Paper with high covering power
09976257 · 2018-05-22
Assignee
Inventors
Cpc classification
D21H17/69
TEXTILES; PAPER
International classification
D21H17/69
TEXTILES; PAPER
G03G7/00
PHYSICS
Abstract
A paper or a decorative base paper for decorative coating materials contains pigment-resin particles that contain a carrier-free pigment and a cured resin and have a mean particle size from 1 to 30 m and delivers a high opacity.
Claims
1. A paper for decorative coating materials, containing cellulose fibers and pigment-resin particles, wherein the pigment-resin particles contain a carrier-free pigment and a cured resin and the mean particle size of the pigment-resin particles is 1 to 30 m, wherein the mass ratio of pigment to resin in the pigment-resin particles is 1:1 to 1:10.
2. The paper according to claim 1, wherein the paper is a decorative base paper.
3. The paper according to claim 1, wherein the pigment-resin particles have a mean particle size of approximately 3 m.
4. The decorative base paper according to claim 3, wherein the mass ratio of pigment to resin in the pigment-resin particles is 1:1.1 to 1:4.
5. The decorative base paper according to claim 1, wherein the pigment of the pigment-resin particles is selected from kaolin, calcium carbonate, calcium sulphate, barium sulphate, titanium dioxide, talc, silica, aluminium oxide, iron oxide, calcium carbonate in its natural form, such as limestone, marble or dolomite brick, and mixtures thereof.
6. The decorative base paper according to claim 5, wherein the pigment is titanium dioxide.
7. The paper according to claim 6, wherein the mass ratio of the titanium dioxide pigment to resin in the pigment-resin particles is 1:1 to 1:4.
8. The decorative base paper according to claim 1, wherein the resin of the pigment-resin particles is selected from melamine-formaldehyde resin, melamine-urea-formaldehyde resin, urea resin, urea-formaldehyde resin, and phenyl-formaldehyde resin, and mixtures thereof.
9. The decorative base paper according to claim 8, wherein the resin is a urea resin.
10. A decorative paper or decorative film comprising a decorative base paper, said decorative base paper contains cellulose fibers and pigment-resin particles, wherein the pigment-resin particles contain a carrier-free pigment and a cured resin and the mean particle size of the pigment-resin particles is 1 to 30 m, wherein the mass ratio of pigment to resin in the pigment-resin particles is 1:1 to 1:10.
Description
DETAILED DESCRIPTION OF THE INVENTION
(1) In contrast to conventional papers, the decorative base paper according to the invention is neither mass sized nor provided with a surface sizing. It fundamentally contains pulp, pigment and where necessary a filler and conventional additives. Conventional additives may be wet strength agents, retention agents and fixing agents. Decorative base papers differ from conventional papers by a much higher filler load or pigment content in the sheet and the absence of a mass sizing or surface sizing, which is conventional in the case of paper. A decorative base paper therefore is able to absorb an impregnating resin.
(2) Softwood pulps (long-fibre pulps) and/or hardwood pulps (short-fibre pulps) can be used as pulps for producing the base papers. The use of cotton fibres and mixtures thereof with the aforementioned pulp types may also be used. By way of example, a mixture of softwood/hardwood pulps in a ratio from 10:90 to 90:10, in particular 20:80 to 80:20, is particularly preferred. However, the use of 100% by weight hardwood pulp has also proven to be advantageous. The specified quantities relate to the mass of the pulps (bone dry).
(3) The pulp mixture may preferably contain a proportion of cationically modified pulp fibres from at least 5% by weight, in relation to the weight of the pulp mixture. A proportion from 10 to 50% by weight, in particular 10 to 20% by weight, of the cationically modified pulp in the pulp mixture has proven to be particularly advantageous. The cationic modification of the pulp fibres may be implemented by reacting the fibres with an epichlorohydrin resin and a tertiary amine or by reaction with quaternary ammonium chlorides, such as chlorohydroxypropyl trimethylammonium chloride or glycidyltrimethylammonium chloride. Cationically modified pulps and production thereof are known for example from DAS PAPIER, issue 12 (1980), pages 575-579.
