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Treatment of a Waste Water Pharmaceutical by Fenton Oxidation - Paracetamol contaminated Waste Water treated by the Heterogeneous Dark- and Photo-Fenton Oxidation

机译:Fenton氧化处理废水制药-异质Fenton氧化和光Fenton氧化处理对乙酰氨基酚污染的废水

摘要

A study in waste water treatment has been performed, using advanced oxidation processes, namely the heterogeneous dark- and photo-Fenton. The applied catalysts were two iron doped zeolites, ZSM-5 (Fe/MFI) and Beta (Fe/BEA).Methods of analysis: the degradation of the paracetamol molecule was analyzed by HPLC, the concentration of aqueous organic pollution was evaluated with total organic carbon (TOC), the oxidant consumption by permanganate titration, the activity of leached iron by homogeneous Fenton and the magnitude of leached iron with inductively coupled plasma (ICP).Three major events were proposed to occur; the oxidation of the aqueous and adsorbed organic molecules, the continuously changing equilibrium between aqueous and adsorbed phase, and the formation of iron-organic-intermediate complexes.A complete degradation of the paracetamol molecule was obtained in every experiment within 5 to 180 minutes, while the degree of mineralization reached 20-70% in five hours. When going from dark- to photo-Fenton an increase in TOC conversion was observed for both zeolites. The magnitudes were between 15-40% for the Fe/MFI and 14-19% for the Fe/BEA. On the other hand, the increase of oxidant (H2O2) concentration affected the TOC concentration of the zeolites differently. For the Fe/MFI the TOC conversion increased between 20-30% while it had a slight decrease in TOC conversion (between 1-5%) for the Fe/BEA. The activity of the leached iron was of a larger magnitude for the Fe/BEA zeolite than for the Fe/MFI zeolite.The highest degree of mineralization based on the liquid phase was found to be 68% for the photo-Fenton reactor setup using the Fe/MFI as catalyst at 30°C and an oxidant amount of two times the stoechiometry for full mineralization (27.7mmolL-1). When including the remaining adsorbed organic pollutant the highest degree of mineralization was 60%. This was obtained with the photo-Fenton using Fe/MFI as catalyst at 30°C and ten times the stoechiometry of oxidant (138.5mmolL-1).
机译:使用先进的氧化工艺,即异质的深色和光芬顿,已经进行了废水处理的研究。所应用的催化剂为两种铁掺杂沸石,ZSM-5(Fe / MFI)和Beta(Fe / BEA)。分析方法:对乙酰氨基酚分子的降解通过HPLC进行分析,对有机污染物的浓度进行总分析。有机碳(TOC),高锰酸盐滴定法消耗的氧化剂,均质Fenton浸出铁的活性以及电感耦合等离子体(ICP)浸出铁的量级。水和吸附的有机分子的氧化,水和吸附的相之间的平衡不断变化以及铁-有机-中间体配合物的形成。在每个实验中,在5至180分钟内对乙酰氨基酚分子均被完全降解,而五小时内矿化度达到20-70%。当从暗Fenton变为光Fenton时,两种沸石的TOC转化率均增加。 Fe / MFI的幅度介于15-40%之间,Fe / BEA的幅度介于14-19%之间。另一方面,氧化剂(H2O2)浓度的增加对沸石的TOC浓度有不同的影响。对于Fe / MFI,TOC转化率在20-30%之间增加,而对于Fe / BEA,TOC转化率略有下降(1-5%之间)。 Fe / BEA沸石的浸出铁的活性比Fe / MFI沸石的浸出铁的活性更大。基于液相的Fenton反应器装置的液相最高矿化度为68%。 Fe / MFI在30°C时作为催化剂,其氧化量是化学计量的两倍,可以完全矿化(27.7mmolL-1)。当包括剩余的吸附有机污染物时,最高矿化度为60%。这是通过在30℃下使用Fe / MFI作为催化剂的光芬顿法得到的,是氧化剂的化学计量(138.5mmolL-1)的十倍。

著录项

  • 作者

    Kjos-Hanssen Øyvind Jacob;

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  • 年度 2012
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  • 原文格式 PDF
  • 正文语种 eng
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