Wood particle boards

Information

  • Patent Grant
  • 10864653
  • Patent Number
    10,864,653
  • Date Filed
    Friday, October 7, 2016
    8 years ago
  • Date Issued
    Tuesday, December 15, 2020
    3 years ago
  • Inventors
  • Examiners
    • Theisen; Mary Lynn F
    Agents
    • Knauf Insulation, Inc.
    • Blodgett; James K.
    • Hudder; Brandon N.
Abstract
A non-carbohydrate polyhydroxy component(s) is used in a binder composition to facilitate manufacture of wood particle boards.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a U.S. national counterpart application of International Application Serial No. PCT/EP2016/074031, filed Oct. 7, 2016, under 35 U.S.C. § 371, which claims priority to GB Application Serial No. 1517867.6, filed Oct. 9, 2015, the disclosures of which are hereby incorporated herein by reference.


The present invention relates to wood particle boards and a method for their production.


A wood particle board is a composite material manufactured from wood particles, for example wood chips, sawmill shavings and/or saw dust at varying particle sizes held together by a binder and used especially for the manufacture of furniture, such as cabinets, kitchens and bathroom furniture. Generally, wood particle board (which is sometimes referred to as “chipboard”) is produced by mixing wood particles and a binder composition, e.g. a thermo-curable resin, subsequently forming the resulting mixture into a sheet or mat and compressing said sheet or mat under elevated temperatures. In order to improve the visual appearance and/or durability, a veneer or melamine layer may be applied to the board's surface(s).


According to one aspect, the present invention provides a method of manufacturing a wood particle board as defined in claim 1. The dependent claims define preferred or alternative embodiments.


The presence of the non-carbohydrate polyhydroxy component of the binder composition may be useful to i) facilitate an even distribution of the binder composition over individual wood particles and/or over a collection of wood particles which are mixed or processed together and/or ii) provide an appropriate quantity of moisture for the resinated wood particles. A binder composition that cannot easily flow or be distributed may lead to clumping of resinated wood particles and/or to a non-homogenous material mix at entry into board press. The non-carbohydrate polyhydroxy component may act as a lubricant and/or a non-drying liquid; this may reduce or prevent clumping of the resinated wood particles.


The resinated wood particles may be mixed or tumbled, for example in a bunker, prior to being formed in to a mat; the non-carbohydrate polyhydroxy component may facilitate binder distribution over surfaces of the wood particles during such mixing. Furthermore, the use of a non-carbohydrate polyhydroxy component may avoid the necessity of providing additional water or diluting the binder composition to facilitate binder distribution and thus avoid the generation of undesired quantities of steam during subsequent curing.


The non-carbohydrate polyhydroxy component may be selected from: a diol, a triol, a polyol, an organic compound containing multiple hydroxyl groups and mixtures thereof. It may comprise, comprise at least 50 wt % or consist essentially of glycerol, polyethylene glycol, polypropylene glycol, trimethylolpropane, pentaerythritol, polyvinyl alcohol, partially hydrolyzed polyvinyl acetate, fully hydrolyzed polyvinyl acetate, or mixtures thereof. Glycerol is particularly preferred because it can be acquired as a cost efficient waste product from other industrial processes, is bio based and is non-hazardous chemical.


The non-carbohydrate polyhydroxy component may have a viscosity when measured at 20° C. which is:

    • greater than or equal to: 10 cP, 50 cP, 100 cP or 250 cP or 500 cP or 750 cP or 1000 cP or 1250 cP; and/or
    • less than or equal to: 10000 cP or 7500 cP or 5000 cP or 2500 or 2000 cP or 1500 cP;


      notably when the viscosity is measured at 20° C. The viscosity of the non-carbohydrate polyhydroxy component and of the binder composition is measured by rotational viscometry notably using a Brookfield viscometer. One such viscosity measurement involves applying a torque through a calibrated spring to a spindle immersed in a test fluid, the amount of viscous drag indicated by the spring deflection providing a measure of the viscosity.


The non-carbohydrate polyhydroxy component may be used in a quantity of:

    • at least 0.1% or at least 1%, or at least 2% or at least 5% and/or
    • no more than 25% or no more than 20% or no more than 15%


      by weight based on the total weight of the binder composition.







The term “binder composition” as used herein means all ingredients applied to the wood particles and/or present on the wood particles, notably prior to curing, (other than the wood particles themselves and any moisture in the wood particles), including reactants, solvents (including water), the non-carbohydrate polyhydroxy component(s) and additives. The term “dry weight of the binder composition” as used herein means the weight of all components of the binder composition other than any water that is present (whether in the form of liquid water or in the form of water of crystallization).


The binder composition applied to the wood particles comprises uncured reactants which cure and cross-link to form a cured binder which holds the particles of the wood particle board together. The binder composition comprises starting materials that will form a thermoset resin upon curing. The reactants may comprise components selected from the group consisting of: protein(s), starch(es), cellulose, carbohydrate(s), gum(s), natural resin(s), bitumen(s), natural rubber(s), synthetic rubber(s), phenolic(s) such as tannin or lignin, notably present in a quantity of at least 30%, at least 40%, at least 50%, at least 60%, at least 70% or at least 80% by dry weight based on the total dry weight of the binder composition.


The binder composition is preferably free of, or comprises no more than 5 wt % or no more than 10 wt % urea formaldehyde (UF), melamine urea formaldehyde (MUF) and/or phenol formaldehyde.


