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磁性生物炭复合材料活化过硫酸盐降解抗生素的研究进展

王桂华 李健 顾迎春 阎斌

王桂华, 李健, 顾迎春, 等. 磁性生物炭复合材料活化过硫酸盐降解抗生素的研究进展[J]. 复合材料学报, 2025, 42(1): 6746-6761. doi: 10.13801/j.cnki.fhclxb.20240521.001
引用本文: 王桂华, 李健, 顾迎春, 等. 磁性生物炭复合材料活化过硫酸盐降解抗生素的研究进展[J]. 复合材料学报, 2025, 42(1): 6746-6761. doi: 10.13801/j.cnki.fhclxb.20240521.001
WANG Guihua, LI Jian, GU Yingchun, et al. Research progress on activated persulfate degradation of antibiotics by magnetic biochar composites[J]. Acta Materiae Compositae Sinica, 2025, 42(1): 6746-6761. doi: 10.13801/j.cnki.fhclxb.20240521.001
Citation: WANG Guihua, LI Jian, GU Yingchun, et al. Research progress on activated persulfate degradation of antibiotics by magnetic biochar composites[J]. Acta Materiae Compositae Sinica, 2025, 42(1): 6746-6761. doi: 10.13801/j.cnki.fhclxb.20240521.001

磁性生物炭复合材料活化过硫酸盐降解抗生素的研究进展

doi: 10.13801/j.cnki.fhclxb.20240521.001
基金项目: 国家自然科学基金(21876119)
详细信息
    通讯作者:

    阎斌,博士,研究员,硕士生/博士生导师,研究方向为生物基高分子材料及表界面功能材料 E-mail: yanbinscu@126.com

  • 中图分类号: X703;TB332

Research progress on activated persulfate degradation of antibiotics by magnetic biochar composites

Funds: National Natural Science Foundation of China (21876119)
  • 摘要: 抗生素具有高水溶性、高化学稳定性、潜在致癌性、明显的生态毒性和难以生物降解等特点,对水环境的可持续性和人类健康构成了严重威胁。因此,建立有效去除水中的抗生素污染物的方法至关重要。磁性生物炭复合材料因其优异的过硫酸盐活化催化能力和可回收性,在抗生素污染物的氧化降解方面受到广泛关注。本文综述了磁性生物炭复合材料活化过硫酸盐降解抗生素的研究进展。首先,我们总结了不同生物质来源的磁性生物炭复合材料及其常用制备方法。然后,探讨了磁性生物炭复合材料活化过硫酸盐降解抗生素类污染物的机制及其对不同类型抗生素的降解行为。最后,针对目前抗生素污染引起的其他问题,提出了未来研究的挑战和展望。

     

  • 图  1  磁性生物炭复合材料活化过硫酸盐(PS)降解抗生素的研究进展

    Figure  1.  Research progress on activated persulfate (PS) degradation of antibiotics by magnetic biochar composites

    AOP—

    图  2  磁性生物炭复合材料活化PS降解抗生素的机制

    Figure  2.  Mechanism of magnetic biochar composite activated persulfate to degrade antibiotics

    图  3  (a) 竹子制备的锰掺杂磁性生物炭(MMBC)用于四环素(TC)的降解;(b) MMBC活化PS的电子自旋共振(ESR)谱; (c) TC的降解过程;(d) PS在MMBC上活化降解TC的主要催化机制[40]

    Figure  3.  (a) Mn doped magnetic biochar (MMBC) prepared from bamboo for TC degradation; (b) Electron spin resonance (ESR) spectra of PS activation by MMBC; (c) Proposed degradation process of TC; (d) Main catalytic mechanism of PS activation on MMBC for TC degradation[40]

    DMPO—5, 5-dimethyl-1-pyrroline N-oxide

    图  4  (a) 丝瓜络生物炭(LBC)、Fe2O3和Fe2O3@LBC对头孢氨苄(CEX)的去除;(b) Fe2O3@LBC/PS体系中的电子顺磁共振(EPR)谱;(c) Fe2O3@LBC活化PS降解CEX的可能机制;(d)降解CEX的反应途径[35]

    Figure  4.  (a) Removal of CEX by loofah biochar (LBC), Fe2O3 and Fe2O3@LBC; (b) DMPO spin trapping electron paramagnetic resonance (EPR) spectra in the Fe2O3@LBC/PS system; (c) Possible mechanism of PS activation by Fe2O3@LBC for CEX degradation; (d) Proposed reaction pathway for the degradation of CEX[35]

