2017
DOI: 10.1039/c6ra26587a
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Preparation, characterization and catalytic performance of HPW/aEVM catalyst on oxidative desulfurization

Abstract: Expanded vermiculite (EVM) was prepared, treated with acid (aEVM) and incorporated with H3PW12O40 (HPW) by an ordinary impregnation method.

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Cited by 23 publications
(7 citation statements)
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“…The calculated rate coefficients k at different temperatures observed the Arrhenius equation quite well (Figure d), and the activation energy E a was calculated as 44.54 kJ/mol. Being similar with the reported common E a values, , the temperature could not be the key parameter to influence the ODS rate, let alone having a maximum limitation in case of the thermal decomposition of H 2 O 2 . To further enhance the reaction rate under the same consumption of the H 2 O 2 oxidant, the only way is to improve the collision frequency between DBT and H 2 O 2 molecules.…”
Section: Resultssupporting
confidence: 84%
“…The calculated rate coefficients k at different temperatures observed the Arrhenius equation quite well (Figure d), and the activation energy E a was calculated as 44.54 kJ/mol. Being similar with the reported common E a values, , the temperature could not be the key parameter to influence the ODS rate, let alone having a maximum limitation in case of the thermal decomposition of H 2 O 2 . To further enhance the reaction rate under the same consumption of the H 2 O 2 oxidant, the only way is to improve the collision frequency between DBT and H 2 O 2 molecules.…”
Section: Resultssupporting
confidence: 84%
“…Figure b and 7d show the obtained activation energies of MF‐NiO/2D‐VT and MW‐NiO/2D‐VT catalysts at different rates. In accordance with the Arrhenius equation, we calculated that the activation energies of MF‐NiO/2D‐VT and MW‐NiO/2D‐VT catalyzed acetylene carbonylation were 44.6198 KJ/mol and 10.3785 KJ/mol, respectively; clearly, the reaction activation energy of the MW‐NiO/2D‐VT catalyst is smaller than that of MF‐NiO/2D‐VT, which theoretically demonstrates that the dispersed and small particle size nano‐nickel oxide catalyst has better catalytic performance …”
Section: Resultsmentioning
confidence: 99%
“…Therefore, it is very important to reduce the load of HPW. The large content of HPW required for the reaction is mainly due to the fact that HPW is prone to agglomeration [ 14 ]. Therefore, to reduce the loading of HPW, it is necessary to prevent agglomeration and increase its dispersion on the surface of the support, thereby providing sufficient active sites.…”
Section: Introductionmentioning
confidence: 99%