The binder composition is preferably a binder that does not comprise any added formaldehyde. It may be “substantially formaldehyde free”, that is to say that it liberates less than 5 ppm formaldehyde as a result of drying and/or curing (or appropriate tests simulating drying and/or curing); more preferably it is “formaldehyde free”, that is to say that it liberates less than 1 ppm formaldehyde in such conditions.


Advantageously, the binder composition may be a carbohydrate based binder composition. The combination of this with the non-carbohydrate polyhydroxy component(s) has been found to provide an advantageous combination of bond strength, notably without penalizing cure speed, whilst facilitating manufacturing processes. The binder composition may comprise (a) reducing sugar reactant(s) and nitrogen-containing reactant(s) and/or (b) curable reaction product(s) of reducing sugar reactant(s) and nitrogen-containing reactant(s). The reducing sugar reactants may be provided in the form of reducing sugars and/or generated in situ, notably from a carbohydrate reactant which yields reducing sugar(s) in situ, for example due to application of heat and/or presence of a catalyst or further reactant.


The binder composition may comprise a binder composition as described in any of WO 2007/014236, WO 2009/019232, WO 2009/019235, WO 2011/138458, WO 2011/138459 or WO 2013/150123, each of which is hereby incorporated by reference.


The nitrogen-containing reactant(s) and the reducing sugar reactant(s) (or their reaction product(s)) may be Maillard reactants that react to form Maillard reaction products, notably melanoidins when cured. Curing of the binder composition may comprise or consist essentially of Maillard reaction(s). The cured binder composition may comprise melanoidin-containing and/or nitrogenous-containing polymer(s); it is preferably a thermoset binder and is preferably substantially water insoluble.


The reducing sugar reactant may comprise: a monosaccharide, a monosaccharide in its aldose or ketose form, a disaccharide, a polysaccharide, a triose, a tetrose, a pentose, xylose, an hexose, dextrose, fructose, a heptose, a sugar, molasses, starch, starch hydrolysate, cellulose hydrolysates, reaction product(s) thereof or mixtures thereof. The reducing sugar reactant(s), or carbohydrate reactant(s) that yield the reducing sugar reactant(s) may have a dextrose equivalent of at least about 50, at least about 60, at least about 70, at least about 80 or at least about 90. The reducing sugar reactant may comprise or consist of high fructose corn syrup (HFCS).


As used herein, the term “nitrogen-containing reactant” means any chemical compound, or mixture of compounds, which contain(s) at least one nitrogen atom and which is/are capable of reacting with the at least one reducing sugar reactant. The nitrogen-containing reactant may be selected from NH3, an inorganic amine or an organic amine comprising at least one primary amine group, as well as salts thereof. It may comprise NH3 used as such (e.g. in form of an aqueous solution), or an inorganic and organic ammonium salt, for example ammonium sulfate (AmSO4), ammonium phosphate, e.g. diammonium phosphate, ammonium chloride, ammonium nitrate or ammonium citrate.


The nitrogen-containing reactant may be a polyamine. Herein, the term “polyamine” includes any organic compound having two or more amine groups, which may independently be substituted or unsubstituted. For example, the polyamine may be a primary polyamine. As used herein, a “primary polyamine” is an organic compound having two or more primary amine groups (—NH2). Within the scope of the term primary polyamine are those compounds which can be modified in situ or isomerize to generate a compound having two or more primary amine groups (—NH2). The primary polyamine may be a molecule having the formula H2N-Q-NH2, wherein Q is an alkanediyl, cycloalkanediyl, heteroalkanediyl, or cycloheteroalkanediyl, each of which may be optionally substituted. For example, Q may be an alkanediyl group selected from —C2-C24—, an alkanediyl group selected from —C2-C9—, or an alkanediyl group selected from —C3-C7—. According to a preferred embodiment, Q is a C6 alkanediyl. According to another embodiment, Q may be a cyclohexanediyl, cyclopentanediyl or cyclobutanediyl, or a divalent benzyl radical. In this context, it should be noted that certain authors prefer using the term “alkyl” instead of the chemically more correct “alkanediyl” nomenclature; the same chemical group is meant.


As used herein, the term “alkanediyl” means a chain of carbon atoms, which may optionally be branched, preferably of limited length, including —C1-C24—, —C1-C12—, —C1-C8—, —C1-C6—, and —C1-C4—. Shorter alkanediyl groups may add less lipophilicity to the compound and accordingly will have different reactivity towards the reducing sugar reactant and/or solubility.


As used herein, the term “cycloalkanediyl” means a chain of carbon atoms, which may optionally be branched, where at least a portion of the chain is cyclic and also includes polycyclic structures, for example, cyclopropanediyl, cyclopentanediyl, cyclohexanediyl, 2-methylcyclopropanediyl, 2-ethylcyclopentanediyl, adamantanediyl. Furthermore, the chain forming cycloalkanediyl is advantageously of limited length, including —C3-C24—, —C3-C12—, —C3-C8—, —C3-C6—, and —C6-C6—. Shorter alkanediyl chains forming cycloalkanediyl may add less lipophilicity to the compound and accordingly will have a different behavior.


As used herein, the term “heteroalkanediyl” means a chain of atoms that includes both carbon and at least one heteroatom, and is optionally branched. Examples of such heteroatoms include nitrogen, oxygen, and sulfur. In certain variations, said hetero-atoms also include phosphorus, and selenium. In one embodiment, the heteroalkanediyl is a polyether. As used herein, the term “cycloheteroalkanediyl”, includes a chain of atoms that includes both carbon and at least one heteroatom, such as heteroalkanediyl, and may optionally be branched, where at least a portion of the chain is cyclic. Particularly, examples of cycloheteroalkanediyl include divalent tetrahydrofuryl, pyrrolidinyl, tetrahydropyranyl, piperidinyl, morpholinyl, piperazinyl, homopiperazinyl, quinuclidinyl.


