Functionalized metal-containing particles and methods of making the same
View Patent ↗Processes for forming functionalized metal-containing particles. The processes employ a reactive precursor material comprising a metal atom, a leaving group attached to the metal atom, and a functional moiety attached to the metal atom. In one embodiment, functionalized metal-containing particles can be formed by grafting reactive precursors with functional groups to particles containing controlled surface hydroxyl concentrations; with the particles produced by a prescribed method. In another embodiment, a process for forming functionalized metal-containing particles comprises (a) providing a first solution comprising water, a surfactant, and a non-polar dispersant; (b) adding a reactive precursor to the first part to form a mixture, the reactive precursor comprising a metal atom comprising a leaving group attached to the metal atom, and an organic functional moiety attached to the metal atom; and (c) adding a catalyst to the mixture of (b) and reacting with heating under reflux to form functionalized metal-containing particles.
1. A process for producing a metal-containing particle having an organofunctional grafted thereto, the method comprising:
forming a metal containing particle by:
(a) forming a first phase comprising a mixture of water, a metal source,
wherein the metal source comprises a metal selected from the group consisting of Si, Ti, Fe, Al, Zr, Nb, Y, B, Ce, V, Zn, Cu, Ni, Co, Ge, Mn, Mg, Cr, Fe, V, a rare earth metal, or a combination of two or more thereof, a first catalyst, a first surfactant, and a first alcohol;
(b) adding the first phase to a second phase comprising water, a second alcohol, and a second surfactant to form a blend;
(c) treating the blend with a phase enhancer; and
(d) treating the blend from (c) with a second catalyst to form metal-containing particles comprising one or more surface hydroxyl groups; and
grafting a reactive precursor to the particles, wherein the reactive precursor comprises a metal component selected from the group consisting of Si, Ti, Fe, Al, Zr, Nb, Y, B, Ce, V, Zn, Cu, Ni, Co, Ge, Mn, Mg, Cr, Fe, V, a rare earth metal, or a combination of two or more thereof.
2. The process of claim 1 , wherein the reactive precursor comprises a metal component comprising a metal atom comprising a leaving group attached to the metal, and an organic functional moiety attached to the metal atom.
3. The process of claim 2 , wherein the leaving group is selected from the group consisting of an alkoxy group, a halogen, or a combination thereof.
4. The process of claim 2 , wherein the organic functional moiety is selected from the group consisting of a glycol, an alkylene glycol, an acrylic, an amide, a quaternary ammonium compound, a phosphate, a phosphonate, a sulfonate, an amino, a mercapto, an alkyl, an alkyne, an alkene, an azo, a conjugated alkene, a cyclic compound, an alcohol, or a combination of two or more thereof.
5. The process of claim 2 , wherein the organic functional moiety is a urethane linked polyalkylene glycol, a urea linked polyalkylene glycol, or a combination of two or more thereof.
6. The process of claim 1 , wherein the metal source is chosen from a metal alkoxide, a hydrolysable organometallic compound, oxo metal oligomers, a metal chloride, a metal nitrate, a metal sulfate, or mixtures of two or more thereof.
7. The process of claim 1 , wherein the metal source comprises a siloxane oligomer derived from an alkoxysilane, and the molar ratio of water to siloxane oligomer in (a) is sufficient to form a siloxane heptamer, a cyclic siloxane, or a mixture thereof.
8. The process of claim 1 , wherein the first catalyst comprises a catalyst selected from the group consisting of hydrochloric acid, nitric acid, sulfuric acid, phosphoric acid, fluoric acid, formic acid, acetic acid, propionic acid, butanoic acid, pentanoic acid, hexanoic acid, monochloroacetic acid, dichloroacetic acid, trichloroacetic acid, trifluoroacetic acid, oxalic acid, malonic acid, sulfonic acid, phthalic acid, fumaric acid, citric acid, maleic acid, methylmalonic acid, adipic acid, p-toluenesulfonic acid, ammonium hydroxide, quaternary ammonium hydroxides, hydroxylamines, derivatives of hydroxylamines, amino pyridines, or a combination of two or more thereof.
9. The process of claim 1 , wherein the first surfactant is selected from the group consisting of a polyglycol, an alkylene oxide, a cyclic hydrocarbon, a linear or branched aliphatic hydrocarbon having carbon numbers from 5 to 12 and alkyl derivatives thereof, or combinations of two or more thereof or a combination thereof.
10. The process of claim 1 , wherein the first alcohol is chosen from a primary alcohol, a secondary alcohol, or a combination of two or more thereof.
11. The process of claim 1 , wherein the first and/or second alcohol comprises a linear alcohol having 1-10 carbon atoms.
12. The process of claim 1 , wherein the second surfactant comprises a nonionic surfactant.
13. The process of claim 1 , wherein the phase enhancer is selected from the group consisting of a primary or secondary alcohol.
14. The process of claim 1 , wherein the second catalyst is selected from the group consisting of an organic base, a non-metal base that promotes nucleophilic substitution or combinations of two or more thereof.
