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Sludge reduction and nutrient removal from an anaerobic/anoxic/oxic(A2/O) process coupled with a modified oxic-settling-anaerobic process
被引:2
|作者:
Sun, Lianpeng
[1
,2
]
Wang, Yushan
[1
]
Xu, Wenli
[1
]
Lin, Yuji
[1
]
Lin, Meishan
[3
]
Luo, Wangxing
[1
]
Shi, Chenyi
[1
]
机构:
[1] Sun Yat Sen Univ, Sch Environm Sci & Engn, Guangzhou 510275, Guangdong, Peoples R China
[2] Sun Yat Sen Univ, Guangdong Prov Key Lab Environm Pollut Control &, Guangzhou 510275, Guangdong, Peoples R China
[3] Foshan Water Grp, Foshan 528000, Peoples R China
关键词:
Anaerobic;
A2/O-MOSA process;
Sludge reduction;
Sludge;
Municipal sewage;
WASTE-WATER TREATMENT;
SIDE-STREAM REACTOR;
EXCESS SLUDGE;
ACTIVATED-SLUDGE;
MEMBRANE BIOREACTOR;
OSA PROCESS;
PRETREATMENT;
PHOSPHORUS;
DISINTEGRATION;
MICROBIOLOGY;
D O I:
10.5004/dwt.2018.22026
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
There is little research that focused on both nutrient removal and sludge reduction based on an anaerobic/anoxic/oxic(A2/O) process. In this study, two systems that consisted of an A2/O process combined with a modified oxic-settling-anaerobic (MOSA) reactor were run for 200 d at the lab-scale to evaluate their effect on sludge reduction and their influence on nutrients removal. The MOSA reactor was run a hydraulic retention time of 5 d and interchange rate of 10%. Our results showed that A2/O-MOSA system performed as well as an A2/O system for removing Chemical Oxygen Demand (COD), ammonia, total nitrogen, and total phosphorus. The A2/O-MOSA system removed an average of 92% of the influent COD, slightly higher than that in the A2/O (90%) system. As for sludge reduction efficiency, the A2/O-MOSA process achieved a sludge reduction of 24%and sludge decay contributed 58% to this sludge reduction.
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页码:144 / 151
页数:8
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