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Active Carbon Supported Rhodium Catalyst in the Hydroformylation of 1-Hexene

机译:活性炭负载的铑催化剂在1-己烯的加氢甲酰化反应中

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Hydroformylation performance of 1-hexene over rhodium solid catalyst was studied under mild reaction condition (H_2/CO = 1/1, Pressure = 3.0 MPa, T = 403 K). Its hydroformylation activities were examined systematically in various solvents. Effects of operating variables on the CO conversion, yields of products and stability of the catalysts also have been discussed in detail. It was found that the rhodium catalyst exhibited the excellent activity in the n-octane solvent, while poor activity in the alcoholic and H_2O solvent. Rh/active carbon (Rh/C) catalyst presented superior catalytic performances over Rh/SiO_2 catalyst in the activity, selectivity and stability. As the most important, Rh/C catalyst showed stable activity in the continuous (olefin and synthesis gas) feeding system even in the low metal loading, giving the total turn over number (TON) of 500 during 14 hs reaction.
机译:在温和的反应条件下(H_2 / CO = 1/1,压力= 3.0 MPa,T = 403 K)研究了1-己烯在铑固体催化剂上的加氢甲酰化性能。在各种溶剂中系统地检查了其加氢甲酰化活性。还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。发现铑催化剂在正辛烷溶剂中表现出优异的活性,而在醇和H_2O溶剂中表现出差的活性。 Rh /活性炭(Rh / C)催化剂在活性,选择性和稳定性方面均优于Rh / SiO_2催化剂。最重要的是,Rh / C催化剂即使在低金属负载量下,在连续(烯烃和合成气)进料系统中也表现出稳定的活性,在14 hs反应期间的总周转数(TON)为500。

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