A 162-day pilot-scale operation for reclamation of urban wastewater was stu
died by using an ultrafiltration membrane bioreactor (UMBR). Performance of
the UMBR was investigated with a sludge retention time (SRT) of 5, 15, and
30 days, a hydraulic retention time (HRT) of 5 h, and membrane flux betwee
n 75 and 1501 m(-2) h(-1), respectively. It was observed that the highest s
ludge concentration in the reactor viz. a suspended solids (SS's) concentra
tion of 23.1 g l(-1) and a volatile suspended solids (VSS's) concentration
of 13.5 g l(-1), respectively, could be reached. The ratio of sludge VSS to
sludge chemical oxygen demand (COD) was 1.428 in the study, which approxim
ated to the theoretical value of 1.415. Mass loading rates of the UMBR were
close to those of conventional activated sludge processes (CASP's), while
the volumetric loading rates were two to five times those of GASP. Averaged
97% of GOD, 96.2% of ammonia nitrogen (NH3-N), and 100% of SS's were remov
ed. It was found that the bioreactor was responsible for 85% of COD removal
, while 12% was due to separation of the membrane module. The reclaimed wat
er could be reused directly for municipal purposes or indirectly for indust
rial uses after additional treatment. (C) 2000 Elsevier Science B.V. All ri
ghts reserved.