(4) The pigment-resin particles contained in the paper according to the invention contain a pigment and a resin. The pigment-resin particles have a mean particle size of 1 to 30 m, preferably 2 to 10 m, and particularly preferably 2 to 5 m, for example approximately 3 m.
(5) The mass ratio of pigment to resin in the pigment-resin particles is 1:10 to 1:1, preferably 1:7 to 1:3. The mass ratio of pigment to resin in the pigment-resin particles in the case of the use of titanium dioxide as pigment is 1:1 to 1:4, preferably approximately 1:2.5. However, any other pigment to resin ratios are also conceivable, provided the desired high opacity of the decorative base paper is achieved.
(6) For the purposes of the invention the term pigments is to be understood to mean fine-particle inorganic or organic substances that are obtained naturally or synthetically and can be used in the paper to achieve opacity, for colouring purposes, or as a filler.
(7) Suitable colour pigments for producing the pigment-resin particles contained in the decorative base paper according to the invention are preferably mineral pigments, which are used to increase the opacity in paints and coatings, and in sheet-shaped materials such as paper or plastic films.
(8) Such pigments by way of example may be kaolins, precipitated calcium carbonate, calcium sulphate, barium sulphate, titanium dioxide, talc, silica, aluminium oxide, iron oxide, calcium carbonate in its natural form, such as limestone, marble or dolomite brick, and mixtures thereof.
(9) Due to the high covering capacity and opacity, titanium dioxide is preferred as white pigment for many applications. This is true in particular for use in decorative base papers. Titanium dioxide, which is usually used in decorative papers, can be used as titanium dioxide for producing the pigment-resin particles contained in the decorative base paper according to the invention. Such titanium dioxides are commercially available and may be used as rutile type or anatase type. Titanium dioxides of the rutile type are preferred. By way of example, commercially available titanium dioxides are Ti-Pure R-796+, Ti-Pure R 902 from DuPont, KRONOS 2800 and KRONOS 2305.
(10) The particle size of the pigments in the pigment-resin particles used in accordance with the invention lies in the range from 100 nm to 3 m, preferably in the range 200 nm to 1 m. For cases in which the pigment particles have a non-spherical form, the term particle size is understood to mean the diameter of a sphere of equal volume compared to the particle.
(11) The pigment-resin particles, besides the pigment, also contain a substantially cured resin. This resin is preferably a thermosetting resin. Substantially cured means that the resin is present in a state cured to an extent of more than 80%, preferably to an extent of more than 90%, preferably to an extent of 95%, particularly preferably to an extent of more than 99%, in particular to an extent of 100%. Substantially cured also means that the resin does not chemically bond to the cellulose fibres. By way of example, melamine-formaldehyde resins, melamine-urea-formaldehyde resins, phenyl-formaldehyde resins, urea resins, polyurethanes and mixtures thereof can be used as suitable thermosetting resins. However, the use of other thermosetting resins is also conceivable. Urea-formaldehyde resins are particularly preferably used as thermosetting resins, wherein a curing is carried out during the production of the pigment-resin particles at a pH value from 3 to 6. Commercially available cross-linking agents may also be used to cure the resin. Further suitable polymers as a resin constituent of the pigment-resin particles are those based on polyacrylic or polyacrylic methyl esters, polyvinyl acetate, polyvinyl chloride, and mixtures thereof.
(12) The pigment-resin particles are preferably produced in such a way that a stable aqueous dispersion of the pigment particles is provided and is then cross-linked with an aqueous preparation of the monomers or oligomers of the resin. The concentration of the pigment particles in the dispersion may be 5 to 50 mass %, in relation to the weight of the dispersion. In order to stabilise the dispersion, a dispersing agent (stabiliser) may be added to the pigment particles. By way of example, steric, electrostatic and electrosteric stabilisers are suitable. The stabiliser types Byk 154 and Calgon neu are cited here by way of example. Besides the stabiliser, the dispersion of the pigment particles may contain further additives, such as rheology agents, UV stabilisers, biocide and further additives.
