Escobedo Ericson, Oh Jin-Ah, Cho Kangwoo, Chang Yoon-Seok
Division of Environmental Science and Engineering, Pohang University of Science and Technology (POSTECH), Pohang 37673, Republic of Korea.
National Institute of Environmental Research, Incheon 22689, Republic of Korea.
Water Res. 2022 Jun 1;216:118305. doi: 10.1016/j.watres.2022.118305. Epub 2022 Mar 15.
Despite the extensive application of electrochemical advanced oxidation processes (EAOPs) in wastewater treatment, the exact speciation of oxidants and their effects on pollutants removal efficiency, by-products formation, and effluent toxicity are largely unknown. In this study, galvanostatic steel anodes were used to drive the electrochemical activation of hydrogen peroxide (EAHP), persulfate (EAP), and free chlorine (EAFC), for industrial-scale treatment of municipal and livestock wastewater with a focus on micropollutants and transformation products (MTPs) and effluent toxicity. Response surface methodology determined the optimized conditions for each treatment towards total organic carbon ([TOC] = 180 mg/L) removal at pH 3.0: persulfate dose = 0.12 mmol/min, 26.5 mA/cm; free chlorine dose = 0.29 mmol/min, 37.4 mA/cm; HO dose = 0.20 mmol/min, 45 mA/cm. Probe-compound degradation revealed that HO, SO and FeO species were simultaneously generated in EAP, whereas HO and FeO were the principal oxidants in EAHP and EAFC, respectively. Samples were analyzed via liquid and gas chromatography in non-target screening (NTS) mode to monitor the generation or removal of MTPs and by-products including compounds that have not been reported previously. The speciation of oxidants, shifted in presence of halide ions (Cl, Br) in real wastewater samples, significantly affected the mineralization efficiency and by-product formation. The production of halogenated by-products in EAFC and EAP substantially increased the effluent toxicity, whereas EAHP provided non-toxic effluent and the highest mineralization efficiency (75 - 80%) to be nominated as the best strategy.
尽管电化学高级氧化工艺(EAOPs)在废水处理中得到了广泛应用,但氧化剂的确切形态及其对污染物去除效率、副产物形成和出水毒性的影响在很大程度上尚不清楚。在本研究中,采用恒电流钢阳极驱动过氧化氢(EAHP)、过硫酸盐(EAP)和游离氯(EAFC)的电化学活化,用于市政和畜牧废水的工业规模处理,重点关注微污染物和转化产物(MTPs)以及出水毒性。响应面法确定了在pH 3.0时每种处理对总有机碳([TOC]=180mg/L)去除的优化条件:过硫酸盐剂量=0.12mmol/min,26.5mA/cm;游离氯剂量=0.29mmol/min,37.4mA/cm;HO剂量=0.20mmol/min,45mA/cm。探针化合物降解表明,EAP中同时生成了HO、SO和FeO物种,而HO和FeO分别是EAHP和EAFC中的主要氧化剂。通过非靶向筛选(NTS)模式下的液相和气相色谱对样品进行分析,以监测MTPs和副产物(包括以前未报道过的化合物)的生成或去除。在实际废水样品中,卤离子(Cl、Br)的存在会使氧化剂的形态发生变化,这显著影响了矿化效率和副产物的形成。EAFC和EAP中卤化副产物的产生显著增加了出水毒性,而EAHP提供了无毒出水和最高的矿化效率(75-80%),被认为是最佳策略。