Pal Raja, Groy Thomas L, Trovitch Ryan J
Department of Chemistry and Biochemistry, Arizona State University, Tempe, Arizona 85287, United States.
Inorg Chem. 2015 Aug 3;54(15):7506-15. doi: 10.1021/acs.inorgchem.5b01102. Epub 2015 Jul 23.
Using a multistep synthetic pathway, a bis(imino)pyridine (or pyridine diimine, PDI) molybdenum catalyst for the selective conversion of carbon dioxide into methanol has been developed. Starting from ((Ph2PPr)PDI)Mo(CO), I2 addition afforded [((Ph2PPr)PDI)MoI(CO)][I], which features a seven-coordinate Mo(II) center. Heating this complex to 100 °C under vacuum resulted in CO loss and the formation of [((Ph2PPr)PDI)MoI][I]. Reduction of [((Ph2PPr)PDI)MoI][I] in the presence of excess K/Hg yielded (κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH following methylene group C-H activation at the α-position of one PDI imine substituent. The addition of CO2 to (κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH resulted in facile insertion to generate the respective η(1)-formate complex, (κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)Mo(OCOH). When low pressures of CO2 were added to solutions of (κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH containing pinacolborane, the selective formation of H3COBPin and O(BPin)2 was observed along with precatalyst regeneration. When HBPin was limited, H2C(OBPin)2 was observed as an intermediate and (κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)Mo(OCOH) remained present throughout CO2 reduction. The hydroboration of CO2 to H3COBPin was optimized and 97% HBPin utilization by 0.1 mol % (κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH was demonstrated over 8 h at 90 °C, resulting in a methoxide formation turnover frequency (TOF) of 40.4 h(-1) (B-H utilization TOF = 121.2 h(-1)). Hydrolysis of the products and distillation at 65 °C allowed for MeOH isolation. The mechanism of (κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH mediated CO2 hydroboration is presented in the context of these experimental observations. Notably, (κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH is the first Mo hydroboration catalyst capable of converting CO2 to MeOH, and the importance of this study as it relates to previously described catalysts is discussed.
通过多步合成途径,开发出一种用于将二氧化碳选择性转化为甲醇的双(亚氨基)吡啶(或吡啶二亚胺,PDI)钼催化剂。从((Ph2PPr)PDI)Mo(CO)开始,加入碘得到[((Ph2PPr)PDI)MoI(CO)][I],其具有七配位的Mo(II)中心。在真空中将该配合物加热至100°C导致CO损失并形成[((Ph2PPr)PDI)MoI][I]。在过量K/Hg存在下还原[((Ph2PPr)PDI)MoI][I],在一个PDI亚胺取代基的α位进行亚甲基C-H活化后得到(κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH。向(κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH中加入CO2导致其容易插入生成相应的η(1)-甲酸配合物(κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)Mo(OCOH)。当向含有频哪醇硼烷的(κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH溶液中加入低压CO2时,观察到选择性形成H3COBPin和O(BPin)2以及预催化剂再生。当HBPin有限时,观察到H2C(OBPin)2作为中间体,并且在整个CO2还原过程中(κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)Mo(OCOH)仍然存在。优化了CO2硼氢化生成H3COBPin的反应,在90°C下0.1 mol%的(κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH在8小时内实现了97%的HBPin利用率,导致甲醇盐形成的周转频率(TOF)为40.4 h(-1)(B-H利用率TOF = 121.2 h(-1))。产物水解并在65°C下蒸馏可分离出甲醇。结合这些实验观察结果阐述了(κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH介导的CO2硼氢化反应机理。值得注意的是,(κ(6)-P,N,N,N,C,P-(Ph2PPr)PDI)MoH是第一种能够将CO2转化为甲醇的钼硼氢化催化剂,并讨论了该研究与先前描述的催化剂相关的重要性。