Claims
- 1. A process for producing a polymeric silicone of defined length comprised of:
a. a organosilane monomer; b. a condensation catalyst for said monomer; c. a porous substrate wherein the pore size is designed to fit only the polymeric silicones of the desired length and shorter; d. a reacting solvent system that solubilizes the desired organosilane monomer, and all polymeric silicones of a size smaller than the target polymeric silicone such that the target polymeric silicone and any larger species are insoluble in said reacting solvent; e. a process for recovering the target polymeric silicone.
- 2. A process according to claim 1 wherein the condensation catalyst is attached or adsorbed to the porous substrate.
- 3. A process according to claim 1 wherein the condensation catalyst is comprised of a protein.
- 4. A process according to claim 3 wherein the protein is derived from the silica spicules of Tethya aurantia.
- 5. A process according to claim 3 wherein the protein is the alpha subunit of the protein filament derived from the silica spicules of Tethya aurantia with a molecular weight of about 29 kDa.
- 6. A process according to claim 3 wherein the protein is a variant form of the alpha subunit of the protein filament derived from the silica spicules of Tethya aurantia wherein the protein has been modified to allow attachment to a substrate.
- 7. A process according to claim 3 wherein the protein is a variant form of the alpha subunit of the protein filament derived from the silica spicules of Tethya aurantia wherein the protein has been modified for improved stability.
- 8. A process according to claim 3 wherein the protein is a variant form of the alpha subunit of the protein filament derived from the silica spicules of Tethya aurantia wherein the protein has been modified to improve the rate of condensation of organosilane monomer.
- 9. A process according to claim 3 wherein the protein is the beta subunit of the protein filament derived from the silica spicules of Tethya aurantia with a molecular weight of about 28 kDa.
- 10. A process according to claim 3 wherein the protein is a variant form of the beta subunit of the protein filament derived from the silica spicules of Tethya aurantia wherein the protein has been modified to allow attachment to a substrate.
- 11. A process according to claim 3 wherein the protein is a variant form of the beta subunit of the protein filament derived from the silica spicules of Tethya aurantia wherein the protein has been modified for improved stability.
- 12. A process according to claim 3 wherein the protein is a variant form of the beta subunit of the protein filament derived from the silica spicules of Tethya aurantia wherein the protein has been modified to improve the rate of condensation of organosilane monomer.
- 13. A process according to claim 3 wherein the protein is the gamma subunit of the protein filament derived from the silica spicules of Tethya aurantia and with a molecular weight of about 27 kDa.
- 14. A process according to claim 3 wherein the protein is a variant form of the gamma subunit of the protein filament derived from the silica spicules of Tethya aurantia wherein the protein has been modified to allow attachment to a substrate.
- 15. A process according to claim 3 wherein the protein is a variant form of the gamma subunit of the protein filament derived from the silica spicules of Tethya aurantia wherein the protein has been modified for improved stability.
- 16. A process according to claim 3 wherein the protein is a variant form of the gamma subunit of the protein filament derived from the silica spicules of Tethya aurantia wherein the protein has been modified to improve the rate of condensation of organosilane monomer.
- 17. A process according to claim 3 wherein the protein is an enzyme.
- 18. A process according to claim 17 wherein the enzyme is a native or mutant Subtilisin protease.
- 19. A process according to claim 17 wherein the enzyme is a native or mutant Cysteine protease.
- 20. A process according to claim 3 wherein the protein is a peptide obtained from screening a diverse peptide library.
- 21. A process according to claim 1 wherein the condensation catalyst and porous substrate are packed in a column that allows the reacting solvent system and organosilane monomer to be added at the top and the target polymeric silicone compound to be recovered at the bottom.
- 22. A process for producing a polymeric silicone of defined length comprised of:
a. the alpha subunit of the protein filament derived from the silica spicules of Tethya aurantia with a molecular weight of about 29 kDa; b. a porous Sodium/Aluminum Zeolite wherein the pore size is designed to fit only the polymeric silicones of the desired length and shorter; c. a silicone-based solvent system that solubilizes organosilane monomers, and all polymeric silicones of a size smaller than the target polysiloxane such that the target polymeric silicone and any larger species are insoluble in said silicone solvent; d. a process for recovering the target polymeric silicone.
- 23. A process according to claim 22 wherein the alpha subunit protein is chemically or physically attached to the Zeolite.
- 24. A process according to claim 22 wherein the Zeolite is replaced by a cyclodextrin having a pore size sufficient to accommodate only the polymeric silicones of the desired length and shorter.
- 25. A process according to claim 22 wherein the Zeolite is replaced by activated carbon wherein the pore size is sufficient to accommodate only the polymeric silicones of the desired length and shorter.
- 26. A process according to claim 22 wherein the Zeolite is replaced by a porous starch particle wherein the pore size is sufficient to accommodate only the polymeric silicones of the desired length and shorter.
- 27. The process according to claim 22 wherein the alpha subunit protein is replaced by a wild type or variant protease enzyme.
- 28. The process according to claim 27 wherein the enzyme is chemically or physically attached to the Zeolite.
- 29. A process for making a siloxane, the process comprising the steps of
a) providing a silane of the formula: RaSi-Lb wherein R is a hydrocarbon group; L is a leaving group; the sum of a and b is 4; b) reacting the silane with a condensation catalyst such that the leaving group is displaced from the silane and at least one —Si—O—Si— bond is formed in the product of the reaction; and c) optionally, recovering the product of the reaction from step b); d) optionally, cyclizing the product of the reaction from step b) to produce a cyclic siloxane.
RELATED APPLICATIONS
[0001] This application claims priority to U.S. Provisional Application Serial No. 60/342,715 filed Dec. 20, 2001.
Provisional Applications (1)
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Number |
Date |
Country |
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60342715 |
Dec 2001 |
US |