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Continuous Gas-Phase Hydroformylation of Propene with CO2 Using SILP Catalysts
| Title: | Continuous Gas-Phase Hydroformylation of Propene with CO2 Using SILP Catalysts |
| Authors: | Hatanaka, Masataka Browse this author | | Yasuda, Tomohiro Browse this author | | Uchiage, Eriko Browse this author | | Nishida, Mayumi Browse this author →KAKEN DB | | Tominaga, Ken-ichi Browse this author |
| Keywords: | Ru complex | | ionic liquid | | homogeneous catalyst | | heterogeneous catalyst | | flow reaction |
| Issue Date: | 6-Sep-2021 |
| Publisher: | American Chemical Society |
| Journal Title: | ACS Sustainable chemistry & engineering |
| Volume: | 9 |
| Issue: | 35 |
| Start Page: | 11674 |
| End Page: | 11680 |
| Publisher DOI: | 10.1021/acssuschemeng.1c02084 |
| Abstract: | Hydroformylation is an important process for the synthesis of aldehydes and alcohols in the chemical industry. Although this process uses toxic CO as one of the reactants, some types of Ru complex catalysts have been known to replace CO with CO2 as a reactant in hydroformylation. Herein, we report the continuous hydroformylation of propene with CO2, heterogeneously catalyzed by supported Ru complexes on silica using ionic liquids [i.e., supported ionic liquid-phase (SILP) catalysts] in a flow reactor. When the reaction was carried out at 170 degrees C, 8.6 MPa, and gas hourly space velocity (GHSV) of 1.13 x 10(3) h(-1) using the SILP catalyst prepared from Ru-3(CO)(12), 1-ethyl-3-methylimidazolium chloride, and silica, the conversion of propene was 81.6% and the selectivity of hydroformylation was 66.1%. Kinetic analysis showed that the reaction rates of CO formation and hydroformylation were near-identical at 170 degrees C, indicating that the CO formed by the reverse water-gas shift reaction was readily used for the subsequent hydroformylation reaction. ESI-MS analysis of the ionic liquid phase showed the formation of trinuclear and mononuclear Ru complexes, and a plausible reaction mechanism was proposed based on these findings. |
| Rights: | This document is the Accepted Manuscript version of a Published Work that appeared in final form in ACS sustainable chemistry & engineering , copyright c American Chemical Society after peer review and technical editing by the publisher. To access the final edited and published work see [https://pubs.acs.org/articlesonrequest/AOR-IPESZFSWR8WG4MWDHTWJ]. |
| Type: | article (author version) |
| URI: | http://hdl.handle.net/2115/86679 |
| Appears in Collections: | 触媒科学研究所 (Institute for Catalysis) > 雑誌発表論文等 (Peer-reviewed Journal Articles, etc)
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Submitter: 西田 まゆみ
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