(13) The resin is cured in aqueous medium by lowering the pH value into the acidic range and where necessary by increasing the temperature of the mixture. The slurry (dispersion) of pigment-resin particles thus obtained is dried. The drying may be performed in a circulating air oven. The drying temperature may preferably be 95 C. to 130 C. However, lower and higher temperatures may also be set for drying, provided the properties of the dispersion are not impaired, in particular provided there is no colour change of the dispersion.
(14) A key step in the provision of the pigment-resin particles is the setting of the particle size. The pigment-resin particles present in the form of chips after the drying are comminuted mechanically for this purpose. The mean particle size of the pigment-resin particles is preferably less than 5 m or less than 4 m, particularly preferably less than 3 m. The particle size was measured by laser scattering. The comminution may preferably be performed in two stages, firstly a rough comminution and then a grinding to the desired particle size.
(15) The mechanical comminution may also be performed by all known comminution methods. Dry grinding or wet grinding using known grinding apparatuses or spray drying or fluidised bed drying is preferred. The comminution methods may also be combined with one another or applied in succession. By way of example, a fine powder having a mean particle size of less than 50 m may be obtained by dry grinding. The desired mean particle sizes of the pigment-resin particles of up to approximately 3 m may be set for example by subsequent wet grinding using a tumbling mill or agitator bead mill.
(16) It may also be conceivable to disperse the pigment, in particular titanium dioxide, in a preparation, for example a solution or dispersion, of the resin constituents to be cured.
(17) The paper or decorative base paper according to the invention, besides the pigment-resin particles, may also contain further mineral and non-mineral fillers.
(18) Decorative base papers can be produced on a Fourdrinier paper machine or a Yankee paper machine. For this purpose, the pulp mixture may be ground with a pulp consistency from 2 to 5% by weight to a grinding degree from 10 to 45 SR. The fillers, such as titanium dioxide and talc, and wet strength agent may be added in a mixing chest and thoroughly mixed with the pulp mixture. The resultant thick matter may be diluted to a pulp consistency of approximately 1%, and where necessary further additives may be mixed in, such as retention agents, anti-foaming agents, aluminium sulphate and other previously mentioned additives. This thin matter is guided to the wire section via the headbox of the paper machine. A fibrous fleece is formed, and, after dewatering, the base paper is obtained, which is then dried again. The weight per unit area of the produced papers may be 15 to 300 g/m.sup.2. In particular, however, base papers having a weight per unit area from 40 to 100 g/m.sup.2 are suitable.
(19) In order to produce decorative papers or decorative films, the decorative base papers are impregnated for this purpose with conventional artificial resin dispersions. These comprise, for example, melamine-formaldehyde resins, melamine-urea-formaldehyde resins, phenyl-formaldehyde resins, urea resins, polyurethanes, and mixtures thereof, or such resins based on polyacrylic or polyacrylic methyl esters, polyvinyl acetate, polyvinyl chloride, and mixtures thereof.
(20) The impregnation then may also be performed in a separate pass in the sizing press or using a film press in the paper machine. The impregnation of the paper with the impregnating resin eliminates substantially all inclusions of air in the sheet. The impregnating resin is distributed homogeneously in the sheet. The proportion of impregnating resin, calculated as solid material, in the paper accounts for 10 to 40% by weight, in relation to the mass of the paper. Because, in contrast with a conventional paper or decorative base paper, substantially no air inclusions are present in an impregnated paper, a decorative paper is also referred to as a decorative film.
(21) After drying, the impregnated papers may be coated and printed and then applied to a substrate, such as a wooden board.
(22)
(23) The invention will be explained further by the following examples.
