Department of Chemistry, Colorado State University, Fort Collins, Colorado 80523, USA.
Langmuir. 2010 Jul 20;26(14):12455-64. doi: 10.1021/la101390e.
"Weakly ligated/labile ligand" nanoparticles, that is nanoparticles where only weakly coordinated ligands plus the desired catalytic reactants are present, are of fundamental interest. Described herein is a catalyst system for benzene hydrogenation to cyclohexane consisting of "weakly ligated/labile ligand" Ir(0) nanoparticles and aggregates plus dry-HCl formed in situ from commercially available (1,5-COD)IrCl plus 40 +/- 1 psig (approximately 2.7 atm) H(2) at 22 +/- 0.1 degrees C. Multiple control and other experiments reveal the following points: (i) that this catalyst system is quite active with a TOF (turnover frequency) of 25 h(-1) and TTO (total turnovers) of 5250; (ii) that the BF(4)(-) and PF(6)(-) iridium salt precursors, [(1,5-COD)Ir(CH(3)CN)(2)]BF(4) and [(1,5-COD)Ir(CH(3)CN)(2)]PF(6), yield inferior catalysts; (iii) that iridium black with or without added, preformed HCl cannot achieve the TOF of 25 h(-1) of the in situ formed Ir(0)/dry-HCl catalyst. However and importantly, CS(2) poisoning experiments yield the same activity per active iridium atom for both the Ir(0)/dry-HCl and Ir black/no-HCl catalysts (12.5 h(-1) Ir(1-)), but reveal that the Ir(0)/dry-HCl system is 10-fold more dispersed compared to the Ir(0) black catalyst. The simple but important and key result is that "weakly ligated/labile ligand" Ir(0) nanoparticles and aggregates have been made in situ as demonstrated by the fact that they have identical, per exposed Ir(0) activity within experimental error to Ir(0) black and that they have no possible ligands other than those desired for the catalysis (benzene and H(2)) plus the at best poor ligand HCl. As expected, the in situ catalyst is poorly stabilized, exhibiting only 60% of its initial activity in a second run of benzene hydrogenation and resulting in bulk metal precipitation. However, stabilization of the Ir(0) nanoparticles with a ca. 2-fold higher catalytic activity and somewhat longer lifetime for the complete hydrogenation of benzene was accomplished by supporting the Ir(0) nanoparticles onto zeolite-Y (TOF of 47 h(-1) and 8600 TTO under otherwise identical conditions). Also reported is the interesting result that Cl(-) (present as Proton Sponge x H(+)Cl(-)) completely poisons benzene hydrogenation catalysis, but not the easier cyclohexene hydrogenation catalysis under otherwise the same conditions, results that suggest different active sites for these ostensibly related hydrogenation reaction. The results suggest that synthetic routes to "weakly ligated/labile ligand" nanoparticles exhibiting improved catalytic performance is an important goal worthy of additional effort.
“弱配位/不稳定配体”纳米粒子是指其中只存在弱配位配体和所需催化反应物的纳米粒子,具有重要的研究意义。本文介绍了一种由“弱配位/不稳定配体”Ir(0)纳米粒子和聚集体以及原位形成的干燥 HCl 组成的苯加氢制环己烷的催化剂体系,该体系由商业可得的(1,5-COD)IrCl与 40 +/- 1 psig(约 2.7 atm)H(2)在 22 +/- 0.1 摄氏度下反应得到。多项控制和其他实验揭示了以下几点:(i) 该催化剂体系具有较高的活性,TOF( turnover frequency)为 25 h(-1),TTO( total turnovers)为 5250;(ii) BF(4)(-)和 PF(6)(-)铱盐前体[(1,5-COD)Ir(CH(3)CN)(2)]BF(4)和[(1,5-COD)Ir(CH(3)CN)(2)]PF(6)生成的催化剂性能较差;(iii) 无论是加入还是不加入预先形成的 HCl,铱黑都无法达到原位形成的 Ir(0)/干燥 HCl 催化剂的 25 h(-1)的 TOF。然而,重要的是,CS(2)中毒实验表明,对于 Ir(0)/干燥 HCl 和 Ir 黑/无 HCl 催化剂,每个活性铱原子的活性相同(12.5 h(-1)Ir(1-)),但表明 Ir(0)/干燥 HCl 体系的分散度比 Ir(0)黑催化剂高 10 倍。简单但重要的关键结果是,“弱配位/不稳定配体”Ir(0)纳米粒子和聚集体已原位形成,这一事实证明,它们与 Ir 黑和 Ir(0)黑催化剂具有相同的、每暴露一个 Ir(0)原子的活性,并且它们除了催化所需的配体(苯和 H(2))外,没有其他可能的配体,外加最多只有较差的配体 HCl。不出所料,原位催化剂的稳定性较差,在苯加氢的第二次运行中仅保持了其初始活性的 60%,并导致大量金属沉淀。然而,通过将 Ir(0)纳米粒子负载到沸石-Y 上,实现了 Ir(0)纳米粒子的稳定性提高,催化活性提高了约 2 倍,完全加氢苯的寿命也有所延长(在其他条件相同的情况下,TOF 为 47 h(-1),TTO 为 8600)。还报道了一个有趣的结果,即 Cl(-)(以 Proton Sponge x H(+)Cl(-)的形式存在)完全抑制了苯加氢催化反应,但不抑制环己烯加氢催化反应,这表明这些表面上相关的加氢反应具有不同的活性位。这些结果表明,开发具有改进催化性能的“弱配位/不稳定配体”纳米粒子的合成途径是一个值得进一步努力的重要目标。