Chinese Journal of Applied Chemistry ›› 2024, Vol. 41 ›› Issue (2): 217-229.DOI: 10.19894/j.issn.1000-0518.230310
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Tian-Li SUN1, Guo ZHU1, Hai HE1, Bing-Kun HUANG2, Zhao-Kun XIONG2(), Bo LAI2()
Received:
2023-10-10
Accepted:
2023-12-24
Published:
2024-02-01
Online:
2024-03-05
Contact:
Zhao-Kun XIONG,Bo LAI
About author:
laibo@scu.edu.cnSupported by:
CLC Number:
Tian-Li SUN, Guo ZHU, Hai HE, Bing-Kun HUANG, Zhao-Kun XIONG, Bo LAI. Research Prospect of Single-Atom Catalysts for Fenton-Like Water Treatment[J]. Chinese Journal of Applied Chemistry, 2024, 41(2): 217-229.
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URL: http://yyhx.ciac.jl.cn/EN/10.19894/j.issn.1000-0518.230310
Fig.1 (a) High-angle annular dark field scanning transmission electron microscopy (HAADF-STEM) images and high-resolution HAADF-STEM images (insets) of Pd-nanoparticles@ZIF-8, intermediate Ⅰ, intermediate Ⅱ and Pd single atoms[24]; (b) Schematic illustrations of Pt ALD mechanism on graphene nanosheets[27]
Fig.3 (a) Energy profiles of Co(Ⅳ)O formation for CoN6/PMS and CoN5O1/PMS systems; *O represents the reactive species of Co(?Ⅳ??)?O[36]; (b) The proposed reaction mechanisms of Vis/TiFeAS/PMS system[37]; (c) Schematic illustration of a local electric field-induced coupled electron-proton transfer process promoting the conversion of high-valent metal-oxo species[38]; (d) Relationship between spin states and Fenton-like catalytic activity of transition metals[39]
Fig.4 (a) Scheme diagram proposed for the Fenton-like reaction mechanism of C3N4-Fe-rGO/PDS[4]?; (b) The degradation performance during cycles of solution with different pH conditions, with C3N4-Fe-rGO as the catalyst[4]; (c) Depiction of Cu1-Cu1 distance manipulation for PDS adsorption and activation[41]; (d) First-order rate constants and TOFs of BPA removal by Cu1/NG with different Cu site densities activating PDS[41]??; (e) Electron density difference for PDS adsorption on 2Cu-N4 and Cu-N4 and the corresponding charge transfer. Yellow and cyan contours stand for electron accumulation and deletion, respectively[41]
Fig.5 (a) Photo and SEM image of the filter medium. Scale bar: 100 μm. Inset, magnified SEM image showing the Cu-C3N4 catalyst coated on the surface of a carbon fibre. Scale bar: 5 μm[44]?; (b) Dye removal and Cu concentration in effluent as functions of filtration time[44]?; (c) Charge density differences of FeN5 and FeN4 models. The yellow and skyblue regions represent electron accumulation and electron depletion, respectively[45]; (d) Energy diagram of the reaction process for FeN5 and FeN4 models[45]?; (e) Degradation of select organic pollutants in FeN4/NG+H2O2, FeN5/NG+H2O2, conventional homogeneous Fenton (Fe2++H2O2) and control (H2O2) systems[45]
Fig.6 (a) Comparison between the apparent rate constants of g-C3N4 and FeCN (inset: TOC result)?[49]; (b) Full-scan chromatogram of CH3COO?-TEMPO[49]; (c) Mass spectral analyses of the 18O-labeled or unlabeled PMSO2 generated in the FeCN+PAA system[49]; (d) Degradation of 4-CP by IO4- activated using different activators[50]; (e) Initial solution pH on the degradation of 4-CP in the N-rGO-CoSA IO4- system[50]; (f) Current response after the sequential addition of IO4- and 4-CP at the working electrode coated with the N-rGO-CoSA powder. The inset shows the EIS profiles of the N-rGO-CoSA and N-rGO-800 electrodes in the electrolyte solution[50]; (g) Substrate dependence diagram in Fe5-NC/O3 system[51]; (h) Dynamic processes simulated by AIMD[51]; (i) Relative energy profile calculated by DFT in the interaction of O3 and the Fe-N4 site[51]
Fig.7 (a) Pilot device and effect of Cu-SA in continuous flow unit[55]; (b) BPA removal in deionized water and secondary effluent of WWTP with Fe-CNW3 coated membrane filter under continuous flow. Inset is the HADDF-STEM image of Fe-CNW3 after the reaction[59]; (c) Schematic and photograph of the catalytic membrane (effective area of 3.1 cm2) are installed and the dead-end filtration cell for micropollutant removal. APAP is selected as a model micropollutant[60]; (c) APAP removal efficiency by the catalytic membranes during filtration[60]
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