WO2000024800A1 - Resin and composite wood panels - Google Patents
Resin and composite wood panels Download PDFInfo
- Publication number
- WO2000024800A1 WO2000024800A1 PCT/AU1999/000928 AU9900928W WO0024800A1 WO 2000024800 A1 WO2000024800 A1 WO 2000024800A1 AU 9900928 W AU9900928 W AU 9900928W WO 0024800 A1 WO0024800 A1 WO 0024800A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- formaldehyde
- range
- comonomer
- composite panel
- binder composition
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/54—Polycondensates of aldehydes
- C08G18/544—Polycondensates of aldehydes with nitrogen compounds
-
- 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
- B27N3/002—Manufacture of substantially flat articles, e.g. boards, from particles or fibres characterised by the type of binder
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L97/00—Compositions of lignin-containing materials
- C08L97/02—Lignocellulosic material, e.g. wood, straw or bagasse
Definitions
- the present invention relates to resin for use in the manufacture of composite panels, composite panels and method of manufacture therefore.
- the present invention relates to formaldehyde based resin for use in the manufacture of composite board, which composite board has low formaldehyde emissions. Desirably, formaldehyde emissions are reduced to a level approaching the formaldehyde emission of timber.
- Wood composite panel products such as particle board and medium density fibre board (“MDF”) are generally manufactured using urea formaldehyde (“UF”) resins.
- UF resins have been manufactured with an excess of formaldehyde to impart increased cure speed and bond strength of the cured resin system.
- Formaldehyde free binders such as 4, 4'- methylenebis (phenyl isocyanate) (“MDI”).
- MDI 4, 4'- methylenebis (phenyl isocyanate)
- UF resins with low formaldehyde content which have been modified with melamine or phenol may also be used.
- the use of these modified UF resins may result in composite panels with improved dimensional stability, panels may still exhibit unacceptable levels of formaldehyde emissions.
- the present invention provides a binder composition
- a binder composition comprising a formaldehyde- based resin and an isocyanate containing compound wherein said formaldehyde-based resin comprises formaldehyde present in a molar ratio of formaldehyde to comonomer in the range of from about 0.2:1 to about 5:1 and wherein the isocyanate containing compound is present in an amount in the range of from about 0.5 to about 50% by weight of the binder composition.
- the binder composition may be supplied to a particle board manufacturer as a two-component system, the formaldehyde-based resin will generally be supplied separately to the isocyanate containing compound. Such a two component system represents a further aspect of the invention. Other additives may also be supplied separately or blended with either the formaldehyde-based resin or the isocyanate containing compound.
- the present invention provides a composite board comprising cellulose-based particles and a binder composition comprising a formaldehyde-based resin and an isocyanate containing compound wherein said formaldehyde-based resin comprises formaldehyde present in a molar ratio of formaldehyde to comonomer in the range of from about 0.2:1 to about 5:1 and wherein the isocyanate containing compound is present in an amount in the range of from about 0.5 to about 50% by weight of the binder composition.
- the present invention provides a method of manufacturing a composite panel comprising the steps of :
- a composite panel manufactured according to this process also represents a further aspect of the invention.
- the binder composition comprises a formaldehyde-based resin.
- Formaldehyde-based resins incorporate formaldehyde along with a comonomer or comonomers.
- the term "comonomer” will be used to refer to one or more comonomers suitable for forming a formaldehyde-based resin.
- the molar ratio of formaldehyde to comonomer is, in binary systems, such as urea- formaldehyde systems, the molar ratio of formaldehyde to comonomer is simply the molar ratio of the formaldehyde to the comonomer (i.e. urea). In the ternary, or more complex systems, the molar ratio of formaldehyde to comonomer is the molar ratio of the formaldehyde to the sum of the molar amounts of the comonomers.
- the formaldehyde-based resin comprises formaldehyde present in a molar ratio of formaldehyde to comonomer is in the range of from about 0.2:1 to about 5:1.
