US4797139A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Boehmite produced by a seeded hydyothermal process and ceramic bodies produced therefrom
Assignee: Saint Gobain Abrasives Inc
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Filing: 1987-12-16
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Granted: 1989-01-10
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Expires: 2007-12-16
Abstract
Abstract Microcrystalline boehmite suitable for conversion to anhydrous alumina products is produced by hydrothermal treatment of precursor alumina raw material at controlled pH and in the presence of microcrystalline boehmite seed material. Reaction mix may include submicron seed material for seedling for later conversion of the microcrystalline boehmite to alpha alumina. Removal of metal cations by ion exchange is employed when high purity product is required. Other materials may be added to reaction mix. Production of alumina products, catalysts, and ceramic bodies is disclosed.
Inventors
- 👤 Ralph Bauer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 15:24
CPC Classifications
C; C01; C01F; C01F7/00; C01F7/02; B; B82; B82Y; B82Y30/00; B01; B01J; B01J21/00; B01J21/02; B01J21/04; B24; B24D; B24D3/00; B24D3/008; B24D3/02; B24D3/04; B24D3/14; C01F7/44; C01F7/447; C01F7/448; C04; C04B; C04B35/00; C04B35/01; C04B35/10; C04B35/111; C04B35/1115; C01P; C01P2004/00; C01P2004/60; C01P2004/64
Claims Analysis
Total Claims: 32
Claim 1
Independent Claim
92 words
A method of making a microcrystalline boehmite product comprising heating under autogenous pressure a boehmite alumina precursor in an aqueous medium having a pH selected from a value of 5 or less and 8 or higher and in the presence of boehmite seed particles finer than 0.02 microns, said seed particles being present in an amount greater than 7.5% by weight of the precursor alumina, calculated as Al 2 O 3 , said heating being carried out above 130° C. for a time sufficient to substantially convert said precursor to microcrystalline boehmite.
Claim 2
Independent Claim
92 words
A method of making a microcrystalline boehmite product comprising heating under autogenous pressure a boehmite alumina precursor in an aqueous medium having a pH selected from a value of 5 or less and 8 or higher and in the presence of boehmite seed particles finer than 0.02 microns, said seed particles being present in an amount greater than 7.5% by weight of the precursor alumina, calculated as Al 2 O 3 , said heating being carried out above 130° C. for a time sufficient to substantially convert said precursor to microcrystalline boehmite.
Claim 3
Dependent Claim
40 words
A method as in claim 1 in which said pH is 5 or less and at least 0.1% by weight of submicron alpha alumina seed is in said aqueous medium during the conversion of the boehmite precursor to microcrystalline boehmite.
Claim 4
Dependent Claim
41 words
A method as in claim 1 in which said pH is 5 or less and said boehmite seed particles are present in an amount of at least 15% by weight of the precursor alumina, calculated as Al 2 O 3 .
Claim 5
Dependent Claim
21 words
A method as in claim 1 further including the step of removing alkali and alkaline earth ions from the aqueous medium.
Claim 6
Dependent Claim
30 words
A method as in claim 2 further including the step of removing alkali and alkaline earth ions from the aqueous medium and firing the boehmite product, to produce abrasive grits.
Claim 7
Dependent Claim
27 words
A method as in claim 3 further including the steps of shaping the boehmite product, and firing the shaped product to produce an article of anhydrous alumina.
Claim 8
Dependent Claim
31 words
A method as in claim 3 in which said boehmite seed particles are finer than 100 Angstroms and further including the step of firing the boehmite product to produce gamma alumina.
Claim 9
Dependent Claim
16 words
A method as in claim 7 wherein said boehmite seed particles are finer than 50 Angstroms.
Claim 10
Dependent Claim
30 words
A method as in claim 2 further including the steps of adding a crystal growth inhibitor to said aqueous medium prior to the conversion of said precursor to microcrystalline boehmite.
Claim 11
Dependent Claim
19 words
A method as in claim 9 wherein said crystal growth inhibitor is magnesium oxide or a magnesium oxide precursor.
Claim 12
Dependent Claim
31 words
A method as in claim 2 further including the step of adding zirconia or zirconium oxide precursor to said aqueous medium prior to the conversion of said precursor to microcrystalline boehmite.
Claim 13
Dependent Claim
34 words
A method as in claim 1 further including the step of adding said boehmite seed particles to said aqueous medium after said medium has been heated to a temperature of at least 120° C.
Claim 14
Dependent Claim
36 words
A method as in claim 1 further including the step of providing in said aqueous medium submicron alpha alumina seed particles having a hydrated boehmite surface prior to the conversion of said precursor to microcrystalline boehmite.
Claim 15
Dependent Claim
28 words
The method of claim 4 wherein said step of removing alkali and alkaline earth ions includes the step of contacting said aqueous medium with an ion exchange medium.
Claim 16
Independent Claim
101 words
A method of producing alpha alumina bodies comprising the steps of: reacting hydrated alumina boehmite precursor in an autoclave in the presence of acidified water, boehmite seed material having a crystal size less than 0.02 microns, and submicron seed material of a type and in an amount effective to promote the formation of alpha alumina upon firing, while maintaining the temperature and pressure at conditions under which boehmite is a stable phase for a time sufficient to convert the major portion of said precursor to microcrystalline boehmite; firing said microcrystalline boehmite at temperatures sufficient to convert said boehmite to alpha alumina.
