脱氢
丙烷
丙烯
化学
催化作用
产量(工程)
空间速度
无机化学
光化学
有机化学
冶金
选择性
材料科学
作者
Qiyang Zhang,Yuming Li,Tatiana Otroshchenko,Vita A. Kondratenko,Kai Wu,Elizaveta A. Fedorova,Dmitry E. Doronkin,Stephan Bartling,Henrik Lund,Guiyuan Jiang,Evgenii V. Kondratenko
标识
DOI:10.1016/j.jcat.2024.115440
摘要
Due to the increased production of shale gas containing propane, the share of non-oxidative propane dehydrogenation (PDH) in the large-scale production of propene is expected to continue to grow. There are, however, some ecofriendly and cost shortcomings associated with the currently applied Cr- or Pt-containing catalysts. Against this background, we present here Co/ZrO2 alternatives and reveal the fundamentals affecting their activity, which can be used for purposeful catalyst design. Co2+ species homogeneously distributed within the lattice of ZrO2 significantly increase the activity of coordinatively unsaturated Zr4+ for the PDH reaction. The increase is caused by accelerating both the cleavage of CH bonds in propane and the recombination of surface H species, with the latter reaction being the rate-limiting step. The best-performing catalyst outperformed an analogue of commercial K-CrOx/Al2O3 in terms of the rate of propene formation and demonstrated durable performance over a series of 10 PDH/regeneration cycles under industrially relevant conditions. It also outperformed most previously developed Co-containing catalysts in terms of propene productivity. The space–time yield of propene formation achieved at 57 % equilibrium propane conversion at 550 °C was 0.71 kg·h−1·kgcat-1.
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