Patent Application
20140128512
The invention relates to a method for producing glitter.
Glitters have many uses for producing a sparkling surface effect and are used inter alia and in particular in cosmetic articles. In order to produce such glitters, there are used foils or films of plastics material which are cut by means of a cutting operation into individual, comparably small particles. If these foils are coated which are produced during the cutting operation, cut edges can become physically and/or chemically weakened. When used, for example, in cosmetic products, the components found in cosmetics, such as water or solvents, can reach the glitter via the cut edges and impair the resistance thereof.
An object of the invention is therefore to provide a method for producing glitter and glitters which are physically and/or chemically resistant after their production so that they can be used, for example in cosmetics, without impairing the surface effects.
This object is achieved according to the invention by the features set out in claim 1 and claim 12.
The dependent claims relate to other configurations of the method according to the invention and of the glitter.
The invention provides a method and a glitter in which the cut edges are protected against physical or chemical weakening when such glitters are used in suspensions or solutions, for example, paints, cosmetics, etc. In particular, the surface effects and the colour components present are intended not to be subject to any impairment such as, for example, colour change, even when used in suspensions, solutions such as paints, cosmetics or polymers.
According to the invention, the glitters are produced using a so-called fluidised bed process in which in principle, in order to coat particles, the individual particles are coated with a suspension or dispersion. In the fluidised bed process, which is known per se, granulates or particles are fluidised by a flow of air, the flow of air constituting a primary flow and the layer of protective material which is provided for the particles being introduced by means of a secondary flow so that the layer of protective material which is in the form of a suspension or dispersion covers the individual particles completely over the entire outer face. Fluidised bed processes and devices for carrying out fluidised bed processes are known, for example, from the publication Operating Guide “Mini Glatt mit Microkit” (“Mini Glatt with Micro kit”), October 2003, and from U.S. Pat. No. 3,241,520 and U.S. Pat. No. 5,632,102.
According to a first aspect, the present invention is directed to a method for producing glitter comprising particles having a thickness of ≧1 μm from a predetermined starting material, which particles are introduced into a mixed bed which is produced by means of a fluidised bed, the mixed bed being adjusted by means of a primary flow and a secondary flow, and the individual particles in the mixed bed being sealed on all sides with a layer of protective material so as to enclose cut and broken edges.
In an embodiment, as a starting material, there is used a carrier layer of plastics foil which is provided on either side with a coating of aluminium and thereon with a coating of polyurethane or epoxide, or a carrier layer of a plastics foil with a coating of polyurethane or epoxide on either side, or a carrier layer of a plastics foil with a coating of aluminium on either side, or a carrier particle of glass or silicate material, or a carrier layer of aluminium foil with a coating of polyurethane or epoxide on either side. Should the carrier particle be of glass or silicate material then, preferably, it is provided with a metal coating.
As preferred metals for the metal coating, silver, aluminium and/or gold may be used.
Preferably, the particles are cut with a preferably hexagon-like shape before the sealing operation with the layer of protective material is carried out in the mixed bed.
In a further embodiment, a hybrid paint or an aqueous polyurethane solution is introduced into the mixed bed as a layer of protective material.
According to the invention, the particles treated in the mixed bed have a diagonal length of 50 μm. Alternatively, the particles may have a diagonal length of 61-500 μm, preferably 61-150 μm.
Preferably, the mixed bed is produced by means of a process air flow which is heated to from 50° C. to 80° C., preferably approximately 60° C.
In a preferred embodiment, the layer of protective material is transparent and/or is provided with a colour component or with colouring pigments. Furthermore, the particles which are coated with a layer of protective material are preferably annealed over a predetermined period of time at from 100° C. to 140° C., preferably 120° C. This annealing operation preferably takes place over from 20 to 40 minutes, preferably 30 minutes.
In a second aspect, a glitter is disclosed comprising a carrier layer of plastics foil which is provided on either side with a coating of aluminium and thereon with a coating of polyurethane or epoxide, or a carrier layer of a plastics foil with a coating of polyurethane or epoxide on either side, or a carrier layer of a plastics foil with a coating of aluminium on either side, or a carrier particle of glass or silicate material, or a carrier layer of aluminium foil with a coating of polyurethane or epoxide on either side, which is provided on all sides with a protective layer so as to enclose cut or broken edges (15a, 15b), or a glitter obtainable by the method as described hereinabove.
The carrier layer preferably is provided on either side with a layer (2a, 2b, 3a, 3b) of aluminium or polyurethane or epoxide, wherein the layer thickness preferably is >1 μm.
As described above, the carrier particle of glass or silicate material may be provided with a metal coating in a further embodiment.
The invention is explained in greater detail below with reference to a preferred embodiment. The Figs. are sectional views through glitters constructed in accordance with the invention, in which:
The method according to the invention for producing glitter is intended to produce a homogeneous coating of glitter particles on all sides, with a size of from 1 μm to 500 μm. Such particles which form the glitters comprise according to a first preferred embodiment a transparent foil, in particular a plastics foil, which is provided with a coating on either side, preferably of polyurethane or epoxide or aluminium. A coating of aluminium is preferably vapour deposited under vacuum in this instance. If an aluminium layer is applied to both sides of a transparent foil, in particular a plastics foil, according to another embodiment this is preferably covered in each case with a layer of polyurethane or epoxide. The particles which form glitter are produced from an aluminium foil according to another configuration.
According to
According to another configuration, as illustrated in
In the fluidised bed process described below, the particles according to
In principle for the particles 8 of glass, it is possible to use irregularly broken fragments of silicate with a thickness ≧1 μm. The provision of metal coatings on these particles is carried out by means of chemical or physical application, for example, vapour deposition.
