The present invention relates to a granular material for digital control decoration, the use thereof as a decorative material, and a process for the preparation thereof.
There are known decoration systems, so-called dry digital control systems, in which it is envisaged to preform, on a ribbon or transfer surface, an image consisting of liquid ejected from inkjet apparatus, make a decorating material in the form of a powder or granules adhere to this image (hence the name “dry” decoration) and then transfer the decoration thus obtained onto the receiving surface of the object to be decorated.
Compared to traditional inkjet technologies, these systems have the advantage of eliminating every risk of possible clogging and wear on delicate inkjet apparatus since the decorating material does not pass through the inkjet apparatus, which limits itself to working with simple liquids devoid of solid suspensions.
Examples of such systems are described in IT1314624, WO2005025828 and WO2007096746, wherein the liquid envisaged is water, which is particularly convenient given its physicochemical and ecological characteristics.
The commercially available decorating materials for this and other so-called “dry” technologies must exhibit good flowability and a minimal dispersal of fine powders into the environment and they are thus produced in the form of granules using different methods.
A first type of material is obtained with a technology which provides for wet grinding of the raw materials and subsequent atomization in order to obtain pseudo-spherical granules. However, due to the fact that they necessarily also contain plastic materials (clay, kaolin etc.) and other additives (binders, thinners, suspending agents etc.), in contact with the inkjet water these granules tend to disintegrate on the surface, thus remaining permanently glued to the transfer surface.
A second type of granular material is obtained using a method which comprises the following steps:
A third type of granular material known in the art is obtained by means of a method which comprises the following steps:
When the aforesaid materials of the second and third type are used, difficulties occur during detachment from the transfer surface, since as the granules are not very absorbent, water tends to remain in the interface between the granule and the transfer surface, thus impeding detachment. Moreover, as these granules are of a sharp and abrasive nature, wear or breakage can occur on the transfer surface. Finally, this production technology is decidedly laborious and costly.
A fourth type of granular material known in the art for use as a decorating material is composed of glass microspheres. These do not present problems of abrasiveness but are difficult to detach from the transfer surface due to their lack of absorbency.
Therefore, one object of the present invention is to resolve the above-described problems, providing a granular decorating material that does not undergo disintegration upon contact with water and can be easily and conveniently used in digital control decoration techniques, in particular in the “dry” water-based inkjet decoration technology.
In a first aspect, the present invention relates to a process for the preparation of a granular material for the digital control decoration, preferably by using water-based inkjet decorating machines, said process comprising the steps of:
In a second aspect, the invention relates to a granular material for digital control decoration, preferably using water-based inkjet decorating machines, obtained (or obtainable) with the above-described process.
In a further aspect, the invention relates to the use of said granular material as a decorative material, preferably for ceramic tiles.
Therefore, in a further aspect, the invention relates to a surface decorated with the present material, preferably a ceramic surface.
As mentioned above, the present invention relates to a process enabling a granular material to be obtained for use in digital control decoration, and which comprises the steps of grinding and granulating a solid composition comprising ceramic raw materials, which is characterized by a subsequent step of calcination at a temperature of at least 500° C.
In particular, in the grinding step a) of the present process, a solid composition comprising ceramic raw materials, optionally in a mixture with at least another additive component as described below, is subjected to grinding, typically using techniques known in the art, such as, for example, wet or dry grinding. In particular, the grinding has the purpose of reducing the size of the granules of the various components and homogenizing the distribution thereof. Preferably, at the end of the grinding step, the composition will have a particle size of less than 0.04 mm, more preferably less than 0.02 mm.
In a preferred embodiment, the solid composition comprising ceramic raw materials undergoes wet grinding, in the presence of a suitable dispersing agent, such as water, preferably using an intermittent drum mill.
Said solid composition comprising ceramic raw materials can be prepared on the spot or also prepared in a preceding step, by means of known techniques, and used at the time of need.
