Physical methods of dispersing characteristic use particles and compositions thereof

The present invention provides compositions that are capable of being dispersed in a target medium. The compositions include characteristic use particles entrapped within a physical entrapment phase, wherein the physical entrapment phase is dispersible in the target medium. Accordingly, the compositions of the present invention physically prevent the agglomeration or self-association of the characteristic use particles. Also disclosed are processes for manufacturing compositions that are capable of being dispersed in a target medium.

If you were to search for Physical methods of dispersing characteristic use particles and compositions thereof using relaxed search criteria, these patents would come up:

What is claimed is:

1. A process for manufacturing a composition that is capable of being dispersed in a target medium, comprising: A. mixing a physical entrapment phase precursor with acharacteristic use particles in a processing medium in which the precursor is dispersible, wherein the characteristic use particles have native sizes and native features; B. converting the precursor into a physical entrapment phase which is notdispersible in said processing medium, thereby entrapping the characteristic use particle within the physical entrapment phase; and C. separating the physical entrapment phase having the characteristic use particles entrapped therein from the processingmedium to obtain said composition, wherein when the composition is dispersed in the target medium a substantial number of the physically entrapped characteristic use particles are released from the composition, whereby the released characteristic useparticles exhibit substantially their original native sizes and native features in the target medium.

2. The process according to claim 1 further comprising drying the composition and grinding the dried composition.

3. The process according to claim 1, wherein the precursor is converted into the physical entrapment phase by adding a triggering agent to the processing medium.

4. The process according to claim 3, wherein the physical entrapment phase comprises a plurality of physical entrapment particles.

5. The composition according to claim 4, wherein the number ratio of physical entrapment phase particles to characteristic use particles is greater than or equal to about 10:1.

6. The process according to claim 4, wherein said process medium is hydrophillic; said physical entrapment phase precursor is a smectite clay; and and said triggering agent is one or more organic cations.

7. The process according to claim 6, wherein said clay is selected from the group consisting of montmorillonite, bentonite, beidellite, hectorite, saponite, stevensite, and mixtures thereof; said organic cation has a formula ##STR2## wherein Xis nitrogen or phosphorus, Y is sulfur, R.sub.1 is a long chain, linear or branched, saturated or unsaturated alkyl group and R.sub.2, R.sub.3 and R.sub.4 can be independently selected from the group consisting of linear or branched alkyl groups, aralkylgroups which are benzyl and substituted benzyl moieties including fused ring moieties having 1 to 22 carbon atoms linear or branched 1 to 22 carbon atoms in the alkyl portion of the structure; aryl groups; beta, gamma-unsaturated groups having six orless carbon atoms or hydroxyalkyl groups having two to six carbon atoms; and hydrogen; and said characteristic use particle is a polymer selected from the group consisting of resins, binders, metal oxides, pigments, extenders, dyes, film formingagents, anticorrosive agents, matting/flattening agents, rheological modifiers, biocides, inorganic fillers, flow modifiers, and mixtures thereof.

8. The process according to claim 7, wherein said characteristic use particle is selected from the group consisting of polytetrafluoroethylene (PTFE), polyethylene (PE), polypropylene (PPE), polyethylene terephthalate (PET), polystyrene,polycarbonate, polymethyl methacrylates, polybutadiene, titanium dioxide (TiO.sub.2), magnesium oxide (MgO), zinc oxide (ZnO), ferrous oxide (FeO), ferric oxide (Fe.sub.2 O.sub.3), calcium carbonate (CaCO.sub.3), lead chromate (PbCrO.sub.4), bariumsulfate (BaSO.sub.4), molybdate orange, hansa yellow, phthalocyanine blue, phthalocyanine green, carbazole violet, carbon black, rubinine red, talc, china clay, mica, feldspar, waxes, and mixtures thereof.

9. The process according to claim 8, wherein said characteristic use particles are selected from the group consisting of PTFE, PE, PPE, TiO.sub.2, carbon black, CaCO.sub.3, and mixtures thereof.

10. The process according to claim 4, wherein said process medium is hydrophillic; said physical entrapment phase precursor is a metal salt; and said triggering agent is selected from the group consisting of an acid and a base.

11. The process according to claim 10, wherein said metal salt is a water soluble metal salt.

12. The process according to claim 10, further comprising adding a dilute acid.

13. The process according to claim 12, wherein said characteristic use particle is selected from the group consisting of polytetrafluoroethylene (PTFE), polyethylene (PE), polypropylene (PPE), polyethylene terephthalate (PET), polystyrene,polycarbonate, polymethyl methacrylates, polybutadiene, titanium dioxide (TiO.sub.2), magnesium oxide (MgO), zinc oxide (ZnO), ferrous oxide (FeO), ferric oxide (Fe.sub.2 O.sub.3), calcium carbonate (CaCO.sub.3), lead chromate (PbCrO.sub.4), bariumsulfate (BaSO.sub.4), molybdate orange, hansa yellow, phthalocyanine blue, phthalocyanine green, carbazole violet, carbon black, rubinine red, talc, china clay, mica, feldspar, waxes, and mixtures thereof.

14. The process according to claim 13 wherein said characteristic use particles are selected from the group consisting of PTFE, PE, PPE, TiO.sub.2, carbon black, CaCO.sub.3, and mixtures thereof.

15. A composition obtained according to the process of any one of claims 1, 6, and 10.

16. The composition according to claim 15, wherein a mixture of the composition with the target medium has a Hegman grind gauge improvement of greater than or equal to 1 unit compared to the Hegman grind gauge value of a control mixture of thetarget medium and agglomeration-exhibiting characteristic use particles that are not trapped in a physical entrapment phase.

17. The composition according to claim 15, wherein a mixture of the composition has a 1 minute sieve weight % result of greater than or equal to about 10% in comparison to a 1 minute sieve weight % result of a control sample of characteristicuse particles that are not trapped in a physical entrapment phase.

18. The composition according to claim 15, wherein the composition has an agglomerated particle size decrease of greater than or equal to about 10% in comparison to the agglomerated particle size of characteristic use particles that are nottrapped in a physical entrapment phase.

19. The process according to claim 1, wherein said characteristic use particle is PTFE in its reactor latex form and wherein said process further comprises drying the composition and irradiating the dried composition, wherein the irradiationtakes place at an intensity of from about 5 megarads to about 50 megarads.

20. The process according to claim 8, wherein said characteristic use particle is a submicron particle.

21. The process according to claim 8, wherein said characteristic use particle is PTFE in its reactor latex form.

22. The process according to claim 13, wherein said characteristic use particle is a submicron particle.

23. The process according to claim 13, wherein said characteristic use particle is PTFE in its reactor latex form.

24. The product according to claim 15, wherein said characteristic use particle is a submicron particle.

25. The product according to claim 15, wherein said characteristic use particle is PTFE in its reactor latex form.