Process for the recovery of alkoxysilanes obtained from the direct reaction of silicon with alkanols
View Patent ↗A process is provided for separating a mixture of alkoxysilanes and alkanol, e.g., the crude product effluent of the Direct Reaction of silicon metal with alkanol, which comprises: a) introducing a mixture of alkoxysilane(s) and alkanol to a separation unit possessing a separation membrane having a first surface and an opposing second surface; b) contacting the mixture of alkoxysilane(s) and alkanol with the first surface of the separation membrane whereby one or more components of the mixture selectively absorb into the first surface and permeate therethrough to the second surface under the influence of a concentration gradient across the membrane thereby separating the mixture into an alkanol-enriched permeate fraction and an alkanol-deficient retentate fraction or an alkoxysilane-enriched permeate fraction and an alkoxysilane-deficient retentate fraction; and, c) recovering the permeate fraction.
1. A process for separating the components in a process stream resulting from the Direct Reaction Process of silicon metal with an alkanol for making alkoxysilanes, which comprises:
a) introducing the process stream from the Direct Reaction Process to a separation unit possessing a separation membrane having a first surface and an opposing second surface, wherein the process stream includes a mixture of alkoxysilane(s), alkanol(s) and optionally alkanol/alkoxysilane azeotropes;
b) contacting the process stream from the Direct Reaction Process with the first surface of the separation membrane whereby one or more components of the mixture of alkoxysilane(s), alkanol(s) and optionally alkanol/alkoxysilane azeotropes selectively absorb into the first surface and permeate therethrough to the second surface under the influence of a concentration gradient across the membrane thereby separating the mixture into an alkanol-enriched permeate fraction and an alkanol-deficient retentate fraction or an alkoxysilane-enriched permeate fraction and an alkoxysilane-deficient retentate fraction; and,
c) recovering the permeate fraction and the retention fraction.
2. The process of claim 1 wherein the process stream from the Direct Reaction Process comprises a mixture of methoxysilanes, methanol and methanol/methoxysilane azeotropes, the process resulting in the breaking of the azeotropes.
3. The process of claim 2 wherein the methoxysilanes in the retentate fraction are separated by fractional distillation.
4. The process of claim 2 wherein recovered methanol is recycled to the Direct Reaction Process.
5. The process of claim 1 wherein the concentration gradient is maintained by vacuum applied to the second surface.
6. The process of claim 1 wherein the concentration gradient is maintained by the application of pressure to the first surface that is higher than the pressure on the second surface.
7. The process of claim 2 conducted in two membrane separation stages, the process stream additionally containing hydrogen, nitrogen and methane gases undergoing a first membrane separation step in a first membrane separation zone equipped with a first separation membrane to provide a first permeate fraction comprising hydrogen, nitrogen and methane and a first retentate fraction of substantially reduced gas content comprising methoxysilanes, methanol and methanol/methoxysilane azeotropes, the first retentate fraction undergoing a second membrane separation step in a second membrane separation zone equipped with a second separation membrane to provide a second permeate fraction comprising methanol and a second retentate fraction possessing a higher concentration of methoxysilanes than that present in the first retentate fraction, the second membrane separation step resulting in the breaking of the azeotropes.
8. The process of claim 7 wherein methanol recovered in the second permeate fraction is recycled to the Direct Reaction Process.
9. The process of claim 7 wherein methoxysilanes present in the second retentate fraction are separated by fractional distillation.
10. The process of claim 1 wherein the process stream is obtained from the Direct Reaction Process and comprises a mixture of ethoxysilanes and ethanol.
11. The process of claim 10 wherein the ethoxysilanes in the retentate fraction are separated by fractional distillation.
12. The process of claim 10 wherein the ethanol recovered in the permeate fraction is recycled to the Direct Reaction Process.
13. The process of claim 1 wherein the separation membrane is fabricated from at least one material selected from the group consisting of polyamide, palladium, polyethylene, palladium-silver alloy, polyacrylonitrile, palladium-silicon alloy, polyphenylene oxide, amorphous Pd x Si (1-x) , x=0.8-0.9, polysulfone, silica, polypropylene, alumina, silicone rubber, zeolite, silicone-polycarbonate, titania and polytetrafluoroethylene, pyrolytic carbon, polyvinyledene fluoride, nafion(in its H+ and alkali metal—exchanged forms) and polyphosphazene, the separation membrane being optionally supported by another material.
14. The process of claim 7 wherein the first and second separation membranes are fabricated from different materials selected from the group consisting of polyamide, palladium, polyethylene, palladium-silver alloy, polyacrylonitrile, palladium-silicon alloy, polyphenylene oxide, amorphous Pd x Si (1-x) , x=0.8-0.9, polysulfone, silica, polypropylene, alumina, silicone rubber, zeolite, silicone-polycarbonate, titania and polytetrafluoroethylene, pyrolytic carbon, polyvinyledene fluoride, nafion (in its H+ and alkali metal—exchanged forms) and polyphosphazene, one or both separation membranes being optionally supported by another material.
15. The process of claim 1 wherein the alkoxysilane includes a trialkoxysilane.
16. The process of claim 15 wherein the trialkoxysilane is trimethoxysilane.