“Ceramic raw materials” means a material known to the person skilled in the art, generally made up of inorganic compounds such as, for example, kaolin, clay, bentonite, titanium dioxide, rutile sand, sodium feldspar, potassium feldspar, nepheline, pegmatite, fluorite, spodumene, talc, quartz, wollastonite, silica, alumina, zirconium silicate, magnesium, titanium, zinc, cobalt, iron, chromium, copper, manganese, selenium, cadmium, cerium, tin, lead and zirconium oxide etc., barium, calcium, lithium and strontium carbonate etc., semi-finished materials such as frits, colouring pigments, enamels etc. Said ceramic raw materials are available on the market and can be purchased for example from: Bal-co S.p.a, Sassuolo (MO); Colorobbia Italia Spa, Sovigliana Vinci (FI); Smalticeram Unicer S.p.a, Roteglia of Castellarano (RE); and Inco Industria colori S.r.I. Montebonello PAVULLO (MO).
In an additional embodiment, the solid composition of step a) comprises the ceramic material described above, in a mixture with at least one additional organic and/or inorganic component capable of being decomposed and released in the form of a gas, at high temperatures, i.e. at temperatures higher than at least 300° C., preferably higher than at least 500° C. For this purpose, the preferred additive components are selected from the group consisting of: cereal husks, preferably rice husks, starches, coal, alkaline or alkaline-earth sulphates or carbonates and cereal flours, the latter being particularly preferred. It has been observed, in fact, that thanks to the presence of at least said additives, it is possible to increase the porosity of the granular material obtainable with the present process and thus obtain an easier detachment of the decorating material from the transfer surface.
Optionally, the solid composition comprising ceramic material can contain further additives known in the art such as, for example, binding agents, surfactants, suspending agents, thinners, deflocculants and the like, usable both individually and in a mixture.
When present, the additive is used in amounts comprised from 1% to 20% by weight, relative to the quantity of ceramic raw materials used, preferably in amounts comprised from 5 to 15%, even more preferably from 5 to 10%.
Therefore, in a preferred embodiment, the initial composition comprises ceramic raw materials in a mixture with at least one cereal flour in a percentage by weight comprised from 5 to 7%.
In an equally preferred embodiment, the initial composition comprises ceramic raw materials in a mixture with at least one deflocculant additive in order to render the aqueous suspension more fluid during the wet grinding step, thus permitting the amount of water used for the dispersion to be reduced. In this regard, examples of deflocculant additives that can be used are polyphosphate salts or alkaline or alkaline-earth silicates, preferably selected from the group consisting of: sodium tripolyphosphate and sodium silicate. Preferably, said deflocculant agent is present in a percentage by weight comprised from 0.2 to 2%, relative to the total weight of the starting ceramic material.
The grinding step a) generally takes place at room temperature (i.e. comprised from 15 to 40° C.), for a time that varies in general according to the amount of material used and the type of system used for grinding.
At the end of step a), the ground composition is subjected to the granulating step b) to form agglomerates having sizes comprised from 0.02 mm to 2 mm, preferably comprised from 0.04 to 0.15 mm.
The term “agglomerate” indicates a granule made up of small aggregates of particles of ground ceramic raw materials.
In a preferred embodiment of the invention, step b) occurs by atomization; still more preferably it is carried out using a cylindrical tower atomizer with the lower conical part converging downward.
Generally, the operating temperature during step b) is comprised from 400° C. to 900° C., depending, for example, on the atomizer type and efficiency, and on the type of ceramic material to be atomized.
In a preferred embodiment, the granulating step b) occurs in the presence of at least one aggregating agent, such as, for example, cellulose derivatives or alkaline silicates, preferably selected from the group consisting of: carboxymethyl cellulose (CMC) and sodium silicate.
At the end of granulation, the agglomerates are subjected to the subsequent calcinating step c), whereby the granular material for digital control decoration according to the invention is obtained. In particular, the calcinating step occurs at a temperature of at least 500° C., i.e. such as to render said aggregates stable and not disintegratable in water, and able to maintain a degree of porosity, expressed as free volume between the particles, preferably of at least 10%, more preferably of at least 30%, and even more preferably comprised from 30% to 50% of the total volume.
Therefore, the preferred calcinating temperatures are higher than 600° C., even more preferably higher than 1000° C.
