US20090145564A1 - Method for production of wood material articles with low emissions of chemical compounds - Google Patents
Method for production of wood material articles with low emissions of chemical compounds Download PDFInfo
- Publication number
- US20090145564A1 US20090145564A1 US11/989,415 US98941508A US2009145564A1 US 20090145564 A1 US20090145564 A1 US 20090145564A1 US 98941508 A US98941508 A US 98941508A US 2009145564 A1 US2009145564 A1 US 2009145564A1
- Authority
- US
- United States
- Prior art keywords
- wood
- formaldehyde
- fibres
- bisulphite
- treated
- 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.)
- Abandoned
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27N—MANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
- B27N3/00—Manufacture of substantially flat articles, e.g. boards, from particles or fibres
- B27N3/08—Moulding or pressing
-
- 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
-
- 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
-
- 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
- B27N1/006—Pretreatment of moulding material for increasing resistance to swelling by humidity
-
- 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
Definitions
- the invention relates to a method for the production of a wood material article with a low emission of chemical compounds as well as a wood material article, which can be obtained by this method.
- Wood material articles as for example, chip boards or fibre boards, are produced of wood chips of fibre materials in combination with glue.
- the glue is applied during the manufacturing of the wood material article onto the hackled wood (chips) or the fibre material and after that the resulting, still moist wood material articles are pressed with high temperatures (hot pressing), whereby the glue is cured respectively hardened.
- formaldehyde containing resins are used in such glues as curing agents and/or binding agents.
- Wood material boards are often used inside of closed rooms. Therefore it is important, that the chipboards do not emit disturbing (like, for example, components with a strong smell) or even harmful components.
- the emitted components can derive from the wood itself or also from the applied glue.
- the resulting articles When using formaldehyde containing resins for the manufacturing of wood material articles, the resulting articles emit amounts of formaldehyde, whereby the amount is limited due to legal regulations and voluntarily restrictions of the industry to extremely low thresholds.
- This object is solved by a method for the production of a wood material article comprising wood chips or wood fibres which are glued together, wherein the wood is treated with bisulphite before the gluing process.
- improved wood material articles can be produced, which in particular show only low or no undesired emissions of (volatile) chemical compounds which originate from the wood itself. Further, the wood chips or wood fibres treated with bisulphite show an improved reaction with the glue.
- wood of broad leaved trees or needle leaved trees are treated either separately or in a mixture.
- the woods are barked and hackled.
- Hackle chips or wood chips can be added to the hackled wood.
- this mixture is screened and separated, whereby undesired articles like for example sand, splinters, stones or metals are removed.
- the mixture is washed, whereby again undesired materials like for example sand or stones are removed.
- the hackled wood is heated and dehydrated. This is done preferably by pressing.
- the hackled and treated wood is then treated at a pressure of 0.8-12 bar in saturated water steam atmosphere.
- an aquarious solution of bisulphate salt is introduced into the steam atmosphere.
- the bisulphate salts may for example be alkali and/or ammonium salts. Preferably sodium salts and/or ammonium bisulphate salts are used. Ammonia salt is particularly preferred.
- the amount of bisulphate salt is in the range of 3 to 30 kg, preferably between 3 and 12 kg per cubic meter of produced board.
- the duration of the treatment is at least 1.5 minutes and preferably between 3 and 8 minutes. In this case large amounts of bisulphate necessitate longer treatment duration to complete the reaction, to enable the bisulphate to permeate into the fibres and to secure a stable impregnation.
- the wood is treated with bisulphate before the production of the wood chips or wood fibres, for example in the cooker, to simplify the implementation of the method.
- a subsequent impregnation of the wood fibres with paraphine does therefore not negatively influence the effect of the method according to the invention.
- the wood chips or wood fibres are treated with bisulphate, for example in a refiner.
- the method can be achieved in a particularly efficient manner.
- the treatment of the hackled wood with the bisulphate is important to bind the volatile substances in the hackled wood and to restrain the regeneration of volatile substances.
- the bisulphate for example the bisulphate-adducts of aldehydes, methylketone or alpha-ketoester may be formed.
- the bisulphate may evolve its bleaching effect and it may react with the pigments present in the wood, so that particularly bright wood material articles can be achieved.
