A pair of related metal–organic frameworks (Zn
3
and Zn
2
Cd) developed in our group were incorporated
into Pebax
30R51 and PVDF Kynar 761 polymers to fabricate mixed matrix membranes
(MMMs). These MOFs were chosen due to the carbon dioxide molecular
sieving ability of Zn
3
, and the
slightly larger pore aperture of Zn
2
Cd that allows carbon dioxide and larger gases
to enter the pores. For Pebax-based MMMs, this work demonstrated an
over two-fold and four-and-a-half-fold increase in carbon dioxide
permeability for Zn
3
- (15 wt
%) and Zn
2
Cd-containing
(10 wt %) MMMs over the pristine polymer. Separation selectivity (CO2:N2) of 4.21 and 7.33 were observed for Zn
3
and Zn
2
Cd (10 wt %). For PVDF-based MMMs, the incorporation
of Zn
3
and Zn
2
Cd (10 wt %) increased the carbon
dioxide permeability approximately two- and three-fold. The CO2/N2 selectivity of the PVDF membranes increased
73% (1.01 to 1.86) and 68% (1.01 to 1.68) when 15 wt % Zn
3
and Zn
2
Cd were incorporated into PVDF. The improved performance
of Pebax over PVDF based MMMs is attributed to matching the permeability
of the polymer bulk phase (Pebax over PVDF) and the dispersed phase
(Zn
3
and Zn
2
Cd). The lower permeability allows
the MOF, which has slow kinetics associated with molecular sieving,
to participate in the permeation process better. With regards to Zn
3
vs Zn
2
Cd, while Zn
3
acts as a molecular sieve and Zn
2
Cd does not, we hypothesize that the faster diffusion
of carbon dioxide gas in Zn
2
Cd can outcompete the lower nitrogen gas permeability and
molecular sieving properties of Zn
3
. However, we expect that further increasing the pore aperture
would increase the permeabilities of nitrogen gas such that differences
in diffusion kinetics due to molecular size would be unimportant.