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US4564496A
Expired / Lapsed
US
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Method of making porous silicon carbide bodies
Assignee: Forschungszentrum Jülich
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Filing: 1985-06-10
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Granted: 1986-01-14
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Expires: 2005-06-10
Abstract
Abstract Porous silicon carbide bodies are obtained by starting with a powder of particle size falling within a single sieve mesh range fraction and consisting either entirely of carbon particles or a mixture of carbon and silicon carbide particles of the same mesh fraction is mixed or coated with 15 to 30% by weight of a binder, moulded to shape, warmed in the temperature range from 40° to 200° C. to vaporize volatile material and then coked at a temperature rising to 850° C. Then it is siliconized by raising the temperature to the range from 1650° to 1950° C. with gaseous silicon or impregnated with silicon by dipping the body into a silicon melt and convert it to carbide, with the excess silicon thereafter being removed by vaporizing out or by boiling in lye. Sieve mesh fractions in the region of a few hundred μm are preferred, and the density of the porous body after pressing but before siliconizing should lie in the neighborhood of 0.6 to 0.7 g/cm 3 .
Inventors
- 👤 Ashok K. Gupta
- 👤 Erno Gyarmati
- 👤 Hermann Kreutz
- 👤 Rudolf Munzer
- 👤 Aristides Naoumidis
- 👤 Hubertus Nickel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 23:26
CPC Classifications
C; C04; C04B; C04B41/00; C04B41/009; C04B35/00; C04B35/515; C04B35/56; C04B35/565; C04B35/573; C04B38/00; C04B41/45; C04B41/50; C04B41/5053; C04B41/5057; C04B41/5059
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
154 words
Method of producing porous silicon carbide bodies comprising the steps of: preparing a carbon precursor body having a density between 0.5 and 0.9 g/cm 3 by the substeps of: mixing a cokable organic binder with a carbon powder of a minimum grain size not less than 50 μm and having a degree of uniformity of grain size such that the maximum grain size is not more than twice the minimum grain size, said binder providing between 15 and 30% by weight of the mixture; pressing said mixture to form a precursor body; heating said precursor body to drive off volatile components at a temperature between 40° and 200° C.; and further heating said precursor body up to 850° C. and thereby coking said binder; and heating said precursor body in contact with gaseous silicon at a temperature between 1650° and 1950° C. to convert the material of said body substantially to porous silicon carbide.
Claim 2
Dependent Claim
154 words
Method of producing porous silicon carbide bodies comprising the steps of: preparing a carbon precursor body having a density between 0.5 and 0.9 g/cm 3 by the substeps of: mixing a cokable organic binder with a carbon powder of a minimum grain size not less than 50 μm and having a degree of uniformity of grain size such that the maximum grain size is not more than twice the minimum grain size, said binder providing between 15 and 30% by weight of the mixture; pressing said mixture to form a precursor body; heating said precursor body to drive off volatile components at a temperature between 40° and 200° C.; and further heating said precursor body up to 850° C. and thereby coking said binder; and heating said precursor body in contact with gaseous silicon at a temperature between 1650° and 1950° C. to convert the material of said body substantially to porous silicon carbide.
Claim 3
Dependent Claim
27 words
Method as defined in claim 1, in which the density of said carbon body after coking is in the range from 0.6 to 0.7 g/cm 3 .
Claim 4
Dependent Claim
21 words
Method as defined in claim 1, in which said binder content of said powder material mixture is approximately 20% by weight.
Claim 5
Dependent Claim
165 words
Method of producing porous silicon carbide bodies comprising the steps of: preparing a carbon precursor body having a density between 0.5 and 0.9 g/cm 3 by the substeps of mixing a cokable organic binder with a carbon powder consisting essentially of carbon and of a minimum grain size not less than 50 μm and having a degree of uniformity of grain size such that the maximum grain size is not more than twice the minimum grain size, said binder providing between 15 and 30% by weight of the mixtures; pressing said mixture to form a precursor body; heating said precursor body to drive off volatile components at a temperature between 40° and 200° C., and further heating said precursor body up to 850° C. and thereby coking said binder; thereafter dipping said carbon body in a silicon melt and thereby impregnating it with silicon and converting the carbon in said body substantially into silicon carbide, and removing the remainder of uncombined silicon from said body.
Claim 6
Dependent Claim
165 words
Method of producing porous silicon carbide bodies comprising the steps of: preparing a carbon precursor body having a density between 0.5 and 0.9 g/cm 3 by the substeps of mixing a cokable organic binder with a carbon powder consisting essentially of carbon and of a minimum grain size not less than 50 μm and having a degree of uniformity of grain size such that the maximum grain size is not more than twice the minimum grain size, said binder providing between 15 and 30% by weight of the mixtures; pressing said mixture to form a precursor body; heating said precursor body to drive off volatile components at a temperature between 40° and 200° C., and further heating said precursor body up to 850° C. and thereby coking said binder; thereafter dipping said carbon body in a silicon melt and thereby impregnating it with silicon and converting the carbon in said body substantially into silicon carbide, and removing the remainder of uncombined silicon from said body.
