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Integration of ozone, UV/H_2O_2 and GAC in a multi-barrier treatment for secondary effluent polishing: Reuse parameters and micropollutants removal

机译:臭氧,UV / H_2O_2和GAC在二级流出物抛光中的多屏障处理中的集成:重用参数和微渗透剂去除

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Current studies tend to combine different advanced treatment technologies to reduce costs and increase efficiency. The objective of this work was to assess the combination of ozonation and UV/H_2O_2 with activated carbon adsorption for the removal of effluent quality parameters and micropollutants from secondary effluent samples. The experiments were carried out using the following configurations: O_3 + GAC + O_3 (1); O_3 + GAC + UV/H_2O_2 (2); UV/H_2O_2 + GAC + O_3 (3); UV/H_2O_2 + GAC + UV/H_2O_2 (4). Configurations 1,3 and 4 were the most efficient for organic matter removal, while configuration 1 had the lowest cost on laboratory scale. An additional ultra-filtration membrane unit (UF) was tested at the end of configuration 1, which was optimized in terms of ozone doses for the removal of three organophosphate micropollutants in ultrapure water (TNBP, TCIPP and TPHP at 10 μgL~(-1)). The best cost-effective configuration of this treatment train was the one using 1 mg L~(-1) of ozone before and after GAC, which achieved around 100% of micropollutants abatement. The role of each treatment to the final micropollutant removal was also discussed, being the first ozone treatment responsible for about 15% removal of the mixture of contaminants, while GAC was responsible for an additional 80% removal. The complete treatment train reached almost 100% of contaminants removal (under detection limit of the method), as well as added security to the system. The achieved results were also compared to international reuse legislations, proving that the combination of O_3 and GAC was an interesting option to achieve enough quality for some reuse purposes.
机译:目前的研究倾向于结合不同的先进治疗技术来降低成本并提高效率。这项工作的目的是评估臭氧和UV / H_2O_2与活性炭吸附的组合,用于去除来自二级污水样品的流出质量参数和微污染物。使用以下配置进行实验:O_3 + GAC + O_3(1); O_3 + GAC + UV / H_2O_2(2); UV / H_2O_2 + GAC + O_3(3); UV / H_2O_2 + GAC + UV / H_2O_2(4)。配置1,3和4对于有机物质去除最有效,而配置1在实验室规模上具有最低的成本。在构造1的末端测试另外的超过滤膜单元(UF),其在臭氧剂量方面进行了优化,用于去除超纯水中的三种有机磷微渗透剂(TNBP,TCIPP和10μg1(-1 )))。这种治疗列车的最佳成本效益配置是使用GAC之前和之后使用1mg L〜(-1)臭氧的臭氧,其达到约100%的微量渗透剂脱落。还讨论了每种治疗对最终微拷贝去除的作用,是第一臭氧处理,其负责除去污染物的混合物的约15%,而GAC负责额外的80%除去。完整的治疗火车达到了几乎100%的污染物去除(在该方法的检测极限下),以及向系统添加安全性。达到的结果也与国际重用立法进行了比较,证明O_3和GAC的组合是一个有趣的选择,可以获得足够的质量以获得一些重用目的。

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