2016
DOI: 10.1016/j.apcatb.2015.07.043
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Selective oxidation of 5-hydroxymethyl furfural over non-precious metal heterogeneous catalysts

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Cited by 117 publications
(73 citation statements)
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“…Therefore, in this study, we propose to clarify some mechanistic aspects for the selective oxidation of p ‐cymene with O 2 in the presence of a Mn–Fe mixed‐oxide heterogeneous catalyst. This catalyst was chosen because Mn 2+ ions are one of the main components of the industrial catalyst for the oxidation of p ‐xylene to TA and because the incorporation of Fe 3+ ions in manganese oxide enhances its redox properties . The role of Mn in Co/Fe/O spinel‐type oxides as an electron/O 2− ion carrier in the chemical‐loop reforming of ethanol was also recently investigated, and Mn affects the redox properties of the spinel…”
Section: Introductionmentioning
confidence: 99%
“…Therefore, in this study, we propose to clarify some mechanistic aspects for the selective oxidation of p ‐cymene with O 2 in the presence of a Mn–Fe mixed‐oxide heterogeneous catalyst. This catalyst was chosen because Mn 2+ ions are one of the main components of the industrial catalyst for the oxidation of p ‐xylene to TA and because the incorporation of Fe 3+ ions in manganese oxide enhances its redox properties . The role of Mn in Co/Fe/O spinel‐type oxides as an electron/O 2− ion carrier in the chemical‐loop reforming of ethanol was also recently investigated, and Mn affects the redox properties of the spinel…”
Section: Introductionmentioning
confidence: 99%
“…7 Among the studied heterogeneous catalysts are noteworthy those based on noble metals such as Pt, 8,9 Au, 10,11 and Ru. 12 However, it should be underlined that in most of the reported reaction procedures a base additive, essentially NaOH, KOH or Na 2 CO 3 , is required, [13][14][15] so only very few works applying base-free catalysts have been reported.…”
Section: Introductionmentioning
confidence: 99%
“…The average particle size of the Co-Mn-0.25 catalyst was approximately 6.5 nm (measured throughi maging software),w hichw as in ag ood agreement with ar ecent literature reporto faM n-modifiedc obalt oxide catalystp repared through solid-state grinding. [40] Thes urface base concentration of the Co-Mn-0.25 catalyst wase stimated to be 0.97 mmol g À1 , which was the highest among the other catalysts analyzed. Both techniques revealed that thesec atalysts contained both acidic and basic sites, as well as the same acid andb ase type.…”
Section: Characterization Of the Fresh And Spent Catalystsmentioning
confidence: 89%
“…[39] The acid-base properties of the catalyst were investigated by ammonia temperature programmed desorption (NH 3 -TPD) and CO 2 -TPD, and the results are presentedi nF igures S6 and S7. [40,15] This variation in the catalytic selectivity with calcination temperature( as shown in Figure 1) could be attributedt ot he variation in the structuralp roperties of the catalysts during thermal treatment (calcination). The total acidity and basicity of the catalysts were measured from the peak areas of the TPD profile and presented in Ta ble S3.A ll catalysts contained both weak and strong acid sites and the Co-Mn-0.25 catalyste xhibited al ower acidity than the others.C onversely,t he CO 2 -TPD profile of the MnO x catalysts howed as harpC O 2 desorption peak in the high-temperatureregion,whereas the Co-Mn catalysts exhibited adistribution of basic sites in the low-and high-temperature regions, indicating the presence of strong basic sites on the catalyst surface.…”
Section: Characterization Of the Fresh And Spent Catalystsmentioning
confidence: 93%