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Hydroformylation of 1-Hexene over Cobalt-based Solid Catalysts at Low Pressure

机译:钴基固体催化剂上低压下1-己烯的加氢甲酰化

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References(20) Cited-By(1) Hydroformylation of 1-hexene has been investigated over cobalt supported on active carbon catalyst (10 wt% Co/A.C.) in a slurry phase reactor under low pressure (3.0 MPa). Added alcohols, such as methanol and other lower alcohols significantly promoted the reaction to realize a low-pressure process for hydroformylation at 3.0 MPa and 403 K, markedly giving acetals and aldehydes. Effects of operating variables on the CO conversion, yields of products and stability of the catalysts have been discussed in detail. The addition of a small amount of Ru (0.5 wt%) to the Co catalyst remarkably shortened the induction period and increased the catalytic activity. Compared with the corresponding homogeneous catalyst, the supported cobalt catalyst was observed to have good stability in the continuous feed system, showing constant CO conversion and yield of oxygenates.
机译:参考文献(20)被引用的By(1)在淤浆相反应器中在低压(3.0MPa)下在活性炭催化剂(10wt%Co / A.C。)上负载的钴上研究了1-己烯的加氢甲酰化。加入的醇,例如甲醇和其他低级醇,显着促进了反应,从而实现了在3.0 MPa和403 K的低压下进行加氢甲酰化的低压工艺,从而显着产生了缩醛和醛。已经详细讨论了操作变量对CO转化率,产物产率和催化剂稳定性的影响。向Co催化剂中添加少量Ru(0.5wt%)显着缩短了诱导期并提高了催化活性。与相应的均相催化剂相比,观察到负载的钴催化剂在连续进料系统中具有良好的稳定性,显示出恒定的CO转化率和含氧化合物的产率。

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