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US4501818A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the preparation of ceramic powders

Assignee: Saint Gobain Abrasives Inc
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Filing: 1983-07-05
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Granted: 1985-02-26
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Expires: 2003-07-05
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Abstract

Abstract Sub-micron sized powders of the ceramic metal oxides such as zirconia, alumina, titania, etc. are produced by precipitation from substantially anhydrous solutions of salts of the corresponding metal(s) with substantially anhydrous solutions of alkali metal hydroxides. The precipitates are subsequently washed with water to remove any residual soluble salt and/or solvent, then are dried and usually calcined. The powders thus produced are readily sintered to high density ceramic bodies after conventional pressing into the desired shape. The process is especially suited to the production of zirconia powders, either pure or doped with conventional stabilizing oxides such as yttria. In a typical example, a zirconia powder doped with 5.4% by weight of yttria is prepared by adding a solution of zirconium tetrachloride and yttrium chloride in anhydrous ethanol to a solution of sodium hydroxide in anhydrous ethanol. After washing, drying at 105° C., and calcining at 500° C. for two hours, the powder is pressed at 5000 psi into a green body with a density of 1.46 Mg/m 3 . After one hour of sintering a 1600° C., the fired body has a density of 5.84 Mg/m 3 , which is 96% of the theoretical maximum.

Inventors

  • 👤 Giulio A. Rossi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 17:45
CPC Classifications
C; C01; C01G; C01G25/00; C01B; C01B13/00; C01B13/14; C01B13/32; C01B13/328; C01G25/02; C04; C04B; C04B35/00; C04B35/01; C04B35/48; C04B35/486; C01P; C01P2002/00; C01P2002/50; C01P2004/00; C01P2004/01; C01P2004/02; C01P2004/03; C01P2006/00; C01P2006/10

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 158 words
A process for the preparation of uniform, sub-micron size sinterable metal oxide ceramic powders, comprising the steps of: (a) forming a substantially anhydrous first solution of salts of all the metals whose oxides are present in said metal oxide ceramic powders in the proportions present therein and forming a substantially anhydrous second solution of alkali metal hydroxides in the amount stoichiometrically required to react with the metal content of said first solution; (b) adding said first solution to said second solution, so as to form without evidence of gellation a solid precipitate containing substantially all the ceramic metal content originally in said first solution; (c) separating said solid precipitate from the bulk of its supernatant liquid; (d) heating said solid precipitate to remove residual solvent; (e) washing said solid precipitate with water sufficiently to remove substantially all water-soluble salts therefrom; and (f) drying said washed solid precipitate at a temperature in excess of the boiling point of water.
Claim 2
Dependent Claim 158 words
A process for the preparation of uniform, sub-micron size sinterable metal oxide ceramic powders, comprising the steps of: (a) forming a substantially anhydrous first solution of salts of all the metals whose oxides are present in said metal oxide ceramic powders in the proportions present therein and forming a substantially anhydrous second solution of alkali metal hydroxides in the amount stoichiometrically required to react with the metal content of said first solution; (b) adding said first solution to said second solution, so as to form without evidence of gellation a solid precipitate containing substantially all the ceramic metal content originally in said first solution; (c) separating said solid precipitate from the bulk of its supernatant liquid; (d) heating said solid precipitate to remove residual solvent; (e) washing said solid precipitate with water sufficiently to remove substantially all water-soluble salts therefrom; and (f) drying said washed solid precipitate at a temperature in excess of the boiling point of water.
Claim 3
Dependent Claim 30 words
A process according to claim 1, comprising the additional step of calcining said dried precipitate at a temperature of at least 500° C. to remove physically bound water and solvents.
Claim 4
Dependent Claim 14 words
A process according to claim 2, wherein said first solution comprises a zirconium salt.
Claim 5
Dependent Claim 31 words
A process according to claim 3, wherein said first solution comprises an yttrium salt in an amount equal to at least 3% by weight of the content of said zirconium salt.
Claim 6
Dependent Claim 14 words
A process according to claim 1, wherein said first solution comprises a zirconium salt.
Claim 7
Dependent Claim 31 words
A process according to claim 5, wherein said first solution comprises an yttrium salt in an amount equal to at least 3% by weight of the content of said zirconium salt.
Claim 8
Dependent Claim 22 words
A process according to claim 1, wherein said first solution or said second solution is formed with anhydrous ethanol as the solvent.
Claim 9
Dependent Claim 22 words
A process according to claim 2, wherein said first solution or said second solution is formed with anhydrous ethanol as the solvent.
Claim 10
Dependent Claim 22 words
A process according to claim 3, wherein said first solution or said second solution is formed with anhydrous ethanol as the solvent.
Claim 11
Dependent Claim 22 words
A process according to claim 4, wherein said first solution or said second solution is formed with anhydrous ethanol as the solvent.
Claim 12
Dependent Claim 14 words
A process according to claim 1, wherein said alkali metal hydroxide is sodium hydroxide.
Claim 13
Dependent Claim 14 words
A process according to claim 2, wherein said alkali metal hydroxide is sodium hydroxide.
Claim 14
Dependent Claim 14 words
A process according to claim 3, wherein said alkali metal hydroxide is sodium hydroxide.
Claim 15
Dependent Claim 14 words
A process according to claim 4, wherein said alkali metal hydroxide is sodium hydroxide.

References Cited (Backward Citations)

US3334962A Cited
US4365011A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-02-26 1988-08-27 1989-02-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-02-26 1992-08-27 1993-02-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-02-26 1996-08-27 1997-02-26 $7700.00 Window Closed / Lapsed

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