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基于过硫酸盐活化的高级氧化技术处理水中磺胺类药物研究进展

刘诗月 彭向天 马瑞瑞 曾萍 李娟 朱幸运

刘诗月,彭向天,马瑞瑞,等.基于过硫酸盐活化的高级氧化技术处理水中磺胺类药物研究进展[J].环境工程技术学报,2024,14(2):642-650 doi: 10.12153/j.issn.1674-991X.20230529
引用本文: 刘诗月,彭向天,马瑞瑞,等.基于过硫酸盐活化的高级氧化技术处理水中磺胺类药物研究进展[J].环境工程技术学报,2024,14(2):642-650 doi: 10.12153/j.issn.1674-991X.20230529
LIU S Y,PENG X T,MA R R,et al.Research progress of advanced oxidation technology based on persulfate activation for the treatment of sulfonamides in water[J].Journal of Environmental Engineering Technology,2024,14(2):642-650 doi: 10.12153/j.issn.1674-991X.20230529
Citation: LIU S Y,PENG X T,MA R R,et al.Research progress of advanced oxidation technology based on persulfate activation for the treatment of sulfonamides in water[J].Journal of Environmental Engineering Technology,2024,14(2):642-650 doi: 10.12153/j.issn.1674-991X.20230529

基于过硫酸盐活化的高级氧化技术处理水中磺胺类药物研究进展

doi: 10.12153/j.issn.1674-991X.20230529
基金项目: 中央级公益性科研院所基本科研业务费专项(2022YSKY-63);国家重点研发计划项目(2022YFC3203301);江西省华赣环境集团有限公司开放课题(HGKF-2020-01)
详细信息
    作者简介:

    刘诗月(1990—),女,讲师,博士,主要研究方向为水污染治理、碳排放管理,liushiyue@sut.edu.cn

    通讯作者:

    李娟(1988—),女,助理研究员,博士,主要研究方向为有毒有害物污染控制技术,lij2007@126.com

  • 中图分类号: X703

Research progress of advanced oxidation technology based on persulfate activation for the treatment of sulfonamides in water

  • 摘要:

    磺胺类药物(SAs)是水中最常被检出的抗生素之一,传统的生物处理无法对其有效降解,研发高效降解SAs的技术具有现实意义。近年来,通过活化过硫酸盐(persulfate,PS)产生硫酸根自由基($\mathrm{SO}_4^{-}\cdot $)的高级氧化技术受到了广泛关注。聚焦于PS的各种活化方法,包括热活化、紫外活化、金属离子及金属氧化物活化、碳材料活化、金属-有机骨架材料活化等,分析了不同活化方法可能的活化机理和优缺点,综述了基于过硫酸盐活化的高级氧化技术(PS-AOPs)在SAs降解中的应用,阐述了PS-AOPs降解SAs的机制。结果表明:活化PS的机制是通过活化方法使其分子结构中的O—O键断裂,从而使PS分解形成$\mathrm{SO}_4^{-}\cdot $或其他活性物质,活化方法决定了PS-AOPs降解SAs的效率。SAs的降解途径分为自由基途径与非自由基途径,其中自由基途径主要包括苯胺部分氧化、磺酰胺基团及相邻位点(C—NH—SO2—C)的裂解等,非自由基途径包括电子传递、表面活化、单线态氧(1O2)作用等。最后,提出未来研究重点应在开发稳定高效活化PS的催化剂以及使用多种处理技术协同作用基础上,加强对SAs降解机制以及含SAs实际废水的研究。

     

  • 图  1  金属离子和金属氧化物对PDS和PMS的活化机理[24]

    Figure  1.  Activation mechanism of metal ions and metal oxide for PDS and PMS

    图  2  SAs的苯胺转化途径

    Figure  2.  Aniline degradation pathways of SAs

    图  3  SAs原子编号

    Figure  3.  Atom numbering of SAs

    表  1  PMS和PDS的基本特征

    Table  1.   Basic features of PMS and PDS

    氧化剂 化学式 结构式 分子量 溶解度/(g/L) 氧化还原电位/V O—O键键长/Å O—O键键能/(kJ/mol)
    PMSHSO5114.07>2501.821.453140~213.3
    PDSH2S2O8194.13>5202.011.497140
    下载: 导出CSV

    表  2  热活化PS降解SAs的条件与效果

    Table  2.   Conditions and effects of thermally activated persulfate for the degradation of SAs

    SAs类别 SAs浓度/
    (μmol/L)
    氧化剂及
    浓度/(mmol/L)
    温度/℃ pH 反应
    时间/h
    去除率/%
    SMX[13] 30 PDS,2 50 7 8 50
    SIX[13] 30 PDS,2 50 7 8 100
    STZ[13] 30 PDS,2 50 7 8 100
    SD[14] 30 PDS,2 60 7 6 100
    SMR[14] 30 PDS,2 50 9 2 86
    SMX[15] 39 PDS,4 70 9.5 1 93
    下载: 导出CSV