Herein, the term “optionally substituted” means the replacement of one or more hydrogen atoms with other functional groups. Such other functional groups may include amino, hydroxyl, halo, thiol, alkyl, haloalkyl, heteroalkyl, aryl, arylalkyl, arylheteroalkyl, nitro, sulfonic acids and derivatives thereof, carboxylic acids and derivatives thereof.


The primary polyamine may be a diamine, triamine, tetramine, or pentamine, for example: a triamine selected from a diethylenetriamine, 1-piperazineethaneamine, or bis(hexamethylene)triamine; triethylenetetramine; or tetraethylenepentamine.


One feature of the primary polyamine is that it may possess low steric hindrance. For example, 1,2-diaminoethane, 1,4-diaminobutane, 1,5-diaminopentane, 1,6-diaminohexane, 1,12-diaminododecane, 1,4-diaminocyclohexane, 1,4-diaminoben-zene, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, 1-piperazine-ethaneamine, 2-methyl-pentamethylenediamine, 1,3-pentanediamine, and bis(hexamethylene)triamine, as well as 1,8-diaminooctane have low steric hindrance.


Preferably, the nitrogen-containing reactant comprises or consists of 1,6-diaminohexane (hexamethylenediamine, HMDA) or 1,5-diamino-2-methylpentane (2-methyl-pentamethylenediamine).


In another embodiment, the nitrogen-containing reactant comprises or consists of a polyether-polyamine, which may be a diamine or a triamine, for example a trifunctional primary amine having an average molecular weight of 440 known as Jeffamine T-403 Polyetheramine (e.g. Huntsman Corporation).


In a further embodiment, the nitrogen-containing reactant may comprise or consist of a polymeric polyamine, for example chitosan, polylysine, polyethylene imine, poly(N-vinyl-N-methyl amine), polyaminostyrene, polyvinyl amine (which can be a homopolymer or a copolymer).


The reducing sugar reactant(s), may make up:

    • at least 30%, preferably at least 40%, preferably at least 50%, more preferably at least 60%, more preferably at least 70%, even more preferably at least 80% by dry weight of the binder composition; and/or
    • less than 97%, more preferably less than 95% by dry weight of the binder composition.


The nitrogen-containing reactant(s) may make up:

    • less than 50% or 40%, preferably less than 30%, more preferably less than 25% by dry weight of the binder composition; and/or
    • at least 2.5%, preferably at least 5%, more preferably at least 10% by dry weight of the binder composition.


The binder composition may comprise (i) at least 25%, and preferably at least 40%, at least 50% or at least 60% by dry weight of: (a) reducing sugar reactant(s) and nitrogen-containing reactant(s) and/or (b) curable reaction product(s) of reducing sugar reactant(s) and nitrogen-containing reactant(s).


The ratio of carbonyl groups in the reducing sugar reactant(s) to reactive amino groups in the nitrogen-containing reactant(s) may be in the range of 5:1 to 1:2. For example, the ratio of carbonyl groups to reactive amino groups may be in the range of 5:1 to 1:1.8, 5:1 to 1:1.5, 5:1 to 1:1.2, 5:1 to 1:1, 5:1 to 1:0.8 and 5:1 to 1:0.5. Further examples include ratios such as 4:1 to 1:2, 3.5:1 to 1:2, 3:1 to 1:2, 2.5:1 to 1:2, 2:1 to 1:2 and 1.5:1 to 1:2.


Herein, the term “reactive amino group” means any amino group in the nitrogen-containing reactant(s) which is capable of reacting with the carbohydrate component. Specifically, examples of such reactive amino groups include primary and secondary amino groups, amide groups, imine and imide groups, as well as cyanate and isocyanate groups.


The binder composition may include ester and/or polyester compounds.


The binder composition may comprise one or more adjuvants, for example waxes, dyes release agents and formaldehyde scavengers (notably urea, tannins, quebracho extract, ammonium phosphate, bisulfite).


The binder composition may be applied to the wood particles, in the form of an aqueous composition, preferably an aqueous solution or dispersion, notably in which the dry weight of the aqueous binder composition makes up: ≥40 wt %, ≥45 wt %, ≥50 wt %, ≥55 wt % or ≥60 wt % and/or ≤95 wt %, ≤90 wt %, ≤85 wt % or ≤80 of the total weight of the aqueous binder composition. The presence of the non-carbohydrate polyhydroxy component(s) is particularly advantageously when the binder composition is used at a high solid content, notably ≥55 wt %, to facilitate even distribution of the binder composition over the resinated wood particles despite the high solid content.


The binder composition, notably in the state in which it is applied to the wood particles may have a viscosity which is:

    • greater than or equal to: 10 cP, 25 cP, 50 cP, 75 cP or 85 cP or 95 cP or 105 cP or 115 cP or 125 cP; and/or
    • less than or equal to: 250 cP or 225 cP or 200 cP or 175 cP or 150 cP; notably when the viscosity is measured at 20° C.


The term “wood particle” used herein means wood particles or fibers, including wood chips, wood flakes, sawmill shavings and saw dust or mixtures thereof. The wood particles may have granular sizes of 0.05-10 mm or 1-10 mm. The wood particle board may be a multi-layer wood particle board; in this case, the particles used for the core layer may have granular sizes between 0.05-10 mm or 1-10 mm and the surface layer particles may have a granular size less than 1.5 mm. The aforementioned granular sizes are in respect of at least 90% by weight of the wood particles, preferably at least 95% by weight. Wood particles from both virgin wood and/or reclaimed wood may be used; the wood may comprise, but are not limited to, birch, beech, alder, pine, spruce tropical wood or wood mixtures. Preferably, the wood particles contacted with the binder composition have a moisture content of less than 8%, less than 6% or less than 5% moisture, for example due to pre-drying; they may be pre-dried to a moisture content of 1 to 5% moisture, e.g. 2 to 4% moisture or 1.5 to 3.5% moisture.


