Performance limits in large scale simulated moving bed ion exclusion o
r ligand exchange chromatography are imposed by three basic variables,
process design, column design and resin kinetics. A column de sign wi
th specific internal flow straighteners has been developed to meet the
need for uniform cross-sectional distribution/collection, and vertica
l plug flow in large industrial size chromatography columns by dividin
g the cross-sectional area of the column into smaller segments. It is
suggested that maximum operating efficiency will be obtained through t
he use of minimum resin particle size and narrow particle size distrib
ution to maintain uniform sorption and de-sorption rates. Commercially
available resins are tested in respect to their separating efficiency
, It was demonstrated that gel-type cation exchange resins which have
similar measurable properties such as % crosslinking (water content),
operating capacity, mean particle size and particle size distribution,
display similar kinetic properties in pulse tests for separating sucr
ose from nonsugars.