METHOD FOR PRODUCING SINGLE OR MULTI-LAYERED LIGNOCELLULOSE MATERIALS BY HARDENING IN A HIGH FREQUENCY ELECTRIC FIELD

Abstract

The present invention relates to a process for the batchwise or continuous, preferably continuous production of single-layer lignocellulose-based boards or of multilayer lignocellulose-based boards with a core and with at least one upper and one lower outer layer,

comprising the following steps: a) mixing of the components of the individual layer(s), b) layer-by-layer scattering of the mixtures to give a mat, c) compaction after the scattering of the individual layer(s), d) application of a high-frequency electrical field, during and/or after the compaction and thermal hardening of the binder(s), e) then optionally hot pressing, and f) cooling the lignocellulose material,

where, in step a),

for the core or the single layer, the lignocellulose particles A) [component A)] are mixed with B) from 0 to 25% by weight of expanded plastics particles with bulk density in the range from 10 to 150 kg/m.sup.3 [componeent B)],, C) from 1 to 15% by weight of one or more binders selected from the group consisting of aminoplastic resin and organic isocyanate having at least two isocyanate groups [component C)], D) from 0 to 3% by weight of ammonium salts [component D)], E) from 0 to 5% by weight of additives [component E)] and F) from 0.1 to 3% by weight of alkali metal salts or alkaline earth metal salts from the group of the sulfates, nitrates, halides and mixtures of these [component F)],

and optionally for the outer layers, the lignocellulose particles G) [component G)] are mixed with H) from 1 to 15% by weight of one or more binders selected from the group consisting of aminoplastic resin and organic isocyanate having at least two isocyanate groups [component H)], I) from 0 to 2% by weight of ammonium salts [component I)], J) from 0 to 5% by weight of additives [component J)] and K) from 0.1 to 3% by weight of alkali metal salts or alkaline earth metal salts from the group of the sulfates, nitrates, halides and mixtures of these [component K)],

wherein at the juncture Z the temperature of the layer of the core or of the single layer is more than 90°C., and this temperature is reached in less than 40 s/mm d after the application of the high-frequency electrical field, where d is the thickness of the sheet of lignocellulose material at the juncture Z.

Claims

1.-18. (canceled)

19. A process for the batchwise or continuous production of single-layer lignocellulose-based boards or of multilayer lignocellulose-based boards with a core and with at least one upper and one lower outer layer, comprising the following steps: a) mixing of the components of the individual layer(s), b) layer-by-layer scattering of the mixtures to give a mat, c) compaction after the scattering of the individual layer(s), d) application of a high-frequency electrical field during and/or after the compaction and thermal hardening of the binder(s), e) then optionally hot pressing, and f) cooling the lignocellulose material, where, in step a), for the core or the single layer, the lignocellulose particles A) [component A)] are mixed with B) from 0 to 25% by weight of expanded plastics particles with bulk density in the range from 10 to 150 kg/m.sup.3 [component B)], C) from 1 to 15% by weight of one or more binders selected from the group consisting of aminoplastic resin and organic isocyanate having at least two isocyanate groups [component C)], D) from 0 to 3% by weight of ammonium salts [component D)], E) from 0 to 5% by weight of additives [component E)] and F) from 0.1 to 3% by weight of alkali metal salts or alkaline earth metal salts from the group of the sulfates, nitrates, halides and mixtures of these [component F)], and optionally for the outer layers, the lignocellulose particles G) [component G)] are mixed with H) from 1 to 15% by weight of one or more binders selected from the group consisting of aminoplastic resin and organic isocyanate having at least two isocyanate groups [component H)], I) from 0 to 2% by weight of ammonium salts [component I)], J) from 0 to 5% by weight of additives [component J)] and K) from 0.1 to 3% by weight of alkali metal salts or alkaline earth metal salts from the group of the sulfates, nitrates, halides and mixtures of these [component K)], wherein at the juncture Z the temperature of the layer of the core or of the single layer is at least 90° C., and this temperature is reached in less than 40 s/mm.Math.d after the application of the high-frequency electrical field, where d is the thickness of the sheet of lignocellulose material in mm at the juncture Z.

20. The process for the production of single- or multilayer lignocellulose materials according to claim 19, wherein the process is carried out continuously.

21. The process for the production of single- or multilayer lignocellulose materials according to claim 19, wherein the process is used for the production of single-layer lignocellulose materials.

22. The process for the production of single- or multilayer lignocellulose materials according to claim 19, wherein the temperature of the layer of the core, or of the single layer, at the juncture Z is from 90 to 170° C.