Advantageously, the calcinating step c) enables the water naturally present in the ceramic raw materials used in the present process to be eliminated and, moreover, enables the combustion of the organic materials and of the compounds deriving, for example, from any additive components present in the initial solid composition, as described above, such as carbonates, sulphates and the like. Such elimination, in fact, contributes to increase the porosity of the final material, since it serves to increase the free volume, which means the space present between the various particles making up the final material.
The size of the granules making up the material of the invention is preferably comprised from 0.02 mm to 2 mm, preferably comprised from 0.04 and 0.15 mm, even more preferably comprised from 0.04 to 0.10 mm. The porosity of the material of the invention, expressed as the free volume between the particles, is at least 10%, more preferably at least 30%, and even more preferably comprised from 30 to 50% of the total volume. Higher values of free volume advantageously lead to better characteristics of the final product in terms of better water absorption and thus make it possible to obtain an easier detachment of the decorating material from the transfer surface.
Step c) of the present process for preparing a granular material for decorative use generally occurs for a time such as to ensure a sufficient linkage in the points of contact between the various particles, while maintaining the porosity at values as described above. In one embodiment, the calcinating takes place for a time of at least 1 minute, preferably for a time comprised from 10 to 30 minutes.
Optionally, and in accordance with a preferred embodiment of the invention, the calcinating step c) can be preceded by a sieving step in order to select agglomerates having specific sizes.
Advantageously, the process of the present invention makes it possible to obtain an “inert” material, i.e. a material capable of not remaining stacked to the transfer surface of the decorating machine in the presence of water. Moreover, the present process makes it possible to realize a non-abrasive, economical, fine granular material with good flowability and composed of granules which have a high porosity and a controllable value, and can be easily and conveniently used in digital control decoration techniques, in particular in “dry” water-based inkjet decoration technology.
Therefore, in a further aspect, the present invention relates to a granular material for digital control decoration, preferably using water-based inkjet decorating machines, obtained (or obtainable) with the process of the present invention as described above.
The invention can be represented in a preferred embodiment by the figures appended hereto. In particular,
These granules were originated by mixing together the various elements (2) and (3) in the presence of water as a dispersing agent and subjecting the suspension thus obtained to the grinding step a) and subsequent granulating by atomization. The final calcination at a temperature of about 1000° C. caused the combustion of the particles of the additive component (3), leaving cavities (4) in the granule (1) as indicated in
The granular material of the present invention is particular suitable for digital control decoration, preferably by water-based inkjet decorating machines. In fact, as illustrated for example in
Advantageously, the present material has characteristics of solidity, resistance to the digital decoration process and ease of preparation such that the use thereof is convenient from both a cost and environmental point o view.
Therefore, a further aspect of the invention is the use of the granular material obtained according to the present process, as a decorative material, preferably for digital control decoration techniques.
In a further aspect, the invention relates to a solid surface decorated with the granular material obtained according to the process of the present invention, wherein said surface is preferably a ceramic surface, even more preferably in the form of a tile.
The present invention will now be illustrated in the experimental part below, without it being intended to limit the scope hereof in any way.
Water (26 Kg) is added to the starting solid composition of Table 1 and the suspension thus obtained is subjected to wet grinding in a drum mill with sintered alumina balls until a size of less than 0.02 mm is obtained for the particles.
Subsequently, it is subjected to the atomization step with 0.9 mm diameter air nebulizer nozzles by the company PNR Italia S.r.I. at a liquid suspension pressure of 1 bar and a nebulization air pressure of 2.5 bar at a temperature of about 850° C. Sieving is thereafter performed to eliminate the fraction with a particle size greater than 0.18 mm and then the final calcination step is carried out in an intermittent muffle furnace for a period of 15 minutes at 900° C., with the granulated material arranged in 12-mm-high layers, so to obtain a final material with a particle size distribution of 90% by weight comprised in the interval of 0.03 mm to 0.15 mm.
The volumetric porosity of the granules is 42%.
In the decoration test, the granulated material detached from the transfer ribbon without leaving significant residues.
Number | Date | Country | Kind |
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MI2012A001163 | Jul 2012 | IT | national |
Filing Document | Filing Date | Country | Kind |
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PCT/IB2013/055285 | 6/27/2013 | WO | 00 |