Claims
- 1. A process for removing surface oxides from a powder, particulate, sheet or foil of at least one member selected from the group consisting of elemental metallic, metallic alloy and intermetallic compounds, the process comprising:
coating the powder, particulate, sheet or foil with an oxide replacing metal by immersing said powder, sheet or foil in a solution containing an electrolyte, said electrolyte being at least one fluoroborate, sulfamate, iodide, cyanide, nitrate, pyrophosphate or sulfide salt of the oxide-replacing metal; and separating the coated powder from the electrolyte solution.
- 2. The process according to claim 1, wherein the oxide-replacing metal is selected from the group consisting of Au, Ag, Fe, Pt, Pd, Ni, Co and Cu.
- 3. The process according to claim 1, wherein the elemental metallic is selected from the group consisting of Ga, Ir, La, Re, Rh, Ru, Sn, Ti, Y, Zn, Nb, Mo, Ta, Sc, Hf, Ce, Pr, Nd, Sm, Gd, Tb, Sy, Ho, Er, Tm, Yb, Lu, U and W.
- 4. The process according to claim 3, wherein the oxide replacing metal is Cu, the elemental metallic is W and the electrolyte is copper pyrophosphate.
- 5. The process according to claim 3, wherein the oxide replacing metal is Ni and the elemental metallic is Ti.
- 6. The process according to claim 1, wherein the intermetallic compound is comprised of at least one first elemental metal being a matrix species, and at least one second elemental metal being a fast diffusing species.
- 7. The process according to claim 1, wherein the powder is comprised of atomized, spherical particles having an equiaxial particle size of from about 0.5 μm to about 50 μm.
- 8. The process according to claim 1, wherein the powder comprises a mixture of a pre-alloyed Ag3Sn or Ag4Sn and first and second elemental metallic powders.
- 9. The process according to claim 1, wherein the powder further comprises a high-strength structural particulate or fiber additive.
- 10. The process according to claim 9, wherein the structural particulate or fiber additive is selected from the group consisting of alumina powder, silicon carbide, graphite, diamond, sapphire and combinations thereof.
- 11. The process according to claim 1, further comprising treating the coated powder with an acid and consolidating the treated powder at near ambient temperature.
- 12. The process according to claim 11, wherein the acid is selected from the group consisting of acetic acid, fluoroboric acid, sulfuric acid, fluoric acid, citric acid, adipic acid, ascorbic acid and nitric acid.
- 13, The process according to claim 12, wherein the acid is fluoroboric acid.
- 14. The process according to claim 12, wherein the concentration of the acid is from about 1% to about 30%.
- 15. A process for consolidating or cold-welding powders, particulates, foils or sheets of metal coated composites, elemental metallic, metallic alloy or intermetallic compounds into net shapes at or near ambient temperature comprising:
removing oxide or adsorbed gases from the surface of the metal coated composites, elemental metallic, metallic alloy or intermetallic compounds thereby forming surface oxide or surface gas free elemental metallic, metallic alloy or intermetallic compounds; surrounding the surface of the powders, particulates, foils or sheets of the metal coated composite, elemental metallic, metallic alloy or intermetallic compound with an environment of a noble or more noble metal, treating the surrounded surface oxide or surface gas free metal coated composites, elemental metallic, metallic alloy or intermetallic compounds with an oxide removing agent; and consolidating the treated metal coated composites, elemental metallic, metallic alloy or intermetallic compounds into a net shape at or near ambient temperature.
- 16. The process according to claim 15, wherein the surrounding is done by coating the surface of the powders, particulates, foils or sheets.
- 17. The process according to claim 15 wherein the powders have dimensions of from about 0.1 μm to about 100 μm, the sheets have a thickness up to about 500 μm and the foils have a thickness of from about 1 μm to about 1000 μm thick.
- 18. The process according to claim 15, wherein the elemental metallic, metallic alloy or intermetallic compound is selected from the group consisting of elemental Ag, Au, In, Sn, Ti, Cu, Al, Mn, Fe, alloys or intermetallics thereof.
