Mixed matrix membranes (MMMs) composed of two different
fillers
such as metal–organic frameworks (MOFs) and covalent–organic
frameworks (COFs) embedded into polymers provide enhanced gas separation
performance. Since it is not possible to experimentally consider all
possible combinations of MOFs, COFs, and polymers, developing computational
methods is urgent to identify the best performing MOF–COF pairs
to be used as dual fillers in polymer membranes for target gas separations.
With this motivation, we combined molecular simulations of gas adsorption
and diffusion in MOFs and COFs with theoretical permeation models
to calculate H2, N2, CH4, and CO2 permeabilities of almost a million types of MOF/COF/polymer
MMMs. We focused on COF/polymer MMMs located below the upper bound
due to their low gas selectivity for five industrially important gas
separations, CO2/N2, CO2/CH4, H2/N2, H2/CH4, and
H2/CO2. We further investigated whether these
MMMs could exceed the upper bound when a second type of filler, a
MOF, was introduced into the polymer. Many MOF/COF/polymer MMMs were
found to exceed the upper bounds showing the promise of using two
different fillers in polymers. Results showed that for polymers having
a relatively high gas permeability (≥104 barrer)
but low selectivity (≤2.5) such as PTMSP, addition of the MOF
as the second filler can have a dramatic effect on the final gas permeability
and selectivity of the MMM. Property–performance relations
were analyzed to understand how the structural and chemical properties
of the fillers affect the permeability of the resulting MMMs, and
MOFs having Zn, Cu, and Cd metals were found to lead to the highest
increase in gas permeability of MMMs. This work highlights the significant
potential of using COF and MOF fillers in MMMs to achieve better gas
separation performances than MMMs with one type of filler, especially
for H2 purification and CO2 capture applications.