Chinese Journal of Applied Chemistry ›› 2024, Vol. 41 ›› Issue (2): 256-267.DOI: 10.19894/j.issn.1000-0518.230307
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Meng-Han CAO1, Peng XU2, Feng-Yin SHI1, Gui-E LI1, Guo-Dong ZHANG1, Qing-Zhu ZHENG1, Guang-Shan ZHANG1()
Received:
2023-10-08
Accepted:
2023-12-24
Published:
2024-02-01
Online:
2024-03-05
Contact:
Guang-Shan ZHANG
About author:
gszhang@qau.edu.cnSupported by:
CLC Number:
Meng-Han CAO, Peng XU, Feng-Yin SHI, Gui-E LI, Guo-Dong ZHANG, Qing-Zhu ZHENG, Guang-Shan ZHANG. Construction of CoFe2O4/MXene Composites and Activation of Persulfate for Degradation of Atrazine[J]. Chinese Journal of Applied Chemistry, 2024, 41(2): 256-267.
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URL: http://yyhx.ciac.jl.cn/EN/10.19894/j.issn.1000-0518.230307
Catalysts | SBET/(m2·g-1) | Pore volume/(cm3·g-1) | Pore size/nm |
---|---|---|---|
CoFe2O4/MXene | 77.83 | 0.10 | 3.09 |
CoFe2O4 | 65.33 | 0.09 | 3.10 |
MXene | 7.32 | 0.07 | 3.82 |
Table 1 Specific surface areas and pore characteristics of MXene, CoFe2O4 and CoFe2O4/MXene
Catalysts | SBET/(m2·g-1) | Pore volume/(cm3·g-1) | Pore size/nm |
---|---|---|---|
CoFe2O4/MXene | 77.83 | 0.10 | 3.09 |
CoFe2O4 | 65.33 | 0.09 | 3.10 |
MXene | 7.32 | 0.07 | 3.82 |
Fig.5 Effect of different oxidation systems on (A) ATZ removal efficiency, (B) corresponding pseudo-first order kinetics (operating condition: ρ(ATZ)= 10 mg/L, ρ(catalyst)= 0.1 g/L, n(PMS)∶n(ATZ)=7∶1, room temperature)
Fig. 6 Effect of mass fraction of MXene on catalyst performance (operating condition: ρ(ATZ)= 10 mg/L, ρ(catalyst)= 0.1 g/L, n(PMS)∶n(ATZ)=7∶1, room temperature)
Fig.7 Effects of (A) the molar ratio of PMS to ATZ, (B) CoFe2O4/MXene dosage, (C) pH values on the ATZ degradation efficiencies, (D) ion dissolution in CoFe2O4/MXene/PMS system (operating condition: ρ(ATZ)= 10 mg/L, mass concentration of catalyst is 0.1 g/L, n(PMS)∶n(ATZ)=7∶1, room temperature)
Fig.8 Coexisting substances (1 mmol/L) on the removal efficiency of ATZ (operating condition: ρ(ATZ)=10 mg/L, ρ(catalyst)= 0.1 g/L, n(PMS)∶n(ATZ)=7∶1, room temperature)
Fig.9 Effects of radical scavengers on (A) the ATZ degradation efficiencies and (B) corresponding pseudo-first order kinetics (operating condition: ρ(ATZ)=10 mg/L, mass concentration of catalyst is 0.1 g/L, n(PMS)∶n(ATZ)=7∶1, n(scavengers)∶n(PMS)=100∶1, room temperature)
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