    C/C0

    图  5  (a) 生物炭负载磁性MIL-53(Fe)衍生物作为过硫酸氢盐活化降解抗生素的有效催化剂;(b) 诺氟沙星(NOR)的降解转化途径;(c) 生物炭负载的MIL-53(Fe)衍生物(1.0-BC@FexC/PDS)同时去除NOR的可能反应机制[41]

    Figure  5.  (a) Biochar supported magnetic MIL-53(Fe) derivatives as an efficient catalyst for peroxydisulfate activation towards antibiotics degradation; (b) Proposed transformation pathways of NOR degradation; (c) Possible reaction mechanism for the simultaneous removals of NOR by the biochar-loaded MIL-53(Fe) derivatives (1.0-BC@FexC/PDS) process[41]

    H2BDC—1, 4-terephthalic acid; DMF—N, N-dimethyl formamide

    图  6  (a) CoFe2O4/BC/PMS/SMX体系可能的催化降解机制;$\text{SO}_{4}^{-}{\text{•}} $和 HO• (b)、 1O2 (c)在不同体系中的EPR谱;(d) SMX在CoFe2O4/BC/PMS体系中可能的降解途径[27]

    Figure  6.  (a) Possible catalytic degradation mechanism over CoFe2O4/BC/PMS/SMX system; EPR spectra of $\text{SO}_{4}^{-}{\text{•}} $ and HO• (b), 1O2 (c) in different systems; (d) Possible degradation pathways of SMX in the CoFe2O4/BC/PMS system[27]

    表  1  不同生物质来源制备的磁性生物炭复合材料的催化性能

    Table  1.   Catalytic properties of magnetic biochar materials prepared from different biomass sources

