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首页> 外文期刊>Catalysis Today >Reprint of: Oxidative dehydrogenation of cyclohexane and cyclohexene over supported gold, -palladium catalysts
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Reprint of: Oxidative dehydrogenation of cyclohexane and cyclohexene over supported gold, -palladium catalysts

机译:转载:负载型金,钯催化剂上环己烷和环己烯的氧化脱氢

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摘要

Supported gold, palladium and gold-palladium catalysts have been used to oxidatively dehydro-genate cyclohexane and cyclohexenes to their aromatic counterpart. The supported metal nanoparticles decreased the activation temperature of the dehydrogenation reaction. We found that the order of reactivity was Pd ≥ Au-Pd > Au supported on TiO2. Attempts were made to lower the reaction temperature whilst retaining high selectivity. The space-time yield of benzene from cyclohexane at 473 K was determined to be 53.7 mol/kg_(cat)/h rising to 87.3 mol/kg_(cat)/h at 673 K for the Pd catalyst. Increasing the temperature in this case improved conversion at a detriment to the benzene selectivity. Oxidative dehydrogenation of cyclohexene over AuPd/TiO2 or Pd/TiO2 catalysts was found to be very effective (conversion >99% at 423 K). These results indicate that the first step in the reaction sequence of cyclohexane to cyclohexene is the slowest step. These initial results suggest that in a fixed-bed reactor the oxidative dehydrogenation in the presence of oxygen, palladium and gold-palladium catalysts are readily able to surpass current literature examples and with further modification should yield even higher performance.
机译:负载的金,钯和金-钯催化剂已经用于将环己烷和环己烯氧化脱氢为它们的芳族对应物。负载的金属纳米颗粒降低了脱氢反应的活化温度。我们发现,在TiO2上负载的反应顺序为Pd≥Au-Pd> Au。尝试降低反应温度,同时保持高选择性。对于Pd催化剂,在473 K下从环己烷得到的苯时空产率经测定为53.7 mol / kg_cat / h,在673 K下增加至87.3 mol / kg_cat / h。在这种情况下,升高温度可改善转化率,而对苯的选择性不利。发现在AuPd / TiO2或Pd / TiO2催化剂上环己烯的氧化脱氢非常有效(在423 K下转化率> 99%)。这些结果表明,环己烷与环己烯的反应顺序中的第一步是最慢的步骤。这些初步结果表明,在固定床反应器中,在氧气,钯和金钯催化剂存在下的氧化脱氢很容易超过当前的文献实例,并且经过进一步的修饰应能获得更高的性能。

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