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电-多相臭氧催化工艺深度处理焦化废水
引用本文:李新洋,李燕楠,祁丹阳,张昊,陈安生,于晓华,姚宏.电-多相臭氧催化工艺深度处理焦化废水[J].中国环境科学,2021,40(10):4354-4361.
作者姓名:李新洋  李燕楠  祁丹阳  张昊  陈安生  于晓华  姚宏
作者单位:1. 北京交通大学土木建筑工程学院, 抗生素/抗性基因水环境污染控制技术北京市国际科技合作基地, 北京 100044;2. 北京交通大学水中典型污染物控制与水质保障北京市重点实验室, 北京 100044
基金项目:北京卓越青年科学家项目(BJJWZYJH01201910004016);北京市优秀人才青年骨干计划(2018000020124G056)
摘    要:本文采用新型电-多相臭氧催化(E-catazone)工艺深度处理焦化废水生化二级出水,开展工艺可行性研究.通过与O3/TiO2纳米花(TiO2-NF)与O3/TiO2-NF/H2O2及单独电化学氧化工艺相比较,对E-catazone工艺技术优势及氧化机理进行探究.结果表明:在相同条件下(O3浓度84mg/L),电-多相臭氧催化获得的COD和TOC的去除率(分别为67.9%,50.0%)显著优于O3/TiO2-NF获得的去除率(25.8%,20.9%),即便在O3/TiO2-NF体系中投加5g/L的H2O2以促进臭氧均相催化效果,但COD和TOC去除率也仅分别提高到63.6%,43.6%.

关 键 词:焦化废水  电-多相臭氧催化  二氧化钛  羟基自由基  

Study on electrochemical heterogeneous catalytic ozonation process for treatment of coking wastewater
LI Xin-yang,LI Yan-nan,QI Dan-yang,ZHANG hao,CHEN An-sheng,YU Xiao-hua,YAO hong.Study on electrochemical heterogeneous catalytic ozonation process for treatment of coking wastewater[J].China Environmental Science,2021,40(10):4354-4361.
Authors:LI Xin-yang  LI Yan-nan  QI Dan-yang  ZHANG hao  CHEN An-sheng  YU Xiao-hua  YAO hong
Affiliation:1. Beijing International Scientific and Technological Cooperation Base for Antibiotics and Resistance Gens Control, School of Civil Engineering and Architecture, Beijing Jiaotong University, Beijing 100044, China;2. Beijing Key Laboratory of Aqueous Typical Pollutants Control and Water Quality Safeguard, Beijing Jiaotong University, Beijing 100044, China
Abstract:In this paper, a new electric-heterogeneous ozone-catalyzed (E-catazone) process was used in advanced treatment of the secondary biochemical effluent from coking wastewater, and the process's feasibility was also studied. By comparing the E-catazone process with three other processes:the O3/TiO2 nanoflowers (TiO2-NF) process, the O3/TiO2-NF/H2O2 process, and the electrochemical oxidation process (EO), the technological advantages and oxidation mechanism of E-catazone were investigated. Under the same conditions (O3 concentration of 84mg/L), the removal rates of COD and TOC (67.9%, 50.0%) in E-catazone process were significantly superior to the performance (25.8%, 20.9%) in O3/TiO2-NF process. Even with 5g/L of H2O2 added in the above O3/TiO2-NF system to promote homogeneous ozone catalytic ability, the obtained removal rates of COD and TOC had only increased to 63.6% and 43.6%, respectively. The performance of O3/TiO2-NF/H2O2 system was still not as good as the E-catazone process.
Keywords:coking wastewater  electrochemical heterogeneous catalytic ozonation  titanium dioxide  hydroxyl radical  
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