Adsorption-enhanced and plasticization resistant composite membranes
The disclosure provides for polymer membranes which comprise metal organic frameworks, methods of making therein, and methods of use thereof, including in gas separation.
1. A composite membrane comprising a plurality of nanocrystalline metal organic framework (MOF) nanoparticles having an average particle size of less than about 200 nanometers dispersed within a polymer material, wherein the composite membrane maintains high selectivity for a component gas in the presence a mixture of gases when compared to the pure polymer material not having the MOF, wherein the mixture of gases contains the component gas and at least one plasticizing gas, wherein the MOF comprises one or more cores comprising one or more linking moieties obtained from:
wherein,
R 1 -R 2 are independently selected from the group comprising H, D, optionally substituted FG, optionally substituted alkyl, optionally substituted heteroalkyl, optionally substituted alkenyl, optionally substituted heteroalkenyl, optionally substituted alkynyl, optionally substituted heteroalkynyl, optionally substituted cycloalkyl, optionally substituted cycloalkenyl, optionally substituted aryl, optionally substituted heterocycle, and optionally substituted mixed ring system, and
wherein the one or more cores comprise CO 2+ and/or Ni 2+ .
2. The composite membrane of claim 1 , wherein the polymer material is selected from the group consisting of polyimides, polyetherimides, polyamides, aryl polyetherimides, cellulosic polymers, polycarbonate polymers, polysulfone, polyether, polyester polymers, polyarylate polymers, polysulfide polymers, and polyphosphazines.
3. The composite membrane of claim 1 , wherein the polymer material is a 6FDA-based polyimide material, wherein 6FDA=(4,4′-hexafluoroisopropylidene) diphthalic anhydride).
4. The composite membrane of claim 3 , wherein the polymer material comprises 6FDA-DAM, 6-FDA-Durene, or 6FDA-Durene:Jeffamine copolymers.
5. The composite membrane of claim 1 , wherein the MOF comprises one or more cores obtained from linking moieties of structural Formula I(a) or Formula II(a):
6. The composite membrane of claim 1 , wherein the MOF material imparts chemical stability to the composite membrane.
7. The composite membrane of claim 1 , wherein the MOF imparts adsorptive selectivity to the composite membrane.
8. A method to separate a component gas from a gas mixture comprising:
contacting the gas mixture with a composite membrane of claim 1 , wherein the component gas is selectively adsorbed to the polymer membrane, and wherein the polymer membrane exhibits resistance to plasticization effects from plasticizing gases when exposed to a mixture of gases continuing at least one plasticizing gas.
9. The method of claim 8 , wherein the method is carried out in the presence of plasticizing gases.
10. The method of claim 9 , wherein the plasticizing gases are selected from CO 2 , C 2 H 4 , C 2 H 6 , C 3 H 6 , C 3 H 8 , and/or butanes.
11. The method of claim 8 , wherein the method can be carried out at a pressure of greater than 10 bar.
12. The method of claim 8 , wherein the membrane selectively adsorbs a high density gas.
13. The method of claim 12 , where the membrane can separate CO 2 from CH 4 , CO 2 from N 2 , CO 2 from H 2 , C 2 H 4 from C 2 H 6 , C 3 H 6 from C 3 H 8 , CH 4 from C 2 H 6 , H 2 from hydrocarbons, and/or butenes or longer chain alkenes from alkanes.
14. The composite membrane of claim 1 , wherein the MOF nanoparticles have an average particle size of less than about 100 nanometers.
15. The composite membrane of claim 1 , wherein the MOF nanoparticles interact with the polymer via a metal-polymer interaction.