A cyclic chromatographic process based on the method of column switchi
ng was used to separate a three-component carbohydrate mixture. It per
mits continuous introduction of the feed and is designed to produce hi
gher product concentration compared to a normal elution cyclic process
. A fixed-bed model incorporating axial dispersion and a linear drivin
g force for mass transfer was successfully used to estimate optimum op
erating conditions (switch times and fluid-flow rates). Its experiment
al setup can be easily constructed by modifying the apparatus of a sim
ulated countercurrent process since both systems comprise segmented co
lumns equipped with on-off valves for fluid-flow control. This allows
one to conduct either multicomponent separation based on elution opera
tion or binary separation based on countercurrent operation using esse
ntially the same set of experimental apparatus with minor modification
.