A simulated high-strength industrial wastewater containing acetate, ph
enol, and orthochlorophenol (2-CP) was treated using an anaerobic flui
dized-bed granular activated carbon (GAC) reactor. Although carbon rep
lacement was initiated to maintain the effluent quality from the react
or and to minimize the inhibitory effects of 2-CP, the latter phase of
this study demonstrated that carbon replacement was not necessary. A
large pulse input of organic feed was introduced to investigate the re
silience of the reactor to severe and sudden increases in influent org
anic loading. With appropriate pH adjustment, the reactor stabilized w
ithin less than two days. A mathematical model was developed to invest
igate the interaction between the adsorption and biodegradation of com
pounds in the reactor during the large pulse input. The model confirme
d that the GAC was instrumental in controlling the buildup of 2-CP in
the reactor.