초록 ▼

Isopycnic or asymmetric mixed matrix hollow fiber membranes for gas separation can be made by a continuous spinning process. Mixed matrix membranes are characterized by a continuous phase of selectively gas permeable polymer in which are uniformly dispersed discrete absorbent particles such as molec

Isopycnic or asymmetric mixed matrix hollow fiber membranes for gas separation can be made by a continuous spinning process. Mixed matrix membranes are characterized by a continuous phase of selectively gas permeable polymer in which are uniformly dispersed discrete absorbent particles such as molecular sieves that also have selectivity enhancing properties. The fibers can be monolithic in which the fiber wall is entirely mixed matrix, or composite in which an active mixed matrix layer is positioned adjacent to a supporting substrate layer. The novel mixed matrix hollow fiber membranes provide higher selectivity than dense film membranes of the continuous phase polymer.

대표청구항 ▼

1. A process for making mixed matrix hollow fiber membrane for gas separation comprising, (A) providing a spinnerette adapted to extrude at least one nascent hollow fiber, (B) feeding a bore fluid through the spinnerette to form a cylindrical fluid stream for each hollow fiber, (C) feeding thro

1. A process for making mixed matrix hollow fiber membrane for gas separation comprising, (A) providing a spinnerette adapted to extrude at least one nascent hollow fiber, (B) feeding a bore fluid through the spinnerette to form a cylindrical fluid stream for each hollow fiber, (C) feeding through the spinnerette to an annular channel surrounding the fluid stream for each hollow fiber a suspension comprising molecular sieve particles uniformly dispersed in a polymer solution comprising a selectively gas permeable polymer and a solvent for the selectively gas permeable polymer, (D) immersing the nascent hollow fiber in a coagulant for a duration effective to solidify the selectively gas permeable polymer, thereby forming a monolithic mixed matrix membrane hollow fiber, and (E) drawing the nascent hollow fiber at a draw ratio in the range of about 1-10. 2. The process of claim 1 in which the weight of molecular seive particles divided by the weight of selectively gas permeable polymer in the polymer solution is within the range of about 0.05-0.4. 3. The process of claim 1 which further comprises feeding through the spinnerette to a second annular channel surrounding the fluid stream for each hollow fiber a core polymer solution comprising a core polymer dissolved in a core solvent, thereby depositing a nascent annular core layer of core polymer solution around the bore fluid stream and a nascent annular sheath layer of the suspension around the nascent annular core layer, to form a nascent composite mixed matrix membrane hollow fiber, in which the nascent composite mixed matrix membrane hollow fiber is immersed in a coagulant for a duration effective to solidify the core polymer and the selectively gas permeable polymer, thereby forming a composite hollow fiber having an inner polymer core and an outer mixed matrix membrane sheath. 4. The process of claim 1 in which the molecular sieve particles comprise chabazite type zeolite. 5. The process of claim 4 in which the chabazite type zeolite is SSZ-13. 6. The process of claim 1 which furthercomprises the step of reacting the molecular sieve particles with a monofunctional organosilicon compound prior to feeding the suspension through the spinnerette. 7. The process of claim 6 in which the monofunctional organosilicon compound has the formula Si(XYR1R2) in which X is displaceable radical, Y is a linking group, and R1 and R2 are each independently any radical other than a displaceable radical. 8. The process of claim 1 in which the nascent hollow fiber has an outer diameter in the range of about 100-500 μm. 9. The process of claim 1 in which the draw ratio is in the range of about 2-6. 10. The process of claim 1 in which the suspension is a stable dispersion at shear rates in the range of 100 to 1000 sec-1. 11. The process of claim 1 in which the molecular sieve particles comprise carbon molecular sieves.