초록 ▼

The present invention discloses a new type of polyimide membranes including hollow fiber and flat sheet membranes with high permeances for air separations and a method of making these membranes. The new polyimide hollow fiber membranes have O2 permeance higher than 300 GPU and O2/N2 selectivity high

The present invention discloses a new type of polyimide membranes including hollow fiber and flat sheet membranes with high permeances for air separations and a method of making these membranes. The new polyimide hollow fiber membranes have O2 permeance higher than 300 GPU and O2/N2 selectivity higher than 3 at 60° C. under 308 kPa for O2/N2 separation. The new polyimide hollow fiber membranes also have CO2 permeance higher than 1000 GPU and single-gas selectivity for CO2/CH4 higher than 20 at 50° C. under 791 kPa for CO2/CH4 separation.

대표청구항 ▼

1. An asymmetric hollow fiber membrane formed from a polyimide comprising a plurality of repeating units of formula (I) wherein X is selected from the group consisting of and mixtures thereof. 2. The asymmetric hollow fiber membrane of claim 1 wherein said polyimide is poly(3,3′,4,4′-diphenylsulfon

1. An asymmetric hollow fiber membrane formed from a polyimide comprising a plurality of repeating units of formula (I) wherein X is selected from the group consisting of and mixtures thereof. 2. The asymmetric hollow fiber membrane of claim 1 wherein said polyimide is poly(3,3′,4,4′-diphenylsulfone tetracarboxylic dianhydride-3,3′,4,4′-benzophenone tetracarboxylic dianhydride-pyromellitic dianhydride-3,3′,5,5′-tetramethyl-4,4′-methylene dianiline) derived from the condensation reaction of 3,3′,4,4′-diphenylsulfone tetracarboxylic dianhydride (DSDA), 3,3′,4,4-benzophenone tetracarboxylic dianhydride (BTDA), and pyromellitic dianhydride (PMDA) with 3,3′,5,5′-tetramethyl-4,4′-methylene dianiline (TMMDA) wherein the molar ratio of said TMMDA to the mixture of said DSDA, said BTDA, and said PMDA is 100:100. 3. The asymmetric hollow fiber membrane of claim 1 wherein said polyimide is poly(3,3′,4,4′-diphenylsulfone tetracarboxylic dianhydride-3,3′,4,4′-benzophenone tetracarboxylic dianhydride-4,4′-oxydiphthalic anhydride-3,3′,5,5′-tetramethyl-4,4′-methylene dianiline) derived from the condensation reaction of 3,3′,4,4′-diphenylsulfone tetracarboxylic dianhydride (DSDA), 3,3′,4,4′-benzophenone tetracarboxylic dianhydride (BTDA) and 4,4 ′-oxydiphthalic anhydride (ODPA) with 3,3′,5,5′-tetramethyl-4,4′-methylene dianiline (TMMDA) wherein the molar ratio of said TMMDA to the mixture of said DSDA, said BTDA and said ODPA is 100:100. 4. A process for preparing a polyimide hollow fiber membrane comprising: a) dissolving a polyimide comprising a plurality of repeating units of formula (I) in a mixture of solvents to form a hollow fiber spinning dope, wherein X is selected from the group consisting of and mixtures thereof; andb) spinning said hollow fiber spinning dope and a bore fluid simultaneously from an annular spinneret to form a nascent hollow fiber, (c) immersing said nascent hollow fiber in a coagulant bath to produce a wet hollow fiber, (d) annealing said wet hollow fiber in a hot water bath at a temperature in a range of 70° to 100° C. for a certain time in a range of 10 minutes to 3 hours, (e) washing the said wet hollow fiber by a sequential solvent exchange, and (f) drying the said wet hollow fiber to produce a polyimide hollow fiber membrane. 5. The process of claim 4 wherein said hollow fiber spinning dope comprises a mixture of N-methylpyrrolidone and 1,3-dioxolane at a weight ratio of from about 99:1 to 50:50. 6. The process of claim 5 wherein said weight ratio is from about 95:5 to about 75:25. 7. A method of separating at least one gas from a mixture of gases comprising: a) contacting an asymmetric hollow fiber polyimide membrane which is permeable to said at least one gas with said mixture of gases, wherein said asymmetric polyimide membrane is formed from a polyimide comprising a plurality of first repeating units of formula (I) wherein X is selected from the group consisting of and mixtures thereof;(b) contacting the mixture of gases on one side of said asymmetric polyimide membrane to cause said at least one gas to permeate the membrane; and(c) removing from the opposite side of said asymmetric polyimide membrane a permeate gas composition comprising a portion of said at least one gas which permeated said asymmetric polyimide membrane. 8. The method of claim 7 wherein said mixture of gases is selected from the group consisting of CO2/CH4, CO2N2, H2/CH4, H2S/CH4, olefin/paraffin, and iso paraffins/normal paraffins. 9. The method of claim 7 wherein said mixture of gas comprises at least one volatile organic compound in an atmospheric gas. 10. The method of claim 7 wherein said mixture of gas comprises a mixture of hydrogen, nitrogen, methane and argon in an ammonia purge stream. 11. The method of claim 7 wherein said mixture of gas comprises hydrogen from a hydrocarbon vapor stream. 12. The method of claim 7 wherein said mixture of gas comprises a mixture of carbon monoxide, helium and methane. 13. The method of claim 7 wherein said, mixture of gas comprises natural gas comprising methane and at least one gas component selected from the group consisting of carbon dioxide, oxygen, nitrogen, water vapor, hydrogen sulfide, and helium. 14. The method of claim 7 wherein said mixture of gas comprises hydrocarbon gases, carbon dioxide, hydrogen sulfide and mixtures thereof. 15. The method of claim 7 wherein said mixture of gas comprises a mixture of organic molecules and water.