia-Pacific Chemicals Llc | Reducing formaldehyde emissions from fiberglass insulation |
WO2008005635A2 (en) * | 2006-06-30 | 2008-01-10 | Georgia-Pacific Chemicals Llc | Reducing formaldehyde emissions from fiberglass insulation |
WO2008005729A3 (en) * | 2006-06-30 | 2008-10-02 | Georgia Pacific Chemicals Llc | Reducing formaldehyde emissions from fiberglass insulation |
WO2008005635A3 (en) * | 2006-06-30 | 2008-10-09 | Georgia Pacific Chemicals Llc | Reducing formaldehyde emissions from fiberglass insulation |
US7989367B2 (en) | 2006-06-30 | 2011-08-02 | Georgia-Pacific Chemicals Llc | Reducing formaldehyde emissions from fiberglass insulation |
US8043383B2 (en) | 2006-06-30 | 2011-10-25 | Georgia-Pacific Chemicals Llc | Reducing formaldehyde emissions |
DE102008049963A1 (de) | 2008-10-02 | 2010-04-08 | Treffert Coatings Gmbh | Wässriger Lack zur Reduktion der Formaldehydemission aus Holzwerkstoffen |
EP2301344B2 (de) † | 2009-09-03 | 2020-01-15 | SWISS KRONO Tec AG | Fungizid wirksames Holzschutzmittel zur Verwendung in Holzfaserplatten |
WO2011026977A1 (de) | 2009-09-07 | 2011-03-10 | Basf Se | Verbundformteil insbesondere für den möbelbau |
EP2565223A1 (de) | 2011-08-31 | 2013-03-06 | Basf Se | Expandierbares Granulat |
CN108070776A (zh) * | 2017-12-19 | 2018-05-25 | 南京蒙福液压机械有限公司 | 一种用于叶片泵的合金钢材料 |
Also Published As
Publication number | Publication date |
---|---|
AU2007206994B2 (en) | 2011-02-10 |
AU2007206994A1 (en) | 2007-07-26 |
JP5328370B2 (ja) | 2013-10-30 |
JP2009523628A (ja) | 2009-06-25 |
US8460761B2 (en) | 2013-06-11 |
NZ569380A (en) | 2010-07-30 |
MY146656A (en) | 2012-09-14 |
US20100190021A1 (en) | 2010-07-29 |
CA2631869A1 (en) | 2007-07-26 |
EP1979139A1 (de) | 2008-10-15 |
BRPI0706437A2 (pt) | 2011-03-29 |
NO20082648L (no) | 2008-08-12 |
CA2631869C (en) | 2014-03-18 |
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