23. The process for the production of multilayer or single-layer lignocellulose materials according to claim 19, wherein the lignocellulose material comprises, in the core or in the single layer, from 0.2 to 2.5% by weight of component F).

24. The process for the production of multilayer or single-layer lignocellulose materials according to claim 19, wherein the density of the lignocellulose material is from 100 to 700 kg/m.sup.3.

25. The process for the production of multilayer or single-layer lignocellulose materials according to claim 19, wherein the density of the lignocellulose material is from 250 to 390 kg/m.sup.3.

26. The process for the production of multilayer lignocellulose materials according to claim 19, wherein the following condition is met: component F)≧1.1.Math.component K).

27. The process for the production of multilayer lignocellulose materials according to claim 19, wherein the following condition is met: [component F)+component D)]≧1.1.Math.[component K)+component I)].

28. The process for the production of multilayer lignocellulose materials according to claim 19, wherein the following condition is met: component F)≦1.1.Math.component K).

29. The process for the production of multilayer lignocellulose materials according to claim 19, wherein the following condition is met: [component F)+component D)]≦1.1.Math.[component K)+component I)].

30. A single- or multilayer lignocellulose material produced by the process according to claim 19.

31. A single- or multilayer lignocellulose material with a core and optionally with at least one upper and one lower outer layer, where the core or the single layer comprises, based on the lignocellulose particles A) [component A)], the following components: B) from 0 to 25% by weight of expanded plastics particles with bulk density in the range from 10 to 150 kg/m.sup.3 [component B)], C) from 1 to 15% by weight of one or more binders selected from the group consisting of aminoplastic resin and organic isocyanate having at least two isocyanate groups [component C)], D) from 0 to 3% by weight of ammonium salts [component D)], E) from 0 to 5% by weight of additives [component E)] and F) from 0.1 to 3% by weight of alkali metal salts or alkaline earth metal salts from the group of the sulfates, nitrates, halides and mixtures of these [component F)], and optionally for the outer layers, based on the lignocellulose particles G) [component G)], the following components: H) from 1 to 15% by weight of one or more binders selected from the group consisting of aminoplastic resin and organic isocyanate having at least two isocyanate groups [component H)], I) from 0 to 2% by weight of ammonium salts [component I)], J) from 0 to 5% by weight of additives [component J)] and K) from 0 to 2% by weight of alkali metal salts or alkaline earth metal salts from the group of the sulfates, nitrates, halides and mixtures of these [component K)].

32. A single- or multilayer lignocellulose material produced according to claim 31, wherein the lignocellulose material comprises, in the core or in the single layer, from 0.2 to 2.5% by weight of component F).

33. The multilayer lignocellulose material according to claim 31, wherein a density distribution perpendicularly to the plane of the board is almost homogeneous and the difference between density maximum in the outer layers and density minimum in the core is at most 100 kg/m.sup.3.

34. The single-layer lignocellulose material according to claim 31, wherein a density distribution perpendicularly to the plane of the board is almost homogeneous and the difference between density maximum and density minimum in the single-layer lignocellulose material is at most 100 kg/cm.sup.3.

35. A material for furniture or as packaging material which comprises the single- or multilayer lignocellulose materials according to claim 31.

36. An inner ply for sandwich boards which comprises the single- or multilayer lignocellulose materials according to claim 31.

37. A roof paneling or wall paneling, infill, shuttering, floors, door inlays, partitions or shelving or as support material for unit furniture, as door material, as worktop, as kitchen front, as outer layers in sandwich structures, or as elements in tables, chairs, and upholstered furniture which comprises the single- or multilayer lignocellulose materials according to claim 31.

Description

EXAMPLES

Particle Boards of the Invention

Mixture 1 for Particle Board 1

[0199] 459 g of Kaurit® 347 glue (BASF SE, solids content 67%) were mixed with 34.0 g of sodium nitrate, 22.5 g of 40% ammonium nitrate solution, 50.0 g of HydroWax® 140 (Sasol, solids content 60%) and 75.6 g of water, with stirring. This mixture was added to 3099 g (3000 g of dry material, 99 g of moisture) of sprucewood particles in a paddle mixer, and mixed. Water content of the finished mixture measured by the Darr method was 9.5%.

Mixture 2 for Particle Boards 2 to 4

[0200] 412 g of Kaurit® 347 glue (BASF SE, solids content 67%) were mixed with 30.5 g of sodium nitrate, 20.3 g of 40% ammonium nitrate solution, 50.0 g of HydroWax® 140 (Sasol, solids content 60%) and 89.4 g of water, with stirring. This mixture was added to 3069 g (3000 g of dry material, 99 g of moisture) of sprucewood particles in a paddle mixer, and mixed. Water content of the finished mixture measured by the Darr method was 9.9%.