The particle boards of the invention may comprise boards commonly called particle boards or oriented strand boards or medium density fiber boards or high density fiber boards.


The wood particle boards, notably once cured, may comprise at least 70%, at least 80%, at least 90% or at least 95% by weight of wood particles.


The wood particle boards, notably once cured, may comprise at least 0.025%, at least 0.05%, at least 0.075% or at least 1% and/or less than 5%, less than 4%, less than 3% or less than 2% of the non-carbohydrate polyhydroxy component(s) by dry weight of the finished particle board. When the particle is a multi-layer board in which the non-carbohydrate polyhydroxy component(s) is not present in all of the layers, the above result may be obtained in respect only of the layer(s) containing the non-carbohydrate polyhydroxy component(s).


The quantitative determination of the non-carbohydrate polyhydroxy component(s) may be made by HPLC (high-pressure liquid chromatography) after an extractive process. The extractive process may consist of a sample of the finished particle board broken into a small piece (for example 2 g) and placed into hot water. The sample in the hot water may be sonicated in an ultrasonic bath (for example during 15 minutes) and then the extrac may be filtered and introduced to a HPLC column. For quantification of glycerol, or other low molecular weight non-carbohydrate polyhydroxy component, an example of a suitable column may be a Luna NH2 (250 mm*4.6 mm*5 microns) eluted with a mobile phase of 10% water and 90% acetonitrile.


The thickness of the wood particle board may be ≥5 mm, ≥8 mm, ≥10 mm, or ≥15 mm and/or ≤100 mm, ≤80 mm, ≤60 mm, ≤50 mm, ≤45 mm or ≤25 mm. Preferred thicknesses are in the range of 10 to 45 mm or 16 to 22 mm. The length of the particle board may be ≥1.5 m, ≥2 m, ≥2.5 m or ≥3 m and/or ≤8 m, ≤6 m or ≤5 m. The width of the particle board may be ≥1 m, ≥1.2 m, ≥1.5 m or ≥1.8 m and/or ≤4 m, ≥3 m or ≥3.5 m.


The wood particle boards may have edges which are trimmed and/or cut and/or machined; they may be piled up and provided as a package comprising a plurality of boards arranged and/or bound together, for example to facilitate transport; the package may comprise an enveloping film, for example of a plastics material.


The binder composition may be applied to the wood particles as a single binder composition, for example by all ingredients of the binder composition being mixed together before being applied as a single spray or projection to the wood particles. Alternatively, two or more portions of the binder composition may be applied separately. For example, the non-carbohydrate polyhydroxy component may be applied to the wood particles separately from the rest of the binder composition. The binder composition may be applied to the wood particles by spraying, for example by passing the wood particles through a spray of the binder composition or by spraying the binder composition over the wood particles whilst the wood particles are being mixed. Preferably, the wood particles are mixed subsequently to application of the binder composition, for example by tumbling, notably in a mixer or bunker. Mixing of the wood particles with the binder composition may comprise applying the binder composition to the wood particles, preferably with subsequent additional mixing of the wood particles, for example by tumbling.


During the curing of the wood particle board, the internal temperature of the board, notably the temperature at the centre of the board in its thickness direction, may be raised to a temperature of:


a) ≥100° C., ≥110° C., ≥115° C., ≥120° C., ≥130° C. or ≥140° C., and/or


b) ≤200° C., ≤180° C., ≤170° C. or ≤160° C.


The curing temperature may range from 110° C. to 280° C. Further examples of the curing temperature include ranges of 110 to 260° C., to 240° C., to 220° C. or to 210° C.


The mat of resinated particles may be pressed, e.g. in a hot press, at a pressure which is ≥20 bar, ≥25 bar or ≥30 bar and/or ≤80 bar, ≤75 bar, ≤70 bar or ≤65 bar to obtain a cured particle board.


The mat of resinated particles may be pressed at a press factor in second per mm of thickness of the wood particle board which is ≥2 seconds/mm, ≥3 seconds/mm, ≥4 seconds/mm or ≥5 seconds/mm and/or ≤60 seconds/mm, ≤40 seconds/mm, ≤30 seconds/mm or ≤20 seconds/mm to obtain a cured particle board. Thus, the press-time may depend on the thickness of the wood particle board.


Embodiments of the invention will now be described, by way of example only, with reference to the accompanying images of which:



FIG. 1 is a representation of a wood particle board made in accordance with the invention; and



FIG. 2 is a representation of a comparative example.


