1960
DOI: 10.1007/bf00906559
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The activity of cadmium oxide as a catalyst for hydrogen dehydrogenation

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Cited by 8 publications
(8 citation statements)
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“…The most restrictive catalytic limitation is the Sabatier principle, which posits that optimal catalysts exhibit intermediate surface binding energies to balance the kinetic rates of two or more reaction phenomena including surface reactions, desorption, or adsorption . Since it was first proposed by Sabatier that the optimal catalyst forms a “surface complex” that readily forms and desorbs, the principle was demonstrated decades later as kinetic plots referred to as “Sabatier volcanoes” with the optimal catalyst existing at the conditions of peak turnover frequency. The lower catalytic rate on either side of the volcano derives from the catalyst favoring one elementary step over the others, resulting in lower overall turnover frequency through the whole sequence of steps. This concept has since been demonstrated across a broad range of chemistries and even extended into “volcano surfaces” or “maps” for multicomponent reactions and dual site catalysts. , …”
Section: Introductionmentioning
confidence: 99%
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“…The most restrictive catalytic limitation is the Sabatier principle, which posits that optimal catalysts exhibit intermediate surface binding energies to balance the kinetic rates of two or more reaction phenomena including surface reactions, desorption, or adsorption . Since it was first proposed by Sabatier that the optimal catalyst forms a “surface complex” that readily forms and desorbs, the principle was demonstrated decades later as kinetic plots referred to as “Sabatier volcanoes” with the optimal catalyst existing at the conditions of peak turnover frequency. The lower catalytic rate on either side of the volcano derives from the catalyst favoring one elementary step over the others, resulting in lower overall turnover frequency through the whole sequence of steps. This concept has since been demonstrated across a broad range of chemistries and even extended into “volcano surfaces” or “maps” for multicomponent reactions and dual site catalysts. , …”
Section: Introductionmentioning
confidence: 99%
“…proposed by Sabatier that the optimal catalyst forms a 'surface complex' that readily forms and desorbs (23) , the principle was demonstrated decades later as kinetic plots referred to as 'Sabatier volcanoes' with the optimal catalyst existing at the conditions of peak turnover frequency (24,25,26) . Lower catalytic rate on either side of the volcano derives from the catalyst favoring one elementary step over the others, resulting in lower overall turnover frequency through the whole sequence of steps.…”
mentioning
confidence: 99%
“…16,17 Quantitative description of the Sabatier principle was captured in Balandin-Sabatier volcano-shaped curves ("volcano curves" for the remainder of the manuscript), which depicted a metric of catalyst activity relative to a descriptor of substrate binding. 18,19 Balandin depicted volcano-shaped curves in 1960 and 1964 for the dehydration and dehydrogenation of alcohols, with the catalytic activity dependent on the bond energies between the alcohol oxygen and the metal oxide catalysts. 18,19 Since that time, volcano curves have been generated for numerous catalytic chemistries including NO x decomposition, 20 propylene oxidation, 21 hydrodesulfurization, 22,23 ammonia synthesis, 24,25 CO oxidation, 26 and oxygenate decomposition, 27 among many other reactions.…”
Section: ■ Introductionmentioning
confidence: 99%
“…18,19 Balandin depicted volcano-shaped curves in 1960 and 1964 for the dehydration and dehydrogenation of alcohols, with the catalytic activity dependent on the bond energies between the alcohol oxygen and the metal oxide catalysts. 18,19 Since that time, volcano curves have been generated for numerous catalytic chemistries including NO x decomposition, 20 propylene oxidation, 21 hydrodesulfurization, 22,23 ammonia synthesis, 24,25 CO oxidation, 26 and oxygenate decomposition, 27 among many other reactions. 28 The simplest surface catalytic mechanism of species A reacting to species B depicted in Figure 1A the surface as A*, undergoes surface reaction to B*, and then desorbs to gas-phase product B; the overall turnover rate can potentially be limited by any one of these three steps.…”
Section: ■ Introductionmentioning
confidence: 99%
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