Many food products and pharmaceuticals industries are looking to integ
rating supercritical extraction and separations processes to fulfill p
rocessing needs due to limitations and regulations concerning the use
of organic solvents. One such technology, which may affect these indus
tries, is continuous supercritical adsorptive separation a processing
technology similar to the separation process of xylenes developed at U
OP. Many products like pharmaceuticals and other human consumables cou
ld be processed more economically and with higher purity by supercriti
cal fluid adsorption/desorption processes. Past studies, however, have
.focused on single-component adsorption/desorption involving a supercr
itical mobile phase, whereas adsorptive separations involving supercri
tical fluids are multicomponent systems. Accurate experimental techniq
ues which can determine both multicomponent solubilities in supercriti
cal fluids and multicomponent adsorption isotherms in the presence of
supercritical fluids, were developed to investigate the multicomponent
supercritical adsorption phenomenon. A dynamic column model developed
takes into account column dispersion as well as mass transfer and dif
fusive resistances. Experimental isotherm data incorporated into the m
odel can predict the breakthrough profiles. An extension of pulse chro
matography was used to identify the important hydrodynamic and transpo
rt parameters, and operating conditions are identified for optimal sep
arations.