US4918035A
Expired / Lapsed
US
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Process for the preparation of complex perovskite type compounds
Assignee: Panasonic Holdings Corp
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Filing: 1989-06-30
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Granted: 1990-04-17
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Expires: 2009-06-30
Abstract
Abstract The present invention provides a process for producing powder of complex perovskite type compounds by using metal alkoxides. In the prior art, methods were known for synthesizing crystalline powder of simple perovskite type compounds such as BaTiO3. According to the conventional methods, however, when synthesizing a complex perovskite type compound having two atoms of different valences at the B site of perovskite structure by hydrolyzing metal alkoxides, there could be obtained only amorphous powder, and for crystallizing it, heating to a temperature of around 600 DEG to 800 DEG C. was necessary. According to the process of this invention, it is possible to synthesize the crystalline complex perovskite type compounds at a low temperature of around 100 DEG C., which is 500 DEG to 700 DEG C. lower than the temperature required in the conventional methods, by adjusting the amount of water added according to the type of the solvent used and controlling the reaction temperature at a specified level or higher.
Inventors
- 👤 Osamu Inoue
- 👤 Syunichiro Kawashima
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 20:55
CPC Classifications
C; C01; C01B; C01B13/00; C01B13/14; C01B13/32; B; B82; B82Y; B82Y30/00; C01F; C01F11/00; C01G; C01G33/00; C01G33/006; C01G35/00; C01G35/006; C01G9/00; C01G9/006; C04; C04B; C04B35/00; C04B35/01; C04B35/495; C04B35/622; C04B35/626; C04B35/62605; C04B35/62625; C04B35/6264; C04B35/62645; C04B35/62655; C01P; C01P2002/00; C01P2002/02; C01P2002/30; C01P2002/34; C01P2002/50; C01P2002/52; C01P2002/54; C01P2004/00; C01P2004/60; C01P2004/64; C01P2006/00; C01P2006/12; C04B2235/00; C04B2235/02; C04B2235/30; C04B2235/32; C04B2235/3205; C04B2235/3206; C04B2235/3213; C04B2235/3215; C04B2235/3231; C04B2235/3251; C04B2235/3284; C04B2235/44; C04B2235/441; C04B2235/70; C04B2235/74; C04B2235/76; C04B2235/768
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
214 words
A process for preparing a crystalline complex perovskite type compound, represented by the chemical formula A(B 1/3 C 2/3 )O 3 , wherein A is a metal selected from the group consisting of Ba and Sr; B is a metal selected from the group consisting of Zn and Mg; and C is a metal selected from the group consisting of Nb and Ta; respectively, which comprises weighing out three types of metal alkoxides represented by the formulae A(OR 1 ) 2 , B(OR 2 ) 2 and C(OR 3 ) 5 , wherein R 1 ,, R 2 and R 3 are each an alkyl group, so that their amounts will be a moles, b moles and c moles, respectively, mixing them with an organic solvent containing z% by volume of a non-polar organic solvent and (100-z)% by volume of a polar solvent, wherein 0<z<100, adding thereto water or a mixed solution of water and an organic solvent so that the amount of water will become (8-0.065z)×(2a+2b+5c) moles or greater to hydrolyze the metal alkoxides, heating the hydrolyzate in the presence of the water/organic solvent at a temperature of 85° C. or higher, at least in the course of or after the hydrolysis reaction, and then removing the solvent to obtain the crystalline compound.
Claim 2
Dependent Claim
214 words
A process for preparing a crystalline complex perovskite type compound, represented by the chemical formula A(B 1/3 C 2/3 )O 3 , wherein A is a metal selected from the group consisting of Ba and Sr; B is a metal selected from the group consisting of Zn and Mg; and C is a metal selected from the group consisting of Nb and Ta; respectively, which comprises weighing out three types of metal alkoxides represented by the formulae A(OR 1 ) 2 , B(OR 2 ) 2 and C(OR 3 ) 5 , wherein R 1 ,, R 2 and R 3 are each an alkyl group, so that their amounts will be a moles, b moles and c moles, respectively, mixing them with an organic solvent containing z% by volume of a non-polar organic solvent and (100-z)% by volume of a polar solvent, wherein 0<z<100, adding thereto water or a mixed solution of water and an organic solvent so that the amount of water will become (8-0.065z)×(2a+2b+5c) moles or greater to hydrolyze the metal alkoxides, heating the hydrolyzate in the presence of the water/organic solvent at a temperature of 85° C. or higher, at least in the course of or after the hydrolysis reaction, and then removing the solvent to obtain the crystalline compound.
Claim 3
Dependent Claim
30 words
The process according to claim 1, where the non-polar organic solvents used is selected from the group consisting of benzene, toluene, xylene, cumene, e thylbenzene, hexane, pentanol, hexanol and heptanol.
Claim 4
Dependent Claim
24 words
The process according to claim 1, wherein the polar organic solvent used is selected from the group consisting of methanol, ethanol, propanol and butanol.
Claim 5
Dependent Claim
45 words
The process according to claim 1, wherein the polar and non-polar organic solvents used are those having boiling points below 85° C., and the heating after addition of water is carried out at the boiling point or below of said organic solvents under 1 atmosphere.
Claim 6
Dependent Claim
51 words
The process according to claim 1, wherein the polar and non-polar organic solvents used are those having boiling points below 85° C. and the heating after addition of water is carried out under a pressure of 1 atm. or higher to make the temperature of the system 85° C. or higher.
Claim 7
Dependent Claim
25 words
The process according to claim 1, wherein when water is added, the water added is diluted 1 time or more with a polar organic solvent.
Claim 8
Dependent Claim
28 words
The process according to claim 1, wherein the course of heating before and after addition of water, evaporation of the solvent is prevented by using a reflux condenser.
Claim 9
Dependent Claim
18 words
The process according to claim 1, wherein the removing of the solvent is accomplished by filtration or centrifuging.
Claim 10
Dependent Claim
25 words
The process according to claim 1, wherein the heating at the time of reaction is effected by a water bath, oil bath or electric heater.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1993-04-16 | 1993-10-16 | 1994-04-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-04-16 | 1997-10-16 | 1998-04-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-04-16 | 2001-10-16 | 2002-04-17 | $7700.00 | Window Closed / Lapsed |