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Enhanced phosphate removal by zero valent iron activated through oxidants from water: batch and breakthrough experiments

In this study, oxidants including hydrogen peroxide (H(2)O(2)), hypochlorite (ClO(−)) and persulfate (S(2)O(8)(2−)) were employed to promote zero-valent iron (ZVI) corrosion and enhance phosphate (P) removal from water through batch and breakthrough experiments. Characterization results indicated th...

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Detalles Bibliográficos
Autores principales: Zeng, Weilong, Li, Bing, Lin, Xueying, Lv, Sihao, Yin, Weizhao, Li, Ping, Zheng, Xiangyu, Wu, Jinhua
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2021
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9044562/
https://www.ncbi.nlm.nih.gov/pubmed/35494108
http://dx.doi.org/10.1039/d1ra05664f
Descripción
Sumario:In this study, oxidants including hydrogen peroxide (H(2)O(2)), hypochlorite (ClO(−)) and persulfate (S(2)O(8)(2−)) were employed to promote zero-valent iron (ZVI) corrosion and enhance phosphate (P) removal from water through batch and breakthrough experiments. Characterization results indicated that the addition of oxidant can cause large-scale corrosion of the iron surface. This subsequently generates more iron ions and active minerals, resulting in a large number of reaction-adsorption sites for P removal. Therefore, compared with the ZVI alone system (29.4%), the removal efficiency of P by oxidant/ZVI system (H(2)O(2) : ClO(−) : S(2)O(8)(2−) = 33.2% : 54% : 67.1%) was improved. For the oxidant/ZVI system, H(2)O(2) can promote the corrosion of ZVI to a certain extent. However, the solution pH could be increased during the corrosion process. This leads to inhibition of P removal performance by the H(2)O(2)/ZVI system, which only increased by 12.9% to 33.2%. The reaction between NaClO and ZVI consumes less H(+), and the reaction product Cl(−) can pierce the passivation layer on the surface of the ZVI through the pitting effect. As such, the NaClO/ZVI system attained a 54% P removal rate. Compared with H(2)O(2) and NaClO, a better P removal effect of about 67.1% can be achieved by using Na(2)S(2)O(8), since the oxidation corrosion process of Na(2)S(2)O(8) does not consume H(+), and it also has the strongest oxidizing properties. Furthermore, an appropriate increase in oxidant dosing (0.1–2 mM) could improve the efficiency at which of P is removed. Five batch cycle experiments showed that the oxidant/ZVI system has a higher removal capacity and longer life-span. In the long-term column running, the P removal capacity and operation life of the NaClO/ZVI column are 9.6 times and 3.2 times higher than that of the ZVI column, respectively. This work demonstrates that an oxidant/ZVI system can be an efficient method for P removal in water, which also provides a new idea for solving the problem of ZVI corrosion passivation.