Mixed matrix materials (MMMs) integrating excellent processability from polymers and distinct separation properties from metal-organic frameworks (MOFs) are of interest for membrane gas separations, and they are often made into freestanding films (> 100 µm) to demonstrate superior gas separation properties. However, they are difficult to fabricate into nanofilm composite membranes due to interfacial incompatibility between polymers and nanofillers. Here we have successfully developed TFN membranes based on MMMs (as thin as 100 nm) comprising amorphous poly(ethylene oxide) (
aPEO) and UiO-66-NH
2 (45-85 nm) enabled by strong hydrogen bonds between the two matrices. A third component of liquid polyethylene glycol dimethyl ether (PEGDME, 240 Da) can be incorporated in the
aPEO to improve CO
2 permeance while retaining CO
2/N
2 selectivity. For example, adding 10 wt% UiO-66-NH
2 in
aPEO increases CO
2 permeance from 630 to 1700 GPU while increasing CO
2/N
2 selectivity to 62; incorporating 40 wt% PEGDME into the selective layer dramatically increases CO
2 permeance from 1700 to 3000 GPU while maintaining CO
2/N
2 selectivity at 60, surpassing Robeson’s upper bound and commercial membrane such as Polaris 2nd Gen (with pure-gas CO
2 permeance of 1700 GPU and CO
2/N
2 selectivity of 50). An example membrane (containing 40% PEGDME and 10% UiO66-NH2) demonstrates mixed-gas CO
2 permeance of 2900 GPU and CO
2/N
2 selectivity of 41 in the presence of 2.1 mol% water vapor at ≈23 °C. The relationships between the membrane nanostructures and CO
2 separation properties will be elucidated.
