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电芬顿-铁氧体法原位生成羟基自由基降解酸性红G的工艺优化及机理研究

Process optimization and mechanism study of acid red G degradation by electro-Fenton-Feox process as an in situ generation of HO.

作者信息

Sun Hailong, Yao Yingwu, Wei Feng, Zhao Qiang, Liu Baichen, Zhang Liman

机构信息

Hebei University of Technology, School of Chemical Engineering and Technology, Tianjin P.R. China.

出版信息

Turk J Chem. 2021 Feb 17;45(1):5-16. doi: 10.3906/kim-2002-10. eCollection 2021.

Abstract

Dye-contaminated wastewaters are industrial wastewaters that are difficult to treat using traditional biochemical and physicochemical methods. In the present work, the acid red G was removed as a model pollutant by the electro-Fenton process for the first time. The anode and cathode used by the electro-Fenton process were iron plate and graphite felt, respectively. It was concluded that under the optimal conditions of current density = 20 mA cm, pH = 3 and initial NaSO concentration = 0.2 M, the removal rate of acid red G (ARG) with an initial concentration of 300 mg L could reach 94.05% after 80 min of electrolysis. This reveals that the electro-Fenton-Feox process used in this work has an excellent removal efficiency on acid red G. The required reagents (Fe and HO) were generated by the electrode reaction, while the optimal generation conditions and mechanism of •OH, HO, and Fe were investigated. By testing •OH, HO, and Fe agents at different pH and current densities, it was revealed that the electro-Fenton reaction was most efficient when the current density was 20 mA cm, and the pH was 3. Moreover, the removal rate of ARG is consistent with first-order reaction kinetics.

摘要

染料污染废水是难以用传统生化和物理化学方法处理的工业废水。在本研究中,首次采用电芬顿法去除酸性红G作为模型污染物。电芬顿法使用的阳极和阴极分别是铁板和石墨毡。结果表明,在电流密度 = 20 mA/cm²、pH = 3和初始Na₂SO₄浓度 = 0.2 M的最佳条件下,初始浓度为300 mg/L的酸性红G(ARG)在电解80分钟后去除率可达94.05%。这表明本研究中使用的电芬顿-Fe³⁺过程对酸性红G具有优异的去除效率。所需试剂(Fe²⁺和H₂O₂)由电极反应产生,同时研究了•OH、H₂O₂和Fe³⁺的最佳生成条件及机理。通过在不同pH和电流密度下测试•OH、H₂O₂和Fe³⁺试剂,结果表明当电流密度为20 mA/cm²且pH为3时,电芬顿反应效率最高。此外,ARG的去除率符合一级反应动力学。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/effe/7925314/121ab912636c/turkjchem-45-5-fig001.jpg

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