This study examined the feasibility of applying an upflow anaerobic sludge
blanket (UASB) reactor to treat septage. The UASB reactor was operated at 3
5 +/- 1 degreesC, and the substrate septage had a total solids (TS) concent
ration of 13 200 mg/L. Reactor operation was initiated at a hydraulic resid
ence time (HRT) of 10 days; thereafter, the HRT was shortened stepwise to 1
.5 days. The TS, volatile solids (VS), and organic loading rates were 1.4 t
o 9.4 kg TS/m(3).d, 5.6 to 8.5 kg VS/m(3).d, and 1.1 to 6.7 kg chemical oxy
gen demand (COD)m(3).d, respectively. At the organic loading rate of 6.7 kg
COD/m(3).d (the HRT of 1.5 days), the total COD, soluble COD, and TS and V
S removal efficiencies were 68, 74, and 66 and 73%, respectively. The avera
ge granule diameter and volatile suspended solids concentration were approx
imately 0.89 mm and 32000 mg/L, respectively. Based on results obtained fro
m 7 months of constant methane production and removal efficiencies, which a
re comparable to values previously reported in the literature for wastewate
r, it was concluded that a UASB reactor can successfully treat septage.