Enhanced treatment of nitroaniline-containing wastewater by a membrane-aerated biofilm reactor: Simultaneous nitroaniline degradation and nitrogen removal

被引:19
|
作者
Mei, Xiang [1 ]
Wang, Yihan [1 ]
Yang, Yang [1 ]
Xu, Lijie [1 ]
Wang, Yong [2 ]
Guo, Zhongwei [1 ]
Shen, Wentian [1 ]
Zhang, Zimiao [1 ]
Ma, Mengyuan [1 ]
Ding, Yang [1 ]
Xiao, Yanyan [3 ]
Yang, Xu [3 ]
Yin, Chengqi [4 ]
Guo, Wei [1 ]
Xu, Kang [1 ]
Wang, Chaofan [1 ]
机构
[1] Nanjing Forestry Univ, Coll Biol & Environm, Nanjing 210037, Peoples R China
[2] Nanjing Univ, Sch Environm, State Key Lab Pollut Control & Resource Reuse, Nanjing 210023, Peoples R China
[3] Nanjing Haiyi Environm Protect Engn Co Ltd, Nanjing 211200, Peoples R China
[4] China Design Grp Co Ltd, Environm Protect Design & Res Ctr, Nanjing 210014, Peoples R China
基金
中国国家自然科学基金;
关键词
Nitroaniline-containing wastewater; Membrane-aerated biofilm reactor; Cometabolism; Acetic acid; Biological nitrogen removal; AMMONIA-OXIDIZING BACTERIA; P-NITROANILINE; CO-METABOLISM; CATALYTIC-REDUCTION; GRAPHENE OXIDE; CARBON SOURCE; 4-NITROANILINE; BIODEGRADATION; NANOPARTICLES; OXIDATION;
D O I
10.1016/j.seppur.2020.117078
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Nitroaniline (NA) is an aniline derivative with high toxicity, potential carcinogenicity and mutagenic effects. At present, the physical, chemical and biological methods used in NA-containing wastewater treatment usually suffer from problems such as low removal efficiency, high energy consumption and secondary pollution generation. In this study, a membrane-aerated biofilm reactor (MABR) was constructed to enhance the treatment of wastewater containing o-nitroaniline (2-NA) and p-nitroaniline (4-NA). The stratified biofilm and counter-diffusion of oxygen in the MABR were conducive to NA degradation. At a lower concentration, NA was primarily removed through direct oxidative degradation in the absence of the cometabolic substrate acetic acid, while at a higher concentration, NA was predominantly removed through oxidative degradation after reduction of NA in the presence of acetic acid. With an influent NA loading of 0.120 kg/(m(3).d), an aeration pressure of 40 kPa and an acetic acid dosing ratio of 2.0, the 2-NA and 4-NA removal loadings reached 0.058 and 0.060 kg/(m(3).d), respectively. Additionally, the chemical oxygen demand (COD) and total nitrogen (TN) removal rates were 82.40 and 88.52%, respectively. The MABR technology promoted simultaneous NA degradation and nitrogen removal from NA-containing wastewater treatment, illustrating its prospects for industrial application.
引用
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页数:12
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