초록 ▼

A mixed matrix membrane is provided which comprises a continuous phase organic polymer and small pore alumina containing molecular sieves dispersed therein. The molecular sieves have a silica-to-alumina molar ratio of less than 1.0, more preferably, less than 0.3, and most preferably less than 0.1.

A mixed matrix membrane is provided which comprises a continuous phase organic polymer and small pore alumina containing molecular sieves dispersed therein. The molecular sieves have a silica-to-alumina molar ratio of less than 1.0, more preferably, less than 0.3, and most preferably less than 0.1. In some cases, the molecular sieves have no appreciable amounts of silica. Exemplary compositions include aluminophosphates (AlPO) and silicoaluminophosphates (SAPO). When these molecular sieves are properly interspersed with a continuous phase polymer, the membrane will exhibit a mixed matrix membrane effect, i.e., a selectivity increase of at least 10% relative to a neat membrane containing no molecular sieves. The molecular sieves have pores with a largest minor crystallographic free diameter of 4.0 Angstroms or less. Finally, methods for making and using such mixed matrix membranes to separate gases from a mixture containing two or more gases are also disclosed.

대표청구항 ▼

What is claimed is: 1. A mixed matrix membrane comprising: a continuous phase organic polymer and small pore alumina containing molecular sieves dispersed therein, the molecular sieves having a silica-to-alumina molar ratio of less than 0.5. 2. The mixed matrix membrane of claim 1 wherein: the s

What is claimed is: 1. A mixed matrix membrane comprising: a continuous phase organic polymer and small pore alumina containing molecular sieves dispersed therein, the molecular sieves having a silica-to-alumina molar ratio of less than 0.5. 2. The mixed matrix membrane of claim 1 wherein: the silica-to-alumina molar ratio is less than 0.2. 3. The mixed matrix membrane of claim 1 wherein: the mixed matrix membrane is made without silanation of the molecular sieves. 4. The mixed matrix membrane of claim 1 wherein: the membrane exhibits a mixed matrix effect. 5. The mixed matrix membrane of claim 1 wherein: the molecular sieves have pores with a minor crystallographic free diameter of 3.8 Å, or less. 6. The mixed matrix membrane of claim 1 wherein: the molecular sieves have pores with a minor crystallographic free diameter of 3.6 Å, or less. 7. The mixed matrix membrane of claim 1 wherein: the molecular sieves have a number average particle size of less than 2 microns. 8. The mixed matrix membrane of claim 1 wherein: the molecular sieves have a number average particle size of less than 0.5 microns. 9. The mixed matrix membrane of claim 1 wherein: the molecular sieves are non-zeolitic molecular sieves. 10. The mixed matrix membrane of claim 9 wherein: the composition of the molecular sieves includes at least one of an aluminophosphate (AlPO), a silicoaluminophosphate (SAPO), a metallo-aluminophosphate (MeAPO), an elementaluminophosphate (ElAPO), a metal silicoaluminophosphate (MeAPSO) and an elementalsilicoaluminophosphate (ELAPSO). 11. The mixed matrix membrane of claim 1 wherein: the composition of the molecular sieves includes a SAPO. 12. The mixed matrix membrane of claim 1 wherein: the composition of the molecular sieves includes a MeAPSO. 13. The mixed matrix membrane of claim 1 wherein: the molecular sieves have an IZA structure type of at least one of AEI, CHA, ERI, LEV, AFX, AFT and GIS. 14. The mixed matrix membrane of claim 1 wherein: the molecular sieves include at least one of ALPO-18, SAPO-18, AlPO-34, SAPO-34, MEAPSO-34, SAPO-44, SAPO-47, AlPO-17, SAPO-17, CVX-7, MeAPSO-17, SAPO-35, SAPO-56, AlPO-52, and SAPO-43. 15. The mixed matrix membrane of claim 1 wherein: the molecular sieves have an IZA structure type of at least one of ERI, LEV, AFX, AFT and GIS. 16. The mixed matrix membrane of claim 1 wherein: the molecular sieves include at least one of AlPO-17, SAPO-17, CVX-7, MeAPSO-17, SAPO-35, SAPO-56, AlPO-52, and SAPO-43. 17. The mixed matrix membrane of claim 1 wherein: the molecular sieves have an IZA structure type of at least one of AFX, AFT and GIS. 18. The mixed matrix membrane of claim 1 wherein: the molecular sieves include at least one of SAPO-56, AlPO-52, and SAPO-43. 19. The mixed matrix membrane of claim 1 wherein: the molecular sieves include SAPO-17 and MeAPSO-17 and CVX-7. 20. The mixed matrix membrane of claim 1 wherein: the polymer is selected from the group comprising polyetherimides and polyimides. 21. A method of making a mixed matrix membrane comprising: providing a continuous phase organic polymer; providing small pore alumina containing molecular sieves having a silica-to-alumina molar ratio of less than 0.5; dispersing the molecular sieves into the continuous phase organic polymer; and allowing the continuous phase organic polymer to solidify about the molecular sieves to produce a mixed matrix membrane; whereby the mixed matrix membrane exhibits a mixed matrix membrane effect. 22. A process for separating two gas components having different molecular sizes from a feed stream including the two gas components, the process including: (a) providing a mixed matrix membrane that has small pore alumina containing molecular sieves that have a silica-to-alumina molar ratio of less than 0.5 interspersed into a continuous phase polymeric carrier, the membrane including feed and permeate sides; and (b) directing a feedstream including first and second gas components to the feed side of the membrane and withdrawing a retentate stream depleted in the first gas component from the retentate side and withdrawing a permeate stream enriched in the first gas component from the permeate side of the membrane; wherein the selectivity of the first gas component through the molecular sieves is greater than the selectivity of the first gas component through the polymer.