Comparison of ozone-based AOPs on the removal of organic matter from the secondary biochemical effluent of coking wastewater

被引:0
作者
Ji, Yuxian [1 ]
Wang, Chunrong [1 ,3 ]
He, Lei [1 ]
Chen, Xiaoya [1 ]
Wang, Jianbing [1 ]
Zhang, Xian [1 ,2 ]
Du, Qingbang [1 ]
机构
[1] China Univ Min & Technol Beijing, Sch Chem & Environm Engn, Beijing, Peoples R China
[2] Inner Mongolia Univ Technol, Hohhot, Peoples R China
[3] China Univ Min & Technol Beijing, Sch Chem & Environm Engn, Ding 11,Xueyuan Rd, Beijing 100083, Peoples R China
关键词
Advanced oxidation processes; Ozone-based process; Organic matter; Coking wastewater; Fluorescence spectroscopy; LANDFILL LEACHATE TREATMENT; ELECTROCHEMICAL OXIDATION; OZONATION; PHENOL; TRANSFORMATION; OPTIMIZATION; O-3/H2O2; TOXICITY; SLUDGE; PAPER;
D O I
10.1080/09593330.2022.2158759
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Advanced oxidation processes (AOPs) based on ozone are gaining continuously growing popularity in wastewater treatment. This study explored the treatment of coking wastewater using a combination of ozonation (O-3), ultraviolet (UV), and hydrogen peroxide (H2O2) process expressed by % chemical oxygen demand (COD) removal, % total organic carbon (TOC), % UV254, % fluorescence intensity removal and its electrical energy consumption. The obtained results demonstrated that, the combination of O-3, UV, and H2O2 which is denoted by O-3/UV/H2O2 in this study achieved great success in COD removal (92.08%), TOC removal (78.25%), and reduction of fluorescence intensity (99.82%). Compared with the O-3 and O-3/UV processes, O-3/UV/H2O2 improved the COD removal by approximately 54-69% and 38-51%, respectively. In addition, the energy consumption was reduced by 53-67%. The TOC removal rate in the effluent ranged 71% and 83%, while the UV254 removal rate was up to 90%. The fluorescence spectroscopy showed that the O-3/UV/H2O2 combination process reduced the fluorescence intensity by almost 97% within 10 min. Furthermore, the total polycyclic aromatic hydrocarbons (PAHs) concentration in the effluent was less than 10 mu g/L (removal efficiency > 80%) and the most toxic benzo(a)pyrene (BaP) was less than 0.03 mu g/L (0.018 mu g/L). In addition, the energy consumption of the O-3/UV/H2O2 process was 53-67% lower than those of O-3 and O-3/UV processes. Furthermore, the energy consumption was 80.26 kWh m(-3) after 60 min of reaction time when the COD (69.3 mg/L) met the standard discharge. Finally, the O-3/UV/H2O2 process could be an effective method for improving the mineralisation of refractory organic matter.
引用
收藏
页码:1943 / 1955
页数:13
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