化工进展 ›› 2025, Vol. 44 ›› Issue (7): 4169-4189.DOI: 10.16085/j.issn.1000-6613.2024-0959
• 资源与环境化工 • 上一篇
罗司玲1(
), 艾建平1,3(
), 李文魁1, 王翼1, 程丽红1, 万芸1, 黄隆1, 李喜宝2(
)
收稿日期:2024-06-14
修回日期:2024-08-16
出版日期:2025-07-25
发布日期:2025-08-04
通讯作者:
艾建平,李喜宝
作者简介:罗司玲(1998—),女,硕士研究生,研究方向为非均相催化降解有机污染物。E-mail:lsl981211@163.com。
基金资助:
LUO Siling1(
), AI Jianping1,3(
), LI Wenkui1, WANG Yi1, CHENG Lihong1, WAN Yun1, HUANG Long1, LI Xibao2(
)
Received:2024-06-14
Revised:2024-08-16
Online:2025-07-25
Published:2025-08-04
Contact:
AI Jianping, LI Xibao
摘要:
抗生素是水环境中一类典型的新兴微污染有机物,具有难降解、高风险、潜在未知毒性和普遍残留等特性。基于羟基自由基、超氧自由基、硫酸根自由基等活性物种的高级氧化技术,因其高效快速、适用范围广等特点,已成为抗生素废水处理领域的研究热点。本文从抗生素的结构特征出发,结合密度泛函理论,首次系统剖析了不同活性物种对常见五大类抗生素的攻击位点和降解机理。同时,综述了电催化法、光催化法、臭氧氧化法、芬顿及类芬顿法四种高级氧化技术在处理抗生素废水方面的优势及适用范围,并展望了未来的发展方向及趋势。
中图分类号:
罗司玲, 艾建平, 李文魁, 王翼, 程丽红, 万芸, 黄隆, 李喜宝. 高级氧化技术降解典型抗生素的研究进展[J]. 化工进展, 2025, 44(7): 4169-4189.
LUO Siling, AI Jianping, LI Wenkui, WANG Yi, CHENG Lihong, WAN Yun, HUANG Long, LI Xibao. Research progress on degradation of typical antibiotics by advanced oxidation processes[J]. Chemical Industry and Engineering Progress, 2025, 44(7): 4169-4189.
图1 (a)不同ROS的氧化还原电位;(b)ZnO/CuCo2O4/PMS、CuCo2O4/PMS和ZnO/PMS体系中DMPO-·OH和DMPO-·SO4-的EPR谱图;(c)ZnO/CuCo2O4/PMS、CuCo2O4/PMS和ZnO/PMS体系中DMPO-·O2-的EPR谱图;(d)ZnO/CuCo2O4/PMS、CuCo2O4/PMS和ZnO/PMS体系中TEMP-·O2的EPR谱图[16]
| 抗生素种类 | 催化体系 | 最优反应条件 | 降解效能 | 参考 文献 |
|---|---|---|---|---|
| 头孢氨苄 | Mn@ZN | [CLX]=1.0mg/L [O3]=0.20mg/L pH=9.12 | 97% (2min) | [ |
| 环丙沙星 | Mn-CeO x @γ-Al2O3 | [CIP]=80g/L [O3]=14mg/L pH=8~9 | 100% (60min) | [ |
| 诺氟沙星 | RuO2/Ti电极 (电催化-O3氧化) | [NOR]=10mg/L [O3]=10mg/L J=3mA/cm2 pH=11 | 100% (40min) | [ |
| 磺胺嘧啶 | Fe-H-Beta-25-EIM Cu-H-Beta-150-DP | VN2=0.0025L/min VO2=445mL/min | 100% (1min) | [ |
| 甲硝唑 | 锂掺杂Mg(OH)2的 纳米片 | [MTZ]=50g/L [O3]=14mg/L t=25℃ | 100% (10min) | [ |
| 四环素 | (MgMnO)3(SCOP) | [TC]=50g/L [O3]=2.0mg/L | 88.4% (80min) (矿化率) | [ |
表1 臭氧氧化法对不同抗生素的降解
| 抗生素种类 | 催化体系 | 最优反应条件 | 降解效能 | 参考 文献 |
|---|---|---|---|---|
| 头孢氨苄 | Mn@ZN | [CLX]=1.0mg/L [O3]=0.20mg/L pH=9.12 | 97% (2min) | [ |
| 环丙沙星 | Mn-CeO x @γ-Al2O3 | [CIP]=80g/L [O3]=14mg/L pH=8~9 | 100% (60min) | [ |
| 诺氟沙星 | RuO2/Ti电极 (电催化-O3氧化) | [NOR]=10mg/L [O3]=10mg/L J=3mA/cm2 pH=11 | 100% (40min) | [ |
| 磺胺嘧啶 | Fe-H-Beta-25-EIM Cu-H-Beta-150-DP | VN2=0.0025L/min VO2=445mL/min | 100% (1min) | [ |
| 甲硝唑 | 锂掺杂Mg(OH)2的 纳米片 | [MTZ]=50g/L [O3]=14mg/L t=25℃ | 100% (10min) | [ |
| 四环素 | (MgMnO)3(SCOP) | [TC]=50g/L [O3]=2.0mg/L | 88.4% (80min) (矿化率) | [ |
| 处理技术 | 主要ROS | 优点 | 适用范围 | 存在问题 |
|---|---|---|---|---|
| 电催化法 | ·OH | 成本低、操作简便且对环境友好 | 小流量含高浓度抗生素和COD的有机废水 | 运营成本较高,处理流量必须控制在较小范围内 |
| 光催化法 | e-/h+、·OH和·O2- | 能源来源简单,成本较低 | 透光性能够达到处理标准的有机废水 | 量子效率低,催化剂价格昂贵,难以回收 |
| 臭氧氧化法 | ·OH、O3 | 反应快速高效、稳定性好 | 水质和水量变化时可用能耗、设备成本及维修费用高,适用于难降解有机废水 | 能耗、设备成本及维修费用高 |
| 芬顿及类芬顿法 | ·OH、·SO4-、·O2-和1O2 | 成本低、水溶性好、氧化性强,活化方式多样 | 光敏感化合物废水和COD浓度较低的水体 | 易受pH、温度、H2O2浓度和目标物浓度影响 |
表2 4种AOP处理抗生素废水的优缺点及适用范围
| 处理技术 | 主要ROS | 优点 | 适用范围 | 存在问题 |
|---|---|---|---|---|
| 电催化法 | ·OH | 成本低、操作简便且对环境友好 | 小流量含高浓度抗生素和COD的有机废水 | 运营成本较高,处理流量必须控制在较小范围内 |
| 光催化法 | e-/h+、·OH和·O2- | 能源来源简单,成本较低 | 透光性能够达到处理标准的有机废水 | 量子效率低,催化剂价格昂贵,难以回收 |
| 臭氧氧化法 | ·OH、O3 | 反应快速高效、稳定性好 | 水质和水量变化时可用能耗、设备成本及维修费用高,适用于难降解有机废水 | 能耗、设备成本及维修费用高 |
| 芬顿及类芬顿法 | ·OH、·SO4-、·O2-和1O2 | 成本低、水溶性好、氧化性强,活化方式多样 | 光敏感化合物废水和COD浓度较低的水体 | 易受pH、温度、H2O2浓度和目标物浓度影响 |
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