Claims
- 1. A process for producing an oxidation resistant black glass having the formula siCxOy where x is greater than zero and up to about 2.0 and y is greater than zero and up to about 2.2 wherein a black glass polymer precursor is pyrolyzed by heating in the presence of oxygen at a rate exceeding 5.degree. C./min to a maximum temperature in the range of 800.degree. C. to 1400.degree. C. and wherein the black glass recursor is the pyrolyzed reaction product of a cyclosiloxane monomer having the formula ##STR3## where n is an integer from 3 to 30, R is hydrogen, and R' is an alkene of from 2 to 20 carbon atoms in which one vinyl carbon atom is directly bonded to silicon or (2) two or more different cyclosiloxane monomers having the formula of (1) where for at least one monomer R is hydrogen and R' is an alkyl group having from 1 to 20 carbon atoms and for the other monomers R is an alkene from 2 to 20 carbon atoms in which one vinyl carbon is directly bonded to silicon and R' is an allkyl group of from 1 to 20 carbon atoms, or (3) cyclosiloxane monomers having the formula of (1) where R and R' are independently selected from hydrogen, an alkene of from 2 to about 20 carbon atoms in which one vinyl carbon atom is directly bonded to silicon, or an alkyl group of from 1 to about 20 carbon atoms and at least some of said monomers contain each of said hydrogen, alkene, and alkyl moieties, said reaction taking place in the presence of an effective amount of hydrosilylation catalyst.
- 2. The process of claim 1 wherein said black glass precursor is heated in the presence of air.
- 3. The process of claim 1 wherein the heating rate is 50.degree. C./min to 1000.degree. C./min.
- 4. The process of claim 3 wherein the heating rate is greater than 100.degree. C./min.
- 5. The process of claim 1 wherein the heating is carried out by direct application of hot combustion gases.
- 6. The process of claim 1 wherein the heating is carried out by radiant energy.
- 7. The process of claim 1 wherein the carbon content is controlled by adjusting the heating rate.
- 8. The process of claim 1 wherein the carbon content is controlled by adjusting access of oxygen to said polymer precursor during pyrolysis.
- 9. The process of claim 1 wherein the carbon content is controlled by adjusting the rate of gas flowing over said black glass precursor.
- 10. The process of claim 1 wherein the heating is carried out by a method selected from the group consisting of laser heating, RF induction heating, plasma heating, liquid and fluidized bed immersion, microwave heating, convective gas heating, and direct resistance heating.
- 11. An oxidation resistant black glass produced by pyrolysis of a black glass polymer precursor in the presence of oxygen by heating at a rate exceeding 5.degree. C./min to a maximum temperature in the range of 800.degree. C. to 1400.degree. C., said black glass containing an increased carbon content relative to a black glass pyrolyzed at a heating rate below 5.degree. C./min and wherein the black glass precursor is the reaction product of a cyclosiloxane monomer having the formula ##STR4## where n is an integer from 3 to 30, R is hydrogen, and R' is an alkene o from 2 to 20 carbon atoms in which one vinyl carbon atom is directly bonded to silicon or (2) two or more different cyclosiloxane monomers having the formula of (1) where for at least one monomer R is hydrogen and R' is an alkyl group having from 1 to 20 carbon atoms and for the other monomers R is an alkene from 2 to 20 carbon atoms in which one vinyl carbon is directly bonded to silicon and R' is an alkyl group of from 1 to 20 carbon atoms, or (3) cyclosiloxane monomers having the formula of (1) where R and R' are independently selected from hydrogen, an alkene of from 2 to about 20 carbon atoms in which one vinyl carbon atom is directly bonded to silicon, or an alkyl group of from 1 to about 20 carbon atoms and at least some of said monomers contain each of said hydrogen, alkene, and alkyl moieties, said reaction taking place in the presence of an effective amount of hydrosilylation catalyst.
- 12. The black glass of claim 11 wherein said black glass precursor is heated in the presence of air.
- 13. The black glass of claim 11 wherein the heating rate is 50.degree. C./min to 1000.degree. C./min.
- 14. The black glass of claim 13 wherein the heating rate is greater than 100.degree. C./min.
- 15. The black glass of claim 11 wherein the carbon content is further controlled by adjusting access of oxygen to said polymer precursor during pyrolysis.
- 16. The black glass of claim 11 wherein the carbon content is further controlled by adjusting the rate of gas flowing over said black glass precursor.
- 17. The black glass of claim 11 wherein the heating is carried out by a method selected from the group consisting of laser heating, RF induction heating, plasma heating, liquid and fluidized bed immersion, microwave heating, convective gas heating, and direct resistance heating.
Parent Case Info
This application is a continuation of U.S. application Ser. No. 07/684,425 filed Apr. 12, 1991 now abandoned.
US Referenced Citations (6)
Foreign Referenced Citations (3)
Number |
Date |
Country |
9010596 |
Oct 1990 |
EPX |
9012835 |
Nov 1990 |
EPX |
2647777 |
Dec 1990 |
FRX |
Non-Patent Literature Citations (1)
Entry |
Ceramic Engineering and Science Proceedings, vol. 12, No. 7/8, Aug., 1991 F. I. Hurwitz et al. "Polymeric Routes to Silicon Carbide and Silicon Oxycarbide CMC", pp. 1292-1303. |
Continuations (1)
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Number |
Date |
Country |
Parent |
684425 |
Apr 1991 |
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