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Elimination of trace organic contaminants during enhanced wastewater treatment with horseradish peroxidase/hydrogen peroxide (HRP/H2O2) catalytic process

机译:在增强废水处理中消除痕量有机污染物,用辣根过氧化物酶/氢过氧化氢(HRP / H2O2)催化过程

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The potential of horseradish peroxidase combined with hydrogen peroxidase (HRP/H2O2) catalytic process was assessed as an enhanced wastewater treatment technology to eliminate trace organic contaminants (micropollutants). Kinetic experiments with 17 alpha-ethinylestradiol (EE2) as a phenolic micropollutant in synthetic buffered solutions showed that the apparent first-order rate constant of EE2 transformation (k(EE2)) increased linearly with increasing HRP concentration but was independent of the concentrations of H2O2 and EE2. The observed kinetic behaviors of EE2 could be well explained by the known chemistry of the HRP/H2O2 system considering the reaction of Compound II with EE2 as the rate-limiting step in the catalytic cycle of HRP under the condition of excess H2O2 over HRP. Using this HRP/H2O2 kinetic model, the second-order rate constants of the reaction of Compound II (k(3)) with a few selected phenolic micropollutants including EE2 and phenol and aniline could be determined and compared with those from the literature. Good correlations were found between the k(3) of various phenolic or anilinic compounds (from this study and the literature) versus Hammett sigma constants, which can be used for predicting the elimination efficiency of phenolic or anilinic micropollutants. Experiments conducted using lake water and wastewater effluent matrices showed that significant elimination of phenolic micropollutants (i.e., % elimination levels of 20%-100%) could be achieved under the following treatment condition: 1.4-5.6 nM (12-48 U/L) of HRP, 20 mu M of H2O2, and 1 h of reaction time. Elimination of the other tested micropollutants without phenolic moieties was less than 5%. The elimination levels of phenolic micropollutants (e.g., EE2) in real water matrices spiked at 2 mu M could be well predicted by the HRP/H2O2 kinetic model with the corresponding k(3) value. However, relatively lower elimination levels were observed when the phenolic micropollutants were spiked at 1 mu g/L, indicating some reduction in the performance of the HRP/H2O2 process for eliminating phenolic micropollutants present at environmentally relevant concentrations (e.g., sub mu g/L). (C) 2016 Elsevier B.V. All rights reserved.
机译:评估辣根过氧化物酶(HRP / H2O2)催化过程的潜在催化过程作为增强的废水处理技术,以消除痕量有机污染物(微污染物)。用17个α-乙丁烯雌二醇(EE2)作为合成缓冲溶液中的酚类微毒剂的动力学实验表明,EE2转化(K(EE2))的表观一阶速率常数随着HRP浓度的增加而升高,但与H2O2的浓度无关和EE2。通过HRP / H2O2系统的已知化学方法,考虑到化合物II与EE2作为HRP的催化循环的催化循环的速率限制步骤,所知的EE2的EE2的动力学行为可以很好地解释。使用该HRP / H2O2动力学模型,可以确定包含EE2和苯酚和苯胺的少量选定的酚类微拷贝的化合物II(K(3))反应的二阶速率常数。在各种酚类或苯胺化合物的K(3)之间发现良好的相关性(来自该研究和文献)与Hammett Sigma常数的k(3),可用于预测酚类或疾病微渗透剂的消除效率。利用湖水和废水污水基质进行的实验表明,在以下处理条件下,可以在以下处理条件下实现显着的酚类微孔(即%-100%)的酚类微孔(即%-100%):1.4-5.6nm(12-48 u / l) HRP,20μm的H 2 O 2和1小时的反应时间。消除没有酚类部分的其他测试的微胶质劳顿小于5%。在2μm下掺入的实际水基质中的酚类微拷贝(例如,EE2)的消除水平可以通过HRP / H2O2动力学模型进行很好的预测,具有相应的K(3)值。然而,当以1μg/ l掺入酚类微拷贝体时观察到相对较低的消除水平,表明HRP / H2O2的性能的一些降低,用于消除在环境相关浓度下存在的酚类微渗透剂(例如,亚mu g / l )。 (c)2016年Elsevier B.v.保留所有权利。

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