1993
DOI: 10.1006/jcat.1993.1204
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Preparation of Promoted Platinum Catalysts of Designed Geometry and the Role of Promoters in the Liquid-Phase Oxidation of 1-Methoxy-2-propanol

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Cited by 75 publications
(53 citation statements)
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“…Due to the low oxygen solubility of oxygen in water, circa 1 tool m-3, compared to the concentration of organic reactants which are usually in the order of 100 tool m-3 or higher, the oxygen containing species such as O and OH on the platinum surface can be removed by the organic reactant as soon as the stirring in the reactor is stopped, generally resulting in a zero-valent platinum surface. The only way to obtain insight in the oxidation state during the catalytic reaction is by measuring the open-circuit potential of the catalyst [9,10,28]. For fresh promoted catalysts, the degree of platinum coverage by tin-atoms can be calculated from the amount of hydrogen adatoms oxidized between 0 an 0.4 V vs. RHE before and after tin deposition:…”
Section: Q~i Mptmentioning
confidence: 99%
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“…Due to the low oxygen solubility of oxygen in water, circa 1 tool m-3, compared to the concentration of organic reactants which are usually in the order of 100 tool m-3 or higher, the oxygen containing species such as O and OH on the platinum surface can be removed by the organic reactant as soon as the stirring in the reactor is stopped, generally resulting in a zero-valent platinum surface. The only way to obtain insight in the oxidation state during the catalytic reaction is by measuring the open-circuit potential of the catalyst [9,10,28]. For fresh promoted catalysts, the degree of platinum coverage by tin-atoms can be calculated from the amount of hydrogen adatoms oxidized between 0 an 0.4 V vs. RHE before and after tin deposition:…”
Section: Q~i Mptmentioning
confidence: 99%
“…The actual cause of activity loss depends on the type of reaction and the conditions applied. It seems that when the oxidation rate is controlled by the gas/liquid transfer of oxygen, the catalysts are more likely to be the subject of coverage by carbonaceous products than when the catalysts are applied in the kinetic regime [7][8][9][10]. This phenomenon is reported to be more pronounced when the catalyst is prereduced by the organic reactant [5,7].…”
Section: Introductionmentioning
confidence: 99%
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“…The promoter itself is inactive for the oxidation reactions, but when associated with the noble metal, it can considerably suppress the oxygen poisoning of the Pd surface [30], increase the reaction rate [33,34] and modify the selectivity [12,13,35]. Models proposed to interpret the role of promoters include the formation of i) a complexes between an α-functionalized alcohol, a surface Pt or Pd atom and a promoter [36], ii) a bifunctional catalysis [37], iii) an ordered alloy [34], iv) Bi may act as cocatalyst due to its higher affinity for oxygen and protect Pt or Pd from overoxidation [36] or v) as a homogeneous catalyst by leached promoter [31]. However, the most accepted role of Bi promotion is the geometric (blocking) effect of a fraction of active sites centered on the noble metal, since providing different coordination environment for substrate and in turn improving the catalytic performance of the original catalysts [12,38].…”
Section: Introductionmentioning
confidence: 99%