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US4514346A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of making thermal-shock resistant molded articles on the basis of silicon carbide

Assignee: CRANE TECHNOLOGIES GROUP Inc
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Filing: 1982-09-16
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Granted: 1985-04-30
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Expires: 2002-09-16
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Abstract

Abstract Refractory parts or articles, even of very large dimensions, are made with starting material of carbon particles mixed with silicon particles in a predetermined ratio which is suspended in a solution of a binder, after which the suspension is squirted into a precipitating liquid to coat the particles with the binder, the solids then being separated and dried, molded under slight pressure, and coked (at 800°-1,000° C.), and then rapidly raised in temperature (to 1,400°-1,600° C.) for formation of silicon carbide throughout the article. It is useful to add powdered silicon carbide and mix it in before the coking step and, also, to hold the heated body at a temperature somewhat below 1,400° C. long enough to remove temperature gradients within it, followed by rapid heating up to a carbide-forming temperature. The porous bodies thus formed can be heated to reduce porosity after the coking step by impregnation with a suspension of silicon powder in a resin, after which the body is again coked, or impregnation may be carried out on the completely fired body, with a liquid resin or a molten metal, after evacuation of the porous body and the application of pressure to the impregnating fluid.

Inventors

  • 👤 Hartmut Luhleich
  • 👤 Francisco J. Dias

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 15:56
CPC Classifications
C; C04; C04B; C04B35/00; C04B35/515; C04B35/56; C04B35/565; C04B35/573

