Treatment of metronidazole pharmaceutical wastewater using pulsed switching peroxi-coagulation combined with electro-Fenton process

IF 8.7 Q1 Environmental Science Water Cycle Pub Date : 2024-01-01 Epub Date: 2024-04-10 DOI:10.1016/j.watcyc.2024.04.002
Yongjun Liao, Yongbei Ye, Xindi Chen, Haoran Xin, Shuyue Ma, Songwei Lin, Haiping Luo
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Abstract

The aim of this study was to investigate the metronidazole (MNZ) degradation and real MNZ pharmaceutical wastewater treatment in the pulsed switching peroxi-coagulation (PSPC) process. Different pulsed switching frequencies and running times of H2O2 and Fe2+ productions were tested in the PSPC process. Results demonstrated that MNZ removal of 96.9 ± 1.2 % was realized in the PSPC process with a 200 mg/L MNZ and 0.1 M Na2SO4 solution within 80 min under a pulsed switching frequency of 6s: 1s and a current density of 20 mA/cm2 (H2O2) and 20 mA/cm2 (Fe2+). High MNZ removal could be attributed to efficient •OH production with the highest •OH concentration reached 321 ± 15 μM in the PSPC process. The hydroxyl and carboxyl groups of MNZ were sequentially oxidated by •OH and mineralized based on seven identified intermediates during the MNZ degradation. However, only 56.9 ± 6.7 % of COD was removed in the real MNZ wastewater treatment by the PSPC process within 90 min. A PSPC combined with electro-Fenton (EF) process was developed to enhance the COD removal in the MNZ wastewater. With MNZ wastewater as electrolytes, 3.3 ± 0.3 g/L of H2O2 was produced in a conventional EF reactor. The final COD removal reached 86–90 % using the mixture of effluent from the PSPC, the anode, and cathode chambers of the EF reactor, resulting in less than 80 mg/L COD in the effluent. Results from this study should provide a useful way to enhance real MNZ pharmaceutical wastewater treatment.

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利用脉冲切换过氧混凝结合电-芬顿工艺处理甲硝唑制药废水
本研究旨在探讨脉冲切换过氧混凝(PSPC)工艺中甲硝唑(MNZ)的降解和实际的 MNZ 制药废水处理。在 PSPC 工艺中测试了 H2O2 和 Fe2+ 生成的不同脉冲切换频率和运行时间。结果表明,在脉冲切换频率为 6s:1 秒,电流密度为 20 mA/cm2(H2O2)和 20 mA/cm2(Fe2+)。MNZ 的高去除率可归因于高效的 -OH 生成,在 PSPC 过程中,最高 -OH 浓度达到 321 ± 15 μM。在 MNZ 降解过程中,MNZ 的羟基和羧基依次被 -OH 氧化,并根据七个已确定的中间产物矿化。然而,在实际的 MNZ 废水处理中,PSPC 工艺在 90 分钟内仅去除了 56.9 ± 6.7 % 的 COD。为了提高 MNZ 废水中 COD 的去除率,我们开发了一种 PSPC 与电-芬顿(EF)相结合的工艺。以 MNZ 废水为电解质,在传统的 EF 反应器中产生了 3.3 ± 0.3 g/L 的 H2O2。使用来自 PSPC、EF 反应器阳极室和阴极室的混合废水,最终 COD 去除率达到 86-90%,使废水中的 COD 含量低于 80 mg/L。这项研究的结果将为加强实际的 MNZ 制药废水处理提供有用的方法。
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来源期刊
Water Cycle
Water Cycle Engineering-Engineering (miscellaneous)
CiteScore
9.20
自引率
0.00%
发文量
20
审稿时长
45 days
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