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首页> 外文期刊>European journal of organic chemistry >Kinetics of (porphyrin)manganese(III)-catalyzed olefin epoxidation with a soluble iodosylbenzene derivative
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Kinetics of (porphyrin)manganese(III)-catalyzed olefin epoxidation with a soluble iodosylbenzene derivative

机译:可溶性碘代苯衍生物在(卟啉)锰(III)催化的烯烃环氧化反应中的动力学

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We examined the kinetics of a well-behaved system for homogeneous porphyrin-catalyzed olefin epoxidation with a soluble iodosylbenzene derivative I as the terminal oxidant and Mn(TPFPP)Cl (2) as the catalyst. The epoxidation rates were measured by using the initial rate method, and the epoxidation products were determined by gas chromatography. The epoxidation rate was found to be first order with respect to the porphyrin catalyst and zero order on the terminal oxidant. In addition, we found the rate law to be sensitive to the nature and concentration of olefin substrates. Saturation kinetics were observed with all olefin substrates at high olefin concentrations, and the kinetic data are consistent with a Michaelis-Menten kinetic model. According to the observed saturation kinetic results, we propose that there is a complexation between the active oxidant and the substrate, and the rate-determining step is thought to be the breakdown of this putative substrate-oxidant complex that generates the epoxidation products and the resting state porphyrin catalyst. Competitive epoxidations further indicate a reversible complexation of the active oxidant and the olefin substrate. The activation parameters Delta H-double dagger and Delta S-double dagger for the oxygen-transfer process (k(2)) in the cis-cyclooctene epoxidation were determined to be 12.3 +/- 0.9kcal mol(-3) and -15.6 +/- 3.2 cal mol(-1) K-1, respectively. In addition, the Hammett constant rho(+) was measured for the epoxidation of parasubstituted styrenes, and the value of -0.27 +/- 0.04 is too low to be consistent with the involvement of a discrete carbocation in the transition state. We also prepared a (porphyrin)manganese catalyst immobilized on silica support, and found the epoxidation of cis-cyclooctene catalyzed by this heterogeneous catalyst proceeds at virtually the same turnover frequency as by the homogeneous porphyrin catalyst. ((c) Wiley-VCH Verlag GmbH & Co. KGaA, 69451 Weinheim, Germany, 2006).
机译:我们检查了行为良好的系统的动力学,该系统用于均相卟啉催化的烯烃环氧化,其中可溶性碘基苯衍生物I作为末端氧化剂,而Mn(TPFPP)Cl(2)作为催化剂。使用初始速率法测量环氧化速率,并通过气相色谱法测定环氧化产物。发现环氧化速率相对于卟啉催化剂为一级,而在末端氧化剂上为零级。另外,我们发现速率定律对烯烃底物的性质和浓度敏感。在高烯烃浓度下,所有烯烃底物均观察到饱和动力学,该动力学数据与Michaelis-Menten动力学模型一致。根据观察到的饱和动力学结果,我们认为活性氧化剂与底物之间存在络合物,速率确定步骤被认为是该推定的底物-氧化剂络合物的分解,后者会产生环氧化产物和残留物。态卟啉催化剂。竞争性环氧化进一步表明活性氧化剂和烯烃底物的可逆络合。氧转移过程(k(2))在顺式-环辛烯环氧化中的活化参数Delta H-双匕首和Delta S-双匕首确定为12.3 +/- 0.9kcal mol(-3)和-15.6分别为+/- 3.2 cal mol(-1)K-1。另外,测量了对位取代的苯乙烯的环氧化的哈米特常数rho(+),并且-0.27 +/- 0.04的值太低,无法与过渡状态中离散碳正离子的参与一致。我们还制备了固定在二氧化硅载体上的(卟啉)锰催化剂,发现这种非均相催化剂催化的顺式环辛烯的环氧化反应的发生频率与均相卟啉催化剂相同。 ((c)Wiley-VCH Verlag GmbH&Co.KGaA,69451 Weinheim,德国,2006年)。

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