Claim 17
Independent Claim
101 words
A method of producing alpha alumina bodies comprising the steps of: reacting hydrated alumina boehmite precursor in an autoclave in the presence of acidified water, boehmite seed material having a crystal size less than 0.02 microns, and submicron seed material of a type and in an amount effective to promote the formation of alpha alumina upon firing, while maintaining the temperature and pressure at conditions under which boehmite is a stable phase for a time sufficient to convert the major portion of said precursor to microcrystalline boehmite; firing said microcrystalline boehmite at temperatures sufficient to convert said boehmite to alpha alumina.
Claim 18
Dependent Claim
17 words
The method of claim 15 further including the step of shaping said microcrystalline boehmite prior to firing.
Claim 19
Dependent Claim
33 words
The method of claim 15 wherein the step of firing said boehmite includes the step of drying and crushing said microcrystalline boehmite prior to firing at a temperature sufficient to form alpha alumina.
Claim 20
Dependent Claim
16 words
The method of claim 15 wherein said acidified water has a pH of 5 or less.
Claim 21
Dependent Claim
19 words
The method of claim 13 further including the step of removing alkali and alkaline earth ions prior to firing.
Claim 22
Independent Claim
87 words
The method of producing gamma alumina bodies comprising the steps of: reacting a hydrated alumina boehmite precursor in an autoclave in the presence of acidified water and boehmite seed material having a crystal size less than 0.02 microns while maintaining the temperature and pressure at conditions under which boehmite is a stable phase for a time sufficient to convert the major portion of said precursor to microcrystalline boehmite, firing said microcrystalline boehmite for a time and at a temperature effective to convert said boehmite to gamma alumina.
Claim 23
Independent Claim
87 words
The method of producing gamma alumina bodies comprising the steps of: reacting a hydrated alumina boehmite precursor in an autoclave in the presence of acidified water and boehmite seed material having a crystal size less than 0.02 microns while maintaining the temperature and pressure at conditions under which boehmite is a stable phase for a time sufficient to convert the major portion of said precursor to microcrystalline boehmite, firing said microcrystalline boehmite for a time and at a temperature effective to convert said boehmite to gamma alumina.
Claim 24
Dependent Claim
13 words
The method of claim 20 further including shaping said boehmite prior to firing.
Claim 25
Dependent Claim
19 words
The method of claim 20 further including the step of removing alkali and alkaline earth ions prior to firing.
Claim 26
Independent Claim
64 words
A method of producing microcrystalline boehmite comprising reacting in an autoclave a hydrated alumina boehmite precursor in the presence of water and boehmite seed material having a crystal size less than 0.02 microns, the temperature, pressure, and pH being maintained at conditions under which boehmite is a stable phase for a time sufficient to convert the major portion of said precursor to microcrystalline boehmite.
Claim 27
Independent Claim
64 words
A method of producing microcrystalline boehmite comprising reacting in an autoclave a hydrated alumina boehmite precursor in the presence of water and boehmite seed material having a crystal size less than 0.02 microns, the temperature, pressure, and pH being maintained at conditions under which boehmite is a stable phase for a time sufficient to convert the major portion of said precursor to microcrystalline boehmite.
Claim 28
Independent Claim
87 words
A method of producing high purity microcrystalline boehmite comprising the steps of (1) providing an aqueous medium containing an aluminum oxide precursor of boehmite and at least 5% by weight, based on alumina precursor solids calculated as trihydrate, of boehmite seed material having a particle size finer than 0.02 microns, (2) heating in an autoclave said medium under at least autogenous pressure to convert said precursor to boehmite, and (3) removing metal cations from said aqueous medium by contact of said medium with an ion exchange medium.
Claim 29
Independent Claim
87 words
A method of producing high purity microcrystalline boehmite comprising the steps of (1) providing an aqueous medium containing an aluminum oxide precursor of boehmite and at least 5% by weight, based on alumina precursor solids calculated as trihydrate, of boehmite seed material having a particle size finer than 0.02 microns, (2) heating in an autoclave said medium under at least autogenous pressure to convert said precursor to boehmite, and (3) removing metal cations from said aqueous medium by contact of said medium with an ion exchange medium.
Claim 30
Dependent Claim
48 words
A method as in claim 24 further including the step of adding submicron alpha alumina nucleation material in the amount of at least 0.1%, by weight of the total alumina calculated as Al 2 O 3 , to the medium before complete conversion of the precursor to boehmite.
Claim 31
Dependent Claim
31 words
A method as in claim 24 wherein said step of providing includes the step of adding said boehmite seed material after the aqueous medium has been heated to at least 120°.
Claim 32
Dependent Claim
42 words
A method of producing an aluminous article comprising firing a boehmite produced by the method of claim 25 in admixture with a material selected from the group consisting of oxides of magnesium, oxides of zirconia, ceramic or metal fibers, and mixtures thereof.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-01-10 | 1992-07-11 | 1993-01-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-01-10 | 1996-07-11 | 1997-01-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-01-10 | 2000-07-11 | 2001-01-10 | $7700.00 | Window Closed / Lapsed |