2021
DOI: 10.1039/d1ra00176k
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A new highly active La2O3–CuO–MgO catalyst for the synthesis of cumyl peroxide by catalytic oxidation

Abstract: The La2O3–CuO–MgO catalyst acts on the oxidation of cumene and shows excellent catalytic activity through the coordination of surface and interior.

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Cited by 12 publications
(9 citation statements)
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“…But, role of CuO oxide can't be neglected, which can provide the surface lattice oxygen to enhance the oxidation of reaction. [37,38] Therefore, this CnHO activity and CnHO selectivity is due to synergetic effect of spinal and oxide present in the catalyst. Catalytic activity exhibited by co-precipitation method having lower Cu 2 + site, is correlated with the contribution of surface oxygen to the reaction (Figure 3c).…”
Section: Resultsmentioning
confidence: 99%
“…But, role of CuO oxide can't be neglected, which can provide the surface lattice oxygen to enhance the oxidation of reaction. [37,38] Therefore, this CnHO activity and CnHO selectivity is due to synergetic effect of spinal and oxide present in the catalyst. Catalytic activity exhibited by co-precipitation method having lower Cu 2 + site, is correlated with the contribution of surface oxygen to the reaction (Figure 3c).…”
Section: Resultsmentioning
confidence: 99%
“…Quantitative calculations of the surface lattice oxygen ratio O α /(O α +O β +−OH) are also presented in Table 2, where the high surface lattice oxygen ratio (27.84 %) was found for HTC‐0.8La. It is worth noting that lattice oxygen is related to the presence of strong base sites on the catalyst surface, and higher lattice oxygen favors the adsorption of ethanol on the catalyst surface [36] …”
Section: Resultsmentioning
confidence: 99%
“…It is worth noting that lattice oxygen is related to the presence of strong base sites on the catalyst surface, and higher lattice oxygen favors the adsorption of ethanol on the catalyst surface. [36] The TG-DTG curves of the HT-0La and HT-0.8La samples are shown in Figure 5. For HT-0La samples, TG curves show three major weight losses: 30-204 °C (adsorbed water), 204-400 °C (bound water, hydroxyl groups and carbonate) and 400-750 °C (further removal of hydroxyl groups and carbonate).…”
Section: Catalystmentioning
confidence: 99%
“…Specifically, the region between 2 θ angles 30–40° displayed peaks corresponding to (0 0 2), (−1 1 1), (2 0 0), and (1 1 1) of CuO in addition to MgO peaks. 56–58 Cu and Mg have similar ionic radii (73 and 72 Å, respectively) and this causes both the solid solution of MgO and CuO as well as a separate CuO nanoparticle phase to form in this catalyst. 56,57 The mesoporous structure of the catalyst material is evident from the type IV isotherm observed by nitrogen physisorption shown in Fig.…”
Section: Resultsmentioning
confidence: 99%
“…56–58 Cu and Mg have similar ionic radii (73 and 72 Å, respectively) and this causes both the solid solution of MgO and CuO as well as a separate CuO nanoparticle phase to form in this catalyst. 56,57 The mesoporous structure of the catalyst material is evident from the type IV isotherm observed by nitrogen physisorption shown in Fig. 2(b).…”
Section: Resultsmentioning
confidence: 99%