EXAMPLE 1

Two wood particle boards, samples A1 and A2, of length and width 300×300 mm having a thickness of 16 mm and a target density of 650 kg/m3 were prepared. Once dried to a residual moisture content of about 3.5 wt % (based on oven dried wood weight) the wood particles were sprayed with the binder composition and thoroughly mixed by tumbling:


Both wood particleboards were three layer particle boards and were made with Urea Formaldehyde (UF) resinated core chips at a 62:38 ratio of core:surface wood chip mass. The UF was 95.5 parts by weight (66.72 g, 66% solid) of UF resin and 4.5 parts by weight (3.81 g, 52% solid) ammonium nitrate catalyst


Surface Layer Binder Composition of Sample A1: According to the Invention

43.5 parts by weight (19.2 g) of dextrose monohydrate (DMH 90.9 wt % dextrose and 9.1 wt % water of crystallisation), 43.5 parts by weight (17.45 g, 100% solid) of fructose, 13.00 parts by weight (7.45 g, 70 wt % in H2O) of HMDA (hexamethylenediamine, 1,6-hexanediamine) and addition of 5 parts by weight (2.91 g, 69% solid) glycerol. The solid content was 69 wt %


Surface Layer Binder Composition of Sample A2: Comparative Example

43.5 parts by weight (19.2 g) of dextrose monohydrate (DMH 90.9 wt % dextrose and 9.1 wt % water of crystallisation), 43;5 parts by weight (17.45 g, 100% solid) of fructose, 13.00 parts by weight (7.45 g, 70 wt % in H2O) of HMDA (hexamethylenediamine, 1,6-hexanediamine) The solid content was 69 wt %.


A mass of coated wood particles adapted to achieve a target board density of 650 kg/m3 was transferred into a forming box in order to form board samples of 300×300×16 mm. The loading of the binder composition is of 10% on surface chips and 7.5% on core chips. Board samples were pressed under 56 bar, to a thickness of 16 mm using metal stops, at a target platen temperature of 230° C. for a given time period such as to reach a press factors of 7 s per mm thickness for a 16 mm thick board.



FIG. 1 shows the particle board of sample A1.



FIG. 2 shows the particle board of sample A2.


The comparative example of Sample A2 in FIG. 2 shows that several spots are clearly visible. These spots are believed to be clumpings of the wood particles with binder due to poor binder distribution. Such clumping can lead to non-homogeneous properties of the wood particle board, notably affecting bond strength and/or breaking resistance.



FIG. 1 shows reduced presence of spots.

