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Kinetics and Mechanisms of Homogeneous Catalytic Reactions. Part 12. Hydroalcoxycarbonylation of 1-Hexene Using Palladium/ Triphenylphosphine Systems as Catalyst Precursors

机译:均相催化反应的动力学和机理。第12部分。使用钯/三苯膦体系作为催化剂前体的1-己烯的氢烷氧羰基化

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Systems prepared in situ by addition of n equivalents of triphenylphosphine to palladium dichloride in the presence of m equivalents of para-toluenesulfonic acid (TSA), PdCl2PPh3/mTSA (n and m varying between 2 and 10), were used as precatalysts for the olefin carbonylation (1-hexene, cyclohexene and styrene) with alcohols (MeOH, EtOH, n-PrOH and i-PrOH) to generate the corresponding esters (hydroalcoxycarbonylation), under mild reaction conditions. For 1-hexene carbonylation in presence of methanol (1-hexene hydromethoxycarbonylation), the most active system was PdCl2/6PPh3/5TSA at P(CO) = 50 atm and T = 125 °C, which was also active for the hydromethoxycarbonylation of other olefins (1-hexene > styrene > cyclohexene). This system was regioselective towards the linear product for 1-hexene and towards the branched product for styrene. A kinetic study of 1-hexene hydromethoxycarbonylation catalyzed by PdCl2/6PPh3/ 5TSA showed that the initial reaction rate (r_o) was first order on Pd and MeOH concentrations and fractional order with respect to CO concentration; for olefin concentration was found a saturation curve. These kinetic results, together with coordination chemistry and computational DFT studies, allow us to propose a catalytic cycle involving species of the type [Pd(H)(L)(PPh3)2]~(+n) (L = Cl, n = 0; L = CO, MeOH, olefin and PPh3, n = 1) as the catalytically active species and three sequential reactions: (1) olefin insertion into the Pd-H bond to yield Pd-alkyl species, (2) CO insertion into the Pd-C bond to generate Pd-acyl intermediates, and (3) the methanolysis of Pd-acyl species to produce the corresponding methyl esters, regenerate the active species and restart the cycle; the last reaction is considered the rate-determining step (rds) of the mechanism.
机译:在m当量对甲苯磺酸(TSA),PdCl2 / nPPh3 / mTSA(n和m在2到10之间变化)的存在下,通过将n当量的三苯基膦加到二氯化钯中的原位制备的系统用作预催化剂。在温和的反应条件下,用醇(MeOH,EtOH,n-PrOH和i-PrOH)将烯烃羰基化(1-己烯,环己烯和苯乙烯),生成相应的酯(氢烷氧羰基化)。对于在甲醇存在下的1-己烯羰基化(1-己烯加氢甲氧羰基化),最活跃的体系是PdCl2 / 6PPh3 / 5TSA,在P(CO)= 50 atm和T = 125°C时也对其他的加氢羰基化有活性烯烃(1-己烯>苯乙烯>环己烯)。该系统对1-己烯的线性产物和对苯乙烯的支链产物具有区域选择性。 PdCl2 / 6PPh3 / 5TSA催化的1-己烯加氢甲氧基羰基化反应动力学研究表明,初始反应速率(r_o)在Pd和MeOH浓度上为一级,相对于CO浓度为分数级。对于烯烃浓度,发现了饱和曲线。这些动力学结果以及配位化学和计算DFT研究,使我们能够提出涉及[Pd(H)(L)(PPh3)2]〜(+ n)类型的物种的催化循环(L = Cl,n = 0; L = CO,MeOH,烯烃和PPh3,n = 1)作为催化活性物质和三个连续反应:(1)烯烃插入Pd-H键以生成Pd-烷基物质,(2)CO插入Pd-C键产生Pd-酰基中间体,和(3)Pd-酰基物质的甲醇分解反应产生相应的甲酯,再生活性物质并重新开始循环;最后的反应被认为是该机理的速率决定步骤(rds)。

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