The anaerobic fluidized bed (AFB) reactor, using spherical granular ac
tivated carbon (GAC) particles as the media, is evaluated for the pret
reatment of hog wastewater. A laboratory investigation is performed to
assess the effects of organic loading-rate on organic removal and met
hane production. The experimental evidence indicates that good removal
of five-day biochemical oxygen demand (BOD5) (filtered and unfiltered
) and filtered chemical oxygen demand (GOD) (i.e., >60%) can be achiev
ed at loadings as high as 10.4 g unfiltered COD L/d. On the other hand
, the removal of unfiltered COD was unsatisfactory because of the pres
ence of high volatile suspended solids (VSS) concentrations in AFB eff
luents. The observed specific methane yield decreases with increasing
loadings; however, the biogas produced is rich in methane, especially
at low loadings. Attached biomass densities ranging from 0.01 to 0.024
g volatile solids (VS)/g carbon are attainable, which accounts for >9
9% of total reactor VS. Therefore, the GAC particles used are conduciv
e for buildup of attached biomass in AFB reactors.