Department of Applied Chemistry, School of Engineering, The University of Tokyo, 7-3-1 Hongo, Bunkyo-ku, Tokyo 113-8656, Japan.
Inorg Chem. 2010 Mar 1;49(5):2471-8. doi: 10.1021/ic902381b.
The dinuclear peroxotungstate with a SeO(4)(2-) ligand, (TBA)(2)[SeO(4){WO(O(2))(2)}(2)] (I; TBA = (n-C(4)H(9))(4)N), could act as an efficient homogeneous catalyst for the selective oxidation of various kinds of organic substances such as olefins, alcohols, and amines with H(2)O(2) as the sole oxidant. The turnover frequency (TOF) was as high as 210 h(-1) for the epoxidation of cyclohexene catalyzed by I with H(2)O(2). The catalyst was easily recovered and reused with maintenance of the catalytic performance. The SeO(4)(2-) ligand in I played an important role in controlling the Lewis acidity of the peroxotungstates, which significantly affects their electrophilic oxygen-transfer reactivity. Several kinetic and spectroscopic results showed that the present catalytic epoxidation included the following two steps: (i) formation of the subsequent peroxo species SeW(m)O(n) (II; m = 1 and 2) by the reaction of I with an olefin and (ii) regeneration of I by the reaction of II with H(2)O(2). Compound I was the dominant species under steady-state turnover conditions. The reaction rate for the catalytic epoxidation showed a first-order dependence on the concentrations of olefin and I and a zero-order dependence on the concentration of H(2)O(2). The rate of the stoichiometric epoxidation with I agreed well with that of the catalytic epoxidation with H(2)O(2) by I. All of these kinetic and spectroscopic results indicate that oxygen transfer from I to the C=C double bond is the rate-determining step. The computational studies support that the oxygen-transfer step is the rate-determining step.
具有 SeO(4)(2-)配体的双核过氧钨酸盐,(TBA)(2)[SeO(4){WO(O(2))(2)}(2)](I;TBA = (n-C(4)H(9))(4)N),可以作为一种高效的均相催化剂,用于各种有机物质如烯烃、醇和胺的选择性氧化,H(2)O(2)是唯一的氧化剂。在 I 催化的环己烯环氧化反应中,TOF 高达 210 h(-1)。催化剂易于回收和重复使用,同时保持催化性能。I 中的 SeO(4)(2-)配体在控制过氧钨酸盐的路易斯酸度方面发挥了重要作用,这显著影响了它们的亲电氧转移反应性。一些动力学和光谱学结果表明,目前的催化环氧化包括以下两个步骤:(i)I 与烯烃反应形成后续的过氧物种SeW(m)O(n)(II;m = 1 和 2),(ii)II 与 H(2)O(2)反应再生 I。在稳态转化率条件下,化合物 I 是主要物种。催化环氧化反应速率对烯烃和 I 的浓度呈一级依赖,对 H(2)O(2)的浓度呈零级依赖。I 的化学计量环氧化反应速率与 I 催化的环氧化反应速率吻合良好。所有这些动力学和光谱学结果表明,I 向 C=C 双键的氧转移是速率决定步骤。计算研究支持氧转移步骤是速率决定步骤。