For mixture separations, metal–organic
frameworks (MOFs)
are of practical interest. Such separations are carried out in fixed
bed adsorption devices that are commonly operated in a transient mode,
utilizing the pressure swing adsorption (PSA) technology, consisting
of adsorption and desorption cycles. The primary objective of this
article is to provide an assessment of the variety of metrics that
are appropriate for screening and ranking MOFs for use in fixed bed
adsorbers. By detailed analysis of several mixture separations of
industrial significance, it is demonstrated that besides the adsorption
selectivity, the performance of a specific MOF in PSA separation technologies
is also dictated by a number of factors that include uptake capacities,
intracrystalline diffusion influences, and regenerability. Low uptake
capacities often reduce the efficacy of separations of MOFs with high
selectivities. A combined selectivity–capacity metric, Δ
q
, termed as the separation potential and calculable from
ideal adsorbed solution theory, quantifies the maximum productivity
of a component that can be recovered in either the adsorption or desorption
cycle of transient fixed bed operations. As a result of intracrystalline
diffusion limitations, the transient breakthroughs have distended
characteristics, leading to diminished productivities in a number
of cases. This article also highlights the possibility of harnessing
intracrystalline diffusion limitations to reverse the adsorption selectivity;
this strategy is useful for selective capture of nitrogen from natural
gas.