Compositions: coating or plastic – Materials or ingredients – Pigment – filler – or aggregate compositions – e.g. – stone,...
Reexamination Certificate
2002-11-13
2003-11-18
Koslow, C. Melissa (Department: 1755)
Compositions: coating or plastic
Materials or ingredients
Pigment, filler, or aggregate compositions, e.g., stone,...
C106S436000, C106S482000
Reexamination Certificate
active
06648958
ABSTRACT:
The invention relates to a pigment mixture for cosmetic formulations in particular which on the one hand gives the human skin a natural appearance but on the other hand makes lines very substantially invisible.
Many female consumers are dissatisfied with the artificial appearance produced by commercial makeup products. Although these makeup products do act to hide the lines, the natural appearance of the skin is lost in the process.
Commercial makeup products often use pearl lustre pigments, whose lustre is reduced by coating or mixing them with barium sulfate or colloidal titanium dioxide.
JP 06-056 628 describes a cosmetic powder consisting of titanium dioxide-coated mica plus a top layer of silicon dioxide.
JP 10-087 433 describes a makeup product consisting of a pearl lustre pigment coated with a spherical material such as silicon dioxide, calcium silicate or an organic polymer. The stated particle size is from 10 to 50 nm.
The use of pearl lustre pigments has the drawback that a significant directed-reflection component deriving from the platelet-shaped structure intensifies the visual effect of lines.
It is an object of the invention to provide a pigment mixture whose refractive index is adapted to the refractive index of the human skin and its colour properties and which provides optimum scattering of the reflected and transmitted light.
This object has been achieved by a pigment mixture comprising
(i) 70-99.9% by weight of a component A consisting of spherical silicon dioxide with a diameter of less than 50 &mgr;m, coated with titanium dioxide and optionally a further layer of SiO
2
, and
(ii) 0.1-30% by weight of a component B consisting of spherical silicon dioxide with a diameter of less than 50 &mgr;m, coated with titanium dioxide as a first layer and iron(III) oxide as a second, outer layer, the refractive index of the pigment being adjusted to a value of between 1.45 and 1.65.
This object is further achieved in accordance with the invention by a process for preparing the pigment mixture of the invention, in which, in a first stage of the process, spherical silicon dioxide with a diameter of less than 50 &mgr;m is coated with titanium dioxide and, in a second stage of the process, the resulting suspension of the component A is admixed, with stirring and at a pH of from 4 to 9, with the uncalcined powder form of component B, which has been prepared beforehand by coating spherical silicon dioxide having a diameter of less than 50 &mgr;m with titanium dioxide as a first layer and iron(III) oxide as a second, outer layer, until the desired hue angle has been reached, and the mixture is stirred for a further 10 to 30 minutes, and the pigment mixture obtained is separated from the reaction medium, washed, dried and calcined at from 500 to 900° C.
In a particular embodiment of the process, the component A, after coating with titanium dioxide, is additionally coated with silicon dioxide.
The invention additionally provides for the use of the pigment of the invention in formulations, especially in paints, varnishes, printing inks, for laser marking, for seed coating, in cosmetic formulations, such as makeup products, face powders, lipsticks, toothpastes, emulsion products, as a peeling additive, and creams and liquid foundations.
Spherical silicon dioxide is used as a starting product for the preparation of the pigment. Because of the process by which they are prepared, the spheres are not uniform in diameter but have a distribution spectrum as regards their particle size. Suitability as the starting product is possessed by fractions in which 99% of the particles are smaller than 50 &mgr;m. Preference is given to fractions in which 95% of the particles are smaller than 35 &mgr;m and particular preference to those fractions in which 90% of the particles are smaller than 20 &mgr;m.
The preparation of spherical silicon dioxide is known. It is carried out by hydrolysing organic or inorganic silicon compounds in an emulsion process. Processes of this kind are described, for example, in DE 21 55 281, DE 26 10 852, GB 1 141 924 and EP 0 162 716. Spherical silicon dioxide is commercially available. Under the designation Ronasphere®, Merck KGaA supplies spherical silicon dioxide with a particle size of less than 20 &mgr;m.
The coating of the spherical silicon dioxide with titanium dioxide, iron oxide and silicon dioxide is carried out by known processes.
Coating with titanium dioxide takes place in accordance with the process described in U.S. Pat. No. 3,553,001 and EP 0 803 550. This involves slowly adding an aqueous titanium salt solution to the suspension of the spherical silicon dioxide heated to 50-100° C., especially 70-80° C., and maintaining a substantially constant pH of about 0.5-5, especially about 1.5-2.5, by simultaneous metered addition of a base, such as aqueous ammonia solution or an aqueous alkali metal hydroxide solution, for example. As soon as the desired thickness of the precipitated TiO
2
layer has been reached, the addition of the titanium salt solution is stopped.
A feature of this process, which is also known as the titration process, is that it avoids an excess of titanium salt. This is achieved by supplying to the hydrolysis per unit time only that amount which is required for uniform coating with the hydrated TiO
2
and which can be accepted per unit time by the available surface area of the particles to be coated. Therefore, no hydrated titanium dioxide particles are formed that are not deposited on the surface to be coated. The amount of titanium salt added per minute in this process is within the order of magnitude of from about 0.01 to 2·10
−4
mol of titanium salt per square meter of surface area to be covered.
In the case of coating with iron(III) oxide it is possible to start both from iron(III) salts and from iron(II) salts, alone or as a mixture, as is described, for example, in U.S. Pat. No. 3,087,828 and U.S. Pat. No. 3,087,829. In U.S. Pat. No. 3,874,890, the initial coating of iron(II) hydroxide is oxidized to iron(III) oxide hydrate. It is preferred to start from iron(III) salts. To this end, a solution of iron(III) chloride is metered in to an aqueous suspension of the titanium dioxide-coated spherical silicon dioxide at a temperature of from 60 to 90° C. and at a pH of from 2.5 to 4.5. The pH is kept constant by simultaneous metered addition of 32% sodium hydroxide solution. This process is described in DE 196 18 568.
To apply the silicon dioxide, layer to the titanium dioxide-coated spherical silicon dioxide it is preferred to apply the process described in DE 196 18 569. A sodium silicate solution is metered in to a suspension of the material to be coated, this suspension being heated at about 50-100° C., especially 70-80° C. The pH is kept constant at from 4 to 10, preferably from 6.5 to 8.5, by simultaneous addition of 10% hydrochloric acid. After the silicate solution has been added, the mixture is stirred for 30 minutes.
The pigment mixture is prepared in a plurality of stages. To start with, in a first stage, the component B is prepared by coating the spherical silicon dioxide first with titanium dioxide and then with iron oxide. After coating, the product is separated from the reaction medium, washed and dried.
In a second stage, the component A is prepared by coating spherical silicon dioxide with titanium dioxide and, if desired, silicon dioxide. The coated material is left in the coating medium.
In a third stage, the component B in powder form, which has only been dried and not calcined, is metered with stirring into the component A, which has remained in the coating medium, until the desired hue angle has been reached. The hue angle of the wet mixture in this procedure is adjusted to 70°-85°, preferably 76°-78°. Thereafter, the mixture is separated off, washed, dried and calcined from 500 to 900° C. The hue angle of the resultant pigment lies within the range from 65° to 80°, preferably 70°-74° C. The L value of the pigment is 80°-90°, preferably 87°-88°. Since the two components are mixed according to hue angle, the m
Anselmann Ralf
Hillgärtner Uta
Knapp Martin
Koslow C. Melissa
Manlove Shalie
Merck Patent Gesellschaft
Millen White Zelano & Branigan P.C.
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