Recuperative parametric pumping in adsorptive membranes, a cyclical ad
sorptive separation process, can lead to two distinct mechanisms of se
paration: rejection and preferential transport. During rejection, the
adsorptive membrane rejects an adsorbing solute while permitting the t
ransport of nonadsorbing solutes. During preferential transport the re
verse occurs; the adsorptive membrane selectively transports an adsorb
ing solute while preventing the transport of nonadsorbing solutes. Swi
tching fr om rejection to preferential transport can be accomplished b
y merely decreasing the ratio of the stroke volume (cyclical volume of
solution pumped into and out of the membrane) to the membrane void vo
lume. Preferential transport, earlier called an ''inverse separation,
''results from the adsorbing solute crossing over from an adsorbing to
a desorbing region in the interior of the membrane and is governed by
the shape of the equilibrium isotherms and by process variables In ex
periments with lysozyme and a membrane chromatography cartridge, selec
tivities obtained by preferential transport were on the order of 5 and
agreed With theoretical predictions. Theoretical predictions suggest
that to further improve separation by preferential transport, experime
nts need to be conducted on low dispersion membranes (Pe > 10(4)) and
that both rejection and preferential transport can lead to continuous
concentrated streams of the adsorbing solutes.