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Oxone/Co~(2+) oxidation as an advanced oxidation process: Comparison with traditional Fenton oxidation for treatment of landfill leachate

机译:Oxone / Co〜(2+)氧化作为高级氧化工艺:与传统的Fenton氧化处理垃圾渗滤液的比较

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摘要

In this paper, the application of Fenton and Oxone/Co~(2+) oxidation processes for landfill leachate treatment was investigated. The removal of the chemical oxygen demand (COD), suspended substances (SS) and the color of the landfill leachate by Fenton oxidation to that by Oxone/Co~(2+) oxidation were compared under optimal operational conditions. For Fenton oxidation process, the optimal conditions were determined as: [H_2O_2] = 80 mmol L~(-1), [H_2O_2]/[Fe~(2+)] = 2.0, initial pH = 2.5, reaction temperature = 37.5 ± 1 ℃, reaction time-= 160 min, number of stepwise addition = 3. Under the given conditions, 56.9% of the COD removal efficiency was achieved, but the SS and the color of the treated landfill leachate increased due to the generation of a large quantity of ferric hydroxide sludge. In reference to Oxone/Co~(2+) oxidation process, the optimal conditions were determined as: [Oxo-ne] = 4.5 mmol L~(-1), [Oxone]/[Co~(2+)] = 10~4, pH = 6.5, reaction temperature - 30 ± 1 ℃, reaction time = 300 min, number of stepwise addition = 7, the COD, SS and the color removal efficiencies were 57.5, 53.3 and 83.3%, respectively. From this work, it can be concluded that Oxone/Co~(2+) oxidation process demonstrated higher degradation efficiencies of the COD, SS and color for landfill leachate treatment than that by Fenton oxidation process. It also suggested that Oxone/Co~(2+) oxidation process could be considered as one of the most promising technologies for practical applicability to treat landfill leachate in large scale. For further improving the efficiency of Oxone/Co~(2+) oxidation process, we proposed that combination of it with other technologies in future such as ultraviolet, ultrasound and biological methods.
机译:本文研究了Fenton和Oxone / Co〜(2+)氧化工艺在垃圾渗滤液处理中的应用。在最佳操作条件下,比较了Fenton氧化与Oxone / Co〜(2+)氧化去除化学需氧量(COD),悬浮物(SS)和垃圾渗滤液的颜色。对于Fenton氧化过程,确定的最佳条件为:[H_2O_2] = 80 mmol L〜(-1),[H_2O_2] / [Fe〜(2+)] = 2.0,初始pH = 2.5,反应温度= 37.5± 1℃,反应时间= 160分钟,逐步添加的数量=3。在给定条件下,COD去除效率达到56.9%,但由于生成了a,因此SS和处理后的垃圾渗滤液的颜色增加了大量的氢氧化铁污泥。参照Oxone / Co〜(2+)的氧化过程,确定了最佳条件:[Oxo-ne] = 4.5 mmol L〜(-1),[Oxone] / [Co〜(2+)] = 10 〜4,pH = 6.5,反应温度-30±1℃,反应时间= 300分钟,逐步添加的数量= 7,COD,SS和脱色效率分别为57.5%,53.3和83.3%。从这项工作可以得出结论,与Fenton氧化工艺相比,Oxone / Co〜(2+)氧化工艺对垃圾渗滤液的化学需氧量,SS和颜色的降解效率更高。这也表明,Oxone / Co〜(2+)氧化工艺可被认为是大规模应用于垃圾渗滤液实际应用的最有前途的技术之一。为了进一步提高Oxone / Co〜(2+)氧化工艺的效率,我们提出将其与未来的其他技术(例如紫外线,超声和生物方法)相结合。

著录项

  • 来源
    《Water Research》 |2009年第17期|4363-4369|共7页
  • 作者单位

    College of Chemistry and Environmental Sciences, Henan Normal University, Henan Key Laboratory for Environmental Pollution Control, Xinxiang, Henan 453007, PR China;

    College of Chemistry and Environmental Sciences, Henan Normal University, Henan Key Laboratory for Environmental Pollution Control, Xinxiang, Henan 453007, PR China;

    College of Chemistry and Environmental Sciences, Henan Normal University, Henan Key Laboratory for Environmental Pollution Control, Xinxiang, Henan 453007, PR China;

    College of Chemistry and Environmental Sciences, Henan Normal University, Henan Key Laboratory for Environmental Pollution Control, Xinxiang, Henan 453007, PR China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Oxone/Co~(2+); fenton; landfill leachate; AOPs;

    机译:Oxone / Co〜(2+);芬顿垃圾渗滤液行动计划;

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