Keraani Adel, Renouard Thierry, Fischmeister Cédric, Bruneau Christian, Rabiller-Baudry Murielle
CNRS - UMR Sciences Chimiques de Rennes, Université Rennes 1, Equipe Chimie et Ingénierie des Procédés, 263 avenue du général Leclerc, CS 74205, Bâtiment 10A, Case 1011, 35042 Rennes cedex, France.
ChemSusChem. 2008;1(11):927-33. doi: 10.1002/cssc.200800152.
This study was aimed at integrating a green separation process without phase change, namely nanofiltration, with olefin metathesis to recover the homogeneous catalyst. As the commercially available Hoveyda II catalyst was not sufficiently retained by the membrane, a set of homogeneous ruthenium-based catalysts were prepared to enhance the recovery of the catalyst by solvent-resistant commercial membranes made of polyimide (Starmem 228). The molecular weights of the catalysts were gradually increased from 627 to 2195 g mol(-1), and recovery was found to increase from around 70 % to 90 % both in toluene and dimethyl carbonate. The most retained catalyst was then engaged in a series of model ring-closing metathesis reactions associated to a final nanofiltration step to recover and recycle the catalyst. Up to five cycles could be performed before a deterioration in the performance of the process was observed.
本研究旨在将无相变的绿色分离过程(即纳滤)与烯烃复分解反应相结合,以回收均相催化剂。由于市售的霍维达II型催化剂不能被膜充分截留,因此制备了一组基于钌的均相催化剂,以提高由聚酰亚胺制成的耐溶剂商业膜(Starmem 228)对催化剂的回收率。催化剂的分子量从627逐渐增加到2195 g·mol⁻¹,发现在甲苯和碳酸二甲酯中回收率均从约70%提高到90%。然后,将截留率最高的催化剂用于一系列与最终纳滤步骤相关的模型闭环复分解反应,以回收和循环使用催化剂。在观察到该过程性能恶化之前,最多可进行五个循环。