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The present invention discloses composite inorganic membranes, methods for making the same, and methods of separating gases, vapors, and liquids using the same. The composite zeolite membrane is prepared by TS-1 zeolite membrane synthesis, and subsequent palladium doping. In the composite zeolite me

The present invention discloses composite inorganic membranes, methods for making the same, and methods of separating gases, vapors, and liquids using the same. The composite zeolite membrane is prepared by TS-1 zeolite membrane synthesis, and subsequent palladium doping. In the composite zeolite membrane synthesis, two different methods can be employed, including in-situ crystallization of one or more layers of zeolite crystals an a porous membrane substrate, and a second growth method by in-situ crystallization of a continuous second layer of zeolite crystals on a seed layer of MFI zeolite crystals supported on a porous membrane substrate. The membranes in the form of disks, tubes, or hollow fibers have high gas selectivity over other small gases, very good impurity resistance, and excellent thermal and chemical stability over polymer membranes and other inorganic membranes for gas, vapor, and liquid, separations.

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1. A metal doped zeolite membrane for gas separation, wherein the membrane comprises a porous substrate and a zeolite layer thereon having pores with metal clusters in the zeolite pores. 2. The metal doped zeolite membrane of claim 1, wherein the zeolite layer comprises an MFI structure framework. 3

1. A metal doped zeolite membrane for gas separation, wherein the membrane comprises a porous substrate and a zeolite layer thereon having pores with metal clusters in the zeolite pores. 2. The metal doped zeolite membrane of claim 1, wherein the zeolite layer comprises an MFI structure framework. 3. The metal doped zeolite membrane of claim 2, wherein heteroatoms are incorporated into the MFI structure framework. 4. The metal doped zeolite membrane of claim 3, wherein the heteroatoms comprise titanium, vanadium, niobium, or a combination of two or more thereof. 5. The metal doped zeolite membrane of claim 2, wherein the MFI structure has channels of zeolite pores and wherein the metal clusters are located in sites in the channels. 6. The metal doped zeolite membrane of claim 1, wherein the metal clusters comprise a transition metal or an alloy of transition metals. 7. The metal doped zeolite membrane of claim 6, wherein the metal clusters comprise a transition metal of Groups 1B and 6B to 8B of the Periodic Table, an alloy thereof, or a combination thereof. 8. The metal doped zeolite membrane of claim 7, wherein the metal clusters comprise a transition metal of Groups 1B and 8B of the Periodic Table, an alloy thereof, or a combination thereof. 9. The metal doped zeolite membrane of claim 8, wherein the metal clusters comprise palladium, silver, or copper or an alloy thereof. 10. A method for making a composite zeolite membrane, comprising the steps of: providing a nano-particle suspension;coating nano-particle seeds on a porous substrate to form one or more seed layers;providing a precursor comprising (i) NaOH, (ii) TiO2, V2O, or Nb2O, (iii) SiO2, (iv) tetrapropyl ammonium hydroxide (TPAOH), (v) ethanol (EtOH), and (vi) H2O;placing the precursor in contact with the seeded porous substrate;heating the precursor and seeded substrate under hydrothermal conditions to form a zeolite membrane having a porous framework; andsubjecting the zeolite membrane to metal doping to form metal clusters in pores of the framework. 11. The method. of claim 10, wherein the porous substrate is coated with a temperature-programmed synthesized nano-particie seed suspension. 12. The method of claim 10, wherein the precursor comprises SiO2, X, TPAOH, H2O, and EtOH in an approximate ratio of 1 SiO2:y X: 0.12 TPAOH:60 H2O:4 EtOH, where X can be TiO2, V2O, or Nb2O and y is in the range of from 0.01 to 0.04. 13. The method of claim 10, wherein a metal is doped on specific sites of the zeolite membrane framework. 14. The method of claim 13, wherein the zeolite membrane framework has channels of zeolite pores and the sites are in the channels. 15. The method of claim 10, wherein the metal doping on zeolite membranes is carried out by one or more of the processes selected from the group consisting of melting salt vapor deposition, plasma treatment, and UV-irradiation. 16. The method of claim 10, wherein the zeolite membrane framework comprises an MR structure. 17. A metal doped zeolite membrane prepared by the method of claim 10. 18. A molecular sieve comprising the metal doped zeolite membrane of claim 17. 19. In an improved method of separating hydrogen from syngas or another gas mixture containing CO2, N2, CH4, CO, H2O, and a small amount of impurities, the improvement wherein the molecular sieve of claim 18 is used as part of the reactor system. 20. The method of claim 19 which is carried out at high temperature. 21. The method of claim 19, wherein the gaseous mixture contains a small amount of one or more impurities. 22. The method of claim 21, wherein the impurity is H2S and/or NH3. 23. The metal doped zeolite membrane of claim 17, wherein the doping metal is a transition metal or an alloy of transition metals. 24. The metal doped zeolite membrane of claim 23, wherein the doping metal is a transition metal of Groups 1B and 6B to 8B of the Periodic Table, an alloy thereof, or a combination thereof. 25. The metal doped zeolite membrane of claim 24, wherein the doping metal is a transition metal of Groups 1B and 8B of the Periodic Table, an alloy thereof, or a combination thereof. 26. The metal doped membrane of claim 25, wherein the doping metal is palladium, silver, or copper or an alloy thereof.