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首页> 外文期刊>Separation and Purification Technology >Simultaneous membrane fouling mitigation and emerging pollutant benzophenone-3 removal by electro-peroxone process
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Simultaneous membrane fouling mitigation and emerging pollutant benzophenone-3 removal by electro-peroxone process

机译:电氧化物过程同时膜污垢缓解和新出现的污染物二苯甲酮-3

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摘要

In this work, the effects of electro-peroxone (E-peroxone, i.e. combination of ozonation and electrolysis using a carbon based cathode) assistance on microfiltration (MF) was systematically investigated from the performance and mechanism viewpoints. Results show that E-peroxone oxidation exhibited better ability than individual processes in membrane fouling mitigation when using bovine serum albumin (BSA), humic acid (HA) and silicon dioxide (SiO2) particles as model foulants. The relative fluxes at 250 s E-peroxone assisted MF treatment were determined to be similar to 0.30-0.71, which are > 15% higher than those in single ozonation or electrolysis assisted MF process. The efficiency of E-peroxone process in membrane fouling reduction was positively correlated with the applied voltage (0-4 V) and inlet ozone concentration (0-48.6 mg/L). The experimental data combined with three-dimensional excitation-emission matrix fluorescence spectra (3D EEMs) analysis indicate that simultaneous fouling mitigation and emerging pollutant benzophenone-3 (BP3) removal could be obtained during actual river water treatment. Furthermore, the comparison tests reveal that generation of hydroxyl radicals (HO center dot) via enhanced O-3/H2O2 decomposition had a significant role on the organic contaminant degradation and membrane fouling mitigation in E-peroxone assisted MF process, and the introduced electrostatic repulsion force could also contribute to the fouling reduction. These observations suggest that E-peroxone maybe a feasible assistive method for membrane filtration water treatment.
机译:在这项工作中,系统地研究了从性能和机构的观点来系统地研究了电 - 过氧化荡(E-过氧锆,即使用碳基阴极的烃基阴极的组合和电解的组合)辅助对微滤(MF)的辅助。结果表明,当使用牛血清白蛋白(BSA),腐殖酸(HA)和二氧化硅(SiO 2)颗粒作为模型污垢时,E-氧化物氧化表现出比膜污染缓解的个体过程更好。确定在250秒的E-过氧硅辅助MF处理中的相对通量与0.30-0.71相似,比单一臭氧或电解辅助MF工艺高出0.30-0.71。膜污染物中的e-过氧化物过程的效率与施加的电压(0-4V)和入口臭氧浓度(0-48.6mg / L)正相关。与三维激发发射矩阵荧光光谱(3D EEM)分析结合的实验数据表明,在实际河水处理期间,可以获得同时污染缓解和新出现的污染物苯并苯胺-3(BP3)去除。此外,比较试验表明,通过增强的O-3 / H 2 O 2分解产生羟基自由基(Ho中心点)对E-过氧化物辅助MF工艺中的有机污染物降解和膜结垢,以及引入的静电排斥性具有重要作用武力也可能导致污染减少。这些观察结果表明E-过氧酮可能是一种可行的膜过滤水处理辅助方法。

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  • 作者单位

    Hohai Univ Key Lab Integrated Regulat &

    Resource Dev Shallow Minist Educ Coll Environm Nanjing 210098 Jiangsu Peoples R China;

    Hohai Univ Key Lab Integrated Regulat &

    Resource Dev Shallow Minist Educ Coll Environm Nanjing 210098 Jiangsu Peoples R China;

    Hohai Univ Key Lab Integrated Regulat &

    Resource Dev Shallow Minist Educ Coll Environm Nanjing 210098 Jiangsu Peoples R China;

    Hohai Univ Key Lab Integrated Regulat &

    Resource Dev Shallow Minist Educ Coll Environm Nanjing 210098 Jiangsu Peoples R China;

    Hohai Univ Key Lab Integrated Regulat &

    Resource Dev Shallow Minist Educ Coll Environm Nanjing 210098 Jiangsu Peoples R China;

  • 收录信息
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 分离过程;气化工艺;
  • 关键词

    Electro-peroxone; Microfiltration; Membrane fouling; Benzophenone-3; Hydroxyl radicals;

    机译:电氧化锆;微滤;膜污垢;二苯甲酮-3;羟基自由基;

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