- the molar ratio of formaldehyde to comonomer is in the range of about 0.3 : 1 to about 4:1. More preferably the molar ratio of formaldehyde to comonomer is in the range of from about 0.4:1 to about 3.5:1.
- Suitable comonomers for use in the formaldehyde-based resin include polyfunctional amines, phenols, and other comonomers capable of forming copolymers with the formaldehyde.
- the polyfunctional amines comprise two or more primary, secondary and or tertiary amine groups.
- suitable polyfunctional amines include melamine, urea, guani dines, para- toluene sulfonamide, triazines, thiourea and dicyandiamide.
- Preferred polyfunctional amines include melamine and urea.
- the polyfunctional amine is urea.
- suitable phenols include phenol, resorcinol, tannins, lignins, bisphenol A, cresol and xylenol.
- the formaldehyde-based resin may be selected from the group consisting of urea formaldehyde resins, phenol formaldehyde resins, phenol urea formaldehyde resins, melamine urea formaldehyde resins, phenol melamine urea formaldehyde resins, phenol melamine formaldehyde resins.
- the molar ratio of formaldehyde to comonomer is in the range of from about 0.3:1 to about 1.5:1, more preferably from about 0.4:1 to about 1.1 :1, even more preferably about 0.4: 1 to about 0.9: 1 , and most preferably about 0.45 to about 0.75.
- urea formaldehyde resins part of the urea may be replaced with melamine.
- the modification of urea formaldehyde resins with melamine may provide improved water resistance to the binder composition, as well as the composite panels resulting in improved dimensional stability.
- the melamine may replace up to 85% by weight of comonomer.
- the urea formaldehyde resin modified with melamine may include a melamine component of from about 0.5 to about 60% and preferably from 1 to 50% weight on solids.
- urea formaldehyde resins are preferably formulated to a viscosity of up to about 700 cps and more preferably in the range of about 30 to 600 cps.
- the viscosity is in range of from about 300 to about 500 cps. It is also possible to use the urea formaldehyde having a viscosity is in the range of from about 30 to about 60 cps.
- the urea formaldehyde resin comprises from about 40% to about 70% by weight solids, more preferably from about 35% to about 70% by weight solids.
- the urea formaldehyde resin has a pH in the range of from about 8 to about 10, more preferably from about 8.5 to about 9.5.
- the resin In phenol formaldehyde resins it is possible to formulate the resin at either acid curing or alkaline curing conditions. Under acid curing conditions it is preferable to use a high phenol content.
- the molar ratio of formaldehyde to comonomer is in the range of from about 0.4:1 to about 1 :1, more preferably from about 0.4:1 to about 0.9:1, and most preferably about 0.45:1 to about 0.7:1.
- the molar ratio of formaldehyde to comonomer is in the range of from about 1.8:1 to about 4:1, more preferably from about 2:1 to about 2.5:1, and about 3.5:1 to about 3.8:1.
- phenol formaldehyde resins part of the phenol may be replaced with urea.
- the urea may replace up to 50% weight on solids.
- the urea may be present in an amount of from about 1% to about 25% weight on solids.
- PF resins are preferably formulated to a viscosity of up to about 400 cps and more preferably in the range of about 30 to 400 cps.
- the viscosity is in range of from about 200 to about 400 cps. It is also possible to use the phenol formaldehyde resins having a viscosity is in the range of from about 30 to about 60 cps.
- the phenol formaldehyde resin comprises from about 30% to about 50% by weight solids, more preferably from about 35%> to about 45% by weight solids.
- the phenol formaldehyde resin has a pH in the range of from about 7 to about 12, more preferably from about 9 to about 12, such as from about 10 to about 12.
- a variety of additives such as those used in the manufacture of conventional formaldehyde resins may incorporated into the formulations of the formaldehyde based resin of the present invention.