Claims
  • 1. A method of manufacturing a wood particle board comprising wood particles bound by a cured thermoset binder comprising: a) mixing wood particles with a binder composition having a dry weight comprising at least 40% by weight (wt. %) of the binder composition to produce resinated wood particles comprising wood particles coated with the binder composition;b) forming a resinated mat comprising the resinated wood particles arranged in the form of a mat of loosely arranged resinated wood particles; andc) forming a wood particle board by curing the binder composition while subjecting the resinated mat to pressure; wherein the binder composition comprises 0.1-25 wt. % of at least one non-carbohydrate polyhydroxy component comprising a viscosity at 20° C. of 10-10,000 cP for reducing or eliminating resinated wood particle clumping.
  • 2. The method of claim 1, wherein the at least one non-carbohydrate polyhydroxy component is selected from the group consisting of glycerol, a polyalkylene glycol, polyethylene glycol, polypropylene glycol, trimethylolpropane, pentaerythritol, polyvinyl alcohol, partially hydrolyzed polyvinyl acetate, fully hydrolyzed polyvinyl acetate and mixtures thereof.
  • 3. The method of claim 1, wherein the binder composition comprises an aqueous binder composition selected from an aqueous solution or dispersion comprising 40-95 wt. % solids, based on the total weight of the aqueous binder composition.
  • 4. The method of claim 1, wherein the at least one non-carbohydrate polyhydroxy component comprises 1-20 wt. % of the binder composition.
  • 5. The method of claim 1, wherein the binder composition comprises at least 30% by dry weight of a carbohydrate reactant.
  • 6. The method of claim 1, wherein the binder composition comprises (a) at least one reducing sugar reactant and at least one nitrogen-containing reactant; and/or(b) at least one curable reaction product of at least one reducing sugar reactant and at least one nitrogen-containing reactant; wherein the combined weight of (a) and (b) comprises at least 30% by dry weight of the binder composition.
  • 7. The method of claim 6, wherein the at least one reducing sugar reactant is selected from the group consisting of monosaccharides, disaccharides, polysaccharides and combinations thereof.
  • 8. The method of claim 6, wherein the at least one nitrogen-containing reactant is selected from the group consisting of NH3, an inorganic amine, an organic amine comprising at least one primary amine group, a salt thereof and combinations thereof.
  • 9. The method of claim 6, wherein the at least one nitrogen-containing reactant comprises a polyamine having the general chemical structure H2N—Q—NH2, wherein Q is an alkanediyl selected from the group consisting of a —C2—C24— group, a C6 alkanediyl group, a cycloalkanediyl group, a cyclohexanediyl group, a cyclopentanediyl group, a cyclobutanediyl group, a heteroalkanediyl group, a cycloheteroalkanediyl group, chemically substituted variants thereof and combinations thereof.
  • 10. The method of claim 9, wherein the polyamine is selected from a polyether-polyamine, a polymeric polyamine and combinations thereof.
  • 11. A wood particle board produced in accordance with the method of claim 1.
  • 12. The wood particle board of claim 11, comprising wood particles held together by a cured, thermoset binder, wherein the wood particle board comprises at least 1-20 wt. % of at least one non-carbohydrate polyhydroxy component.
  • 13. The wood particle board of claim 11, comprising a multilayer wood particle board comprising wood particles held together by a cured, thermoset binder, wherein at least one layer of the wood particle board comprises at least 1-20 wt. % of at least one non-carbohydrate polyhydroxy component.
  • 14. The method of claim 1, wherein the at least one non-carbohydrate polyhydroxy component comprises 2-18 wt. % of the binder composition.
  • 15. The method of claim 1, wherein the at least one non-carbohydrate polyhydroxy component comprises 5-10 wt. % of the binder composition.
  • 16. The method of claim 6, wherein the polyamine is selected from 1,6-diaminohexane (hexamethylenediamine (HMDA)), 1,5-diamino-2-methylpentane (2-methyl-pentamethylenediamine) and combinations thereof.
  • 17. The method of claim 6, wherein the at least one nitrogen-containing reactant comprises a polyamine having the general chemical structure H2N—Q—NH2, wherein Q is a divalent benzyl radical.
  • 18. The method of claim 1, wherein the at least one non-carbohydrate polyhydroxy component comprises a viscosity at 20° C. of 100-5,000 cP.
Priority Claims (1)
Number Date Country Kind
1517867.6 Oct 2015 GB national
PCT Information
Filing Document Filing Date Country Kind
PCT/EP2016/074031 10/7/2016 WO 00
Publishing Document Publishing Date Country Kind
WO2017/060447 4/13/2017 WO A
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Petition for Inter Partes Review of U.S. Pat. No. 8,114,210 (52 pages, filed Jun. 12, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Declaration of Dr. Frederick J. Hirsekorn Regarding U.S. Pat. No. 8,114,210 (58 pages, filed Jun. 12, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with Petition for Inter Partes Review of U.S. Pat. No. 8,114,210).
1st Petition for Inter Partes Review of U.S. Patent No. D631,670 (68 pages, filed Jun. 19, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
2nd Petition for Inter Partes Review of U.S. Patent No. D631,670 (62 pages, filed Nov. 2, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Decision of PTAB regarding Institution of Inter Partes Review for U.S. Patent No. D631,670 (33 pages)—Jan. 12, 2016.
Decision2 of PTAB regarding Institution of Inter Partes Review for U.S. Patent No. D631,670 (27 pages)—May 9, 2016.
Final Written Decision of PTAB regarding Inter Partes Review of D631,670 based on 1st Petition (56 pages)—Jan. 11, 2017.
