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采用 Fe/AC/Ni 阴极的电芬顿法处理焦化废水的多相反应:电极和反应器有机负荷的优化。

Heterogeneous electro-Fenton treatment of coking wastewater using Fe/AC/Ni cathode: optimization of electrode and reactor organic loading.

机构信息

School of chemical engineering, University of Science and Technology Liaoning, Anshan, People's Republic of China.

Ansteel Beijing Research Institute Co., Ltd., Beijing, People's Republic of China.

出版信息

Environ Technol. 2024 Apr;45(11):2180-2195. doi: 10.1080/09593330.2023.2165971. Epub 2023 Jan 30.

DOI:10.1080/09593330.2023.2165971
PMID:36602885
Abstract

A self-developed iron-loaded activated carbon-based nickel foam electrode (Fe/AC/Ni cathode) was used to construct electro-Fenton reaction system to treat coking wastewater. To meet the gap between laboratory beaker experiments and field trials for practical applications, we proposed and validated a method for obtaining organic loads, the essential parameters used in the design of electrochemical systems for wastewater treatment. The three influencing factors most relevant to organic loading, the effective surface area of cathode, chemical oxygen demand (COD) concentration of influent, and treatment time, were selected and investigated for their effects on the COD removal rate of coking wastewater by single-factor experiments and further optimized by response surface method. The appropriate electrode area load (L) and reactor volume load (L) were calculated by their corresponding intrinsic relationships with the three factors. The optimum application conditions were effective surface area of cathode 28.5 cm, COD concentration of influent 1.76 kg·m, and treatment time 160.43 min. Under these conditions, the maximum COD removal rate was 98.51%. The L and L were 8.905 mgCOD·cm·h and 0.634 kgCOD·m·h, respectively. The characterization experiment results showed that the Fe/AC/Ni cathode had a significant effect on the treatment of refractory organic contaminants in coking wastewater.

摘要

采用自行研制的载铁活性炭泡沫镍电极(Fe/AC/Ni 阴极)构建电芬顿反应体系处理焦化废水。为了满足实验室烧杯实验和实际应用现场试验之间的差距,提出并验证了一种获取有机负荷的方法,这是用于设计电化学系统处理废水的重要参数。选择并研究了与有机负荷、阴极有效表面积、进水 COD 浓度和处理时间三个最相关的影响因素,通过单因素实验考察它们对焦化废水 COD 去除率的影响,并通过响应面法进一步优化。通过它们与三个因素的内在关系计算出合适的电极面积负荷(L)和反应器体积负荷(L)。最佳应用条件为阴极有效表面积 28.5 cm、进水 COD 浓度 1.76 kg·m 和处理时间 160.43 min。在此条件下,COD 去除率最高可达 98.51%。L 和 L 分别为 8.905 mgCOD·cm·h 和 0.634 kgCOD·m·h。特征实验结果表明,Fe/AC/Ni 阴极对处理焦化废水中难降解有机污染物有显著效果。

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