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Frontiers of Materials Science

ISSN 2095-025X

ISSN 2095-0268(Online)

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2018 Impact Factor: 1.701

Front. Mater. Sci.    2024, Vol. 18 Issue (1) : 240673    https://doi.org/10.1007/s11706-024-0673-0
Comparative studies on Fenton-like reactions catalyzed by Fe3O4 loaded inside and outside halloysite nanotubes for the removal of organic pollutants
Yang Li, Jia-Qi Zhou, Huan-Yan Xu(), Li-Min Dong, Mao-Chang Cao, Lian-Wei Shan, Li-Guo Jin, Xiu-Lan He, Shu-Yan Qi
Heilongjiang Provincial Key Laboratory of CO2 Resource Utilization and Energy Catalytic Materials, School of Materials Science and Chemical Engineering, Harbin University of Science and Technology, Harbin 150040, China
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Abstract

In this work, Fe3O4 nanoparticles (NPs) loaded inside and outside halloysite nanotubes (HNTs) were prepared and developed as the heterogeneous Fenton-like catalysts for the removal of representative organic pollutants. Characterization results indicated that the samples with Fe3O4 NPs loaded outside the HNTs lumen (Fe3O4/HNTs) and inside the HNTs lumen (Fe3O4@HNTs) were successfully prepared. Both samples had typical magnetic hysteresis loops, while Fe3O4@HNTs exhibited higher magnetization intensity. The comparative experiments showed that Fe3O4@HNTs had better Fenton-like catalytic ability than that of Fe3O4/HNTs in the degradation of various organic pollutants. Taking Rhodamine B (RhB) as an example, the adsorption thermodynamics and kinetics of RhB onto Fe3O4/HNTs and Fe3O4@HNTs were also investigated. The comparative results demonstrated that the adsorption ability of Fe3O4/HNTs was better than that of Fe3O4@HNTs. Moreover, the dissolved concentration of Fe2+ and production amount of hydroxyl radical (·OH) in the Fe3O4@HNTs-H2O2 system were significantly higher than those in the Fe3O4/HNTs-H2O2 system. Based on aforementioned comparison, the nano-confinement effect in the Fe3O4@HNTs-H2O2 system was verified. This work provides meaningful guidance for the cheap and convenient design of nanoreactors for Fenton-like applications.

Keywords Fe3O4      halloysite nanotube      adsorption      Fenton-like reaction      mechanism     
Corresponding Author(s): Huan-Yan Xu   
Issue Date: 07 February 2024
 Cite this article:   
Yang Li,Jia-Qi Zhou,Huan-Yan Xu, et al. Comparative studies on Fenton-like reactions catalyzed by Fe3O4 loaded inside and outside halloysite nanotubes for the removal of organic pollutants[J]. Front. Mater. Sci., 2024, 18(1): 240673.
 URL:  
https://academic.hep.com.cn/foms/EN/10.1007/s11706-024-0673-0
https://academic.hep.com.cn/foms/EN/Y2024/V18/I1/240673
Fig.1  XRD patterns of Fe3O4, HNTs, Fe3O4/HNTs and Fe3O4@HNTs.
Fig.2  FTIR spectra of Fe3O4, HNTs, Fe3O4/HNTs and Fe3O4@HNTs.
Fig.3  SEM images of (a) Fe3O4 NPs, (b) HNTs, (c) Fe3O4/HNTs, and (d) Fe3O4@HNTs. TEM images of (e) Fe3O4/HNTs and (f) Fe3O4@HNTs (inset: image with higher magnification).
Fig.4  Magnetization curves of Fe3O4/HNTs and Fe3O4@HNTs (insets: digital photographs of the separation of both samples by an external magnet).
Fig.5  Comparative Fenton-like degradation of (a) RhB, (b) MB, (c) MG, (d) MO, (e) CR, and (f) PNP over Fe3O4/HNTs and Fe3O4@HNTs (experimental conditions: [H2O2] = 3 mL·L?1, [RhB] = [MB] = [MG] = [MO] = [CR] = [PNP] = 30 mg·L?1, [Fe3O4@HNTs] = [Fe3O4/HNTs] = 0.5 g·L?1, pH = 2, and T = 20 °C).
Fig.6  (a) Comparative evaluation of the RhB degradation in different systems, (b) ·OH quenching tests with 0.1 mmol·L?1 TBA and (c) cyclic experiments (experimental conditions: [H2O2] = 3 mL·L?1, [RhB] = 30 mg·L?1, [Fe3O4@HNTs] = [Fe3O4/HNTs] = 0.5 g·L?1, pH = 2, and T = 20 °C).
Fig.7  (a)(b) Adsorption isothermal curves, (c)(d) Langmuir fitting lines, and (e)(f) Freundlich fitting lines of RhB adsorption onto Fe3O4/HNTs (upper panels) and Fe3O4@HNTs (lower panels) (experimental conditions: pH = 2 and [Fe3O4/HNTs] = [Fe3O4@HNTs] = 0.5 g·L?1).
Fig.8  (a)(b) Evolution of the adsorption capacity over time, (c)(d) the quasi-first-order kinetic fitting lines, and (e)(f) the quasi-second-order kinetic fitting lines of the RhB adsorption onto Fe3O4/HNTs and Fe3O4@HNTs (experimental conditions: pH = 2, [RhB] = 30 mg·L?1, and [Fe3O4/HNTs] = [Fe3O4@HNTs] = 0.5 g·L?1).
SampleT/°CLangmuir modelFreundlich model
QmKLR21/nKFR2
Fe3O4/HNTs204.55001.72070.99930.04493.79630.9072
304.96921.14030.99830.06413.83020.9629
405.02211.45990.99920.06103.94600.9665
505.10001.30890.99900.06933.88120.9528
Fe3O4@HNTs201.75500.75190.99400.07931.25950.7630
301.88471.00150.99790.07961.37000.9055
402.07632.44840.99930.04671.73510.7172
502.12791.28990.99890.08291.54470.8774
Tab.1  Fitting parameters of Langmuir and Freundlich models for the RhB adsorption onto Fe3O4/HNTs and Fe3O4@HNTs at different temperatures
SampleQuasi-first-order kineticsQuasi-second order kinetics
Qe/(mg·g?1)K1/min?1R2Qe/(mg·g?1)K2/min?1R2
Fe3O4/HNTs3.97200.27060.97145.60600.07220.9838
Fe3O4@HNTs1.91430.28290.95753.02700.04270.9786
Tab.2  Kinetic fitting parameters of quasi-first-order and quasi-second-order models
Fig.9  The evolution of reactive species in the Fe3O4@HNTs-H2O2 and Fe3O4/HNTs-H2O2 systems: (a) total iron ion concentration; (b) ferrous ion concentration; (c) absorbance of ·OH adduct; (d) H2O2 concentration.
Fig.10  Mechanism illustration of Fenton-like reactions catalyzed by Fe3O4/HNTs and Fe3O4@HNTs.
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