The models developed in the first part of this study are applied to predict
the removal of 4-nitrophenol by powdered activated carbon (PAC) in a bench
-scale reactor. A series of continuous-flow filtration experiments were con
ducted with different carbon doses to verify the modeling approach when the
activated carbon was added directly to the membrane reactor, either as ste
p or pulse input, and when the carbon was dosed as a step input to a contin
uous-flow stirred tank reactor followed by the membrane reactor. The models
predicted well the experimental data for all cases investigated. The verif
ied model was used to investigate the effect of various operating parameter
s on the efficiency of the adsorption process. This analysis included the e
ffect of filtration time, membrane reactor volume, dosing procedure, and th
r effect of dosing the carbon in reactors installed in series upstream of t
he membrane reactor.