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Hydroformylation of 1-hexene using polymer-supported rhodium catalysts in supercritical carbon dioxide

机译:使用聚合物负载的铑催化剂在超临界二氧化碳中将1-己烯加氢甲酰化

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摘要

Hydroformylation of 1-hexene was carried out in supercritical CO2 (scCO2) and in organic solvents (toluene and ethyl acetate) using polymer-supported rhodium catalysts, which were prepared from polystyrene bound triphenylphosphine (TPP) and dicarbonylacetylecetonato rhodium. Preparation variables such as TPP/Rh ratio, time of rhodium precursor fixation on the support and time of syngas pretreatment do not produce significant effects on the reaction. The product distribution slightly changes with CO2 pressure. The conversion increases appreciably as H2 pressure is raised in scCO2 but CO retards the reaction. The influence of H2 pressure in scCO2 is slightly different from that in toluene. Changes of the structure of rhodium complexes on the polymer during the catalyst preparation and the reaction were investigated by diffuse reflectance FT-IR. It should be noted that the catalyst is recyclable for the reaction in scCO2 and that the reaction rate and selectivity of the hydroformylation are much higher than those in the organic solvents.
机译:1-己烯的加氢甲酰化反应是在超临界CO2(scCO2)和有机溶剂(甲苯和乙酸乙酯)中使用聚合物负载的铑催化剂进行的,该催化剂由聚苯乙烯键合的三苯基膦(TPP)和二羰基乙酰基乙二酮铑制得。制备变量(例如TPP / Rh比,铑前体在载体上的固定时间和合成气预处理的时间)对反应没有明显影响。产品分布随二氧化碳压力而略有变化。随着scCO2中H2压力的升高,转化率明显增加,但CO会延迟反应。 H2压力在scCO2中的影响与在甲苯中的影响略有不同。通过漫反射FT-IR研究了铑在催化剂制备和反应过程中在聚合物上的配合物的结构变化。应当指出,该催化剂可在scCO 2中循环用于反应,并且加氢甲酰化的反应速率和选择性远高于有机溶剂中的反应速率和选择性。

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