Our work involves experimental and simulation studies of the adsorption bre
akthrough and equilibria of ethyl benzene (a pollutant commonly encountered
in industrial waste streams) on activated carbon in the presence of superc
ritical carbon dioxide. Frontal and single breakthrough saturations were an
alyzed for a range of operating conditions of pressure (100-130 bar) and te
mperature (313-338 K). The equilibrium data correlated well with the Langmu
ir isotherm. The adsorption process was successfully modeled by a three-par
ameter model with comparable fitting parameters for the two types of breakt
hrough curves.