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 236 words
A process for the production of homogeneous and uniformly and throughgoingly porous molded articles or parts, utilizing carbonaceous particles selected from the group consisting of ground coke, natural graphite, electrographite, charcoal, and carbon black, as a starting material in the form of powder or granules, and including the steps of coating particles of said powder or granular material wih an organic binder, molding a mass of the coated particle to form a "green" molded body, and coking said body up to a maximal temperature in the range from 800° to 1,000° C., said process comprising the improvement which consists in that: the powdery or granular starting material is a mixture consisting essentially of particles of silicon and said carbonaceous particles in a predetermined mixture proportion and containing substantially no silicon carbide particles; the coating of the particles with a binder is performed the binder is precipitated by introducing the suspension into a liquid serving to precipitate the binder on the particles as an even coating; after the coking step, the molded body is heated up, to convert silicon and carbon into silicon carbide, to a temperature in the range from 1,400° C. to 1,600° C., in an inert gas atmosphere at a pressure not less than about 1 bar, said heating up, at least in the temperature range around and above 1,400° C., being at a rapid rate, in order to mitigate the evaporation of silicon.
Claim 2
Dependent Claim 236 words
A process for the production of homogeneous and uniformly and throughgoingly porous molded articles or parts, utilizing carbonaceous particles selected from the group consisting of ground coke, natural graphite, electrographite, charcoal, and carbon black, as a starting material in the form of powder or granules, and including the steps of coating particles of said powder or granular material wih an organic binder, molding a mass of the coated particle to form a "green" molded body, and coking said body up to a maximal temperature in the range from 800° to 1,000° C., said process comprising the improvement which consists in that: the powdery or granular starting material is a mixture consisting essentially of particles of silicon and said carbonaceous particles in a predetermined mixture proportion and containing substantially no silicon carbide particles; the coating of the particles with a binder is performed the binder is precipitated by introducing the suspension into a liquid serving to precipitate the binder on the particles as an even coating; after the coking step, the molded body is heated up, to convert silicon and carbon into silicon carbide, to a temperature in the range from 1,400° C. to 1,600° C., in an inert gas atmosphere at a pressure not less than about 1 bar, said heating up, at least in the temperature range around and above 1,400° C., being at a rapid rate, in order to mitigate the evaporation of silicon.
Claim 3
Dependent Claim 35 words
A process as defined in claim 1, wherein the proportional content by weight of binder in the coated particle mixture with reference to the weight of the coated particle mixture is between 20% and 35%.
Claim 4
Dependent Claim 21 words
A process as defined in claim 1, wherein the step of molding said mass of coated particles is performed by extrusion.
Claim 5
Dependent Claim 28 words
A process as defined in claim 1, wherein the step of molding said mass of molded particles is performed by die-pressing under not more than a slight pressure.
Claim 6
Dependent Claim 107 words
A process as defined in claim 1, wherein said coking step is carried out in a protective gas atmosphere and wherein the following heating-up step is carried out by first heating up said molded body to a temperature in the range between 1,350° C. and 1,400° C., then maintaining it at a temperature in said last-mentioned range long enough practically to prevent a temperature gradient from remaining within said body and then heating up said body with great rapidity to a temperature in the range between 1,500° and 1,600° C., and after the conversion of silicon and carbon in said body into silicon carbide, cooling said body.
Claim 7
Dependent Claim 45 words
A process as defined in claim 1, wherein the process is carried out by producing a plurality of molded parts which are fastened together during the process to form an article of complicated shape, this fastening together being done at least before the conversion step.
Claim 8
Dependent Claim 21 words
A process as defined in claim 1, wherein after the cooling step the molded body is machined to obtain final dimensions.
Claim 9
Dependent Claim 271 words
A process for the production of molded articles or parts, utilizing carbonaceous particles selected from the group consisting of ground coke, natural graphite, electro-graphite, charcoal, and carbon black, as a starting material, in the form of powders or granules and including the steps of coating particles of said powder or granular material with an organic binder, molding a mass of the coated particles to form a "green" molded body, and coking said body up to a maximal temperature in the range from 800° C. to 1,000° C., said process comprising the improvement which consists in that: the powdery or granular starting material is a mixture consisting essentially of particles of silicon and said carbonaceous particles in a predetermined mixture proportion the coating of the particles with a binder is performed by suspending the particles in a binder solution from which the binder is precipitated by introducing the suspension into a liquid serving to precipitate the binder on the particles as an even coating; after the first coking step, said molded body, in order to reduce the porosity thereof, is soaked or impregnated with a suspension of silicon powder in synthethic resin and then subjected to a further coking step; after said further coking step, the molded body is heated up, to convert silicon and carbon into silicon carbide, to a temperature in the range from 1,400° C. to 1,600° C., in an inert gas atmosphere at a pressure not less than about 1 bar, said heating up, at least in the temperature range around and above 1,400° C., being at a rapid rate in order to mitigate the evaporation of silicon.
