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US4788045A Expired / Lapsed US ⏱️ 0.0 years remaining

Stabilized zirconia a process for its preparation and its application in ceramic compositions

Assignee: Rhone Poulenc Specialites Chimiques
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Filing: 1986-03-03
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Granted: 1988-11-29
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Expires: 2006-03-03
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Abstract

Abstract A fine powder of stabilized zirconia a process for its preparation and application of the powder in ceramic compositions to obtain good mechanical, thermomechanical and electrical properties. A zirconia hydrate sol having a pH between 0.5 and 5 and containing elementary acicular crystals having dimensions of from about 10 to 500 Å which are agglomerated into submicron aggregates of from abuot 100 to 5000 Å in diameter is mixed with a solution of a stabilizing agent, preferably yttrium; the suspension is dried; the dried suspension is calcined at a temperature of from about 700° C. to 1,300° C. for preferably from about 30 minutes to 24 hours; and if needed, the powder obtained is milled.

Inventors

  • 👤 Jean-Francois Colombet
  • 👤 Claude Magnier

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 08:52
CPC Classifications
B; B82; B82Y; B82Y30/00; C; C01; C01G; C01G25/00; C01G25/02; C04; C04B; C04B35/00; C04B35/01; C04B35/48; C04B35/486; C01P; C01P2002/00; C01P2002/60; C01P2004/00; C01P2004/10; C01P2004/30; C01P2004/32; C01P2004/50; C01P2004/60; C01P2004/61; C01P2004/64; C01P2006/00; C01P2006/10

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 112 words
A process for preparing a fine powder of stabilized zirconia, comprising the steps of forming a suspension containing particles by mixing a zirconia hydrate sol having a pH of from about 0.5 to 5 and containing elementary acicular crystals of ZrO 2 having dimensions from about 10 to 500 Å, which crystals are agglomerated into submicron aggregates of ZrO 2 having dimensions from about 100 to 5,000 Å in diameter with a solution having a concentration of a stabilizing agent; drying said suspension to obtain a dried product; and calcining the dried product at a temperature of from about 700° C. to about 1,300° C. to obtain said powder of stabilized zirconia.
Claim 2
Dependent Claim 112 words
A process for preparing a fine powder of stabilized zirconia, comprising the steps of forming a suspension containing particles by mixing a zirconia hydrate sol having a pH of from about 0.5 to 5 and containing elementary acicular crystals of ZrO 2 having dimensions from about 10 to 500 Å, which crystals are agglomerated into submicron aggregates of ZrO 2 having dimensions from about 100 to 5,000 Å in diameter with a solution having a concentration of a stabilizing agent; drying said suspension to obtain a dried product; and calcining the dried product at a temperature of from about 700° C. to about 1,300° C. to obtain said powder of stabilized zirconia.
Claim 3
Dependent Claim 34 words
The process of claim 1, wherein the stabilizing agent is selected from the group consisting of yttrium, calcium, magnesium and cerium, and wherein the calcining is conducted for about 30 minutes to 24 hours.
Claim 4
Dependent Claim 32 words
The process of claim 1, wherein the concentration of the stabilizing agent is selected so that the stabilized zirconia powder will contain from about 0.001 to about 30 mole percent stabilizing agent.
Claim 5
Dependent Claim 11 words
The process of claim 3, wherein said stabilizng agent is yttrium.
Claim 6
Dependent Claim 27 words
The process of claim 2, wherein said concentration is selected so that said stabilized zirconia powder will contain from about 2 to 10 mole percent stabilizing agent.
Claim 7
Dependent Claim 11 words
The process of claim 5, wherein said stabilizing agent is yttrium.
Claim 8
Dependent Claim 34 words
The process of claim 2, wherein said stabilizing agent is yttrium and wherein the concentration of yttrium is selected so that the stabilized zirconia powder will contain from 2 to 3 mole percent yttrium.
Claim 9
Dependent Claim 115 words
The process of claim 7, wherein the drying step includes injecting the suspension containing particles into a gas reactor containing at least one gas given a helicoidal motion and flowing in a vortex well, and wherein said suspension is injected along a trajectory coincident with the axis of symmetry of the helicoidal trajectories of the gas to enable a complete transfer of the motion of said gas to the particles of the suspension, wherein the residence time in the reactor is less than about 1/10 second; wherein the input temperature of the gas is from about 400 to 900° C. and wherein the temperature of the dried product is from about 100° to 500° C.
Claim 10
Dependent Claim 115 words
The process of claim 1, wherein the drying step includes injecting the suspension containing particles into a gas reactor containing at least one gas given a helicoidal motion and flowing in a vortex well, and wherein said suspension is injected along a trajectory coincident with the axis of symmetry of the helicoidal trajectories of the gas to enable a complete transfer of the motion of said gas to the particles of the suspension, wherein the residence time in the reactor is less than about 1/10 second; wherein the input temperature of the gas is from about 400° to 900° C. and wherein the temperature of the dried product is from about 100° to 500° C.
Claim 11
Dependent Claim 19 words
The process of claim 1, wherein the duration of the calcination is from about 30 minutes to 24 hours.
Claim 12
Dependent Claim 35 words
The process of claim 1, wherein the calcination is carried out at a temperature from about 800° C. to 1,050° C. and the duration of the calcination is from about 30 minutes to 24 hours.
Claim 13
Dependent Claim 13 words
The process of claim 1 further comprising the step of milling the powder.
Claim 14
Dependent Claim 22 words
The process of claim 1, wherein said stabilizing agent remains in solution until the solvent therefor is removed in the drying step.

References Cited (Backward Citations)

US3645910A Cited
US3514252A Cited
US3957500A Cited
JPS57191234A Cited
JPS5879818A Cited
JPS58135131A Cited
JPS59213673A Cited
US4520114A Cited
JPS60127240A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1991-11-29 1992-05-30 1992-11-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1995-11-29 1996-05-30 1996-11-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1999-11-29 2000-05-30 2000-11-29 $7700.00 Window Closed / Lapsed

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