Institut für Technische und Makromolekulare Chemie, RWTH Aachen University, Worringerweg 1, 52074 Aachen, Germany.
Chemistry. 2013 Apr 2;19(14):4538-47. doi: 10.1002/chem.201204159. Epub 2013 Mar 5.
A continuous-flow process based on a chiral transition-metal complex in a supported ionic liquid phase (SILP) with supercritical carbon dioxide (scCO(2)) as the mobile phase is presented for asymmetric catalytic transformations of low-volatility organic substrates at mild reaction temperatures. Enantioselectivity of >99% ee and quantitative conversion were achieved in the hydrogenation of dimethylitaconate for up to 30 h, reaching turnover numbers beyond 100000 for the chiral QUINAPHOS-rhodium complex. By using an automated high-pressure continuous-flow setup, the product was isolated in analytically pure form without the use of any organic co-solvent and with no detectable catalyst leaching. Phase-behaviour studies and high-pressure NMR spectroscopy assisted the localisation of optimum process parameters by quantification of substrate partitioning between the IL and scCO(2). Fundamental insight into the molecular interactions of the metal complex, ionic liquid and the surface of the support in working SILP catalyst materials was gained by means of systematic variations, spectroscopic studies and labelling experiments. In concert, the obtained results provided a rationale for avoiding progressive long-term deactivation. The optimised system reached stable selectivities and productivities that correspond to 0.7 kgL(-1)h(-1) space-time yield and at least 100 kg product per gram of rhodium, thus making such processes attractive for larger-scale application.
介绍了一种基于手性过渡金属配合物在负载离子液体相(SILP)中与超临界二氧化碳(scCO2)作为流动相的连续流过程,用于在温和反应温度下对低挥发性有机底物进行不对称催化转化。在手性 QUINAPHOS-铑配合物的情况下,在马来酸二甲酯的加氢反应中实现了超过 99%ee 的对映选择性和定量转化率,长达 30 小时,达到了超过 100000 的转化数。通过使用自动化高压连续流装置,在不使用任何有机溶剂的情况下以分析纯形式分离产物,并且没有检测到催化剂浸出。相行为研究和高压 NMR 光谱通过定量测定 IL 和 scCO2 之间的底物分配,有助于定位最佳过程参数。通过系统变化、光谱研究和标记实验,对手性配合物、离子液体和载体表面的 SILP 催化剂材料中的分子相互作用进行了深入了解。总之,所得结果为避免渐进性长期失活提供了依据。优化后的系统达到了稳定的选择性和产率,对应于 0.7 kgL(-1)h(-1)时空产率和至少 100 kg 产品每克铑,因此使此类工艺更适合大规模应用。