- pH modifying agents such as acids, bases and buffers. Acids typically used may include formic acid, hydrochloric acid and sulfuric acid. Bases typically used may include sodium hydroxide and potassium hydroxide. Buffers which may be used include triethanolamines and borax. Other additives include hexamine, which advantageously breaks down to formaldehyde in situ, sulfites, polyvinyl alcohol and sodium metabisulfite.
- the formaldehyde-based resin component may advantageously be blended with a release agent for supply to a fabricator of composite boards.
- fabricators will generally employ release agents to facilitate removal of the boards from the presses.
- release agents such as waxes are independently applied to the cellulose fibres.
- the incorporation of release agents into the formaldehyde-based resin allows greater convenience in the manufacturing process, the fabricator may operate a reduced stock inventory and reduces likelihood of incorrect dosages being used.
- the release agent may be included in the isocyanate component of the system.
- suitable release agents include paraffin and synthetic waxes such as montan waxes, polyethylene waxes and polypropylene waxes.
- the release agent may be present in the formaldehyde based resin an amount of at least 5% by weight solids of the isocyanate based compound, preferably at an amount of about 10% by weight solids of the isocyanate based compound.
- Release agents may preferably be incorporated into the formaldehyde-based resin in the form of an emulsion.
- An emulsion of the release agent may be formed by emulsifying a blend of the release agent and water in the presence of a surfactant. Preferably the blend is heated to an elevated temperature which promotes the formation of the emulsion.
- Suitable surfactants for promoting the formation and stabilisation of the emulsion include ethyl ene oxide derivatives.
- the release agent may be incorporated in an unemulsified form. This advantageously enables the release agent to be incorporated without the need for additional surfactant.
- the release agents may preferably be incorporated into the formaldehyde resin in the final stages of manufacture or may be incorporated by blending with the formaldehyde resin after the manufacture of the formaldehyde resin has been completed.
- the release agent may be added as an emulsion.
- the release agent may be added in solid form.
- the isocyanate containing compound may be a polyisocyanate including blocked isocyanates.
- Suitable polyisocyanates include toluene diisocyanate ("TDI") and 4, 4'- methylenebis (phenyl isocyanate).
- TDI toluene diisocyanate
- 4'- methylenebis phenyl isocyanate
- the isocyanate containing compound for use in the present invention is 4,4'-methylenebis (phenyl isocyanate) or commercial alternatives, generally referred to in the art as MDI.
- One example of a suitable MDI is Rubinate DUO B200 (ex Orica Australia Pty Ltd).
- the isocyanate containing compound may be provided in a variety of forms, such as neat or in an emulsified form.
- the isocyanate containing compound for use in the present invention is present in the binder composition in an amount in the range of from 0.5 to 50% by weight of said binder composition.
- the isocyanate containing compound is present in the binder composition in an amount in the range of from 5 to 30%, more preferably from 10 to 25%).
- the formaldehyde-based resin is preferably pre-reacted with up to 50% w/w on resin solids of melamine.
- the binder composition manufactured from such a pre-reacted formaldehyde-based resin may impart superior cold and hot water swell properties to the composite board, i.e. improved dimensional stability.
- the cellulose-based particles selected for use in the manufacture of composite panels will be dependant upon the nature of the composite panels to be produced.
- the cellulose-based fibres, particles or chips may be in the form of raw fibres.
- the cellulose-based fibres, particles or chips may be in the form of fibres which have not been pre-dried. In a preferred method the cellulose- based fibres, particles or chips may be in the form of untreated, moist raw fibres.
- Composite panels which may be manufactured in accordance with the present invention include particle board, medium density fibreboard, oriented strand board (OSB) plywood and combinations thereof fibreboard. such as tri-board which is a combination of oriented strand board and medium density fibreboard.
- OSB oriented strand board
- Particle board may be made from small discreet particles of wood.
- the wood particles may be made by cutting or breaking of the wood, their shape not being narrowly critical to the construction of the particle board.
