In ideal displacement chromatography (systems with infinite mass-transfer k
inetics), various solutes are separated by sharp discontinuities In real sy
stems, however, the shocks are eroded into shock layers because of the fini
te rates of mass transfer The thickness of these shock layers, which can re
duce the yields achievable in these systems, depend on the flow rate, parti
cle diameter and the "difficulty" of these separations. The steric mass act
ion formalism of ion-exchange chromatography was toed in concert with a sol
id film lineal driving force model to describe the effects of flow rate, pa
rticle diameter; and the degree of difficulty of the separation on ion-exch
ange displacement systems. Simple pulse techniques are employed to estimate
the thermodynamic and mass-transfer parameters. The simulations are then c
ompared to experimental results over a range of conditions. The results dem
onstrate that this relatively simple modeling approach can be employed to d
escribe the behavior of these nonideal displacement systems.