Flux decline behaviors in dead-end microfiltration of activated sludge and its supernatant

被引:36
作者
Iritani, E.
Katagiri, N.
Sengoku, T.
Yoo, K. M.
Kawasaki, K.
Matsuda, A.
机构
[1] Nagoya Univ, Dept Chem Engn, Chikusa Ku, Nagoya, Aichi 4648603, Japan
[2] Ehime Univ, Dept Appl Chem, Matsuyama, Ehime 7908577, Japan
关键词
microfiltration; membrane filtration; activated sludge; supernatant; cake compressibility;
D O I
10.1016/j.memsci.2007.04.041
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The properties of dead-end microfiltration were explored under constant pressure using two types of activated sludge controlled under the condition of different air flow rates. The activated sludge cultured at the air flow rate of 0.15 L min(-1) (the anaerobic condition) exhibited a significant flux decline compared with the case of the air flow rate of 2.33 L min(-1) (the aerobic condition). It was found from the results of microfiltration of the supernatant separated by centrifugation that the constituents in the Supernatant caused a major cake resistance in microfiltration of the activated sludge. The average specific filtration resistance for filtration of the activated sludge was closely consistent with that for filtration of the supernatant at low pressure (49 kPa). However, the cake resistance of the microbial floc in microfiltration of the activated sludge became substantial with increasing filtration pressure because of high compressibility of the microbial floc. Moreover, the foulant and the fouling mechanism in microfiltration of the supernatant were evaluated from both microfiltration test of the supernatant and rnicrofiltration test of the filtrate collected thereby. As a result, the effects of the pore size and material of the microfiltration membrane on the flux decline behaviors in dead-end microfiltration were reasonably elucidated. (C) 2007 Elsevier B.V.. All rights reserved.
引用
收藏
页码:36 / 44
页数:9
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