- the particles of wood generally contain a moisture content of from 2 to 10%> by weight.
- the manufacture of particle board generally combines a mechanical mixing of the particles and the binder composition followed by the application of heat and pressure so as to cure the resin and form the particle board.
- the curing temperatures are in the range of from 130°C to 240°C although, dependent on the formulation other temperatures may be possible.
- particle boards contain from 3 to 40%> by weight of resin, preferably from 5 to 20% by weight of resin.
- the composite board is a medium density fibreboard.
- the medium density fibreboard comprises cellulose-based fibres which are in the form of a wood pulp.
- the binder is added to the wood pulp and the mixture dried to form a mat of dried fibres and binder.
- the temperatures chosen for the drying of the mixture are preferably such that the mixture is dried whilst the binder is not subject to conditions which will induce substantial curing.
- the dried mat is consolidated into the desired preform which is subsequently subjected to heat and pressure so as to cure the binder and produce the desired composite board.
- the cellulose fibre may be dried at temperatures ranging from 80°C to 140°C.
- the cellulose-based particles may be blended with the formaldehyde-based resin, either where the formaldehyde based resin is premixed with the isocyanate containing compound or where the components are simply added simultaneously.
- one or more components of the binder composition may be pre-blended with the cellulose-based particles and the remaining components subsequently combined with the pre- blended materials.
- the cellulose-based particles may be blended with the formaldehyde-based resin and subsequently the isocyanate containing compound may be incorporated into the pre-blended composition.
- a formaldehyde-based resin and an isocyanate containing compound may be blended with the cellulose particles and subsequently further comonomer may be added to the pre-blended components to decrease the molar ratio of formaldehyde to comonomer.
- the blending of the cellulose particles with the resin composition may be performed in situ, such as in a blender or a blow line.
- the curing of the binder composition to form a composite board may be by the process of hot pressing where the curing of the binder composition is effected at elevated temperatures and under applied pressure.
- the binder composition will be present in the composite board in the range of from 3 to 40% by weight.
- the addition rate of the binder composition will generally be dependant upon the physical properties which are required for the composite board and will be dependant upon the nature of the cellulose particles.
- the binder composition is present in the composite board in the range of from 5 to 30% by weight.
- Panel products for use in non-humid applications where low formaldehyde emissions are required a urea formaldehyde based binder with a low formaldehyde to urea ratio can be employed in conjunction with an isocyanate compound.
- This technique will provide an end product with su ⁇ risingly low emissions and unexpectedly superior excellent physical properties.
- Panel products for use in humid conditions or where higher dimensional stability is required MUF or more durable formaldehyde base resins such as phenol formaldehyde can be employed in conjunction with an isocyanate compound. These panel products will have high dimensional stability and low levels of formaldehyde emission. In order to further reduce formaldehyde emissions lower formaldehyde to comonomer ratios can also be employed. In order to improve general performance, binder loadings may be increased to achieve the desired physical properties.
- the binder composition may be reacted before the fibre is dried and pressed.
- the reaction may be generally slower and may not be complete before the fibre may be dried and pressed. This is particularly advantageous in obtaining a composite board having acceptable structural properties and dimensional stability.
- Example 1 100 solid parts of Sylvic DUO Al 10 (ex Orica Australia Pty Ltd), a urea formaldehyde resin, was mixed with 8.3 parts of Rubinate DUO B200 (ex Orica Australia Pty Ltd), an MDI, and 1.28 solid parts of montan wax to form the binder composition. In Example 2, 12.5 parts of Rubinate DUO B200 was used. 2. Manufacture of MDF
- the binder compositions described above were applied to wood fibres in an MDF process via a blowline.
- the binder composition was applied at a rate of 13.1 solid parts of binder to 100 parts of dry wood.
- the binder composition was applied at a rate of 9.10 solid parts of binder to 100 parts of dry wood.
