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A device useful for separating the components of gas mixtures includes a selectively gas permeable mixed matrix membrane of a dispersed phase of chabazite type molecular sieve particles uniformly distributed throughout a continuous phase of a polymer. The membrane can be fabricated by dispersing the

A device useful for separating the components of gas mixtures includes a selectively gas permeable mixed matrix membrane of a dispersed phase of chabazite type molecular sieve particles uniformly distributed throughout a continuous phase of a polymer. The membrane can be fabricated by dispersing the chabazite type molecular sieve particles in a solution of the polymer dissolved in a suitable solvent, and then forming the suspension into a membrane structure by conventional polymer membrane fabrication techniques. Mixed matrix membranes with chabazite type molecular sieves are well suited to separations of oxygen, carbon dioxide or helium from nitrogen or methane.

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1. A process for separating at least one component gas from a mixture comprising the component gas, the process comprising the steps of (A) providing a mixed matrix gas separation membrane comprising particles of CHA type molecular sieve dispersed in a continuous phase consisting essentially of a

1. A process for separating at least one component gas from a mixture comprising the component gas, the process comprising the steps of (A) providing a mixed matrix gas separation membrane comprising particles of CHA type molecular sieve dispersed in a continuous phase consisting essentially of a polymer which is permeable to the component gas, (B) contacting the mixture on one side of the membrane to cause the component gas to permeate the membrane, and (C) removing from the opposite side of the membrane a permeate gas composition comprising a portion of the component gas which permeated the membrane. 2. The process of claim 1 in which the component gas to be separated from the gas mixture has a kinetic diameter of about 2-5 .ANG. (0.2-0.5 nm). 3. The process of claim 2 in which the component gas is oxygen. 4. The process of claim 2 in which the component gas is carbon dioxide. 5. The process of claim 1 in which the molecular sieve is selected from the group consisting of SSZ-13 aluminosilicate molecular sieve, SAPO-34 silicoaluminophosphate molecular sieve, SAPO-44 silicoaluminophosphate molecular sieve, and mixtures thereof. 6. The process of claim 5 in which the membrane comprises about 5-25 weight parts molecular sieve per 100 weight parts polymer and the polymer is selected from the group consisting of polysiloxane, polycarbonate, cellulosic polymer, silicone-containing polycarbonate, brominated polycarbonate, polysulfone, polyether sulfone, sulfonated polysulfone, sulfonated polyether sulfone, polyimide, polyether imide, polyketone, polyether ketone, polyamide, polyamide/imide, polyester, polyvinyl ester, polyolefin, polyacetylene, polytrimethysilylpropyne, fluorinated polymer and a mixture thereof. 7. A mixed matrix gas separation membrane comprising particles of CHA type molecular sieve dispersed in a continuous phase consisting essentially of a polymer. 8. The membrane of claim 7 in which the molecular sieve is selected from the group consisting of SSZ-13 aluminosilicate molecular sieve, SAPO-34 silicoaluminophosphate molecular sieve, SAPO-44 silicoaluminophosphate molecular sieve, and mixtures thereof. 9. The membrane of claim 8 in which the membrane comprises about 5-30 weight parts molecular sieve per 100 weight parts polymer. 10. The membrane of claim 8 in which the polymer is selected from the group consisting of polysiloxane, polycarbonate, silicone-containing polycarbonate, brominated polycarbonate, cellulosic polymer, polysulfone, polyether sulfone, sulfonated polysulfone, sulfonated polyether sulfone, polyimide, polyether imide, polyketone, polyether ketone, polyamide, polyamide/imide, polyester, polyvinyl ester, polyolefin, polyacetylene, fluorinated polymer and mixtures thereof. 11. The membrane of claim 8 in which the molecular sieve is SSZ-13.