15. The process of claim 1 , wherein (d) further comprises drying the particles, calcining the particles, or both drying and calcining the particles to reduce the concentration of surface hydroxyls on the particles.
16. The process of claim 15 , wherein the particles have a residual water content of between 0.1% to 15 wt % after the drying, calcining, or both the drying and calcining of the particles.
17. The process of claim 1 , wherein grafting the reactive precursor to the particles comprises:
(e) adding the reactive precursor material to a system comprising the particles, a water free aprotic solvent, and a non-ionic surfactant; and
(f) adding a base catalyst to the resulting solution of (e).
18. The process of claim 17 , wherein the water free aprotic solvent is chosen an alkane having 5-20 carbon atoms; an alkene having 5-20 carbon atoms; an aromatic compound; tetrahydrofuran; pyrrolidone; a substituted pyrrolidone; diethyl ether; chloroform; carbon tetrachloride; acetone; acetonitrile; dimethyl sulfoxide; furfural; or a combination of two or more thereof.
19. The process of claim 17 , wherein the non-ionic surfactant of the system in (e) comprises polyethylene glycol, polypropylene glycol, block copolymers of ethylene oxide and propylene oxide, cyclic, phenolic, substituted aromatics and substituted phenolics in a polyethylenepolypropylene glycol, alkyl polyethers, polyols, and combinations of two or more thereof.
20. The process of claim 17 , wherein the base catalyst of (f) is chosen from ammonium hydroxide, quaternary ammonium hydroxides, hydroxylamines, tetramethylammonium hydroxide, derivatives of hydroxylamines, amino pyridines, or combinations of two or more thereof.
21. The process of claim 17 wherein the resulting mixture of (e) and (f) is reacted with stirring at a rate of from about 30 RPM to about 400 RPM.
22. The process of claim 17 , wherein the metal-containing particles have a mean particle size of from about 0.5 micron to about 300 microns.
23. The process of claim 17 , wherein the metal-containing particles have a surface area of from about 20 m 2 /gram to about 1200 m 2 /gram.
24. A process for forming a functionalized metal-containing particle comprising:
(a) providing a first solution comprising water, a surfactant, and a non-polar dispersant;
(b) adding a reactive precursor to the first part to form a mixture, wherein the reactive precursor comprises a metal selected from the group consisting of Si, Ti, Fe, Al, Zr, Nb, Y, B, Ce, V, Zn, Cu, Ni, Co, Ge, Mn, Mg, Cr, Fe, V, a rare earth metal, or a combination of two or more thereof, the reactive precursor comprising a metal atom comprising a leaving group attached to the metal atom, and an organic functional moiety attached to the metal atom, wherein the organic functional moiety is selected from the group consisting of a glycol, an alkylene glycol, an acrylic, an amide, a quaternary ammonium compound, a phosphate, a phosphonate, a sulfonate, or a combination of two or more thereof; and
(c) adding a catalyst to the mixture of (b) and reacting with heating under reflux to form functionalized metal-containing particles.
25. The process of claim 24 , wherein the leaving group is selected from the group consisting of an alkoxy group, a halogen, or a combination thereof.
26. The process of claim 24 , wherein the organic functional moiety is selected from the group consisting of a urethane linked polyalkylene glycol, a urea linked polyalkylene glycol, or a combination of two or more thereof.
27. The process of claim 24 , wherein the surfactant of solution (a) is an ionic or a non-ionic surfactant.
28. The process of claim 27 , wherein the non-ionic surfactant is selected from the group consisting of polyethylene glycol, polypropylene glycol, block copolymers of ethylene oxide and propylene oxide, cyclic, phenolic, substituted aromatics and substituted phenolics in a polyethylenepolypropylene glycol, alkyl polyethers, polyols, and combinations of two or more thereof.
29. The process of claim 24 , wherein the non-polar dispersant is selected from the group consisting of a cycloaliphatic compound, an alkane comprising 5-20 carbon atoms, an alkene comprising 5-20 carbon atoms, an aromatic compound, a substituted aromatic compound, an alcohol comprising 8-12 carbon atoms, or a combination of two or more thereof.
30. The process of claim 24 , wherein the catalyst is chosen from derivatives of hydroxylamines, tetramethylammonium hydroxide, amino pyridines, or combinations of two or more thereof.
31. The process of claim 24 , wherein the temperature of the reaction is from about 30° C to about 100° C.
32. The process of claim 24 , wherein the temperature of the reaction is from about 50 to about 90° C.
33. The process of claim 24 wherein the reaction of (c) is conducted with stirring at a rate of from about 30 RPM to about 250 RPM.
34. The process of claim 24 , wherein the functionalized metal-containing particles have a mean particle size of from about 0.5 micron to about 100 microns.
35. The process of claim 24 , wherein the functionalized metal-containing particles have a surface area of from about 20 m 2 /gram to about 500 m 2 /gram.