- the brightness of a board is an important quality criterion.
- the glue which is used for the gluing of the wood chips or wood fibres, is preferably an aminoplast resin. It is particularly preferred, that a formaldehyde containing resin is used. This is preferably chosen from the group consisting of urea formaldehyde resin, melanin-formaldehyde resin, urea melanin-formaldehyde resin and melamine urea-phenol-formaldehyde resin. Suitable resins are commercially available as solutions or as powder and the production and application of suitable resins is also described in the prior art. For the method according to the invention, in particular urea-formaldehyde resins and urea-melamine-formaldehyde resins are preferred, which are applied in common amounts.
- resins which are low of formaldehyde which show a low molar relation of formaldehyde to urea.
- the molar relation of formaldehyde to urea is advantageously between 0.8:1 to 1.05:1.
- the glue may comprise in addition to the aminoplast resin further additives as for example curing agents to accelerate the curing or hardening, hydrophobic agents, inert salts, pH-conditioners, stabilizers, fungicides or biocides.
- the gluing is achieved preferably by pressing the finally hackled wood, which is provided with the glue, at temperatures of 120° to 250° Celsius. Under these conditions, the aminoplast resin cures relatively fast and one achieves wood material articles with positive mechanical properties, which are for the most part insensitive against moisture.
- Two fibre boards S1 and V1 were produced with the above described method by using a formaldehyde-urea resin, having a molar ratio of formaldehyde to urea of 1:1.08, with the only distinguishing feature, that for the manufacturing of the fibre board V1 the hackled wood was not treated with bisulphate before the impregnation process.
- the treatment of the hackled wood with bisulphate was done at a pressure of 8.5 bar with an amount of bisulphate of 3 kg per m 3 of hackled wood and for a duration of 3.5 minutes. After the pre-treatment of the wood, the wetting with a none-impregnation agent and after that the pressing was done.
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)
Abstract
Description
- The invention relates to a method for the production of a wood material article with a low emission of chemical compounds as well as a wood material article, which can be obtained by this method.
- Wood material articles, as for example, chip boards or fibre boards, are produced of wood chips of fibre materials in combination with glue. Usually, the glue is applied during the manufacturing of the wood material article onto the hackled wood (chips) or the fibre material and after that the resulting, still moist wood material articles are pressed with high temperatures (hot pressing), whereby the glue is cured respectively hardened. For a long time, formaldehyde containing resins are used in such glues as curing agents and/or binding agents.
- Wood material boards are often used inside of closed rooms. Therefore it is important, that the chipboards do not emit disturbing (like, for example, components with a strong smell) or even harmful components. The emitted components can derive from the wood itself or also from the applied glue.
- When using formaldehyde containing resins for the manufacturing of wood material articles, the resulting articles emit amounts of formaldehyde, whereby the amount is limited due to legal regulations and voluntarily restrictions of the industry to extremely low thresholds.
- Different methods are known to reduce the formaldehyde content and in particular the emission of formaldehyde from the resulting wood material articles. Some of them are:
-
- Modification of the glue by reducing the molar relationship of formaldehyde to the other components of the resin;
- Adding of substances which bind formaldehyde, as for example carbamide;
- Mixing of resins containing formaldehyde with other resins; or
- Increasing the pressing time.
- These methods, however, lower the efficiency of the production process (increased costs, lower production capacity by increased production time, etc.) or they have negative physical or mechanical effects to the product (reduction of the resin stability, reduction of the stability and the resistance of the glue seams etc.)
- It is therefore one object of the present invention to provide an improved method for the production of wood material articles, whereby the resulting wood material articles show in particular a lower emission of chemical compounds.
- This object is solved by a method for the production of a wood material article comprising wood chips or wood fibres which are glued together, wherein the wood is treated with bisulphite before the gluing process.
- Surprisingly it has been found, that by means of the inventive method, improved wood material articles can be produced, which in particular show only low or no undesired emissions of (volatile) chemical compounds which originate from the wood itself. Further, the wood chips or wood fibres treated with bisulphite show an improved reaction with the glue.
- Further preferred embodiments of the method are subject to the sub claims.