Claim 7
Dependent Claim
24 words
Method as defined in claim 4, in which the step of removing the remaining uncombined silicon is performed by vaporizing the uncombined silicon remainder.
Claim 8
Dependent Claim
22 words
Method as defined in claim 4, in which the step of removing the uncombined silicon remainder is performed by boiling in lye.
Claim 9
Dependent Claim
44 words
Method as defined in claim 4, 5, or 6, in which said carbon powder is a powder selected from the group consisting of electrographite powder, petroleum coke powder, charcoal powder from wood or vegetable matter and mixtures of two or more of the foregoing.
Claim 10
Dependent Claim
28 words
Method as defined in claim 7, in which said powder is of a particle size of which the upper particle size limit is not greater than 1000 μm.
Claim 11
Dependent Claim
27 words
Method as defined in claim 8, in which the grains of said powder are of sizes not less than 105 μm and not more than 150 μm.
Claim 12
Dependent Claim
27 words
Method as defined in claim 8, in which the grains of said powder of sizes is not less than 600 μm and not more than 1000 μm.
Claim 13
Dependent Claim
175 words
Method of producing porous silicon carbide bodies comprising the steps of: preparing a carbon-containing precursor body having a density of approximately 1.5 g/cm 3 by the substeps of mixing a cokable organic binder with a powder consisting of not more than 70% by weight of silicon carbide powder and the remainder of carbon powder, said powder having a minimum grain size not less than 50 μm and having a degree of uniformity of grain size such that the maximum grain size is not more than twice the minimum grain size, said binder providing between 15 and 30% by weight of the mixture; pressing said mixture to form a precursor body; heating said precursor body to drive off volatile components at a temperature between 40° and 200° C.; and further heating said precursor body up to 850° C. and thereby coking said binder; and thereafter heating the precursor body so prepared in contact with gaseous silicon at a temperature between 1650° and 1950° C. to convert the material of said body substantially to porous silicon carbide.
Claim 14
Dependent Claim
175 words
Method of producing porous silicon carbide bodies comprising the steps of: preparing a carbon-containing precursor body having a density of approximately 1.5 g/cm 3 by the substeps of mixing a cokable organic binder with a powder consisting of not more than 70% by weight of silicon carbide powder and the remainder of carbon powder, said powder having a minimum grain size not less than 50 μm and having a degree of uniformity of grain size such that the maximum grain size is not more than twice the minimum grain size, said binder providing between 15 and 30% by weight of the mixture; pressing said mixture to form a precursor body; heating said precursor body to drive off volatile components at a temperature between 40° and 200° C.; and further heating said precursor body up to 850° C. and thereby coking said binder; and thereafter heating the precursor body so prepared in contact with gaseous silicon at a temperature between 1650° and 1950° C. to convert the material of said body substantially to porous silicon carbide.
Claim 15
Dependent Claim
180 words
Method of producing porous silicon carbide bodies comprising the steps of: preparing a carbon-containing precursor body having a density of approximately 1.5 g/cm 3 by the substeps of mixing a cokable organic binder with a powder consisting of not more than 70% by weight of silicon carbide powder and the remainder of carbon powder, said powder having a minimum grain size not less than 50 μm and having a degree of uniformity of grain size such that the maximum grain size is not more than twice the minimum grain size, said binder providing between 15 and 30% by weight of the mixture; pressing said mixture to form a precursor body; heating said precursor body to drive off volatile components at a temperature between 40° and 200° C.; and further heating said precursor body up to 850° C. and thereby coking said binder; and thereafter dipping the body so prepared in a silicon melt and thereby impregnating it with silicon and converting the carbon in said body substantially into silicon carbide, and removing the remainder of uncombined silicon from said body.
Claim 16
Dependent Claim
180 words
Method of producing porous silicon carbide bodies comprising the steps of: preparing a carbon-containing precursor body having a density of approximately 1.5 g/cm 3 by the substeps of mixing a cokable organic binder with a powder consisting of not more than 70% by weight of silicon carbide powder and the remainder of carbon powder, said powder having a minimum grain size not less than 50 μm and having a degree of uniformity of grain size such that the maximum grain size is not more than twice the minimum grain size, said binder providing between 15 and 30% by weight of the mixture; pressing said mixture to form a precursor body; heating said precursor body to drive off volatile components at a temperature between 40° and 200° C.; and further heating said precursor body up to 850° C. and thereby coking said binder; and thereafter dipping the body so prepared in a silicon melt and thereby impregnating it with silicon and converting the carbon in said body substantially into silicon carbide, and removing the remainder of uncombined silicon from said body.
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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) | 1989-01-13 | 1989-07-15 | 1990-01-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-01-13 | 1993-07-15 | 1994-01-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-01-13 | 1997-07-15 | 1998-01-14 | $7700.00 | Window Closed / Lapsed |