Final Written Decision of PTAB regarding Inter Partes Review of D631,670 based on 2nd Petition (55 pages)—May 8, 2017.
Court of Appeals for Federal Circuit Judgment from Appeal of PTAB Decisions in Inter Partes Reviews of U.S. Patent No. D631,670 (2 pages)—Jul. 13, 2018.
1st Petition for Inter Partes Review of U.S. Pat. No. 8,940,089 (61 pages, filed Jul. 1, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Declaration of Dr. Frederick J. Hirsekorn Regarding U.S. Pat. No. 8,940,089 (70 pages, filed Jul. 1, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with 1st Petition for Inter Partes Review of U.S. Pat. No. 8,940,089).
2nd Petition for Inter Partes Review of U.S. Pat. No. 8,940,089 (56 pages, filed Jul. 10, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Declaration of Dr. Frederick J. Hirsekorn Regarding U.S. Pat. No. 8,940,089 (67 pages, filed Jul. 10, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with 2nd Petition for Inter Partes Review of U.S. Pat. No. 8,940,089).
3rd Petition for Inter Partes Review of U.S. Pat. No. 8,940,089 (62 pages, filed Jul. 17, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Declaration of Dr. Frederick J. Hirsekorn Regarding U.S. Pat. No. 8,940,089 (76 pages, filed Jul. 17, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with 3rd Petition for Inter Partes Review of U.S. Pat. No. 8,940,089).
Declaration of Dr. Elam Leed (11 pages, filed Jul. 1, Jul. 10, and Jul. 17, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with 1st, 2nd and 3rd Petition for Inter Partes Review of U.S. Pat. No. 8,940,089, respectively).
Declaration of Dr. Jonathan Vickers (10 pages, filed Jul. 1, Jul. 10, and Jul. 17, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with 1st, 2nd and 3rd Petition for Inter Partes Review of U.S. Pat. No. 8,940,089, respectively).
1st Petition for Inter Partes Review of U.S. Pat. No. 9,039,827 (60 pages, filed Jul. 29, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Declaration of Dr. Frederick J. Hirsekorn Regarding U.S. Pat. No. 9,039,827 (72 pages, filed Jul. 29, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with 1st Petition for Inter Partes Review of U.S. Pat. No. 9,039,827).
2nd Petition for Inter Partes Review of U.S. Pat. No. 9,039,827 (51 pages, filed Aug. 5, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Declaration of Dr. Frederick J. Hirsekorn Regarding U.S. Pat. No. 9,039,827 (65 pages, filed Aug. 5, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with 2nd Petition for Inter Partes Review of U.S. Pat. No. 9,039,827).
3rd Petition for Inter Partes Review of U.S. Pat. No. 9,039,827 (57 pages, filed Aug. 7, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Declaration of Dr. Frederick J. Hirsekorn Regarding U.S. Pat. No. 9,039,827 (75 pages, filed Aug. 7, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with 3rd Petition for Inter Partes Review of U.S. Pat. No. 9,039,827).
Declaration of Dr. Elam Leed (11 pages, filed Jul. 29, Aug. 5, and Aug. 7, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with 1st, 2nd and 3rd Petition for Inter Partes Review of U.S. Pat. No. 9,039,827, respectively).
Declaration of Dr. Jonathan Vickers (10 pages, filed Jul. 29, Aug. 5, and Aug. 7, 2015 by Petitioners Johns Manville Corporation and Johns Manville, Inc. in connection with 1st, 2nd and 3rd Petition for Inter Partes Review of U.S. Pat. No. 9,039,827, respectively).
Petition for Inter Partes Review of U.S. Pat. No. 9,469,747 (67 pages, filed Mar. 20, 2018 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Petition for Inter Partes Review of U.S. Pat. No. 9,828,287 (86 pages, filed Mar. 23, 2018 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Petition for Inter Partes Review of U.S. Pat. No. 9,464,207 (78 pages, filed Mar. 28, 2018 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Petition for Inter Partes Review of U.S. Pat. No. 9,926,464 (74 pages, filed Mar. 30, 2018 by Petitioners Johns Manville Corporation and Johns Manville, Inc.).
Office Action Granting Ex Parte Reexamination of U.S. Pat. No. 7,888,445, dated Dec. 24, 2013, in U.S. Appl. No. 90/013,029, 11 pages.
Office Action Granting Ex Parte Reexamination of U.S. Pat. No. 7,772,347, dated Dec. 24, 2013, in U.S. Appl. No. 90/013,030, 14 pages.
Office Action Granting Ex Parte Reexamination of U.S. Pat. No. 7,854,980, dated Apr. 15, 2014, in U.S. Appl. No. 90/013,156, 20 pages.
Declaration of Jan Rud Andersen submitted in Ex parte Reexamination U.S. Appl. No. 90/013,030, as Document OTH-C, Oct. 10, 2013, 4 pages.
Final Rejection in Ex Parte Reexamination of U.S. Pat. No. 7,888,445 (20 pages)—Jul. 24, 2015.
Final Rejection in Ex Parte Reexamination of U.S. Pat. No. 7,772,347 (23 pages)—Jul. 24, 2015.
Final Rejection in Ex Parte Reexamination of U.S. Pat. No. 7,854,980 (31 pages)—Aug. 18, 2015.
Advisory Action in Ex Parte Reexamination of U.S. Pat. No. 7,888,445 (4 pages)—Oct. 6, 2015.
Advisory Action in Ex Parte Reexamination of U.S. Pat. No. 7,772,347 (4 pages)—Oct. 6, 2015.
Advisory Action in Ex Parte Reexamination of U.S. Pat. No. 7,854,980 (4 pages)—Nov. 18, 2015.
Examiner's Answer in Ex Parte Reexamination of U.S. Pat. No. 7,888,445 (8 pages)—Mar. 23, 2016.
Examiner's Answer in Ex Parte Reexamination of U.S. Pat. No. 7,772,347 (8 pages)—Mar. 23, 2016.
Examiner's Answer in Ex Parte Reexamination of U.S. Pat. No. 7,854,980 (8 pages)—Mar. 22, 2016.
Decision of PTAB in Ex Parte Reexamination of U.S. Pat. No. 7,888,445 (17 pages)—Sep. 29, 2016.
Decision of PTAB in Ex Parte Reexamination of U.S. Pat. No. 7,772,347 (18 pages)—Sep. 29, 2016.
Decision of PTAB in Ex Parte Reexamination of U.S. Pat. No. 7,854,980 (22 pages)—Sep. 30, 2016.
Court of Appeals for Federal Circuit Judgment from Consolidated Appeal of PTAB Decisions in Ex Parte Reexamination of U.S. Pat. Nos. 7,888,445, 7,772,347 and 7,854,980 (5 pages)—Mar. 9, 2018.
Notice of Intent to Issue Ex Parte Reexamination Certificate for U.S. Pat. No. 7,772,347 (4 pages)—Oct. 24, 2018.
