The present invention relates to an organophilic smectite clay that is capable of thickening organic solvents, in particular, ethyl acetate and butyl acetate, the organic solvents used commonly in producing nail lacquer compositions. Unlike the organophilic clays described in the art, the organophilic smectite clay of the present invention is necessarily produced by adsorbing an amine-free or a non-quaternary-ammonium compound onto the surface of the smectite clay. The amine-free or the non-quaternary-ammonium compound used for treating the smectite clay surface is essentially an amphiphilic copolymer. The amphiphilic copolymer useful for the object of the present invention is a block or a graft copolymer prepared from i) a hydrophilic comonomer that generates a homopolymer that is insoluble in the nail lacquer solvents, and ii) a hydrophobic comonomer that generates a homopolymer that is soluble in the nail lacquer solvents. Preferably, the mole fraction of the hydrophilic comonomer is in the range of 0.05-0.5, while the mole fraction of the hydrophobic comonomer is in the range of 0.5-0.95, with the molar ratio of the two comonomers being such that the copolymer is soluble and/or dispersible in the nail lacquer solvents, but is insoluble or merely dispersible in water. Most preferably, the amphiphilic copolymer is an A-B-A type of triblock copolymer, wherein the letter “A” represents a hydrophobic comonomer and the letter “B” represents a hydrophilic comonomer. According to a preferred embodiment, the amphiphilic copolymer should have a weight average molecular weight (Mw) of at least 1,000 Dalton. Presently, the most preferred amphiphilic copolymer for producing the organophilic smectite clay of the present invention is a triblock copolymer, PEG 30 Dipolyhydroxystearate, available from Uniqema under the tradename of Arlacel P-135.
The organophilic smectite clay of the present invention is produced in accordance with a procedure comprising of the following sequential steps:
i) The smectite clay is dispersed in water under high-shear mixing, using, for example, a high-shear homogenizer or a colloid mill, preferably while maintaining the temperature of the dispersion in the range of 15-75° C. The clay content (based on dry or moisture-free clay) of the dispersion is preferably in the range of 0.5-75%, and most preferably in the range of 2-10% by weight, based on the total weight of clay and water. The dispersion is subjected to high-shear mixing until the particle size of the sheared clay particles is less than the particle size of the unsheared clay particles by an amount preferably ranging from about 10 to about 80%, and most preferably from about 30 to about 50%.
ii) Upon obtaining the aforementioned particle size reduction via shearing the clay dispersion, an amphiphilic copolymer of the type described above is mixed into the clay dispersion and the resulting clay dispersion composition is subjected to further shearing until at least about 2.5% by weight of the added amphiphilic polymer is adsorbed on the clay surface, while maintaining the dispersion-temperature in the range of 35-60° C. The weight of the amphiphilic copolymer added to the clay dispersion is preferably in the range of 10-200%, and most preferably in the range of 50-100%, based on the weight of the smectite clay (dry-basis).
iii) The clay dispersion composition from step (ii) is subjected to drying using methods or unit operations known in the art, in order to obtain a final moisture-content ranging from about 5 to about 20%, based on the total weight of the final organophilic clay composition.
iv) The dried organophilic clay gallant is typically ground to a particle size in the range of 0.1-5,000 microns, using grinding equipments known in the art.
Alternatively, the organophilic clay composition may be produced by mixing a smectite with a mixture of water and an amphiphilic copolymer of the type described in a preceding section, using a high-shear mixer, wherein the organophilic clay composition conforms to the following ingredient proportions by weight:
Smectite clay: 10-55%
The ability of the organophilic clay of the present invention for thickening nail lacquer solvents, namely, ethyl acetate and butyl acetate, is demonstrated as per the data presented in Table I. To illustrate further the benefit of the present invention, Table I also includes viscosity data for a quaternary ammonium compound-modified organoclay known in the art. The method used for conducting the viscosity tests whose results are presented in Table I is as follows.