EXAMPLES
Example 1
Production of the Pigment-resin Particles (A)
(24) Production of the TiO.sub.2 dispersion91.25 g of titanium dioxide (Ti-Pure R-796+ Laminate Grade Titanium Dioxide Pigment, manufactured by DuPont) were mixed with 158.75 g of deionised water and 1.4 g of Byk 154 (ammonium polyacrylate, manufactured by Byk Altana) and the mixture was dispersed using an ULTRA-TURRAX rotor-stator dispersing system, model T25, for five minutes at 10,000 revolutions per minute (rpm).
(25) Production of the resin-TiO.sub.2 dispersion387.6 g of resin (Kaurit 210, manufactured by BASF SE) and 212.4 g of the titanium dioxide dispersion produced in step 1 were mixed together (corresponds to a ratio of TiO.sub.2 (solid substance): resin (solid substance) of 1:2.5) and the mixture was dispersed using the ULTRA-TURRAX model T25 for five minutes at 10,000 revolutions per minute (rpm). Here, the pH value of the dispersion was reduced to 5 using a 10% sulphuric acid.
(26) Drying of the resin-TiO.sub.2 dispersionThe 500 g of resin-TiO.sub.2 dispersion were introduced in equal proportions (125 g) into four commercially available silicone shells having an area of 750 cm.sup.2. The shells were then placed together with the content in a laboratory circulating air dryer (WTC Binder) and dried for one hour at 95 C., then for a further half an hour at 130 C. The bowls could then be removed from the dryer.
(27) Dry grinding of the chipsThe dried resin-TiO.sub.2 dispersion was solid and had an area of approximately 4750 cm.sup.2. These chips had to be manually comminuted preliminarily prior to the dry grinding. Here, sizes below 3 cm3 cm were sought. The chips were then dry ground. For this purpose, the chips were placed in a 3 liter grinding container made of white ceramic (for example zirconium dioxide). In addition, the grinding beads, which were also produced from white ceramic, were placed in the container ([numberbead diameter] 54 cm, 123 cm, 552 cm, 1001, 5 cm, 1650.9 cm). Once the container had been tightly closed, it was placed on two rolls, wherein one of the rolls was motor-driven. At a rotational speed from 100 to 150 revolutions/minute, the chips were dry ground for 20 hours.
(28) Wet grinding of the powderThe powder obtained after the dry grinding was not yet fine enough, with a mean particle size from 10 to 20 m. Thus, it had to be ground more finely. This was done by means of wet grinding. For this purpose, 125 g of the composite powder and 400 g of deionised water were dispersed using the ULTRA-TURRAX model T25 for five minutes at 10,000 revolutions per minute (rpm). This dispersion was then ground for one hour in an agitator bead mill (MiniCer, Netszch GmbH; complete zirconium dioxide furnishing, grinding media 0.7 to 0.9 mm (140 ml), 3,600 revolutions/minute). Here, mean particle sizes from 2 to 3 m were attained.
Comparative Example 1
Batch of a Titanium Dioxide Dispersion Usually Used in the Decorating Industry (C)
(29) 91.25 g of titanium dioxide (Ti-Pure R-796+ Laminate Grade Titanium Dioxide Pigment, manufactured by DuPont) were mixed with 158.75 g of deionised water and the mixture was dispersed using an ULTRA-TURRAX rotor-stator dispersing system, model T25, for five minutes at 10,000 revolutions per minute (rpm), the pH value of the dispersion was then set to 8.5 using 10% by weight sodium hydroxide solution.
(30) Production of the decorative base paper according to the invention and of the comparative decorative base paper50 g of eucalyptus pulp (25 g Cacia from Portucel-Empresa Produtora de Pasta e Papel, 25 g Aracruz from Fibria Cellulose SA) were filled into a three-liter dispersion vessel containing 1.5 liters of water, such that a pulp consistency of approximately 3% was set. The pulp was impacted for 30 minutes at 3700 rpm using a laboratory dissolver and a dispersing plate (diameter 50 mm). The resultant pulp slurry was then filled into a distributing apparatus, to which water was added to give a total quantity of 8 liters, such that a pulp consistency of approximately 1% was obtained. 25 g of a 1.5% by weight solution of an adipic acid-diethylenetriamine-epichlorohydrin copolymer (Giluton XP 14, BK Giulini GmbH) was additionally added to the distributor, and the suspension was set to pH 6 using 10% sulphuric acid.