    表  3  紫外活化PS降解SAs的条件与效果

    Table  3.   Conditions and effects of UV-activated PS for the degradation of SAs

    SAs类别 SAs浓度/
    (μmol/L)
    氧化剂及
    浓度/
    (mmol/L)
    紫外线
    功率/W
    紫外线
    波长/nm
    pH 反应
    时间/min
    去除
    率/%
    SD[21] 3.9 PDS,0.18 28 254 10 99.8
    SMX[22] 20 PDS,1 10 254 3 60 100
    SMZ[18] 53 PDS,0.44 15 254 7 60 100
    SMZ[19] 20 PDS,0.2 15 254 6.5 45 96.5
    SMX[20] 100 PDS,2 46 7 5 接近100
    下载: 导出CSV

    表  4  金属离子及其氧化物活化PS降解SAs的条件与效果

    Table  4.   Conditions and effects of metal ions and metal oxide-activated PS for the degradation of SAs

    SAs类别 SAs浓度/(μmol/L) 氧化剂及浓度/(mmol/L) 催化剂 pH 反应时间/min 去除率/%
    SMX[25] 10 PMS,0.1 Co2+ 3 30 62.3
    SMR[26] 100 PDS,0.4 Ag+ 3 240 85
    SMX[27] 63047 PDS,1 849 656 Fe2+ 3 30 57.3
    SD[28] 8 PMS,0.033 CuFeO2RCs 6.8 24 接近100
    SMX[29] 39 PMS,0.65 CoFe2O4 7 10 91
    SMM[30] 64 PDS,0.9 Fe3O4 6 180 88
    SDM[30] 64 PDS,100 Fe3O4 7 180 99.8
    SMX[31] 6 PDS,0.14 α-Fe2O3 6.8 180 接近100
    下载: 导出CSV

    表  5  碳材料活化PS降解SAs的条件与效果

    Table  5.   Conditions and effects of carbon material-activated PS for the degradation of SAs

    SAs类别 催化剂 催化剂
    浓度/(g/L)
    氧化剂
    及浓度/
    (mmol/L)
    pH 掺杂
    类型
    去除
    率/%
    SMX[36] 活性炭 0.1 PMS,0.5 7.2 91.2
    SMX[37] 活性炭 PMS,5 95
    SMX[38] 生物炭 0.05 PMS,4 接近100
    SMX[39] 生物炭 0.1 PDS,0.5 10 氮、硫 68.8
    SCP[41] 氧化还原
    石墨烯(RGO)
    0.2 PDS,7.39 100
    SMX[42] 碳纳米管
    (CNTs)
    0.1 PMS,1 7 Fe3C 100
    SMX[43] 石墨烯 0.5 PMS,800 3.4 91.7
    SMX[44] 石墨烯 0.05 PMS,1 6 N 99.9
    下载: 导出CSV

    表  6  MOFs材料活化PS降解SAs的条件与效果

    Table  6.   Conditions and effects of MOFs-activated PS for the degradation of SAs

    SAs类别 催化剂 催化剂浓度/(g/L) 氧化剂及浓度/(mmol/L) pH 改性类型 去除率/%
    SMZ[49] MIL-10(Cr) 0.15 PDS,10 6.0 80
    SMX[50] MIL/PDA 0.1 PDS,4 79.2
    SMX[51] Fe-MOFs-2 1 PDS,3.7 3 调节剂 91.95
    SMT[52] DMOFS 0.1 PMS,1 10 高温碳化 提高1.8倍
    SMX[53] MnOx@NC 0.05 PMS,0.55 5.2 氮掺杂、碳化 72.9
    SMX[54] Co-NC-C 0.1 PMS,0.74 7 碳化 接近100
    SMX[55] CuFe2O4/Fe2O3 0.2 PMS,6 3.4 双金属、碳化 99.7
    下载: 导出CSV

    表  7  PS-AOPs在降解SAs过程中的主要活性物种

    Table  7.   Main active species in the degradation of SAs by PS-AOPs

    SAs类别 氧化剂 活化方法 起主要作用的活性氧剂
    SMX[28] PMS CoFe2O4 ·OH、1O2
    SMX[38] PMS 氮掺杂碳材料 $\mathrm{SO}_4^{-}\cdot $、1O2
    SMZ[48] PDS MIL-101(Cr) $\mathrm{SO}_4^{-}\cdot $
    SMX[53] PMS MOFs衍生碳材料 $\mathrm{SO}_4^{-}\cdot $、1O2、$\mathrm{O}_2^{-} \cdot$
    下载: 导出CSV
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  • 收稿日期:  2023-07-17
  • 录用日期:  2023-12-29
  • 修回日期:  2023-10-22

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