Critical analysis of submerged membrane sequencing batch reactor operating conditions

被引:30
|
作者
McAdam, E [1 ]
Judd, SJ
Gildemeister, R
Drews, A
Kraume, M
机构
[1] Cranfield Univ, Sch Water Sci, Cranfield MK43 0AL, Beds, England
[2] Tech Univ Berlin, Dept Chem Engn, D-13355 Berlin, Germany
关键词
sequencing batch reactor; microfiltration; submerged; fouling;
D O I
10.1016/j.watres.2005.07.028
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
To evaluate the Submerged Membrane Sequencing Batch Reactor process, several short-term studies were conducted to define critical flux, membrane aeration and intermittent filtration operation. Critical flux trials indicated that as mixed liquor suspended solids increased in concentration so would the propensity for membrane fouling. Consequently in order to characterise the impact of biomass concentration increase (that develops during permeate withdrawal) upon submerged microfiltration operation, two longer term studies were conducted, one with a falling hydraulic head and another with a continuous hydraulic head (as in membrane bio-reactors). Trans membrane pressure data was used to predict the maximum possible operating periods at 10 and 62 days for the falling hydraulic head and continuous hydraulic head respectively. Further analysis revealed that falling hydraulic head operation would require 21% more aeration to maintain a consistent crossflow velocity than continuous operation and would rely on pumping for full permeate withdrawal 80% earlier. This study concluded that further optimisation would be required to make this technology technically and economically viable. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4011 / 4019
页数:9
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