2021
DOI: 10.1016/j.apcata.2020.117961
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Selective hydrogenation of phenol to cyclohexanone over Pd nanoparticles encaged hollow mesoporous silica catalytic nanoreactors

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Cited by 20 publications
(8 citation statements)
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“…Figure S6 presents H 2 -TPR studies of the mentioned (PdO) 1 –(Fe x O y ) 1/ x @HMSNs. As shown in Figure S6, the peak at 94 °C is due to the reduction of PdO and is slightly higher than that (70 °C) of PdO@HMSNs reported in our previous work, suggesting the presence of PdO and Fe x O y interaction. The two peaks centered at 427 and 518 °C are due to the reduction of Fe x O y , where the former can be assigned to the reduction of Fe 2 O 3 to Fe 3 O 4 and the latter is ascribed to the reduction of Fe 3 O 4 to metallic Fe. , Although literatures and our TPR studies reported the complete reduction of Fe x O y to metallic Fe at 500–600 °C, , we cannot exclude the possibility of complete reduction of a small amount of Fe x O y at 350 °C in the presence of metallic Pd.…”
Section: Resultscontrasting
confidence: 50%
“…Figure S6 presents H 2 -TPR studies of the mentioned (PdO) 1 –(Fe x O y ) 1/ x @HMSNs. As shown in Figure S6, the peak at 94 °C is due to the reduction of PdO and is slightly higher than that (70 °C) of PdO@HMSNs reported in our previous work, suggesting the presence of PdO and Fe x O y interaction. The two peaks centered at 427 and 518 °C are due to the reduction of Fe x O y , where the former can be assigned to the reduction of Fe 2 O 3 to Fe 3 O 4 and the latter is ascribed to the reduction of Fe 3 O 4 to metallic Fe. , Although literatures and our TPR studies reported the complete reduction of Fe x O y to metallic Fe at 500–600 °C, , we cannot exclude the possibility of complete reduction of a small amount of Fe x O y at 350 °C in the presence of metallic Pd.…”
Section: Resultscontrasting
confidence: 50%
“…The spherical morphology of COF-280 is conducive to the formation of Pd with higher Pd 0 proportion on the catalyst surface (Figures and , Table ), which is in favor of the contact between the reactants and Pd NPs. The current studies suggest that Pd 0 is the active site for the phenol hydrogenation. , Furthermore, the abundant mesopores in COF-280 (Figure , Table ) can enhance the mass transfer during the phenol hydrogenation. These aspects together lead to the superior catalytic activity of Pd@COF-280 for the phenol hydrogenation.…”
Section: Results and Discussionmentioning
confidence: 68%
“…For instance, Pd/C gives the phenol conversion of 96% and the cyclohexanone selectivity of 95% at 80°C and 0.1 MPa H 2 with hexane as solvent [9] . Pd@HMSNs e ciently catalyze hydrogenation of phenol and m-cresol to cyclohexanone derivatives with ≥ 98.3% selectivity at ≥ 99.0% conversions at 55 o C, ambient H 2 pressure and water media [10] . A nearly full conversion of phenol with high selectivity (> 99.0%) to cyclohexanone can be achieved on TiO 2 nanowires supported Pd at 50°C and 5.0 bar H 2 in water [11] Although noble metal catalysts possess high activity, the high-cost limits the wide industrial application.…”
Section: Introductionmentioning
confidence: 99%