(31) From the pulp suspension thus produced, individual batches were used to produce decorative base paper sheets on a sheet former (manufactured by ERNST HAAGE Apparatebau) in the following manner.
(32) The titanium dioxide preparations A or C were added in each case to 300 g of the pulp suspension (in other words approximately 2 g of pure TiO.sub.2 per sheet) and the suspension was mixed using a paddle mixer for 15 seconds. A further 0.95 g were then added to the 1.5% by weight adipic acid-diethylenetriamine-epichlorohydrin copolymer solution, and this was mixed for a further 45 seconds.
(33) The individual batch thus produced was introduced into the filling chamber of the sheet former with 2 liters of water, filled to a total volume of 4 l, and the sheet-forming process was started.
(34) The individual sheets A1 to A4 were thus produced with use of the pigment-resin particles (titanium dioxide preparation A) according to the invention, and the individual sheets C1 to C8 were thus produced from the comparison titanium dioxide dispersion C.
(35) Impregnation and pressing of the decorative base paper according to the invention and of the comparison decorative base paperIn order to impregnate the individual sheets, a solution containing 52% by weight of melamine-formaldehyde resin (KAURAMIN 773 from BASF SE) was used in water, to which 1.6% by weight of wetting agent (Hypersal VXT 3797 from Surface Specialities Germany) and 0.8% by weight of MADURIT curing agent MH 835/70W, obtainable from Ineos melamines, Germany, were added.
(36) The decorative base paper sheets were placed on the resin solution until complete, full penetration, but at least for 60 seconds, and then were immersed completely into the resin bath. Excess resin was then scraped off, and the sheet was dried for 25 seconds at 130 C. The sheet was then immersed again completely in the resin solution, excess resin was scraped off again, and the sheet was dried at 130 C. up to a residual moisture of 6% by weight.
(37) In accordance with the high-pressure method (HPL) the impregnated decorative paper sheets were pressed for 4 minutes with a laminate panel measuring 4040 cm at a temperature of 140 C. and a pressing force of 234 bar, and were cooled in the press to 60 C. Here, a much smaller black and white decorative paper sheet were also pressed at two different locations beneath the sheet to be examined in order to measure the opacity.
(38) The opacity of the decorative paper sheet to be examined was determined, measured in the reflection density, and compared. For this purpose a white and a black sheet were arranged side by side. The sheet to be examined for opacity was laminated on top of this and then mounted onto a board. The reflection density measurements via the white and via the black sheet were taken using a Datacolor 600 colorimeter.
(39) The reflection density determined via the black sheet was divided by the reflection density determined via the white sheet and the result was multiplied by 100.
(40) The weight per unit area (determined in accordance with EN ISO 536) of the obtained sheets, the ash content thereof and the attained opacity are presented in the table below, wherein the ash content (DIN 54730) can be equated to the quantity of titanium dioxide contained, in relation to the sheet weight or the sheet area.
(41) TABLE-US-00001 TABLE 1 Test results Sheet weight Ash content Ash content Opacity Sheet [g/m.sup.2] [%] [g/m.sup.2] [%] A1 74.2 6.4 4.8 66.9 A2 87.9 10.1 8.9 81.4 A3 93.5 12.2 11.4 86.8 A4 105 14.5 15.2 90.9 C1 79.5 21.6 17.2 79.63 C2 82 24.6 20.2 82.2 C3 85.7 26.3 22.6 83.31 C4 86 28.4 24.4 85.82 C5 86 28.7 24.7 85.81 C6 89.4 31.9 28.6 87.23 C7 92.2 30.3 27.9 88.04 C8 94.7 34 32.2 89.87
(42) In