Claim 10
Dependent Claim 271 words
A process for the production of molded articles or parts, utilizing carbonaceous particles selected from the group consisting of ground coke, natural graphite, electro-graphite, charcoal, and carbon black, as a starting material, in the form of powders or granules and including the steps of coating particles of said powder or granular material with an organic binder, molding a mass of the coated particles to form a "green" molded body, and coking said body up to a maximal temperature in the range from 800° C. to 1,000° C., said process comprising the improvement which consists in that: the powdery or granular starting material is a mixture consisting essentially of particles of silicon and said carbonaceous particles in a predetermined mixture proportion the coating of the particles with a binder is performed by suspending the particles in a binder solution from which the binder is precipitated by introducing the suspension into a liquid serving to precipitate the binder on the particles as an even coating; after the first coking step, said molded body, in order to reduce the porosity thereof, is soaked or impregnated with a suspension of silicon powder in synthethic resin and then subjected to a further coking step; after said further coking step, the molded body is heated up, to convert silicon and carbon into silicon carbide, to a temperature in the range from 1,400° C. to 1,600° C., in an inert gas atmosphere at a pressure not less than about 1 bar, said heating up, at least in the temperature range around and above 1,400° C., being at a rapid rate in order to mitigate the evaporation of silicon.
Claim 11
Dependent Claim 306 words
A process for the production of molded articles or parts, utilizing carbonaceous particles selected from the group consisting of ground coke, natural graphite, electro-graphite, charcoal, carbon black and other carbonized organic material, as a starting material in the form of powders or granules, and including the steps of coating particles of said powder or granular material with an organic binder, molding a mass of the coated particles to form a "green" molded body, and coking said body up to a maximal temperature in the range from 800° C. to 1,000° C., said process comprising the improvement which consists in that: the powdery or granular starting material is a mixture consisting essentially of particles of silicon and said carbonaceous particles in a predetermined mixture proportion; the coating of the particles with the binder is performed by suspending the particles in a binder solution from which the binder is precipitated by introducing the suspension into a liquid serving to precipitate the binder on the particles as an even coating; after the coking step, the molded body is heated up, to convert silicon and carbon into silicon carbide, to a temperature in the range from 1,400° C. to 1,600° C., in an inert gas atmosphere at a pressure not less than about 1 bar, said heating-up, at least in the temperature range around and above 1,400° C., being at a rapid rate in order to mitigate the evaporation of silicon, and after the conversion of silicon and carbon into silicon carbide as aforesaid, said molded body is soaked in or impregnated with molten metal while contained in a pressure vessel, the interior of which is evacuated when or soon after said body is first placed therein, and not in contact with said molten metal, said molten metal has a pressure applied to it which does not exceed 50 bars.
Claim 12
Dependent Claim 306 words
A process for the production of molded articles or parts, utilizing carbonaceous particles selected from the group consisting of ground coke, natural graphite, electro-graphite, charcoal, carbon black and other carbonized organic material, as a starting material in the form of powders or granules, and including the steps of coating particles of said powder or granular material with an organic binder, molding a mass of the coated particles to form a "green" molded body, and coking said body up to a maximal temperature in the range from 800° C. to 1,000° C., said process comprising the improvement which consists in that: the powdery or granular starting material is a mixture consisting essentially of particles of silicon and said carbonaceous particles in a predetermined mixture proportion; the coating of the particles with the binder is performed by suspending the particles in a binder solution from which the binder is precipitated by introducing the suspension into a liquid serving to precipitate the binder on the particles as an even coating; after the coking step, the molded body is heated up, to convert silicon and carbon into silicon carbide, to a temperature in the range from 1,400° C. to 1,600° C., in an inert gas atmosphere at a pressure not less than about 1 bar, said heating-up, at least in the temperature range around and above 1,400° C., being at a rapid rate in order to mitigate the evaporation of silicon, and after the conversion of silicon and carbon into silicon carbide as aforesaid, said molded body is soaked in or impregnated with molten metal while contained in a pressure vessel, the interior of which is evacuated when or soon after said body is first placed therein, and not in contact with said molten metal, said molten metal has a pressure applied to it which does not exceed 50 bars.
Claim 13
Dependent Claim 307 words
