Covalent
organic
frameworks (COFs) are promising materials for
gas storage and separation; however, the potential of COFs for separation
of CH
4
from industrially relevant gases such as H
2
, N
2
, and C
2
H
6
is yet to be investigated.
In this work, we followed a multiscale computational approach to unlock
both the adsorption- and membrane-based CH
4
/H
2
, CH
4
/N
2
, and C
2
H
6
/CH
4
separation potentials of 572 COFs by combining grand canonical
Monte Carlo (GCMC) and molecular dynamics (MD) simulations and density
functional theory (DFT) calculations. Adsorbent performance evaluation
metrics of COFs, adsorption selectivity, working capacity, regenerability,
and adsorbent performance score were calculated for separation of
equimolar CH
4
/H
2
, CH
4
/N
2
, and C
2
H
6
/CH
4
mixtures at vacuum
swing adsorption (VSA) and pressure swing adsorption (PSA) conditions
to identify the best-performing COFs for each mixture. Results showed
that COFs could achieve selectivities of 2–85, 1–7,
and 2–23 for PSA-based CH
4
/H
2
, CH
4
/N
2
, and C
2
H
6
/CH
4
separations, respectively, outperforming conventional adsorbents
such as zeolites and activated carbons for each mixture. Structure–performance
relations revealed that COFs with pore sizes <10 Å are promising
adsorbents for all mixtures. We identified the gas adsorption sites
in the three top-performing COFs commonly identified for each mixture
by DFT calculations and computed the binding strength of gases, which
were found to be on the order of C
2
H
6
> CH
4
> N
2
> H
2
, supporting the GCMC
results.
Nucleus-independent chemical shift (NICS) indexes of aromaticity for
adsorption sites were calculated, and the results revealed that the
degree of linker aromaticity could be a measure for the selection
or design of highly alkane-selective COF adsorbents over N
2
and H
2
. Finally, COF membranes were shown to achieve
high H
2
permeabilities, 4.57 × 10
3
–
1.25 × 10
6
Barrer, and decent membrane
selectivities, as high as 4.3, outperforming polymeric and MOF-based
membranes for separation of H
2
from CH
4
.