- For the production of wood material articles, usually wood of broad leaved trees or needle leaved trees are treated either separately or in a mixture. First, the woods are barked and hackled. Hackle chips or wood chips can be added to the hackled wood. After that, this mixture is screened and separated, whereby undesired articles like for example sand, splinters, stones or metals are removed. After that, the mixture is washed, whereby again undesired materials like for example sand or stones are removed. In the next step the hackled wood is heated and dehydrated. This is done preferably by pressing.
- The hackled and treated wood is then treated at a pressure of 0.8-12 bar in saturated water steam atmosphere. According to the invention additionally an aquarious solution of bisulphate salt is introduced into the steam atmosphere. The bisulphate salts may for example be alkali and/or ammonium salts. Preferably sodium salts and/or ammonium bisulphate salts are used. Ammonia salt is particularly preferred. The amount of bisulphate salt is in the range of 3 to 30 kg, preferably between 3 and 12 kg per cubic meter of produced board. The duration of the treatment is at least 1.5 minutes and preferably between 3 and 8 minutes. In this case large amounts of bisulphate necessitate longer treatment duration to complete the reaction, to enable the bisulphate to permeate into the fibres and to secure a stable impregnation.
- According to the invention, in one embodiment the wood is treated with bisulphate before the production of the wood chips or wood fibres, for example in the cooker, to simplify the implementation of the method. A subsequent impregnation of the wood fibres with paraphine does therefore not negatively influence the effect of the method according to the invention.
- According to a further embodiment, the wood chips or wood fibres are treated with bisulphate, for example in a refiner. In this way, the method can be achieved in a particularly efficient manner.
- Without being bound to this theory, the treatment of the hackled wood with the bisulphate is important to bind the volatile substances in the hackled wood and to restrain the regeneration of volatile substances. During the treatment with bisulphate, for example the bisulphate-adducts of aldehydes, methylketone or alpha-ketoester may be formed. Additionally, the bisulphate may evolve its bleaching effect and it may react with the pigments present in the wood, so that particularly bright wood material articles can be achieved. The brightness of a board is an important quality criterion.
- Additionally, when treating the wood with bisulphate a slightly acidic impregnation of the fibres occurs, so that in the case of application of formaldehyde containing resins in the glue a complete polycondensation with the resin and thus a complete consumption of the free formaldehyde is achieved. Both effects lead to wood material articles, which show extreme low perforation values and therefore an extremely low emission of formaldehyde.
- With a treatment duration with bisulphate of at least 1.5 minutes, it is secured, that the disintegration of the wood is almost complete and the subsequently following treatment with the impregnation agent against an expansion due to moisture is not ineffective.
- After that the impregnated wood pieces are further hackled to wood chips or wood fibres, glued, dried and pressed. This is done by common methods.
- The glue, which is used for the gluing of the wood chips or wood fibres, is preferably an aminoplast resin. It is particularly preferred, that a formaldehyde containing resin is used. This is preferably chosen from the group consisting of urea formaldehyde resin, melanin-formaldehyde resin, urea melanin-formaldehyde resin and melamine urea-phenol-formaldehyde resin. Suitable resins are commercially available as solutions or as powder and the production and application of suitable resins is also described in the prior art. For the method according to the invention, in particular urea-formaldehyde resins and urea-melamine-formaldehyde resins are preferred, which are applied in common amounts. It is particularly advantageous to use resins which are low of formaldehyde, which show a low molar relation of formaldehyde to urea. The molar relation of formaldehyde to urea is advantageously between 0.8:1 to 1.05:1.
- By treating the hackled wood with bisulphate however, also glues with a higher molar relationship of formaldehyde to urea as mentioned above may be applied. Also the wood material articles produced thereby show extremely low perforation values, which all satisfy the current regulations. With these resins—which are more reactive and cheaper compared to resins, which are low in formaldehyde—even boards of class E1 can be produced. The method according to the invention has the advantage, that common resins without additional formaldehyde binding agents can be used in the glue, without having any negative physical or mechanical effects to the end product. However, the applied glue may—if desired—contain additionally formaldehyde binding substances.
- The glue may comprise in addition to the aminoplast resin further additives as for example curing agents to accelerate the curing or hardening, hydrophobic agents, inert salts, pH-conditioners, stabilizers, fungicides or biocides.