A process for the production of molded articles or parts, utilizing carbonaceous particles selected from the group consisting of ground coke, natural graphite, electro-graphite, charcoal, carbon black and other carbonized organic material, as a starting material in the form of powders or granules, and including the steps of coating particles of said powder or granular material with an organic binder, molding a mass of the coated particles to form a "green" molded body, and coking said body up to a maximal temperature in the range from 800° C. to 1,000° C., said process comprising the improvement which consists in that: the powdery or granular starting material is of a mixture consisting essentially of particles of silicon and said carbonaceous particles in a predetermined mixture porportion; the coating of the particles with the binder is performed by suspending the particles in a binder solution from which the binder is precipitated by introducing the suspension into a liquid serving to precipitate the binder on the particles as an even coating; after the coking step, the molded body is heated up, to convert silicon and carbon into silicon carbide, to a temperature in the range from 1,400° C. to 1,600° C., in an inert gas atmosphere at a pressure not less than about 1 bar, said heating-up, at least in the temperature range around and above 1,400° C., being at a rapid rate in order to mitigate the evaporation of silicon, and after the conversion of silicon and carbon into silicon carbide as aforesaid, said molded body is soaked in or impregnated with synthetic resin while contained in a pressure vessel, the interior of which is evacuated when or soon after said body is first placed therein, and not in contact with said synthetic resin, said synthetic resin has a pressure applied to it which does not exceed 50 bars.
Claim 14
Dependent Claim 307 words
A process for the production of molded articles or parts, utilizing carbonaceous particles selected from the group consisting of ground coke, natural graphite, electro-graphite, charcoal, carbon black and other carbonized organic material, as a starting material in the form of powders or granules, and including the steps of coating particles of said powder or granular material with an organic binder, molding a mass of the coated particles to form a "green" molded body, and coking said body up to a maximal temperature in the range from 800° C. to 1,000° C., said process comprising the improvement which consists in that: the powdery or granular starting material is of a mixture consisting essentially of particles of silicon and said carbonaceous particles in a predetermined mixture porportion; the coating of the particles with the binder is performed by suspending the particles in a binder solution from which the binder is precipitated by introducing the suspension into a liquid serving to precipitate the binder on the particles as an even coating; after the coking step, the molded body is heated up, to convert silicon and carbon into silicon carbide, to a temperature in the range from 1,400° C. to 1,600° C., in an inert gas atmosphere at a pressure not less than about 1 bar, said heating-up, at least in the temperature range around and above 1,400° C., being at a rapid rate in order to mitigate the evaporation of silicon, and after the conversion of silicon and carbon into silicon carbide as aforesaid, said molded body is soaked in or impregnated with synthetic resin while contained in a pressure vessel, the interior of which is evacuated when or soon after said body is first placed therein, and not in contact with said synthetic resin, said synthetic resin has a pressure applied to it which does not exceed 50 bars.
Claim 15
Dependent Claim 238 words
A process for the production of homogeneous and uniformly and throughgoingly porous molded articles or parts, utilizing carbonaceous particles selected from the group consisting of ground coke, natural graphite, electrographite, charcoal, and carbon black material, as a starting material in the form of powder or granules, and including the steps of coating said particles with an organic binder, molding a mass of the coated particles to form a "green" molded body, and coking said body up to a maximal temperature in the range from 800° to 1000° C., said process comprising the improvement which consists in that: the powdery or granular starting material is a mixture consisting of particles of silicon, said carbonaceous particles, and particles of silicon carbide, in a predetermined mixture proportion; the coating of the particles with a binder is performed by suspending the particles in a binder solution from which the binder is precipitated by introducing the suspension into a liquid serving to precipitate the binder on the particles as an even coating; after the coking step, the molded body is heated up, to convert silicon and carbon into silicon carbide, to a temperature in the range from 1,400° C. to 1,600° C., in an inert gas atmosphere at a pressure not less than about 1 bar, said heating up, at least in the temperature range around and above 1,400° C., being at a rapid rate, in order to mitigate the evaporation of silicon.
Claim 16
Dependent Claim 238 words
A process for the production of homogeneous and uniformly and throughgoingly porous molded articles or parts, utilizing carbonaceous particles selected from the group consisting of ground coke, natural graphite, electrographite, charcoal, and carbon black material, as a starting material in the form of powder or granules, and including the steps of coating said particles with an organic binder, molding a mass of the coated particles to form a "green" molded body, and coking said body up to a maximal temperature in the range from 800° to 1000° C., said process comprising the improvement which consists in that: the powdery or granular starting material is a mixture consisting of particles of silicon, said carbonaceous particles, and particles of silicon carbide, in a predetermined mixture proportion; the coating of the particles with a binder is performed by suspending the particles in a binder solution from which the binder is precipitated by introducing the suspension into a liquid serving to precipitate the binder on the particles as an even coating; after the coking step, the molded body is heated up, to convert silicon and carbon into silicon carbide, to a temperature in the range from 1,400° C. to 1,600° C., in an inert gas atmosphere at a pressure not less than about 1 bar, said heating up, at least in the temperature range around and above 1,400° C., being at a rapid rate, in order to mitigate the evaporation of silicon.

References Cited (Backward Citations)

US3947550A Cited
US3966855A Cited
US3998646A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-04-29 1988-10-29 1989-04-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-04-29 1992-10-29 1993-04-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-04-29 1996-10-29 1997-04-30 $7700.00 Window Closed / Lapsed

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