An axial dispersion model for the operation of a fixed-bed adsorber with a
linear adsorption isotherm was formulated and solved analytically using the
separation of variables method. The asymptotic solution for a large Peclet
number and/or a small operation time was also obtained using two limiting
cases. The results can be used to correlate or to predict both the mass-tra
nsfer zones and the breakthrough curves of a fixed-bed adsorber. Influence
of both the Peclet number and the retardation coefficient on the operation
of a fired-bed adsorber was also studied As an example, the axial dispersio
n model was applied to the experimental data of the removal of phenol from
the solution in the activated carbon and the Amberlite resin XAD-4 fixed-be
d adsorbers.