首页> 外文期刊>Environmental Science & Technology >Organic Contaminant Abatement in Reclaimed Water by UV/H_2O_2 and a Combined Process Consisting of O_3/H_2O_2 Followed by UV/H_2O_2: Prediction of Abatement Efficiency, Energy Consumption, and Byproduct Formation
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Organic Contaminant Abatement in Reclaimed Water by UV/H_2O_2 and a Combined Process Consisting of O_3/H_2O_2 Followed by UV/H_2O_2: Prediction of Abatement Efficiency, Energy Consumption, and Byproduct Formation

机译:UV / H_2O_2和O_3 / H_2O_2继之以UV / H_2O_2组成的联合过程在再生水中减少有机污染物:减排效率,能耗和副产物形成的预测

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摘要

UV/H_2O_2 processes can be applied to improve the quality of effluents from municipal wastewater treatment plants by attenuating trace organic contaminants (micropollutants). This study presents a kinetic model based on UV photolysis parameters, including UV absorption rate and quantum yield, and hydroxyl radical (·OH) oxidation parameters, including second-order rate constants for ·OH reactions and steady-state ·OH concentrations, that can be used to predict micropollutant abatement in wastewater. The UV/H_2O_2 kinetic model successfully predicted the abatement efficiencies of 16 target micropollutants in bench-scale UV and UV/H_2O_2 experiments in 10 secondary wastewater effluents. The model was then used to calculate the electric energies required to achieve specific levels of micropollutant abatement in several advanced wastewater treatment scenarios using various combinations of ozone, UV, and H_2O_2. UV/H_2O_2 is more energy-intensive than ozonation for abatement of most micropollutants. Nevertheless, UV/H_2O_2 is not limited by the formation of N-nitrosodimethylamine (NDMA) and bromate whereas ozonation may produce significant concentrations of these oxidation byproducts, as observed in some of the tested wastewater effluents. The combined process of O_3/H_2O_2 followed by UV/H_2O_2, which may be warranted in some potable reuse applications, can achieve superior micropollutant abatement with reduced energy consumption compared to UV/H_2O_2 and reduced oxidation byproduct formation (i.e., NDMA and/or bromate) compared to conventional ozonation.
机译:UV / H_2O_2工艺可用于通过减轻痕量有机污染物(微污染物)来改善市政废水处理厂的出水质量。这项研究提出了一个基于紫外线光解参数的动力学模型,其中包括紫外线吸收率和量子产率,以及羟基自由基(·OH)氧化参数,包括·OH反应的二级速率常数和稳态·OH浓度,用于预测废水中的微污染物排放。 UV / H_2O_2动力学模型成功地预测了16种目标微污染物在实验室规模的UV和UV / H_2O_2实验中对10种二级废水的减排效率。然后,该模型用于计算使用臭氧,UV和H_2O_2的各种组合在几种先进的废水处理方案中实现特定水平的微污染物减排所需的电能。与臭氧化相比,UV / H_2O_2的能源消耗更大,可以减少大多数微污染物。但是,UV / H_2O_2不受N-亚硝基二甲胺(NDMA)和溴酸盐的形成的限制,而臭氧氧化可能会产生大量的氧化副产物,如在某些测试废水中所观察到的。 O_3 / H_2O_2继之以UV / H_2O_2的组合过程(在某些饮用水重复使用应用中可能得到保证)与UV / H_2O_2相比,可实现卓越的微污染物减排,并降低了能耗,并减少了氧化副产物的形成(即NDMA和/或溴酸盐) )相比,传统的臭氧化。

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  • 来源
    《Environmental Science & Technology》 |2016年第7期|3809-3819|共11页
  • 作者单位

    School of Environmental Science and Engineering, Gwangju Institute of Science and Technology, 123, Oryong-dong, Buk-gu, Gwangju 500-712, Korea,Eawag, Swiss Federal Institute of Aquatic Science and Technology, Ueberlandstrasse 133, P.O. Box 611, 8600 Duebendorf, Switzerland;

    Department of Civil and Environmental Engineering, University of Nevada, Las Vegas, Box 454015, 4505 S. Maryland Parkway, Las Vegas, Nevada 89154-4015, United States,Trussell Technologies, Inc., 6540 Lusk Boulevard, Suite C274, San Diego, California 92121, United States,Applied Research and Development Center, Southern Nevada Water Authority, P.O. Box 99954, Las Vegas, Nevada 89193-9954, United States;

    Eawag, Swiss Federal Institute of Aquatic Science and Technology, Ueberlandstrasse 133, P.O. Box 611, 8600 Duebendorf, Switzerland,School of Architecture, Civil, and Environmental Engineering (ENAC), Ecole Polytechnique Federate de Lausanne, CH-1015, Lausanne, Switzerland;

    Applied Research and Development Center, Southern Nevada Water Authority, P.O. Box 99954, Las Vegas, Nevada 89193-9954, United States;

    Trussell Technologies, Inc., 6540 Lusk Boulevard, Suite C274, San Diego, California 92121, United States,Applied Research and Development Center, Southern Nevada Water Authority, P.O. Box 99954, Las Vegas, Nevada 89193-9954, United States;

    Applied Research and Development Center, Southern Nevada Water Authority, P.O. Box 99954, Las Vegas, Nevada 89193-9954, United States;

    Eawag, Swiss Federal Institute of Aquatic Science and Technology, Ueberlandstrasse 133, P.O. Box 611, 8600 Duebendorf, Switzerland;

    Department of Chemical and Environmental Engineering, University of Arizona, 1133 E. James E. Rogers Way, Harshbarger 108, Tucson, Arizona 85721-0011, United States;

    Eawag, Swiss Federal Institute of Aquatic Science and Technology, Ueberlandstrasse 133, P.O. Box 611, 8600 Duebendorf, Switzerland,School of Architecture, Civil, and Environmental Engineering (ENAC), Ecole Polytechnique Federate de Lausanne, CH-1015, Lausanne, Switzerland;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);美国《化学文摘》(CA);
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  • 入库时间 2022-08-17 13:58:42

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