Simultaneous decarburization, nitrification and denitrification (SDCND) in coking wastewater treatment using an integrated fluidized-bed reactor

被引:20
|
作者
Li, Kui [1 ]
Wu, Haizhen [1 ]
Wei, Jingyue [2 ,4 ]
Qiu, Guanglei [2 ]
Wei, Chaohai [2 ]
Cheng, Dangyu [3 ]
Zhong, Lianwen [3 ]
机构
[1] South China Univ Technol, Sch Biol & Biol Engn, Guangzhou 510006, Guangdong, Peoples R China
[2] South China Univ Technol, Sch Environm & Energy, Guangzhou 510006, Guangdong, Peoples R China
[3] Huaxin Environm Technol Co, Shaoguan 512122, Peoples R China
[4] Gifu Univ, River Basin Res Ctr, Gifu 5011193, Japan
基金
中国国家自然科学基金;
关键词
Coking wastewater; Integrated fluidized-bed reactor; Carbon and nitrogen removal; Differential DO distribution; Microbial community; MICROBIAL COMMUNITY COMPOSITION; POLYCYCLIC AROMATIC-HYDROCARBONS; ANOXIC-OXIC PROCESS; SP NOV; GEN; NOV; NITROGEN REMOVAL; BACTERIUM; PERFORMANCE; FATE; DEGRADATION;
D O I
10.1016/j.jenvman.2019.109661
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
There are two problems in biological treatment of coking wastewater (CWW): incapability of pre-anaerobic treatment to eliminate the toxicity in wastewater, and the lack of carbon source for subsequent denitrification in pre-aerobic treatment. To achieve simultaneous decarburization, nitrification and denitrification (SDCND) in CWW treatment, biological carrier materials was used to build an integrated fluidized-bed reactor (Reactor B, RB). A conventional fluidized-bed reactor (Reactor A, RA) was used as a control reactor under the same condition. The results showed that RB was more advantageous since its removal efficiencies of COD and TN were 90% and 87%, respectively, which were significantly higher than these in RA (82% and 45%), at a hydraulic retention time (HRT) of 60 h. Microelectrode measurement indicated that oxygen transfer was limited inside the carrier where the formation of a dissolved oxygen (DO) concentration gradient was observed. Microbial community analysis showed that the aerobic and anoxic microenvironments in RB promoted the co-existence of a wider variety of bacteria, thus achieving SDCND. These results indicated the integrated fluidized-bed reactor exhibited promising feasibility for simultaneous carbon and nitrogen removal in CWW treatment under the same aeration driven conditions. The SDCND process realized by fluidized-bed reactor provided a reference for the treatment of toxic industrial wastewater with high carbon to nitrogen ratio.
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页数:8
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