乙苯
脱氢
催化作用
苯乙烯
氧化还原
化学
氧气
无机化学
产量(工程)
氧化物
氧化磷酸化
材料科学
有机化学
聚合物
共聚物
生物化学
冶金
作者
Sebastian Geisler,I. Vauthey,D. Farusseng,H.‐W. Zanthoff,Martin Muhler
标识
DOI:10.1016/s0920-5861(03)00141-x
摘要
Catalyst development for non-stationary redox application is still time consuming. A new method for high-throughput screening of catalysts under non-steady-state conditions is introduced enabling catalyst screening with >50 samples per day. The new method was applied to the oxidative dehydrogenation of ethylbenzene (ODEB) performed by alternately feeding ethylbenzene and oxygen. A highly selective mixed metal oxide catalyst (composition K2O (0.3 wt.%)/V2O5 (16 wt.%)/MgO) was found which converts ethylbenzene into styrene with an overall yield of 80.2% obtained by adding up both the wt.% ethylbenzene and the oxygen pulse. Selectivities in the ethylbenzene pulse amounted up to 98%. Mechanistic investigations reveal that the reaction does not proceed in a typical redox type mode.
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