- 19. The process according to claim 15, wherein the oxide removing agent is an acid selected from the group consisting of fluoroboric acid, sulfuric acid, hydrofluoric acid, hydrochloric acid, citric acid, adipic acid, ascorbic acid, sodium asorbate, potassium asorbate, sulfamic acid with or without ammonium biflouride and nitric acid.
- 20. The process according to claim 19, wherein the acid is dilute acid and is in a concentration of from about 1% to about 30%.
- 21. The process according to claim 19, wherein the acid is fluoroboric acid and is in a concentration of from about 2% to about 10% by volume.
- 22. The process according to claim 15, wherein the surface oxide or surface gas is removed by anodically or cathodically treating the metal coated composites, elemental metallic, metallic alloy or intermetallic compounds in a dilute acid.
- 23. The process according to claim 22, wherein the dilute acid is selected from the group consisting of acetic, fluoroboric acid, sulfuric acid, fluoric acid, citric acid, adipic acid, ascorbic acid and nitric acid.
- 24. The process according to claim 15, wherein the surface oxide or surface gas is removed by immersing the metal coated composite, elemental metallic, metallic alloy, or intermetallic compound in an electrolytic solution of an oxide replacing metal.
- 25. The process according to claim 24, wherein the oxide replacing metal is selected from the group consisting of Au, Ag, Fe, Pt, Pd, Ni, Co and Cu.
- 26. The process according to claim 25, wherein the electrolytic solution is selected from the group consisting of sulfamate, iodide, cyanide, nitrate, pyrophosphate, fluoroborate or sulfide salt of the oxide-replacing metal.
- 27. The process according to claim 26, wherein the electrolytic solution is the fluoroborate of the oxide-replacing metal.
- 28. The process according to claim 15, wherein the metal coated composite compound is selected from the group consisting of copper coated graphite, copper coated diamond, copper coated tungsten, nickel coated titanium, copper coated aluminum, tin coated nickel, and tin and nickel coated titanium.
- 29. The process according to claim 28, wherein the oxide removing agent is from about 1 to about 30% fluoroboric acid and the metal coated composite compound is copper coated tungsten.
- 30. The process according to claim 28, wherein the metal coated composite is consolidated in a hardened steel mold at a pressure of from about 828 to about 1380 MPa.
- 31. The process according to claim 15, wherein the consolidating takes place in a forging or coining press.
- 32. The process according to claim 15, wherein the consolidating is done by roll bonding foils or sheets.
- 33. The process according to claim 28, wherein particle size distribution of the diamond, tungsten or graphite is bimodal or trimodal, thereby allowing small sized metal coated composite particles to fill spaces between larger metal coated composite particles.
- 34. The process according to claim 15, wherein an elemental metallic is consolidated and removal of the surface oxide is followed by rinsing the elemental metallic in dilute acid of from about 1 to about 5% concentration.
- 35. The process according to claim 15, wherein a fast diffusion couple is consolidated in situ in a dental cavity while being treated with the oxide removing agent.
- 36. The process according to claim 35, wherein the fast diffusion couple is silver and tin.
- 37. The process according to claim 15, wherein the elemental metallic, metallic alloy or intermetallic compound is in the form of a foil; is consolidated after removing surface oxides or adsorbed gases cathodically in a dilute acid; and welded together to fill a dental cavity in situ in the mouth of a patient.
- 38. The process according to claim 15, wherein the elemental metallic is gold and adsorbed surface layers are removed by cathodic treatment in dilute sulfuric acid.
- 39. The process according to claim 15, wherein dental tools are used to consolidate the powders, foils or sheets into net shape.
- 40. The process according to claim 15, wherein roll bonding is used to consolidate or weld a first metal or alloy together with a second metal or alloy, said second metal or alloy being different from the first metal or alloy.
- 41. The process according to claim 15, wherein isostatic pressing is used to consolidate the powders, foils or sheets.
- 42. A process for synthesizing bulk intermetallics or homogeneously distributed two-phase alloys comprising:
generating a large interface between a first powder of a less noble element and a second more noble element by dissolving the second element in an electrolyte, immersing the first powder element in the electrolyte, allowing the second element to deposit from the electrolyte onto the first powder element; and allowing the first powder element and the second element to form an intermetallic compound or a homogeneous two-phase alloy at or about ambient temperature due to the large interface between the first powder and the second element.