- The gluing is achieved preferably by pressing the finally hackled wood, which is provided with the glue, at temperatures of 120° to 250° Celsius. Under these conditions, the aminoplast resin cures relatively fast and one achieves wood material articles with positive mechanical properties, which are for the most part insensitive against moisture.
- Two fibre boards S1 and V1 were produced with the above described method by using a formaldehyde-urea resin, having a molar ratio of formaldehyde to urea of 1:1.08, with the only distinguishing feature, that for the manufacturing of the fibre board V1 the hackled wood was not treated with bisulphate before the impregnation process. The treatment of the hackled wood with bisulphate was done at a pressure of 8.5 bar with an amount of bisulphate of 3 kg per m3 of hackled wood and for a duration of 3.5 minutes. After the pre-treatment of the wood, the wetting with a none-impregnation agent and after that the pressing was done.
- In table 1 the perforation values (according to DIN EN 120—wood materials—determination of formaldehyde content) of both fibre boards S1 and V1 are shown.
-
TABLE 1 Perforation values in MCHO/100 g Fibre board fibre board S1 6.5 V1 2.5 - The values in table 1 show, that by treating the hackled wood with bisulphate wood material articles can be obtained, which show extremely low formaldehyde emissions. Further, the fibre board S1 emitted only extremely low amounts of other chemical compounds. Additionally, fibre board S1 was significantly brighter than fibre board V1.
Claims (8)
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13/312,469 US20120077908A1 (en) | 2005-07-27 | 2011-12-06 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
| US15/202,097 US20160311130A1 (en) | 2005-07-27 | 2016-07-05 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
| US15/480,964 US20170210028A1 (en) | 2005-07-27 | 2017-04-06 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
| US15/962,793 US20180243939A1 (en) | 2005-07-27 | 2018-04-25 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/EP2005/053674 WO2007012350A1 (en) | 2005-07-27 | 2005-07-27 | Method for production of wood material articles with low emissions of chemical compounds |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2005/053674 A-371-Of-International WO2007012350A1 (en) | 2005-07-27 | 2005-07-27 | Method for production of wood material articles with low emissions of chemical compounds |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US13/312,469 Continuation US20120077908A1 (en) | 2005-07-27 | 2011-12-06 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20090145564A1 true US20090145564A1 (en) | 2009-06-11 |
Family
ID=35134611
Family Applications (5)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US11/989,415 Abandoned US20090145564A1 (en) | 2005-07-27 | 2005-07-27 | Method for production of wood material articles with low emissions of chemical compounds |
| US13/312,469 Abandoned US20120077908A1 (en) | 2005-07-27 | 2011-12-06 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
| US15/202,097 Abandoned US20160311130A1 (en) | 2005-07-27 | 2016-07-05 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
| US15/480,964 Abandoned US20170210028A1 (en) | 2005-07-27 | 2017-04-06 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
| US15/962,793 Abandoned US20180243939A1 (en) | 2005-07-27 | 2018-04-25 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
Family Applications After (4)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US13/312,469 Abandoned US20120077908A1 (en) | 2005-07-27 | 2011-12-06 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
| US15/202,097 Abandoned US20160311130A1 (en) | 2005-07-27 | 2016-07-05 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
| US15/480,964 Abandoned US20170210028A1 (en) | 2005-07-27 | 2017-04-06 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
