Analysis of the mixing performance of a full-scale membrane bioreactor for municipal wastewater treatment

被引:2
|
作者
Wu, Qing [1 ]
Yan, Xiaoxu [1 ]
Xia, Xue [1 ]
Zhang, Changyong [1 ]
Xue, Tao [1 ]
Yu, Kaichang [1 ]
Liang, Peng [1 ]
Huang, Xia [1 ]
机构
[1] Tsinghua Univ, State Key Joint Lab Environm Simulat & Pollut Con, THU Beijing Origin Water Joint Res Ctr Environm M, Sch Environm, Beijing 100084, Peoples R China
基金
中国国家自然科学基金;
关键词
Full-scale membrane bioreactor; Mixing performance; Residence time distribution; Dead zone; COMPUTATIONAL FLUID-DYNAMICS; OPTIMIZATION; TRACER; CHINA;
D O I
10.1016/j.biortech.2017.11.073
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
High energy consumption remains to be a key problem for application of membrane bioreactor (MBR). Optimization of MBR to save energy requires a compressive understanding of the performance of the reactor, among which the mixing performance is a significant parameter, however received little attention. In this study, a tracer experiment was carried out in a full-scale MBR for municipal wastewater treatment in China. The mixing performance of both the entire plant and the membrane tanks were evaluated. The entire plant was found to be a cascade of 2.15 continuous stirred tank reactors (CSTRs) with 8.02% of dead zones. The membrane tanks were also found to deviate from CSTR. The mixing energy was analyzed and compared with literature data from three aspects: the specific power used per unit of tank volume (P-s,P-v), per unit of permeate volume (P-s,P-p), and per unit of membrane area (P-s,P-m).
引用
收藏
页码:932 / 935
页数:4
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