An intermittently aerated membrane bioreactor using a submerged hollow fibe
r membrane was applied in laboratory scale to treat household wastewater in
cluding toilet flushing water. Nitrogen removal was optimized with intermit
tent aeration of the reactor and adjusting the time lengths of anoxic and a
erobic phases of a cycle. Membrane filtration occurred during the aeration
period to take advantage of the air bubbles for fouling control. With 8-15
h HRT and a very long SRT, 96% of TCOD and 100% SS could be removed. On ave
rage, the removal efficiency for TN was 83%. No significant accumulation of
inert matter was observed after 4 and 5 months of operations without sludg
e wasting. Fast and complete nitrification was accomplished regardless of t
he operation cycle mode, and denitrification appears to be the rate-limitin
g step. Results from track studies revealed that the specific denitrificati
on rate (SDNR) varied between 0.6 and 1.8 mg/gVSS h. Endogenous SDNR was de
termined in a separate batch experiment and found to be 0.56 mg/gVSS.h. A l
inear relationship between the measured SDNR and the influent BOD/TN value
was found. Based on this relationship, a rule-of-thumb method to determine
the optimum time length for the anoxic phase was proposed. Intermittently a
erated MBR appears to have advantages over other biological nitrogen remova
l processes in that denitrification can be enhanced under high MLVSS condit
ions. Endogenous denitrification may pray a significant role, making the sy
stem more robust to the fluctuation or the limitation of external carbon su
pply.