    Magnetic biochar Source Magnetic
    substance
    Preparation method PS Antibiotics Active
    substance
    Removal efficiency/% Ref.
    Magnetic rape straw biochar Rape straw Fe3O4 Pyrolysis PDS TC $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 99.0 [26]
    CoFe2O4/biochar Rape straw CoFe2O4 Solvothermal PMS SMX $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 93.0 [27]
    Magnetic biochar Rice straw Fe3C
    Fe4N
    Pyrolysis PDS TC $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 90.5 [28]
    Coral reef-like FeS2/biochar Corn stalks FeS2 Solvothermal PMS TC $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 100.0 [29]
    Modified red mud biochar Corn straw Fe3O4 Pyrolysis PDS LFX $\text{SO}_{4}^{-}{\text{•}} $ and HO• 88.6 [30]
    Fe3O4 supported by N-doped biochar Corncob Fe3O4
    ZnFe2O4
    Coprecipitation PDS TC $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 91.6 [31]
    Nitrogen-doped magnetic carbon nanotubes-bridged biochar Rice husk Fe3O4 Impregnation-
    pyrolysis
    PMS SMX $\text{SO}_{4}^{-}{\text{•}} $, HO• and 1O2 98.2 [32]
    Magnetic iron-char
    composites
    Peanut shells Fe3O4 Impregnation-
    pyrolysis
    PDS SMX $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 99.4 [33]
    FeS@biochar Peanut shells FeS Pyrolysis PDS SMT $\text{SO}_{4}^{-}{\text{•}} $, HO• and 1O2 96.4 [34]
    Magnetic loofah biochar Loofah Fe2O3 Impregnation-
    pyrolysis
    PDS CEX $\text{SO}_{4}^{-}{\text{•}} $ and HO• 73.9 [35]
    Cobalt and iron coloaded pomelo peel biochar composite Pomelo peels CoFe2O4 Impregnation and
    coprecipitation
    PMS TC $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 86.2 [36]
    MgFe2O4/biochar Pomelo peels MgFe2O4 Coprecipitation PDS LFX $\text{O}_{2}^{-} {\text{•}}$ and 1O2 87.9 [37]
    MnFe2O4/biochar Banana
    pseudo-stem
    MnFe2O4 Sol-gel pyrolysis PDS TC $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 94.7 [38]
    Lanthanum-doped
    magnetic biochar
    Bagasse Fe3O4 Impregnation-
    pyrolysis
    PDS FLO $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 99.5 [39]
    Mn doped magnetic biochar Bamboo Fe3O4, Fe3C
    and MnFe2O4
    Impregnation-
    pyrolysis
    PDS TC $\text{SO}_{4}^{-}{\text{•}} $ and HO• 93.0 [40]
    Biochar-loaded MIL-53(Fe) derivatives Bamboo Fe3O4, Fe0 and
    α-Fe2O3
    Pyrolysis PDS NOR $\text{SO}_{4}^{-}{\text{•}} $, HO• and 1O2 91.2 [41]
    FeS@biochar Pine sawdust FeS Ball milling PDS TC $\text{SO}_{4}^{-}{\text{•}} $ and HO• 87.4 [42]
    Potassium-doped magnetic
    biochar
    Pine sawdust Fe3O4,
    α-Fe2O3
    Impregnation-
    pyrolysis
    PDS MNZ $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 98.4 [43]
    Mn-based magnetic biochar Pine sawdust Fe3O4 Impregnation-
    pyrolysis
    PDS MNZ $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 95.6 [44]
    Nitrogen-rich magnetic
    biochar
    Pine sawdust Fe3O4,
    α-Fe2O3
    Impregnation-
    pyrolysis
    PDS MNZ $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 99.6 [45]
    CoFe2O4/biochar Sludge/pine
    needle
    CoFe2O4 Hydrothermal PMS TC SO4• and HO• 99.8 [46]
    Magnetic N-doped iron sludge based biochar Sycamore leaves and sludge Fe3O4 Pyrolysis PDS TC $\text{SO}_{4}^{-}{\text{•}} $, HO• and 1O2 86.6 [47]
    MnFe2O4/biochar Eichhornia crassipes MnFe2O4 Coprecipitation PMS TC,
    SMX
    $\text{SO}_{4}^{-}{\text{•}} $, HO• and 1O2 90.1
    96.5
    [48]
    Co/N co-doped biochar Kelp Co Pyrolysis PMS TC $\text{SO}_{4}^{-}{\text{•}} $, HO• and 1O2 99.0 [49]
    Copper doping in magnetic
    biochar
    Cow dung Fe3O4 Impregnation-
    pyrolysis
    PMS SMX,
    CIP
    $\text{SO}_{4}^{-}{\text{•}} $, HO•, O2and 1O2 91.7
    97.3
    [21]
    Magnetic biochar Piggery sludge Fe3O4
    α-Fe2O3
    Coprecipitation PMS TC $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 77.2 [50]
    Fe/Mn bimetal co-functionalized sludge biochar Sludge Fe3O4 Impregnation-
    pyrolysis
    PDS SMX 1O2 98.8 [51]
    Magnetic nitrogen-doped
    sludge-derived biochar
    Sludge γ-Fe2O3 Pyrolysis PDS TC $\text{SO}_{4}^{-}{\text{•}} $ and HO• 82.2 [52]
    N-functionalized sewage sludge -red mud complex biochar Sludge Fe3O4 Pyrolysis PMS SMX $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 97.5 [53]
    Co-Fe/SiO2 Iron sludge Co-Fe-LBH Solvothermal PMS CIP $\text{SO}_{4}^{-}{\text{•}} $ and HO• 98.0 [54]
    Iron-loaded biochar Fermentation dreg Fe3O4 Coprecipitation PDS TC $\text{SO}_{4}^{-}{\text{•}} $, HO•, $\text{O}_{2}^{-} {\text{•}}$ and 1O2 85.1 [55]
    Notes: LBH—Layered double hydroxide; PS—Persulfate; PMS—Peroxymonosulfate; PDS—Peroxysulphate; TC—Tetracycline; SMX—Sulfamethoxazole; SMT—Sulfamethazine; CEX—Cephalexin; LFX—Levofloxacin; FLO—Florfenicol; NOR—Norfloxacin; MNZ—Metronidazole; CIP—Ciprofloxacin.
    下载: 导出CSV

    表  2  不同制备磁性生物炭复合材料方法的优点和缺点

    Table  2.   Advantages and disadvantages of different preparation methods

    Preparation method Advantage Disadvantage Ref.
    Impregnation-pyrolysis Magnetization and pyrolysis at the same time,
    simple operation
    Gas pollutants are easy to cause secondary pollution, high temperature energy-consuming crystallinity, size and porosity are difficult to control. [25, 57-59]
    Coprecipitation Simple operation, controlled reaction The introduction of alkaline reagents is required, and the usable surface area of the prepared material is small. [60-61]
    Hydrothermal Low temperatures (100-300℃), mild reaction conditions, no need for bases or strong reducing agents, no need for energy-intensive pre-drying processes Higher dependence on production equipment [18, 22, 62-63]
    Chemical reduction Convenient operation, controllable reaction,
    high product purity
    Reducing agents added are toxic and need to be stored and used properly. [64]
    下载: 导出CSV
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  • 收稿日期:  2024-03-21
  • 修回日期:  2024-05-07
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