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A membrane and method for separating carbon dioxide from a mixture of gases, where the membrane includes expanded polytetrafluoroethylene and polysiloxane. The membrane is highly stable and can separate carbon dioxide at high flux in harsh environments and high temperatures, such as exhaust gases fr

A membrane and method for separating carbon dioxide from a mixture of gases, where the membrane includes expanded polytetrafluoroethylene and polysiloxane. The membrane is highly stable and can separate carbon dioxide at high flux in harsh environments and high temperatures, such as exhaust gases from power plants.

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Having described the invention, that which is claimed is: 1. A membrane for separating carbon dioxide from a mixture of gases comprising carbon dioxide, wherein the membrane comprises expanded polytetrafluoroethylene and polysiloxane and further comprises two support layers and an active layer. 2

Having described the invention, that which is claimed is: 1. A membrane for separating carbon dioxide from a mixture of gases comprising carbon dioxide, wherein the membrane comprises expanded polytetrafluoroethylene and polysiloxane and further comprises two support layers and an active layer. 2. The membrane of claim 1 wherein the mixture of gases comprises carbon dioxide and nitrogen. 3. The membrane of claim 1 wherein the polysiloxane is a polyorganosiloxane having the formula: MDqTsM wherein: M is R2aR33-aSiO1/2; D is R42SiO2/2; T is R5SiO3/2, R2 is an alkoxy, aryloxy or araalkoxy having from 1 to 60 carbon atoms; R3, R4 and R5 are each independently alkyl, aryl or aralkyl having from one to sixty carbon atoms; q and s are each independently integers from 0 to 300 and a is an integer from 1 to 3. 4. The membrane of claim 3 wherein the polyorganosiloxane has a viscosity in the range of from about 10 centistokes to about 1,000,000 centistokes. 5. The membrane of claim 3 wherein the polyorganosiloxane is a linear hydroxyl-terminated polydimethylsiloxane. 6. The membrane of claim 1, wherein the active layer is sandwiched between the two support layers. 7. The membrane of claim 6, wherein the support layers comprise expanded polytetrafluoroethylene and the active layer comprises polysiloxane. 8. The membrane of claim 7 wherein the support layers have a thickness in the range of from about 10 microns to about 50 microns. 9. The membrane of claim 7 wherein the active layer has a thickness in the range of from about 10 microns to about 600 microns. 10. The membrane of claim 7 wherein the active layer further comprises a porous ceramic. 11. The membrane of claim 10 wherein the ceramic is selected from the group consisting of zeolite, Al2O3, Y2O3, MgO, SiO2, Si3N4 or ZrO2. 12. The membrane of claim 1 wherein the membrane has a permeability of greater than 4000 barrers for carbon dioxide. 13. A method for separating carbon dioxide from a gas mixture comprising carbon dioxide, wherein the method comprises feeding the gas mixture through a membrane comprising expanded polytetrafluoroethylene and polysiloxane, wherein said membrane further comprises two support layers and an active layer. 14. The method of claim 13 wherein the mixture of gases comprises carbon dioxide and nitrogen. 15. The method of claim 13 wherein the polysiloxane is a polyorganosiloxane having the formula: MDqTsM wherein: M is R2aR33-aSiO1/2; D is R42SiO2/2; T is R5SiO3/2, R2 is an alkoxy, aryloxy or araalkoxy having from 1 to 60 carbon atoms; R3, R4 and R5 are each independently alkyl, aryl or aralkyl having from one to sixty carbon atoms; q and s are each independently integers from 0 to 300 and a is an integer from 1 to 3. 16. The method of claim 15 wherein the polyorganosiloxane has a viscosity in the range of from about 10 centistokes to about 1,000,000 centistokes. 17. The method of claim 15 wherein the polyorganosiloxane is a linear hydroxyl-terminated polydimethylsiloxane. 18. The method of claim 13, wherein the active layer is sandwiched between the two support layers. 19. The method of claim 18, wherein the support layers comprise expanded polytetrafluoroethylene and the active layer comprises polysiloxane. 20. The method of claim 18 wherein the support layers have a thickness in the range of from about 10 microns to about 50 microns. 21. The method of claim 18 wherein the active layer has a thickness in the range of from about 10 microns to about 600 microns. 22. The method of claim 18 wherein the active layer further comprises a porous ceramic. 23. The method of claim 22 wherein the ceramic is selected from the group consisting of zeolite, Al2O3, Y2O3, MgO, SiO2, Si3N4 or ZrO2. 24. The method of claim 13 wherein the membrane has a permeability of greater than 4000 barrers for carbon dioxide. 25. A membrane for separating carbon dioxide from a mixture of gases comprising carbon dioxide, wherein the membrane comprises two support layers each comprising expanded polytetrafluoroethylene and an active layer comprising polysiloxane, wherein the active layer is sandwiched between the two support layers.