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Characteristics and mechanisms of catalytic ozonation with Fe- shaving-based catalyst in industrial wastewater advanced treatment

机译:刨花基催化剂催化臭氧氧化工业废水的特点及机理

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Iron shavings were modified and used as the catalyst (named as Fe-shaving-based catalyst) for the ozonation of bio-treated coking wastewater. The difference of organic pollutants oxidation between catalytic and sole ozonation processes was characterized by MW (Molecular Weight) distribution and 3DEEM (Three-dimensional Excitation and Emission Matrix Fluorescence) analysis. Removals of the pollutants with MW of 5-10 kDa and 10-20 kDa in catalytic ozonation process were 81.5% and 85.2%, which were far better than that in sole ozonation process (31.1% and 41.8%). Organics with MW of 0.3 -2 kDa and 2-5 kDa would accumulate in both two processes, while the accumulation amount in catalytic ozonation process was half of it in sole ozonation process. The removal of fluorescent substances in catalytic ozonation process experienced a procedure of lower firstly (15 min) and then higher (15 min) than that in sole ozonation process. The slight residual fluorescent substances were completely removed in catalytic ozonation process, while remained unchanged in sole ozonation process with the reaction time increasing to 180 min. The catalytic effect of Fe-shaving-based catalyst was better than commonly used powder catalysts and the TOC (Total Organic Carbon) removal attained to 78%. Hydroxyl radicals (center dot OH) were confirmed to be the effective oxidant in catalytic ozonation process through inhibition experiments. The cumulative-OH formations with 200 Fe-shaving-based catalyst during 180 min were 362 mol, which explained the better catalytic effect of it. The surface hydroxyl groups were determined to be the most probable active sites for-OH generation through phosphate inhibition experiments. Besides the excellent catalytic effect, using Fe-shaving-based catalyst provided a feasible resource utilization method of industrial waste Fe-shavings. Thereby, it is a promising catalyst for practical industrial wastewater advanced treatment with catalytic ozonation process. (C) 2019 Elsevier Ltd. All rights reserved.
机译:对铁屑进行了改性,并将其用作生物处理焦化废水臭氧化的催化剂(称为铁屑基催化剂)。通过分子量分布和3DEEM(三维激发和发射矩阵荧光)分析,表征了催化和单一臭氧氧化过程中有机污染物氧化的差异。催化臭氧氧化工艺去除的MW分别为5-10 kDa和10-20 kDa的污染物分别为81.5%和85.2%,远优于单独臭氧氧化工艺的31.1%和41.8%。 MW分别为0.3 -2 kDa和2-5 kDa的有机物会在这两个过程中积累,而催化臭氧化过程中的累积量是单独臭氧化过程中的一半。催化臭氧氧化过程中荧光物质的去除首先经历了比单独臭氧氧化过程中更低的过程(<15分钟)然后更高(> 15分钟)。轻微的残留荧光物质在催化臭氧化过程中被完全去除,而在单独的臭氧化过程中保持不变,反应时间增加到180分钟。剃须铁基催化剂的催化效果优于常用的粉末催化剂,TOC(总有机碳)去除率达到78%。通过抑制实验,证实了羟基自由基(中心点OH)是催化臭氧化过程中的有效氧化剂。在200分钟内,使用200 Fe的金属屑形成的催化剂累积的OH形成量为362 mol,这说明了其更好的催化作用。通过磷酸盐抑制实验,表面羟基被确定为最可能产生OH的活性位点。除了具有优异的催化效果外,使用铁屑基催化剂还为工业废铁屑的资源利用提供了一种可行的方法。因此,它是通过催化臭氧化工艺用于实际工业废水深度处理的有前途的催化剂。 (C)2019 Elsevier Ltd.保留所有权利。

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  • 来源
    《Journal of Cleaner Production》 |2019年第10期|174-181|共8页
  • 作者单位

    Tongji Univ, Sch Environm Sci & Engn, State Key Lab Pollut Control & Resource Reuse, Shanghai 200092, Peoples R China|Shanghai Inst Pollut Control & Ecol Secur, Shanghai 200092, Peoples R China;

    Tongji Univ, Sch Environm Sci & Engn, State Key Lab Pollut Control & Resource Reuse, Shanghai 200092, Peoples R China;

    Tongji Univ, Sch Environm Sci & Engn, State Key Lab Pollut Control & Resource Reuse, Shanghai 200092, Peoples R China;

    Univ Shanghai Sci & Technol, Sch Environm & Architecture, Shanghai 200093, Peoples R China;

    Tongji Univ, Sch Environm Sci & Engn, State Key Lab Pollut Control & Resource Reuse, Shanghai 200092, Peoples R China|Shanghai Inst Pollut Control & Ecol Secur, Shanghai 200092, Peoples R China;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Organics oxidation order; Fe-shaving-based catalyst; Surface hydroxyl groups; Cumulative center dot OH formation; Catalytic ozonation;

    机译:有机物的氧化顺序;铁屑基催化剂;表面羟基;累积中心点OH的形成;催化臭氧化;

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