If the particles comprise a carrier layer in the form of a plastics foil 1, as explained in connection with
Finally, as shown in
Generally, the different initial particles are treated using comparable parameters and are completely surrounded with the layer of protective material in the fluidised bed process so that all the cut edges or broken edges of the initial particles are enclosed. The precise adaptation of the parameters during the fluidised bed process is achieved through the densities and sizes of the respective materials.
In the production of particles from a plastics foil with the coating mentioned above, the individual particles are cut from the foil, preferably in a hexagonal shape, so that cut edges are produced which are formed especially at the side of the foil. Whilst the carrier layer is chemically and physically resistant even at the uncoated side thereof, by means of vapour deposition of aluminium and an additional coating of polyurethane or epoxide, the desired optical effect is achieved on the opposite surface by adding colour. Both surfaces are physically and chemically resistant, whilst over the lateral cut edges, owing to weakening caused by solvents, such as water or the like and when used in paints and cosmetics, it is not possible to prevent a deterioration of the appearance. To this end, the glitters are provided, by means of a fluidised bed process, with a protective layer 11 which completely surrounds the glitters in each case.
All of the particles shown in
According to one example, using a WFP-8 unit fluidised bed unit from the company DMR Prozesstechnologie GmbH (Switzerland), five kilograms of glitter particles of polyester of the type 2510-52-3 hex are coated with an organically modified silane solution, that is to say, a clear hybrid paint. The particles of polyester were produced in this instance from a polyester foil which has a thickness of 25 μm and which was aluminised and subsequently coloured red. The particles were cut from this foil, for example, as hexagonal particles with a size of 200 μm, measured over the length of the mutually parallel cut edges. The thickness of the particles is on average 25-35 μm. These particles were swirled in the mentioned unit by means of process air which was preheated to 60° C. with an air throughput of 60 m3/h in order to produce a so-called mixed bed to which an organically modified silane solution was supplied by means of bottom spray, that is to say from below.
The primary pressure (process air) and the secondary pressure were adjusted in the ratio 1:2.5 in order to achieve good wetting of the entire mixed bed and consequently the glitter particles in the mixed bed. In this instance, the droplets of the clear hybrid paint are distributed finely and blown into the fluidised bed in a uniform manner. In this example, 1000 ml of clear hybrid paint is sprayed in within 60 minutes in order to counteract quick drying of the droplets on the particles. After this time has elapsed, it was possible to remove 5 kg of coated glitter from the unit and, by means of a subsequent 30 minute annealing operation at 120° C., the coating was cross-linked in a stable manner. In this instance, there was a homogeneous coating of all the glitter particles and consequently also a coating in the region of the cut edges which prevents chemical or physical weakening of the glitter.
Depending on the particle size and the particle density of the glitters to be produced, different degrees of fluidisation are to be set in the fluidised bed. Depending on the weight of the glitters, with larger glitter particles a higher process pressure is required, both with respect to the process air which produces the swirling and with respect to the hybrid paint which is blown into the fluidised bed, than with smaller particles which form the glitters. Great expansion of the fluidised bed is required in order to ensure sufficiently great spacing between the individual glitter particles, so that the individual glitter particles, which can be accessed separately, can be coated with the layer of protective material and on the other hand the particles do not become bonded together during the coating operation.
As a coating layer, it is also possible to use an aqueous polyurethane solution instead of a hybrid paint, for example, an organically modified silane solution which is optionally or preferably coloured.
The fluidised bed is produced by means of jets which produce a primary flow, the pressure of this primary flow determining the length of the atomising cone, and by a secondary flow of which the pressure determines the width of the atomising cone.
It has been found that the smaller the solution droplets or the finer the spray mist are to be, the greater the primary pressure should be set. In the case of relatively small particles, the droplets should be as fine as possible. However, smaller droplets dry faster than larger droplets so that, when producing smaller droplets, a larger quantity, for example, of hybrid paint must be used so that the moisture in the fluidised bed is uniform.
As an alternative to jets which are arranged in the base (bottom spray), these jets may also be provided at another location within the unit, for example, in the upper region of the unit or in the lateral region (top spray, tangential spray).
The addition of the layer of protective material in the form of polyurethane solutions or clear or coloured hybrid paints, with preferably organically modified silane solutions is carried out by a time-controlled metering system, for example, a hose pump. The drying or the cross-linking is carried out, depending on the solvent, by the process air being heated or the mixed or fluidised bed being heated. If necessary, the glitters can subsequently be subjected to an additional thermal processing operation, for example in the form of a polymerisation of the protective layer at temperatures higher than 50° C.
Optionally, an adaptation with respect to the temperatures may be necessary, and also with respect to the parameters with which the fluidised bed process is carried out.
The coating by means of the fluidised bed can optionally be repeated in order to carry out a multiple coating of the glitter particles, in order, for example, to achieve modified chemical or physical properties of the protective layer or to allow different protective properties.
Using the fluidised bed process described above, the multi-layer structure is provided with a protective layer 11, which covers all the surfaces of the glitter particle and consequently also covers in particular the lateral cut edges 15a, 15b in an enclosing manner.
In accordance with requirements, colour components, for example, in the form of colouring pigments, can be introduced either into the protective layer 11 or also beforehand together with the application of the other layers 2a to 3b in order to provide colouring on the relevant surface.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10 2010 001 971.2 | Feb 2010 | DE | national |
This application is a continuation of U.S. application Ser. No. 13/027,890, filed Feb. 15, 2011 which claims priority to German Application No. 10 2010 001 971.2, filed Feb. 16, 2010. The contents of which are hereby incorporated by reference in their entirety.
| Number | Date | Country | |
|---|---|---|---|
| Parent | 13027890 | Feb 2011 | US |
| Child | 14152138 | US |
