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Sequential use of Fenton and electro-Fenton process for the oxidation of an effluent-containing hypophosphite and phosphite

机译:依次使用Fenton和Fenton电法对含废水的次磷酸盐和亚磷酸盐进行氧化

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摘要

The efficiency of both chemical and electrochemical Fenton processes to treat wastewater effluents from the manufacture of phosphorus-based flame retardants was investigated. Experimental tests were performed on solutions ranging from 600 to 2000mgl(-1) in terms of reduced phosphorus. Different concentrations and ratios of hydrogen peroxide and ferrous ions were tested, and the best conditions were found for both the processes. For the electrochemical treatment, where a gas diffusion cathode was adopted, the effect of carbon coating and current density was investigated, identifying the hydrophilic carbon coating, named Vulcan, as the best cathode material and the value of 100Am(-2) as the optimal current density. The results show that both the Fenton processes provide a powerful conversion to phosphate, with oxidation yields higher than 99%. However, a more cost-friendly sequential treatment, combining a preliminary chemical step to a final electro-oxidation, was proposed to reach a residual concentration of non-oxidized phosphorus less than 10mgl(-1), in compliance with the Italian regulation limits for industrial wastewater disposal. A preliminary economic evaluation is provided.
机译:研究了化学和电化学Fenton工艺处理磷基阻燃剂生产废水的效率。对磷含量从600到2000mgl(-1)的溶液进行了实验测试。测试了不同浓度和比例的过氧化氢和亚铁离子,并找到了两种工艺的最佳条件。对于采用气体扩散阴极的电化学处理,研究了碳涂层和电流密度的影响,确定了名为Vulcan的亲水性碳涂层为最佳阴极材料,最佳值为100Am(-2)当前密度。结果表明,两种Fenton工艺都可将磷酸转化为强力化合物,氧化收率高于99%。但是,提出了一种更具成本效益的顺序处理方法,将初步的化学步骤与最终的电氧化方法相结合,以达到残留的未氧化磷浓度小于10mgl(-1),这符合意大利的法规限制工业废水处理。提供了初步的经济评估。

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