Determination of Dielectric Loss

[0201] Dielectric loss was determined on mixture 1. For this, the mixture was charged to a test chamber composed of an exterior and interior metal cylinder. The structure corresponds to that of a cylindrical capacitor where the basal surfaces of the exterior and the interior cylinder lie in the same plane and the two cylindrical surfaces (internal side of the exterior cylinder and external side of the interior cylinder) are coaxial. The mixture to be tested is charged to the annular intervening space between the exterior (inside diameter 9.5 cm) and interior (diameter 5 cm) metal cylinder. The material is charged to a height of 11.9 cm. An alternating electrical field is applied to the cylindrical capacitor and the dielectric response at various frequencies (1 kHz, 10 kHz, 100 kHz, 1 MHz, 10 MHz) is determined by measuring the current flowing through the mixture of materials. An HP 4192A LF impedance analyzer from Hewlett-Packard was used for this purpose. Dielectric loss E″ was determined by extrapolation as 27.12 MHz for both mixtures.

ε| (mixture 1)=0.0258

Production of the Particle Board of the Invention

[0202] x g of the mixture 1 were scattered into a scattering frame (46×44 cm). The scattered mat was precompacted at room temperature for 60 seconds in the scattering frame at a specific pressure of 10 bar in a down-stroke press. Using a y mm mat here (depth after scattering), outgoing compacted depth was z mm. The scattering frame was then removed. For monitoring of the temperature profile in the middle of the sheet and in the middle of the outer layers, optical sensors were introduced into the edge of the mat, respectively into a horizontal hole in the center of the outer layers and of the core. Nonwoven separators were then provided to the upper and lower side of the mat, and this was compacted to 17.5 mm (particle board 1) or 20.0 mm (particle board 2 to 4) in a HLOP 170 press from Hoefer Presstechnik GmbH within a period of 2 s, and then heated by applying a high-frequency alternating field (27.12 MHz). After the time t, the temperature T in the core was measured and the press was opened. After conditioning (at 65% humidity and 20° C.) to constant mass, the thicknesses and densities (in accordance with EN 1058), and the transverse tensile strengths (in accordance with EN 319) of the resultant particle board was determined.

TABLE-US-00001 Particle board Particle board Particle board Particle board 1 2 3 4 x [g] 2508 2407 1955 1517 y [mm] 120 105 90 65 z [mm] 55 55 40 30 z in HF [mm] 17.5 20 20 20 T [° C.] 130 130 130 130 t [s] 96 126 116 102 Thickness 17.9 19.8 19.5 19.2 [mm] Density 670 589 479 381 [kg/m.sup.2] Transverse 1.31 1.00 0.69 0.35 tensile strength [N/mm.sup.2]

Reference Particle Board

Mixture 3

[0203] 459 g of Kaurit® 347 glue (BASF SE, solids content 67%), 22.5 g of 40% ammonium nitrate solution, 50.0 g of HydroWax® 140 (Sasol, solids content 60%) and 75.6 g of water were mixed, with stirring. This mixture was added in a paddle mixer to 3099 g (3000 g of dry material, 99 g of moisture) of sprucewood particles, and mixed. Water content of the finished mixture measured by the Darr method was 9.7%.

Production of Reference Particle Board

[0204] 2513 g of mixture 3 were scattered into a scattering frame (46×44 cm). The scattered mat was precompacted at room temperature for 60 seconds in the scattering frame at a specific pressure of 10 bar in a down-stroke press. Using a 100 mm mat here (depth after scattering), outgoing compacted depth was 50 mm. The scattering frame was then removed. Nonwoven separators were then provided to the upper and lower side of the mat, and this was cold-precompacted to 20 mm in an HLOP 170 press from Hoefer Presstechnik GmbH within a period of 2 s. An automatic transfer system was used to move the mat into a heated press from Hoefer, where it was pressed to a thickness of 17.5 mm at a temperature of 227° C. (press time 175 s).

[0205] After conditioning (65% humidity and 20° C.) to constant mass, thickness, density (in accordance with EN 1058) and transverse tensile strength (in accordance with EN 319) of the resultant particle board were determined in accordance with EN 319.

Thickness=17.9 mm

[0206] Density=678 kg/m.sup.2
Transverse tensile strength =0.93 N/mm2