| US15/962,793 Abandoned US20180243939A1 (en) | 2005-07-27 | 2018-04-25 | Method for the Production of Wood Material Articles with Low Emissions of Chemical Compounds |
Country Status (10)
| Country | Link |
|---|---|
| US (5) | US20090145564A1 (en) |
| EP (1) | EP1907178B1 (en) |
| CN (1) | CN101351313B (en) |
| AU (1) | AU2005334999A1 (en) |
| CA (1) | CA2616336A1 (en) |
| ES (1) | ES2599909T3 (en) |
| LT (1) | LT1907178T (en) |
| PL (1) | PL1907178T3 (en) |
| PT (1) | PT1907178T (en) |
| WO (1) | WO2007012350A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110237713A1 (en) * | 2007-08-10 | 2011-09-29 | Kronotec Ag | Method for reducing the emisson of aldehydes and volatile organic compounds of wood material |
| US11007668B2 (en) | 2017-04-25 | 2021-05-18 | SWISS KRONO Tec AG | Process for the production of OSB wood-based boards with reduced emission of volatile organic compounds (VOCs) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102007055415C5 (en) | 2007-11-19 | 2018-11-29 | SWISS KRONO Tec AG | Method for reducing the emission of saturated and unsaturated aldehydes from wood-based materials |
| ES2749198T3 (en) * | 2008-12-05 | 2020-03-19 | SWISS KRONO Tec AG | Procedure for making wood-based materials from crushing products containing lignocellulose and such wood-based materials |
| EP2546039B1 (en) | 2009-07-06 | 2014-03-26 | Kronotec AG | Method of reducing the emissions of aldehydes and fleeting organic compounds in OSB-boards, use of additives therefore and OSB-board |
| DE102009057208A1 (en) | 2009-11-27 | 2011-06-01 | Technische Universität Dresden | Process for the production of lignocellulosic paper pulps and papers, cartons and boards derived therefrom |
| SI3147093T1 (en) | 2015-09-24 | 2019-02-28 | SWISS KRONO Tec AG | Method for reducing the emissions of volatile organic compounds from wooden materials and wooden material |
| AT518800B1 (en) * | 2016-06-17 | 2019-09-15 | Andritz Ag Maschf | METHOD FOR PRODUCING FIBROUS MATERIAL |
| CN109514685A (en) * | 2018-12-12 | 2019-03-26 | 大亚木业(茂名)有限公司 | A kind of production technology of low density fiberboard |
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| US3597310A (en) * | 1966-04-25 | 1971-08-03 | Kokusaku Pulp Ind Co Ltd | Method of producing high yield pulp by disc refining at ph of 12 to 14 |
| US3607618A (en) * | 1967-11-06 | 1971-09-21 | Process Dev Corp | Wood-pulping process |
| US3790417A (en) * | 1971-12-17 | 1974-02-05 | A Paterson | Process for preparing fiberboard having improved dimensional stability |
| US3950472A (en) * | 1975-02-26 | 1976-04-13 | Continental Can Company, Inc. | Molding wood articles from ammonium salt-wood particle mixtures |
| US4186242A (en) * | 1976-03-08 | 1980-01-29 | Georgia-Pacific Corporation | Preparation of a lignocellulosic composite |
| US4409375A (en) * | 1982-02-11 | 1983-10-11 | Champion International Corporation | Method for scavenging aldehydes |
| US5578371A (en) * | 1995-08-25 | 1996-11-26 | Schuller International, Inc. | Phenol/formaldehyde fiberglass binder compositions exhibiting reduced emissions |
| US6043350A (en) * | 1997-08-06 | 2000-03-28 | Bakelite Ag | Bonding agent composition, its use as well as a process for the production of particle board |
| US6730718B1 (en) * | 1999-10-13 | 2004-05-04 | Celanese Emulsions Gmbh | Discoloration-fast dispersion adhesives having a prolonged potlife |
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| DE3427694A1 (en) * | 1984-07-27 | 1986-02-06 | Basf Ag, 6700 Ludwigshafen | Formaldehyde-binding agents, the use thereof in the production of wood chip materials, and a process for the production of wood chip materials having reduced formaldehyde emission |
| SE470330B (en) * | 1992-06-11 | 1994-01-24 | Sunds Defibrator Ind Ab | Process for making fiberboard according to the dry method |
| JPH0919906A (en) | 1995-07-06 | 1997-01-21 | New Oji Paper Co Ltd | Wood fiberboard manufacturing method |