- the wood fibre was then pressed into MDF panels.
- the panels of Example 1 were pressed and cured at a temperature of 145°C.
- the panels of Example 2 were pressed and cured at a temperature of 180°C.
- the binder compositions described above were applied to wood fibres in an MDF process via a blowline.
- the binder composition was applied at a rate of 28 solid parts of binder to 100 parts of dry wood.
- the wood fibre was then pressed into MDF panels.
- the panels of Example 3 were pressed and cured at a temperature of 130°C.
- the panels of Example 4 were pressed and cured at a temperature of 185°C.
- the resultant panel results are as follows:
- Example 5 100 solid parts of Sylvic DUO A 125 (ex Orica Australia Pty Ltd), an MUF resin, was mixed with 17.7 parts of Rubinate DUO B200 (ex Orica Australia Pty Ltd), an MDI, and 1.77 solid parts of montan wax to form the binder composition.
- the binder compositions described above were applied to wood fibres in an MDF process via a blowline.
- the binder composition was applied at a rate of 23.3 solid parts of binder to 100 parts of dry wood.
- Comparative Example A QM1329 (ex Orica Australia Pty Ltd), a conventional MUF binder, was applied at a rate of 20.0 solid parts of binder to 100 parts of dry wood. The wood fibre was then pressed into MDF panels.
- Example 5 100 solid parts of Sylvic DUO A133 (ex Orica Australia Pty Ltd), a PF resin, was mixed with 25 parts of Rubinate DUO B200 (ex Orica Australia Pty Ltd), an MDI, montan wax to form the binder composition.
- the binder compositions described above were applied to wood fibres in an MDF process via a blowline.
- the binder composition was applied at a rate of 13 solid parts of binder to 100 parts of dry wood.
- Comparative Example B the binder composition manufactured using DPL 6323 (ex Orica Australia Pty Ltd) was applied at a rate of 13 solid parts of binder to 100 parts of dry wood.
- the wood fibre was then pressed into MDF panels.
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Wood Science & Technology (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Forests & Forestry (AREA)
- Polyurethanes Or Polyureas (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU11424/00A AU748693B2 (en) | 1998-10-26 | 1999-10-26 | Resin and composite wood panels |
NZ511419A NZ511419A (en) | 1998-10-26 | 1999-10-26 | Formaldehyde based resin used in the manufacture of composite board, where the formaldehyde emissions of the composite board are at a level similar to that of wood |
Applications Claiming Priority (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AUPP6742A AUPP674298A0 (en) | 1998-10-26 | 1998-10-26 | Method of manufacture |
AUPP6742 | 1998-10-26 | ||
AUPP9865A AUPP986599A0 (en) | 1999-04-20 | 1999-04-20 | Method of manufacture ii |
AUPP9865 | 1999-04-20 | ||
AUPQ2125 | 1999-08-10 | ||
AUPQ2125A AUPQ212599A0 (en) | 1999-08-10 | 1999-08-10 | Method of manufacture |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2000024800A1 true WO2000024800A1 (en) | 2000-05-04 |
Family
ID=27158115
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/AU1999/000928 WO2000024800A1 (en) | 1998-10-26 | 1999-10-26 | Resin and composite wood panels |
Country Status (2)
Country | Link |
---|---|
NZ (1) | NZ511419A (en) |
WO (1) | WO2000024800A1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004113428A1 (en) * | 2003-06-24 | 2004-12-29 | Agro Biomass Consult Aps | Method for mixing and homogenisation of binding agents and additives |
WO2007039591A1 (en) * | 2005-10-04 | 2007-04-12 | Basf Se | Lignocellulosic material which is low in formaldehyde and method for the production thereof |
WO2008117138A1 (en) | 2007-03-27 | 2008-10-02 | Universidade De Trás-Os-Montes E Alto Douro | Agglomeration process of wood fibres (fibreboard) for the production of agglomerate slabs or panels |
