A feasibility investigation of a pilot-scale bioelectrochemical coupled anaerobic digestion system with centric electrode module for real membrane manufacturing wastewater treatment

被引:14
作者
Xie, Jiawei [1 ]
Zou, Xinyi [1 ]
Chang, Yaofeng [1 ]
Liu, He [2 ]
Cui, Min-Hua [2 ]
Zhang, Tian C. [3 ]
Xi, Jiajian [5 ]
Chen, Chongjun [1 ,4 ,6 ]
机构
[1] Suzhou Univ Sci & Technol, Sch Environm Sci & Engn, Suzhou 215009, Peoples R China
[2] Jiangnan Univ, Sch Environm & Civil Engn, Wuxi 214122, Peoples R China
[3] Univ Nebraska, Civil & Environm Engn Dept, Omaha, NE USA
[4] Suzhou Univ Sci & Technol, Jiangsu Collaborat Innovat Ctr Technol & Mat Water, Suzhou 215009, Peoples R China
[5] Suzhou Sujing Environm Engn Co Ltd, Suzhou 215200, Peoples R China
[6] Xuefu Rd 99, Suzhou 215009, Peoples R China
基金
中国国家自然科学基金;
关键词
Bioelectrochemical system; Anaerobic digestion; Pilot-scale; Electrode module; Membrane manufacturing wastewater; AZO-DYE DECOLORIZATION; REMOVAL; REACTOR; PERFORMANCE; COMMUNITY; CELL;
D O I
10.1016/j.biortech.2022.128371
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The large-scale application of bioelectrochemical coupled anaerobic digestion (BES-AD) is limited by the matching of electrode configuration and the applicability of real wastewater. In this study, a pilot-scale BES-AD system with an effective system volume of 5 m3 and a 1 m3 volume of a carbon fiber brush electrode module was constructed and tested for treatment of the membrane manufacturing wastewater. The results showed that the BOD5/COD of the wastewater was increased from 0.238 to 0.398 when the applied voltage was 0.9 V. The pollutants such as N, N-Dimethylacetamide and glycerol in wastewater were degraded significantly. The microorganisms in the electrode modules were spatially enriched. The fermenters (Norank_f__ML635J-40_aquatic_group, 6.55 %; unclassified_f__Propionibacteriaceae, 5.25 %) and degraders (Corynebacterium, 29.31 %) were mostly enriched at the bottom, while electroactive bacteria (Pseudomonas, 29.39 %, Geobacter, 7.86 %) were mostly enriched at the top. Combined with the economical construction and operation cost ($1708.8/m3 and $0.76/m3) of the BES-AD system.
引用
收藏
页数:12
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