2021
DOI: 10.1016/j.mcat.2021.111770
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Highly selective and stable ZnO-supported bimetallic RuSn catalyst for the hydrogenation of octanoic acid to octanol

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Cited by 5 publications
(5 citation statements)
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“…According to DFT calculations selective hydrogenation of benzoic acid to benzyl alcohol over Pt/SnO2 catalyst occurred due to selective absorption of carboxylic group instead of aromatic ring of benzoic acid [5]. For hydrogenation of octanoic acid Ru-Sn supported on ZnO catalyst gives 99.4% conversion and 93.0% selective to octanol [6,7]. To date, no comprehensive study has been conducted on the influence of the Sn/Ru ratio in the Ru-Sn/Al2O3 catalyst on the hydrogenation of aromatic carboxylic acids, which could elucidate the role of Sn in inhibiting hydrogenolysis.…”
Section: Introductionmentioning
confidence: 99%
“…According to DFT calculations selective hydrogenation of benzoic acid to benzyl alcohol over Pt/SnO2 catalyst occurred due to selective absorption of carboxylic group instead of aromatic ring of benzoic acid [5]. For hydrogenation of octanoic acid Ru-Sn supported on ZnO catalyst gives 99.4% conversion and 93.0% selective to octanol [6,7]. To date, no comprehensive study has been conducted on the influence of the Sn/Ru ratio in the Ru-Sn/Al2O3 catalyst on the hydrogenation of aromatic carboxylic acids, which could elucidate the role of Sn in inhibiting hydrogenolysis.…”
Section: Introductionmentioning
confidence: 99%
“…Most recently, Ru-Sn/ZnO catalyst was employed for hydrogenation of octanoic acid to octanol in a fixed-bed continuous reactor system at elevated temperatures (300 °C) and 30 bar H2. The presence of Ru3Sn7 al-loy phase was the active site for the significant improvement of the hydrogenation activity and selectivity to octanol as well as the stability in long-term reactions [35].…”
Section: Introductionmentioning
confidence: 99%
“…They claimed that Ru 3 Sn 7 and SnO x were active species in the bimetallic Ru-Sn catalyst as indicated by the conversion and product selectivity, and computational modelling calculation. 37,38 In the case of direct modication of PGM with metal oxides, oxophilic metal oxides (e.g., ReO x , MoO x , and WO x )-modied PGM-based catalysts showed excellent performance for the catalytic HDO of biomass-derived oxygenates into chemicals and fuels. [39][40][41][42][43][44][45] The presence of oxophilic metal oxides played the bifunctional catalytic roles, whereas the metal sites can catalyse the hydrogen uptake, dissociation, and spill-over onto the metal-oxide in vicinity.…”
Section: Introductionmentioning
confidence: 99%
“…They claimed that Ru 3 Sn 7 and SnO x were active species in the bimetallic Ru–Sn catalyst as indicated by the conversion and product selectivity, and computational modelling calculation. 37,38 In the case of direct modification of PGM with metal oxides, oxophilic metal oxides ( e.g. , ReO x , MoO x , and WO x )-modified PGM-based catalysts showed excellent performance for the catalytic HDO of biomass-derived oxygenates into chemicals and fuels.…”
Section: Introductionmentioning
confidence: 99%