The organophilic clay of the present invention was prepared by mixing a smectite clay with PEG 30 Dipolyhydroxystearate (amphiphilic copolymer), as per the manufacturing steps described above. Prior to step (iii) involving drying of clay dispersion, the clay dispersion contained 7.52% (dry-basis—8.25% on wet basis) of the smectite clay, 8.25% of the amphiphilic copolymer, and 83.5% of water (excluding the water associated with the moist clay). The dried and ground organophilic clay produced finally had a moisture content of about 13.5% by weight of the whole organophilic clay. A butyl acetate-mastergel (pregel) of the dried organophilic clay was prepared by shearing the organoclay in butyl acetate using a rotor-stator homogenizer (Silverson Homogenizer). Subsequently, the mastergel was diluted in each of ethyl acetate and butyl acetate, by mixing the mastergel into the respective solvents, using a dispersion-blade agitator. The clay-content (dry and surface modifier-free basis) of the diluted compositions was about 3% by weight. The diluted compositions were stored for a period of one hour before they were taken for Brookfield viscosity measurements.
Likewise, a butyl acetate-mastergel of a quaternary ammonium compound-modified organoclay (Tradename: Bentone 27V obtained from Elementis) was prepared. The organoclay mastergel was diluted in each of the aforementioned solvents to a final clay-content (dry and surface modifier-free basis) of about 3% by weight, wherein two polar compounds (commonly referred to as polar activators in the organoclay prior art), propylene carbonate and water, had to be added in order to produce thickening in the dilute compositions (the compositions hardly thickened when either of the two polar activators was added singly). The amount of water added as a polar activator was about 27% by weight, based on the weight of clay (dry and surface modifier-free basis). The amount of propylene carbonate added as a polar activator was about 30% by weight, based on the weight of clay (dry and surface modifier-free basis), an amount typically used in the art.
Ranges may be expressed herein as from “about” or “approximately” one particular value and/or to “about” or “approximately” another particular value. When such a range is expressed, another embodiment includes from the one particular value and/or to the other particular value. Similarly, when values are expressed as approximations, by use of the antecedent “about,” it will be understood that the particular value forms another embodiment.
It has been found that excellent organic liquid thickening is achieved by adding water to the layered silicate material and shearing the layered silicate/water combination prior to adding the copolymer to the layered silicate/water composition, and thereafter continuing to mix the copolymer uniformly throughout the layered silicate/water combination. Alternatively, the water and copolymer can both be added to the layered silicate material and the composition sheared until homogeneous. When the layered silicate/water copolymer composition is homogeneous, the composition then is dried to a moisture content in the range of about 5% to about 20% by weight, based on the total weight of the composition.
The water content of the layered silicate/water/copolymer composition, when sheared to provide a homogeneous blend, should be at least 5% by weight based on the dry weight of the layered silicate material, preferably at least 10% by weight, more preferably at least 20% by weight water, based on the dry weight of the layered silicate material. Any higher amount of water, e.g., a layered silicate slurry having 200-500% water, can be used but is not economical since the composition is then dried to a moisture content of about 5% to about 20%, preferably about 10% to about 15% water, based on the dry weight of the layered silicate material, prior to adding the composition to one or more organic/liquid(s), e.g., film formers, for increasing the viscosity of the liquid(s). The final product (organophilic clay containing the amphipathic copolymer) should have a water content of at least 10% by weight, preferably 10% to 20% by weight water, based on the dry weight of the layered silicate material, to be effective in viscosifying organic liquids. The water content can be increased by adding water to the organophilic clay just prior to use if it has dried below 10% by weight prior to use.
The amount of copolymer contained in the organoclay should be at least about 10% by weight, based on the dry weight of the layered silicate material, preferably about 15% to about 150%, more preferably about 25% to about 100%, based on the dry weight of the layered silicate material.
This application claims the benefit of U.S. Provisional application Ser. No. 60/804,137 filed on Jun. 7, 2006, which is a continuation-in-part of U.S. application Ser. No. 10/626,009 filed Jul. 24, 2003, hereby incorporated by reference which claims the benefit of U.S. provisional patent application Ser. No. 60/455,049 filed Mar. 14, 2003, and U.S. provisional patent application Ser. No. 60/398,631, filed Jul. 25, 2002.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US07/13354 | 6/6/2007 | WO | 00 | 9/10/2008 |
Number | Date | Country | |
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60804137 | Jun 2006 | US |