WO2011002314A1 (en) * | 2009-06-30 | 2011-01-06 | New Zealand Forest Research Institute Limited | Method for producing wood fibre-plastics composite products |
DE102007054123B4 (en) * | 2006-11-15 | 2012-03-15 | Edmone Roffael | Process for the production of fiberboard with reduced formaldehyde emission, high moisture resistance and hydrolysis resistance of the gluing |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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US4201835A (en) * | 1977-04-16 | 1980-05-06 | Rutgerswerke Aktiengesellschaft | Boiling water and weather resistant cellulose fiber reinforced board material |
EP0232642A1 (en) * | 1985-12-30 | 1987-08-19 | Elf Atochem S.A. | Process for the preparation of isocyanate modified aminoplast resins |
US5011886A (en) * | 1983-12-21 | 1991-04-30 | Rwe-Dea Aktiengesellschaft Fur Mineraloel Und Chemie | Process for producing modified phenolic resin bonding agents and use thereof for producing particle board |
-
1999
- 1999-10-26 NZ NZ511419A patent/NZ511419A/en unknown
- 1999-10-26 WO PCT/AU1999/000928 patent/WO2000024800A1/en active IP Right Grant
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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US4201835A (en) * | 1977-04-16 | 1980-05-06 | Rutgerswerke Aktiengesellschaft | Boiling water and weather resistant cellulose fiber reinforced board material |
US4268649A (en) * | 1977-04-16 | 1981-05-19 | Rutgerswerke Aktiengesellschaft | Binder for cellulose fiber reinforced board material |
US5011886A (en) * | 1983-12-21 | 1991-04-30 | Rwe-Dea Aktiengesellschaft Fur Mineraloel Und Chemie | Process for producing modified phenolic resin bonding agents and use thereof for producing particle board |
EP0232642A1 (en) * | 1985-12-30 | 1987-08-19 | Elf Atochem S.A. | Process for the preparation of isocyanate modified aminoplast resins |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004113428A1 (en) * | 2003-06-24 | 2004-12-29 | Agro Biomass Consult Aps | Method for mixing and homogenisation of binding agents and additives |
WO2007039591A1 (en) * | 2005-10-04 | 2007-04-12 | Basf Se | Lignocellulosic material which is low in formaldehyde and method for the production thereof |
JP2009509817A (en) * | 2005-10-04 | 2009-03-12 | ビーエーエスエフ ソシエタス・ヨーロピア | Low formaldehyde / lignocellulose material and method for producing the same |
US7939177B2 (en) | 2005-10-04 | 2011-05-10 | Basf Aktiengesellschaft | Lignocelluosic material which is low in formaldehyde and method for the production thereof |
AU2006298715B2 (en) * | 2005-10-04 | 2011-07-28 | Basf Se | Lignocellulosic material which is low in formaldehyde and method for the production thereof |
AU2006298715B8 (en) * | 2005-10-04 | 2011-08-11 | Basf Se | Lignocellulosic material which is low in formaldehyde and method for the production thereof |
DE102007054123B4 (en) * | 2006-11-15 | 2012-03-15 | Edmone Roffael | Process for the production of fiberboard with reduced formaldehyde emission, high moisture resistance and hydrolysis resistance of the gluing |
WO2008117138A1 (en) | 2007-03-27 | 2008-10-02 | Universidade De Trás-Os-Montes E Alto Douro | Agglomeration process of wood fibres (fibreboard) for the production of agglomerate slabs or panels |
WO2011002314A1 (en) * | 2009-06-30 | 2011-01-06 | New Zealand Forest Research Institute Limited | Method for producing wood fibre-plastics composite products |
US9283692B2 (en) | 2009-06-30 | 2016-03-15 | New Zealand Forest Research Institute Limited | Method for producing wood fibre-plastics composite products |
Also Published As
Publication number | Publication date |
---|---|
NZ511419A (en) | 2002-10-25 |
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