Intensified activated sludge process with submerged membrane microfiltration
被引:57
|
作者:
Davies, WJ
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机构:
NW Water Ltd, Technol Dev Team, Ellesmere Port Effluent Treatment Works, Chester CH4 5JA, Cheshire, EnglandNW Water Ltd, Technol Dev Team, Ellesmere Port Effluent Treatment Works, Chester CH4 5JA, Cheshire, England
Davies, WJ
[1
]
Le, MS
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h-index: 0
机构:
NW Water Ltd, Technol Dev Team, Ellesmere Port Effluent Treatment Works, Chester CH4 5JA, Cheshire, EnglandNW Water Ltd, Technol Dev Team, Ellesmere Port Effluent Treatment Works, Chester CH4 5JA, Cheshire, England
Le, MS
[1
]
Heath, CR
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机构:
NW Water Ltd, Technol Dev Team, Ellesmere Port Effluent Treatment Works, Chester CH4 5JA, Cheshire, EnglandNW Water Ltd, Technol Dev Team, Ellesmere Port Effluent Treatment Works, Chester CH4 5JA, Cheshire, England
Heath, CR
[1
]
机构:
[1] NW Water Ltd, Technol Dev Team, Ellesmere Port Effluent Treatment Works, Chester CH4 5JA, Cheshire, England
intensified activated sludge;
membrane microfiltration;
process economics;
submerged biological contactor;
D O I:
10.1016/S0273-1223(98)00541-1
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
A pilot bio-reactor based on the Kubota membrane filtration system using screened domestic sewage has shown impressive results. Operating with an average MLSS of 16,000 mg/l and 4.5 hours HRT the bioreactor produced a very high quality effluent with typical values of 4 mg/l and 5 mg/l for BOD and NH4-N respectively. The sludge age from the bio-reactor was about 45 days. The cost of secondary treatment by membrane bio-reactor (including land and civil costs) starts from 12 p/m(3) for a 1.4 Ml/d plant and reduces to 6p/m(3) for a 22.5 Ml/d plant based on full treatment up to 3DWF. The corresponding treatment costs by conventional technologies are 13 p/m(3) for a 1.4 Ml/d SBC plant and 5 p/m(3) for a 22.5 Ml/d FBDA activated sludge plant. (C) 1998 Published by Elsevier Science Ltd. All rights reserved.