ADVANCED PERFORMANCE OF SMALL-SCALE DOMESTIC SEWAGE-TREATMENT PLANTS USING ANAEROBIC-AEROBIC FILTER SYSTEMS WITH FLOW-EQUALIZATION AND RECIRCULATION
Citation
T. Iyo et al., ADVANCED PERFORMANCE OF SMALL-SCALE DOMESTIC SEWAGE-TREATMENT PLANTS USING ANAEROBIC-AEROBIC FILTER SYSTEMS WITH FLOW-EQUALIZATION AND RECIRCULATION, Environmental technology, 17(11), 1996, pp. 1235-1243
Categorie Soggetti
Environmental Sciences
SICI code
0959-3330(1996)17:11<1235:APOSDS>2.0.ZU;2-C
Abstract
The treatment characteristics of small-scale domestic sewage treatment
plants (SDSTP) using anaerobic-aerobic filler systems with flow-equal
ization and recirculation were investigated. Plant experiments were co
nducted under three different operating conditions (Runs 1, 2, and 3),
and were carried out in sequence using the same SDSTP. Run 1 was the
control series with continuous fixed feeding and recirculation In Runs
2 and 3, the influent had two maximum flow rates (peak coefficient 6)
and a feeding time of 14 hours. This inflow pattern simulates the typ
ical inflow pattern of domestic sewage. Run 2 was an operating series
with no flow-equalization and no recirculation, and was the convention
al treatment mode for SDSTPs installed in Japan. On the other hand, th
e SDSTP in Run 3 had a novel operational mode with flow-equalization a
nd recirculation for denitrification. The SDSTP in Run 3 demonstrated
a high performance for flow-equalization and stable effluent quality i
n comparison with that in Run 2. In Run 3, the removal percentages of
BOD and SS were more than 90%, the effluent BOD was less than 10 mg l(
-1), and the effluent SS was less than 5 mg l(-1). The nitrogen remova
l and effluent nitrogen in Run 3 were about 60% and less than 10 mg l(
-1), respectively. The treatment efficiency in Run 3 was almost the sa
me as that in Run 1. Furthermore, it is suggested that flow-equalizati
on and denitrification could reduce sludge production.