Chemical Industry and Engineering Progress ›› 2025, Vol. 44 ›› Issue (7): 4169-4189.DOI: 10.16085/j.issn.1000-6613.2024-0959
• Resources and environmental engineering • Previous Articles
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:2025-08-04
Published:2025-07-25
Contact:
AI Jianping, LI Xibao
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(
)
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:CLC Number:
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.
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.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2024-0959
| 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) | [ |
| 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 |
| 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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