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| DE10160316A1 (en) * | 2001-12-07 | 2003-06-26 | Ihd Inst Fuer Holztechnologie | Production of moisture-resistant fibreboard by the dry process, e.g. for laminated flooring, involves treating wood chips or fibre with alkali under more drastic digestion conditions and using moisture-resistant binder |
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-
2005
- 2005-07-27 CN CN2005800516974A patent/CN101351313B/en not_active Expired - Lifetime
- 2005-07-27 PT PT57639775T patent/PT1907178T/en unknown
- 2005-07-27 CA CA002616336A patent/CA2616336A1/en not_active Abandoned
- 2005-07-27 LT LTEP05763977.5T patent/LT1907178T/en unknown
- 2005-07-27 EP EP05763977.5A patent/EP1907178B1/en not_active Expired - Lifetime
- 2005-07-27 WO PCT/EP2005/053674 patent/WO2007012350A1/en not_active Ceased
- 2005-07-27 AU AU2005334999A patent/AU2005334999A1/en not_active Abandoned
- 2005-07-27 PL PL05763977T patent/PL1907178T3/en unknown
- 2005-07-27 ES ES05763977.5T patent/ES2599909T3/en not_active Expired - Lifetime
- 2005-07-27 US US11/989,415 patent/US20090145564A1/en not_active Abandoned
-
2011
- 2011-12-06 US US13/312,469 patent/US20120077908A1/en not_active Abandoned
-
2016
- 2016-07-05 US US15/202,097 patent/US20160311130A1/en not_active Abandoned
-
2017
- 2017-04-06 US US15/480,964 patent/US20170210028A1/en not_active Abandoned
-
2018
- 2018-04-25 US US15/962,793 patent/US20180243939A1/en not_active Abandoned
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3597310A (en) * | 1966-04-25 | 1971-08-03 | Kokusaku Pulp Ind Co Ltd | Method of producing high yield pulp by disc refining at ph of 12 to 14 |
| US3607618A (en) * | 1967-11-06 | 1971-09-21 | Process Dev Corp | Wood-pulping process |
| US3790417A (en) * | 1971-12-17 | 1974-02-05 | A Paterson | Process for preparing fiberboard having improved dimensional stability |
| US3950472A (en) * | 1975-02-26 | 1976-04-13 | Continental Can Company, Inc. | Molding wood articles from ammonium salt-wood particle mixtures |
| US4186242A (en) * | 1976-03-08 | 1980-01-29 | Georgia-Pacific Corporation | Preparation of a lignocellulosic composite |
| US4409375A (en) * | 1982-02-11 | 1983-10-11 | Champion International Corporation | Method for scavenging aldehydes |
| US5578371A (en) * | 1995-08-25 | 1996-11-26 | Schuller International, Inc. | Phenol/formaldehyde fiberglass binder compositions exhibiting reduced emissions |
| US6043350A (en) * | 1997-08-06 | 2000-03-28 | Bakelite Ag | Bonding agent composition, its use as well as a process for the production of particle board |
| US6730718B1 (en) * | 1999-10-13 | 2004-05-04 | Celanese Emulsions Gmbh | Discoloration-fast dispersion adhesives having a prolonged potlife |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110237713A1 (en) * | 2007-08-10 | 2011-09-29 | Kronotec Ag | Method for reducing the emisson of aldehydes and volatile organic compounds of wood material |
| US9012539B2 (en) * | 2007-08-10 | 2015-04-21 | Kronotec Ag | Method for reducing the emission of aldehydes and volatile organic compounds of wood materials |
| US11007668B2 (en) | 2017-04-25 | 2021-05-18 | SWISS KRONO Tec AG | Process for the production of OSB wood-based boards with reduced emission of volatile organic compounds (VOCs) |
| US11904496B2 (en) | 2017-04-25 | 2024-02-20 | SWISS KRONO Tec AG | Process for the production of OSB wood-based boards with reduced emission of volatile organic compounds (VOCs) |
Also Published As
| Publication number | Publication date |
|---|---|
| EP1907178B1 (en) | 2016-07-20 |
| US20160311130A1 (en) | 2016-10-27 |
| PL1907178T3 (en) | 2017-01-31 |
| CN101351313B (en) | 2011-06-01 |
| ES2599909T3 (en) | 2017-02-06 |
| EP1907178A1 (en) | 2008-04-09 |
| WO2007012350A1 (en) | 2007-02-01 |
| LT1907178T (en) | 2016-11-10 |
| CA2616336A1 (en) | 2007-02-01 |
| US20180243939A1 (en) | 2018-08-30 |
| US20120077908A1 (en) | 2012-03-29 |
| PT1907178T (en) | 2016-09-30 |
| US20170210028A1 (en) | 2017-07-27 |
| AU2005334999A1 (en) | 2007-02-01 |
| CN101351313A (en) | 2009-01-21 |
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