- 43. The process according to claim 42, wherein the first element is selected from the group consisting of Sc, Y, Ln, Ti, Zr, Th, U, Np and Pu and the second element is selected from the group consisting of Fe, Co, Ni, Pd and Pt.
- 44. The process according to claim 43, further comprising controlling concentration of electrolyte, amounts of electrolyte solution and solid component and time-duration of the immersion so as to control composition ratio of the intermetallic formed.
- 45. The process according to claim 42, wherein the first element is selected from the group consisting of Nb, Mo, Ta and W and the second element is selected from the group consisting of Cu, Ag and Au.
- 46. The process according to claim 45, wherein a homogeneously dispersed two-phase alloy is formed.
- 47. The process according to claim 42, wherein the first element is selected from the group consisting of In, Ti, Sn and Pb and the second element is selected from the group consisting of Pd, Cu, Ag and Au.
- 48. The process according to claim 47, further comprising adding a chemically inert fine dispersion component to the electrolye thereby forming a metal matrix component wherein the chemically inert component is homogeneously dispersed in the matrix.
- 49. The process according to claim 48, wherein the chemically inert fine dispersion component is selected from the group consisting of alumina powder, silicon carbide, graphite, diamond, sapphire and combinations thereof.
- 50. The process according to claim 47, further comprising controlling concentration of electrolyte, amounts of electrolyte solution and solid component and time-duration of the immersion so as to control composition ratio of the two phase alloy formed.
- 51. The process according to claim 42, wherein a two phase alloy is formed and the first element is aluminum and the second element is selected from the group consisting of Zn, Sn, Cr, Fe and Ni.
- 52. The process according to claim 42, further comprising applying axial pressure or injection molding to consolidate the bulk intermetallic or two-phase alloy into near net shape.
- 53. A process for forming dental restorative materials at ambient temperature and under pressure exerted by dental manual intrumentation comprising:
surface treating a hard intermetallic or metallic component by coating it with a noble metal, adding the surface treated hard intermetallic or metallic component to a dilute acid to form a slurry, and consolidating the slurry into a solid mass using manual dental intrumentation.
- 54. The process according to claim 53, wherein the hard intermetallic is Ag4Sn.
- 55. The process according to claim 53, wherein the metal is tin and the noble metal is Ag.
- 56. The process according to claim 54, wherein the noble metal is Au, Ag, Pt, or Pd.
- 57. The process according to claim 53, wherein the noble metal is present in a volume which is from about 10 to about 100% of a mixture of the hard intermetallic or metallic component and the noble metal.
- 58. The process according to claim 53, wherein the consolidation is performed in situ in the oral cavity of a dental patient.
- 59. The process according to claim 53, wherein the acid is selected from the group consisting of acetic acid, sulfuric acid, fluoroboric acid, hydrofluoric acid, citric acid, adipic acid, ascorbic acid and nitric acid.
- 60. The process according to claim 59, wherein the acid is fluoroboric acid.
- 61. The process according to claim 59, wherein the acid has a concentration of from about 1% to about 30%.
- 62. The process according to claim 60, wherein the fluoroboric acid is in a concentration from about 2 to about 10% by volume.
- 63. The process according to claim 62, wherein the fluoroboric acid is in a concentration of about 2.5% by volume.
Parent Case Info
[0001] This application is a continuation-in-part of U.S. patent application Ser. No. 08/133,316, filed Oct. 8, 1993, which is in turn a continuation-in-part of U.S. patent application Ser. No. 07/802,420, filed Dec. 4, 1991, which issued on Jun. 7, 1994 as U.S. Pat. No. 5,318,746.
Divisions (2)
|
Number |
Date |
Country |
Parent |
08437650 |
May 1995 |
US |
Child |
10034861 |
Dec 2001 |
US |
Parent |
08317729 |
Oct 1994 |
US |
Child |
08437650 |
May 1995 |
US |
Continuation in Parts (2)
|
Number |
Date |
Country |
Parent |
08133316 |
Oct 1993 |
US |
Child |
08317729 |
Oct 1994 |
US |
Parent |
07802420 |
Dec 1991 |
US |
Child |
08133316 |
Oct 1993 |
US |