This study examined the feasibility of applying a membrane bioreactor
to small wastewater treatment using a pilot-scale plant. The operation
was continued for 336 days. From the start to 251st day, the operatio
n was continued without membrane washing. During the latter term of th
e operation, however, suction pressure increased rapidly corresponding
to the increase of sludge viscosity. Because sludge viscosity increas
e occurred right after the suspension of sludge wasting, excess sludge
must be wasted at regular intervals in order to keep low sludge visco
sity. More than 90% of organic matter, suspended solids; and coliform
bacteria were successfully removed. As far as nitrogen removal was con
cerned, denitrification was the rate determining step in this system.
To enhance denitrification, the following three points should be consi
dered: i) to concentrate inflow of raw sewage at the beginning of anox
ic period, ii) to shorten aeration time, and iii) to maintain high MLS
S concentration. Copyright (C) 1996 IAWQ. Published by Elsevier Scienc
e Ltd.