Notice of Intent to Issue Ex Parte Reexamination Certificate for U.S. Pat. No. 7,888,445 (4 pages)—Dec. 7, 2018.
Decision of USPTO to Reopen Prosecution in Ex Parte Reexamination of U.S. Pat. No. 7,854,980 (7 pages)—Jan. 7, 2019.
Non-final Office Action from Reopened Prosecution in Ex Parte Reexamination of U.S. Pat. No. 7,854,980 (26 pages)—dated Apr. 3, 2019.
Final Office Action from Reopened Prosecution in Ex Parte Reexamination of U.S. Pat. No. 7,854,980 (11 ppages)—dated Aug. 8, 2019.
Notice of Intent to Issue Ex Parte Reexamination Certificate for U.S. Pat. No. 7,854,980 (3 pages)—Oct. 29, 2019.
Notice of Intent to Issue Inter Partes Reexamination Certificate for U.S. Pat. No. 7,807,771 (4 pages)—Jan. 30, 2014.
Notice of Intent to Issue Inter Partes Reexamination Certificate for U.S. Pat. No. 7,854,980 (6 pages)—Aug. 31, 2017.
Decision of PTAB in Inter Partes Reexamination of U.S. Pat. No. 7,888,445 (34 pages)—May 1, 2015.
Decision of PTAB in Inter Partes Reexamination of U.S. Pat. No. 7,772,347 (36 pages)—May 1, 2015.
Decision of PTAB in Inter Partes Reexamination of U.S. Pat. No. 7,854,980 (25 pages)—Jul. 30, 2015.
Remand Order of PTAB in Inter Partes Reexamination of U.S. Pat. No. 7,888,445 (5 pages)—Dec. 9, 2015.
Remand Order of PTAB in Inter Partes Reexamination of U.S. Pat. No. 7,772,347 (5 pages)—Dec. 9 , 2015.
Examiner's Determination on Patent Owner Response/Requester Comments after Board Decision in Inter Partes Reexamination of U.S. Pat. No. 7,888,445 (22 pages)—Oct. 17, 2016.
Examiner's Determination on Patent Owner Response/Requester Comments after Board Decision in Inter Partes Reexamination of U.S. Pat. No. 7,772,347 (17 pages)—Oct. 17, 2016.
Court of Appeals for Federal Circuit Opinion/Judgment from Appeal of PTAB Decision in Inter Partes Reexamination of U.S. Pat. No. 7,854,980 (13 pages)—Feb. 27, 2017.
Final Decision of PTAB in Inter Partes Reexamination of U.S. Pat. No. 7,888,445 (25 pages)—Sep. 8, 2017.
Final Decision of PTAB in Inter Partes Reexamination of U.S. Pat. No. 7,772,347 (24 pages)—Sep. 8, 2017.
Decision of PTAB re Request for Rehearing in Inter Partes Reexamination of U.S. Pat. No. 7,888,445 (7 pages)—Feb. 12, 2018.
Decision of PTAB re Request for Rehearing in Inter Partes Reexamination of U.S. Pat. No. 7,772,347 (7 pages)—Feb. 12, 2018.
Court of Appeals for Federal Circuit Decision re Consolidated Appeal of PTAB Decision in Inter Partes Reexamination of U.S. Pat. No. 7,772,347 and U.S. Pat. No. 7,888,445 (14 pages)—Oct. 15, 2019.
Remand Order of PTAB in Inter Partes Reexamination of U.S. Pat. No. 7,888,445 (3 pages)—Jul. 1, 2020.
Remand Order of PTAB in Inter Partes Reexamination of U.S. Pat. No. 7,772,347 (3 pages)—Jul. 1, 2020.
Decision of PTAB regarding Institution of Inter Partes Review for U.S. Pat. No. 8,114,210 (20 pages)—Oct. 21, 2015.
Final Written Decision of PTAB regarding Inter Partes Review of U.S. Pat. No. 8,114,210 (39 pages)—Oct. 19, 2016.
Court of Appeals for Federal Circuit Judgment from Appeal of PTAB Decision in Inter Partes Review of U.S. Pat. No. 8,114,210 (5 pages)—Jan. 16, 2018.
Decision of USPTO Granting Ex Parte Re-exam of U.S. Pat. No. 8,114,210 (11 pages)—Apr. 9, 2020.
Decision1 of PTAB declining Institution of Inter Partes Review for U.S. Pat. No. 8,940,089 (16 pages)—Dec. 17, 2015.
Decision2 of PTAB declining Institution of Inter Partes Review for U.S. Pat. No. 8,940,089 (19 pages)—Dec. 17, 2015.
Decision3 of PTAB declining Institution of Inter Partes Review for U.S. Pat. No. 8,940,089 (14 pages)—Dec. 17, 2015.
Decision1 of PTAB declining Institution of Inter Partes Review for U.S. Pat. No. 9,039,827 (16 pages)—Jan. 4, 2016.
Decision2 of PTAB declining Institution of Inter Partes Review for U.S. Pat. No. 9,039,827 (19 pages)—Jan. 4, 2016.
Decision3 of PTAB declining Institution of Inter Partes Review for U.S. Pat. No. 9,039,827 (14 pages)—Jan. 4, 2016.
Decision of PTAB denying Institution of Inter Partes Review for U.S. Pat. No. 9,926,464 (29 pages)—Oct. 2, 2018.
Decision of PTAB denying Institution of Inter Partes Review for U.S. Pat. No. 9,464,207 (28 pages)—Oct. 2, 2018.
Decision of PTAB denying Institution of Inter Partes Review for U.S. Pat. No. 9,469,747 (29 pages)—Oct. 3, 2018.
Decision of PTAB denying Institution of Inter Partes Review for U.S. Pat. No. 9,828,287 (22 pages)—Oct. 16, 2018.
Decision of USPTO Granting Ex Parte Re-exam of U.S. Pat. No. 9,828,287 (13 pages)—Jul. 17, 2020.
Decision of USPTO Granting Ex Parte Re-exam of U.S. Pat. No. 9,464,207 (14 pages)—Jul. 31, 2020.
Statement of Revocation Grounds re GB2496951-Claimant Rockwool International (May 21, 2018, 22 pages).
Statement of Revocation Grounds re GB2451719-Claimant Rockwool International (May 18, 2018, 22 pages).
Expert Report re Revocation of GB2451719 and GB2496951-Claimant Rockwool International (Nov. 12, 2018, 11 pages).
United Kingdom Intellectual Property Office, Decision in Rockwool International v. Knauf Insulation Limited, Application under Section 72 for revocation of patents GB2451719 and GB2496951 (May 28, 2019—18 pages).
Decision of EPO Board of Appeal re Added Matter vis-á-vis EP06788492.4 (Jul. 17, 2019—14 pages).
U.S. Pat. No. 2,965,504—Part 1 (10 pages).
U.S. Pat. No. 2,965,504—Part 2 (14 pages).
U.S. Pat. No. 2,965,504—Part 3 (14 pages).
Gogek Attorney Comments re U.S. Pat. No. 2,965,504—Apr. 6, 1960 (3 pages).
Gogek Affidavit Under Rule 132 re U.S. Pat. No. 2,965,504—Feb. 26, 1960 (3 pages).
Decision of USPTO Granting Ex Parte Re-exam of U.S. Pat. No. 9,926,464 (18 pages)—Aug. 5, 2020.
Decision of USPTO Granting Ex Parte Re-exam of U.S. Pat. No. 8,940,089 (17 pages)—Oct. 16, 2020.
Decision of USPTO Granting Ex Parte Re-exam of U.S. Pat. No. 9,039,827 (16 pages)—Oct. 16, 2020.
Decision of USPTO Granting Ex Parte Re-exam of U.S. Pat. No. 9,469,747 (16 pages)—Nov. 9, 2020.
Related Publications (1)
Number Date Country
20180297231 A1 Oct 2018 US