2021
DOI: 10.1016/j.micromeso.2020.110599
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Dichloromethane catalytic combustion over Co3O4 catalysts supported on MFI type zeolites

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Cited by 18 publications
(5 citation statements)
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“…For the O 1s XPS spectra, three kinds of oxygen species can be observed at BE = 529.8, 531.9, and 532.7 eV assigned to the surface lattice oxygen (O latt ), oxygen within the nonchemical oxide or oxygen-deficient region (O v ) and the surface absorbed water or hydroxyl species (O sur ), respectively. As shown, only one peak corresponding to O sur species is observed for Pt/ZSM-5 catalyst due to the existence of plentiful silicon hydroxyl groups on the ZSM-5 zeolite surface . Two peaks of O latt and O v appear in the spectra of Pt/CeTi and the O v /O total molar ratio is 0.22.…”
Section: Resultsmentioning
confidence: 96%
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“…For the O 1s XPS spectra, three kinds of oxygen species can be observed at BE = 529.8, 531.9, and 532.7 eV assigned to the surface lattice oxygen (O latt ), oxygen within the nonchemical oxide or oxygen-deficient region (O v ) and the surface absorbed water or hydroxyl species (O sur ), respectively. As shown, only one peak corresponding to O sur species is observed for Pt/ZSM-5 catalyst due to the existence of plentiful silicon hydroxyl groups on the ZSM-5 zeolite surface . Two peaks of O latt and O v appear in the spectra of Pt/CeTi and the O v /O total molar ratio is 0.22.…”
Section: Resultsmentioning
confidence: 96%
“…49−51 As shown, only one peak corresponding to O sur species is observed for Pt/ ZSM-5 catalyst due to the existence of plentiful silicon hydroxyl groups on the ZSM-5 zeolite surface. 51 More specifically, the peaks α, β, and γ are ascribed to the desorption of NH 3 adsorbed on the weak acid sites and the peak δ is assigned to the desorption of NH 3 that was chemically absorbed on the strong acid sites, 27 while only NH 3 desorption peaks (peaks α, β, and γ) corresponding to the weak acid sites occur for the Pt/CeTi. After peak fitting and quantitative analysis, Figure 10(B) exhibits that the number of strong acid sites and total acid sites of the Pt−CeTi/ZSM-5 catalysts apparently reduce when the CeO 2 −TiO 2 /ZSM-5 mass ratio generally increases, which may be connected to the reducing amount of the ZSM-5 zeolite and the coverage of Bronsted acid sites by the CeO 2 −TiO 2 mixed oxides.…”
Section: ■ Experimental Sectionmentioning
confidence: 99%
“…Single catalyst has a certain oxidation effect on DCM, but its effect is generally inferior to that of supported catalyst. In the spectrum recorded by Zhang et al [46], compared with the pure Co 3 O 4 catalyst, the A1g band of the Co 3 O 4 /ZSM-5 ratio shifts to a lower frequency, and the analytical peak is about 550℃, which is lower than that of the pure Co 3 O 4 catalyst. During the oxidation process, DCM will be adsorbed by acid sites on the surface of molecular sieve, and chlorine atoms will be removed in the form of HCl.…”
Section: Molecular Sieve Supported Co Catalystmentioning
confidence: 89%
“…Some similar types of observations are also reported previously. 69,70 We have also calculated the average crystalline sizes of the sample by using the Debye-Scherrer equation. 71,72 Table 3 summarizes the results which confirmed that at 400 1C, Co 3 O 4 offers the lowest crystalline size.…”
Section: Transmission Electron Microscopy (Tem) Analysismentioning
confidence: 99%