Azo dye wastewater treatment in a bioelectrochemical-aerobic integrated system: effect of initial azo dye concentration and aerobic sludge concentration

被引:5
作者
Cui, Min-Hua [1 ,2 ]
Gao, Jian [3 ]
Wang, Ai-Jie [2 ,4 ]
Sangeetha, Thangavel [5 ,6 ]
机构
[1] Jiangnan Univ, Sch Environm & Civil Engn, Jiangsu Key Lab Anaerob Biotechnol, Wuxi 214122, Jiangsu, Peoples R China
[2] Harbin Inst Technol, State Key Lab Urban Water Resource & Environm, Harbin 150090, Heilongjiang, Peoples R China
[3] China Construct Municipal Engn Corp Ltd, Beijing 100071, Peoples R China
[4] Chinese Acad Sci, Res Ctr Ecoenvironm Sci, Key Lab Environm Biotechnol, Beijing 100085, Peoples R China
[5] Natl Taipei Univ Technol, Dept Energy & Refrigerating Air Conditioning Engn, Taipei 10608, Taiwan
[6] Natl Taipei Univ Technol, Res Ctr Energy Conservat New Generat Residential, Taipei 10608, Taiwan
关键词
Azo dye wastewater; Electrochemical-aerobic integrated system; Initial azo dye concentration; Coulombic efficiency; Sludge concentration; DECOLORIZATION; REACTOR; BIOELECTRICITY; DEGRADATION; REDUCTION; ELECTRON; REMOVAL; DESIGN;
D O I
10.5004/dwt.2019.24395
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An integrated system that consisted of a bioelectrochemical reactor (BER) and an aerobic completely stirred tank reactor (ACSTR) was constructed to treat simulated wastewater mixed with azo dye Acid Orange 7 (AO7) and real municipal wastewater. It was found that AO7 could be efficiently decolorized in BER within 6 h while initial concentration fluctuated from 25 to 100 mg/L. With an initial AO7 concentration of 75 mg/L, BER reached a decolorization efficiency of 93.65 +/- 2.45% at 6 h and contributed 26.56 +/- 8.91% of chemical oxygen demand (COD) removal. Coulombic efficiency (CE) of current generation varied from 23.19 +/- 6.96 to 37.23 +/- 3.48% and CE for AO7 decolorization decreased from 30.45 +/- 3.19 to 14.59 +/- 1.21% at the initial AO7 concentration of 50 mg/L, which illustrated the important contribution of electrochemical reduction on AO7 decolorization. The effluent of BERs can be subsequently refined by ACSTR, the residual COD was 72 +/- 10 mg/L after 6 h treatment with an activated sludge concentration of 6000 mg/L. Further increasing the sludge concentration to 9000 mg/L, final COD concentration decreased to 62 +/- 7 mg/L. Results showed that the bioelectrochemical-aerobic integrated system effectively treated the mixed azo dye containing wastewater.
引用
收藏
页码:314 / 320
页数:7
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